HomeMy WebLinkAbout343 Monroe Rd 17-230 PLUMBINGCITY OF SANFORD
E MAY 2 t 27OVI BUILDING & FIRE PREVENTION
PERMIT APPLICATION
50
r
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Oaf
No:
Documented Construction Value: S- 2:5 66a °—
Job Address: 34 3 M -M 23historic District: Yes No
Parcel ID: 1(,— 1. 3 a' S 11 rc- C>OO 0
1
Residential Commercials.
Type of Work: NewEl Addition Alterration Repair Demo Change of Use Move
Description of Work: _TA;-f_-
1 Ine. w `1 e y - 4i C o.. \ e1 ec+- c ' r P otjvvn n -
Plan Review Contact Person: Kelli Sessions Title: Operations AA
Phone: 407-585-3252 Fax: 407-585-3277 Email: kas0wiainton net
Property Owner Information
Name U -L Pholid:
Street: J' 70( DC) T- COMo(Z.-T S
o
Resident of property?:
City, State ZipO u I CCV3
Contractor Information
t'
n Phone: 407-585-32.52Name ginton Fire S istem -Charles Patrick -
Street: 699 Aero Lane Fax: 407-585-3277
City, State Zip: Sanford Florida 32771 State License No.: FPC15-000105
Architect/Engineer Information
Name: Phone:
Street: Fax:
City, St, Zip:
Bonding Company:
Address:
E-mail:
Mortgage Lender:
Address:
WARNING TO OWNER: YOUR FAILURE TO RECORD A NOTICE OF COMMENCEMENT MAY RESULT IN YOUR
PAYING TWICE FOR IMPROVEMENTS TO YOUR PROPERTY. A NOTICE OF COMMENCEMENT MUST BE
RECORDED AND POSTED ON THE JOB SITE BEFORE THE FIRST INSPECTION. IF YOU INTEND TO OBTAIN
FINANCING, CONSULT WITH YOUR LENDER OR AN ATTORNEY BEFORE RECORDING YOUR NOTICE OF
COMMENCEMENT.
Application is hereby made to obtain a permit to do the work and installations as indicated. I certify that no work or installation has
commenced prior to the issuance of a permit and that all work will be performed to meet standards of all laws regulating construction
in this jurisdiction. 1 understand that a separate permit must be secured for electricnl work, plumbing, signs, wells, pools,
furnaces, boilers, heaters, tanks, and air conditioners, etc.
FBC 105.3 Shall be inscribed with the date of application and the code in effect as of that date: 51^ Edition (2014) Florida Building Code
Revised: June 30,
2015Permit Application
ici1 A A Fee
M
NO-TICE: In addition to the requirements of this permit, there may be additional restrictions applicable to this property that may be
found in the public records of this county, and there may be additional permits required from other governmental entities such as water
management districts, state agencies, or federal agencies.
Acceptance of permit is verification that I will notify the owner of the.property of the requirements of Florida Lien Law, FS 713.
The City of Sanford requires payment of a plan review fee at the time of permit submittal. A copy of the executed contract is required
in order to calculate a plan review charge and will be considered the estimated construction value of the job at the time of submittal.
The actual construction value will be figured based on the current ICC Valuation Table in effect at the time the permit is issued, in
accordance with local ordinance. Should calculated charges figured off the executed contract exceed the actual construction value,
credit will be applied to your permit fees when the permit is issued.
OWNER'S AFFIDAVIT: I certify that all of the foregoing information is accurate and that all work will
be done in compliance with all applicable laws regulating construction and zoning.
1,V ., Q-- C23 L,
Signature of Owner/Agent Date Signature of Contractor/Agent Date
Print Omer/Agent's Name
Signature of Notary -State or Florida Date
Charles Patrick
Print Co tractor/Agent's Name
V
KELLI SESSIONS
Notary Public - State of Florida
Commission # FF 215202
My Comm. Expires Mar 90, 2011
Owner/Agent is Personally Known to Me or Contractor/Agent is X_
Produced ID Type of ID Produced ID Type of 1D
BELOW IS FOR OFFICE USE ONLY
Permits Required: Building Electrical Mechanical Plumbing Gas[] Roof
Construction Type: Occupancy Use:
Total Sq Ft of Bldg: Min. Occupancy Load:
Flood Zone:
of Stories:
New Construction: Electric - # of Amps Plumbing - # of Fixtures
Fire Sprinkler Permit: Yes No # of Heads Fire Alarm Permit: Yes No
APPROVALS: ZONING: UTILITIES: WASTE WATER:
ENGINEERING: FIRE S k l
BUILDING:
COMMENTS:
Revised: lune 30.2015 Permit Application
McKee ?'a
frmrot Road
SSamford,o/rtl, R. 32771
CONSTRVCTIOM CO. (4117) 323-1150 F1\ 1407023-10WW
GENERAL CONTRACTORS
SUBCONTRACT AGREEMENT
CONTRACTOR: McKee Construction Co.
SUBCONTRACTOR: Wiginion Fire Systems
PROJECT: GANESH NORTH LLC
ADDRESS: 343 MONROE ROAD SANFORD. FL 32771
CONTRACT NO: 2016-05-42
JOB NO: 2016.05 GANESH NORTH LLC
DATE. November 14, 2016
CODE: 15500•--5415,000.00
CONTRACT PRICE (INCLUDES ALL TAXES) NOT TO EXCEED $415.000.00 WITH TEN 110%) RETAINAGE,
PAYABLE AS FOLLOWS: MONTHLY PROGRESS PAYMENTS SHALL BE BILLED ON OR BEFORE 2011, OF 140111H FOR WORK THROUGH THE END OF MONTH.
PAYMENT BY THE OWNER TO MCKEE CONSTRUCTION CO. SHALL BE AN ABSOLU TE CONDITION PRECEDENT TO MCKEE CONSTRUCTION CO. OBLIGATION TO
MAKE INTERIM PROGRESS PAYMENT TO SUBCONTRACTOR, AND NO FUNDS SHALL BE OWED BY MCKEE CONSTRUCTION CO. TO SUBCONTRACTOR UNLESS
MCKEE CONSTRUCTION CO. IS PAID BY OWNER. ONLY MCKEE CONS TRUC I ION CO. SUPPLIED PAY APPLICATION WILL BE ACCEPTED FOR ALL PROGRESS
AND RETAINAGE PAYMENTS, ALL LIEN LAWS ARE APPLICABLE. FINAL PAYMENT BY OWNER rO MCKEE CONSTRUCTION CO. IS A CONDITION PRECEDENT TO
MCKEE CONSTRUCTION CO. OBLIGATION TO MAKE FILIAL PAYMENT TO SUBCONTRACTOR. THE RELEASE OF MCKEE CONSTRUCTION CO. RETAINAGE BY THE
OWNER IS A CONDITION PRECEDENT TO TO RELEASE OF SUBCONTRACTOR'S RETAINAGE BY MCKEE CONSTRUCTION CO.
SUBCONTRACTORS PROPOSAL DOES NOT SUPERSEDE ANY AND ALL ITEMS REQUIRED IN PLANS AND SPECIFICATIONS FOR WORK TO BE PERFORMED ON
PROJECT, UNLESS SUBCONTRACTOR'S PROPOSAL CHANGES HAVE BEEN AGREED UPON BY BOTH PARTIES AT PRICING STAGE OF PROJECT.SC1OPEOF
WORK WRITTEN SCHEDULE MUST BE PROVIDED PRIOR TO it' APPLICATION FOR PAYMENT BEING PROCESSEDI
1.Subcontractor agrees to participate In weekly Jobsbe and Salery meeting's on site. Meeting will discuss project and issues that may arise during construction of
project. Subcontractor is responsible for updating McKee Construction Co. in regards to schedule, material availability and general progress of subcontractor SCAM. -
of work on a vreekly basis.
2.Subcontractor agrees to perform all labor In a workmanlike manner. to prosecute said work In accordance vnth Contractors schedule and to complete all vork in a
prompt and professional manner. Subcontractor is rye ulred to clean up scop= of work fob debris on a doily basis. failure to maintain this policy will result In McKee
Construction Co. issuing a vritten notice of deficency and will subseguenlly hire clean mD workers which vAll result In a hackcharme to the subcontmctor.
3. Subcontractor further agrees that he has in lull force and effect this date and will continue in force during the course of his work, Workmen's Compensation
Insurance, as required by law, and Public Liability and Property Damage Insurance as is reasonably necessary to insure against the risk arising out of this contract A
certificate of said Insurance Is to be received by the Contractor within three 131 days follovAng the execution of this contract. In no case will any work be commenced
prior to recelpt of the Certificate by the Contractor. "Prior to the completion of work operations on this property, none of the above Insurance Is to be cancelled,
changed, or allolved to lapse until 30 days prior written notice has been given to the Contractor."
4. In addition to standard manufacturers warrantles for any equipment installed by Subcontractor. Subcontractor guarantees all work against defects from the use of
ferlor or defective materials, equipment or workmanship for one year from the dale at occupancy b X theaotmet (Certificate of Occupancy I Ce ificate of
ompletlon)_ All repairs or changes required In connection with this Guarantee will be performed promptly at the Subcontractor's expense.
6. Subcontractor required to acknowledge McKee Conotruclion Co. safely policies manual on rile, and adhere to all such policies. McKee Construction Cu. requires
Hard hats to be worn at all times on jobsile, failure to adhere to this policy +null result in the immediate expulsion o: violators from jobsile. The subcontractor agrees t:
furnish McKee Construction Co. with Material Safety Data Sheets for all hazardous materials that will be used on this project by subcontractor or his sub.
subcontractors.
7. The subcontractor is to comply with all current OSHA regulations. Sdfely to. the Subconu3ctor's employees is the responsibility of the Subcontractor.
Subcontractor shall maintain a competent person on site during the course of the subcontractor's work. In the event that the Subcontractor is in viciadon on any
OSHA safety regulations. all loses, damages• and expenses incurred including OSHA fines mcurrnd as a result of said violation shall be borne by and Charged against
the Subcontractor.
8. Atckee Construction Co adhere's to a drug free work environment. All companies and their employees who perform work under this subcorlract agreement on
McKee Construction Co. jobsites are subject to random drug testing as a requirement of this contract. If relusal or positive lasting takes place McKee Construclru.t
Co. reserves the right to ban Irom performing work under this contract individual or inoivnduafs that violate this policy.
8. hlcKee Construction Co. requires the subcontractor to have on )obstle at all limes a qualified lorentan to maintain proper comimunlwtion vrnh McKee Consuucuon
Co. project manager and or superintendent. Violation of this agreement will result in immediate termination of this subcontract after written notice has been delivered
to subcontractor. It termination of contract occurs. subcontractor agrees to cover any cost overage's that may lake place in completing the scope of rrorlt.
9. As part of the acceptance of this Subcontract. Subcontractor wilt provide to McKee Construction Co. a list of all princl aI ss and key empIoy_ee't cellular -phone
numbers. Monthly Pay request will not be paid until these numbers have boon supplied to McKee Construction Co. If at any time the Subcontractor fails to respond in
atimely manner, McKee Construction Co. has the right to terminale said contract upon written notice of deficencies.
10. Subcontractor Is responsible for the maintenance of their scope of work items until Certificate of Occupancy I Certificate of Complotion is secured.
11. Subcontractor may after subcontract issuance request written permission for substitutions of items specified in project documents, a complete submittal wAll be
required with any possible savings which will be reviewed for conformity by both the contractor and related design professionals. Contractor will issue a written lelte•
of approval or denial as to the suhstihdon request being granted
Accepted: Contractor
McKee Construction Co.
790 MONROE ROAD
Accepted- Subcontractor
Wigrnion Fire Systems
699 Aero Lane Sanford, FL 32707
SANFORD, FL 32771 Pete Aziz (407) 585.3277 ce!I (407 453-9269
Authorized Signature: ,uthorized Corporate Signature
l
int Nome: ,) C -
ate:_ _//* b Print ' Title: Date.
IF
6—- riarfes M. -Patrick ____.-- I
Vice President, Branch Manager
M., t /-.
ltwo1
FIRE Mill OSinQ
Form S-600
PROPOSAL
Page 1 of 10
Date: 11-2-16 1 WFS Proposal #:
Customer: McKee Construction Co.
Address: 790 Monroe Rd. Sanford FL. 32771
Contact: Joe Nicholas
Phone: 407-323-1150 Fax: 407-323-9304 Cell:
Project: Ganesh North Revised 11-2-16
Location: NEC Monroe Rd. & Narcissus Ave.
Owner:
Eng.: 1 Architectural Dynamics, Inc.
Sheet #'s & Dates: 7-20-16
Addenda (list):
EOR:
Wiginton Fire Systems (WFS) proposes to fumish materials and labor as specified below at the prices stated below:
SCOPE OF WORK INCLUDED:
Begin work 1'-0" AFF in cub of five (5) buildings and install five (5) wet pipe automatic fire sprinklers systems in building I and one (1) system in buildings
2-5.
Price does not comply with fire protection plans of specifications or metal building manufacturer's hanger requirements and is based on 8" steel purlins.
Systems will be designed, fabricated and installed per NFPA 13. All materials including pipe will be per NFPA 13. All pipes will be supported Rom the sides
of purlins. Trapeze hangers are not included. Price does not include in -rack sprinklers, hose stations (see alternate) or sprinklers inside or below exterior
canopies. Per City Sanford, signs prohibiting storage must be posted at the loading dock where canopies will be concocted.
Price does not comply with insurer's requirements and is subject to change after confirming the composition of any stored commodities and any requirements
the owner's insurer may have pertaining to the design of the fire protection systems.
All mains will be installed tight against the bottom of beams running north to south.
High Volume low Speed (HVLS) fens should be wired to be shut down in the event of a fire/flow switch activation.
Price is subject to change after review of the project schedule and discussing manpower expectations.
All systems in building 1 will be limited to 40,000 square feet.
Price for building 1 Includes a Ore pump,
Mclarifications
are as follows.
u protection of class 3 commodities stored on double row pallet racks, nomencapsulated, with minimum 8'-O" aisles to a maximum of twenty
feet. Price includes five (5) systems.
Four (4) systems will be designed as ESFR systems designed to include 12 K16.8 sprinklers operating at 52 PSI and One system (vacant space -SW comer)
utilizing standard storage sprinklers to protect a class 3 commodity also on double row racks to a maximum height of TWENTY (20) feet.
Proposal includes a fug pump and the necessary underground for a free standing yard -type rim department connection.
Jatno work: 313,652.00
Under un :
Total (Building 1): S325,066.00
Buildings 2-5:
Systems will be designed per NFPA 13 -light hazard. Depending on future tenants, light hazard may not be adequate and upgrades will be required (not
included). Buildings will be protected as "shells" with upright sprinklers installed at the root Seller reserves the right to utilize extended coverage sprinklers.
Building 2:$22.777.00
Building 3:$22,190.00
Building 4: 522,777.00
Building s: 522,190.00
Additional clarifications, exclusions are noted below and throughout proposal.
NOTE: Attachments referenced by project name and WFS proposal 0 and dated shall be Incorporated completely as If written berein.
Prouosed Schedule: TBD
Wiginton Fire Systems
699 Aero Lane, Sanford, FL 32771 - Phone: (407) 585-3200- Fax: (407) 585-3277
TO: City of Sanford
300 North Park Avenue
Sanford, FL 32771
Attn: Building Department
Re: Letter of Authorization for Permit
Ladies/Gentlemen:
Please accept this letter as my authorizationfor 1k ss o s to
represent me (Charles Patrick) in my absence, to eliver, sign for and pick-up
approved drawings for our permits.
Sincerely,
WIGINT IR TEMS
BY:
Nginton Fire Systems Vice President, Branch Manager
Charles Patrick
License Number: FPC15-000105
State of: Florida
County of: Seminole
The foregoing instrument was acknowledged this -day of /, f , 2017,
by Charles Patrick, who personally appeared before me and ackno edged that
he, signed the instrument voluntarily for the purposes expressed in it.
t5 Personally Known
o Produced Identification
JOANE L. SUAREZ
awXavl J,
t
Nobry Poetic Stine of FloorldsI . LC ' • Canmlttlon I, FF 92558060
NOTA -AY PUBLIC, STATE OF ORIDA ;•, tinugh °
IationamN2tary2, ssn
Additional Full Service Locations
Jacksonville, FL (904) 262-6107 - Daytona Beach, FL (386) 257.4300 - Miami, FL (305) 625-0004 - Tampa. FL (8 13) 623-2333
yWigintonFireS stems
699 Aero Lane, Sanford, FL 32771 - Phone, (407) 585-3200 - Fax* (407) 585-3277
LETTER OF TRANSMITTAL
TO: City of Sanford
300 North Park Avenue
Sanford, FL 32771
We are sending you the following items:
o Fire Sprinkler Permit Package
Date: May 23, 2017
Job#: 2010771
Attn: Plan Review
Re: Ganesh North — Bldg. 1
OH
COPIES NO. DESCRIPTION
1 31159 Check for deposit on permit fee $25.00
3 Signed and Sealed Plans, Submittals, and Calcs
1 Permit Application
1 Certificate of Insurance
1 Certificate of Competency
1 Signed subcontract Agreement with Proposal Price Breakdown
1 Letter of Authorization
Remarks: If you have any questions, please call me at (407) 585-3252, or email
at kasa-wiginton.net.
Cc: Contract File Signed
Thank You,
Kelli SessioAs
Operations Administrative
Assistant
Wayne Ammons, Designer
Additional Full Service Locations
Jacksonville, FL (904) 262-6107 - Daytona Beach, FL (386) 2574300 - Miami. FL (305) 625.0004 - Tampa. FL (813) 623-2333
FIRE INSPECTIONS CITY OF SANFORD
407.562.2786 BUILDING & FIRE PREVENTION
BUILDING INSPECTIONS 300 N PARK AVE
855.541.2112 SANFORD FL 32771
DRIVEWAYS -SIDEWALK 407.688.5080
Page 2
Application Number . . . . . 17-00000230 Date 5/23/17
Application pin number . . . 713890
Revision number . . . . . . . 3
Special Notes and Comments
No new plumbing fixtures per plans.
no additional impact fees
March 29, 2017 11:25:05 AM blaker.
additional impact fees
Add- water impact fee $4700.50
Add -sewer impact fee 10,587.50
Other Fees . . . . . . . . . 01-APPLCTN FEE -ELECTRIC 25.00
01-APPLCTN FEE -BUILDING 100.00
01-APPLCTN FEE -PLUMBING 25.00
01 -BLDG PLAN REVIEW 21243.00
01 -EARLY START AUTHORIZED 250.00
01 -FIRE SPRINKLER TESTING 150.00
01 -FIRE INSPECT -NEW CONST 8056.00
01 -FIRE IMPACT 8-2015 13297.67
01 -PLAN ALTERATIONS 50.00
01 -POLICE IMPACT 8-2015 16664.60
01 -SEM CNTY RD IMPACT FEE 59607.00
WD IMPACT:COMMERCIAL 8058.00
SD IMPACT:COMMERCIAL 18150.00
01 -BLDG DCA SURCHARGE 1082.12
01 -BLDG DBPR SURCHARGE 1082.09
Fee summary Charged Paid Credited Due
Permit Fee Total 124.00 124.00 .00 00
Other Fee Total 147840.48 147815.48 .00 25.00
Grand Total 147964.48 147939.48 .00 25.00
CITY OF SANFORD
r+t CUSTOMER RECEIPT mr*
Oper: BLANDA Type: OC Drawer: 1
Date: 5/23/17 81 Receipt no: 129M
Year Number Amount
343
NO1%
RD
238
N}
SANFORD, FL 32771
BP BUILDING PERMIT RECEIPTS
25.88
Tender detail
CK CHE(X 31159 $25.88
Total tendered $25.88
Total payment $25.88
frans date: 5/23/17 Time: 18:8:44
FAILURE TO COMPLY WITH MECHANIC'S LEIN LAW CAN RESULT IN THE
PROPERTY OWNER PAYING TWICE FOR BUILDING IMPROVEMENTS.
NOTE: ALL FEES MUST BE PAID PRIOR TO C.O. BEING ISSUED.
NOTE: PLEASE BE ADVISED ALL PERMITS MUST BE INSPECTED.
DATE: '5/ v
CITY OF SANFORD BUILDING AND FIRE PREVENTION DIVISION
PEck CE 17- 10
BUSINESS/PROJECT NAME:
JJ
ADDRESS:
CONTACT NAME:
FIRE PLAN REVIEW SERVICE FEES
PHONE: 407.688.5052
FAX: 407.688.5051
PERMIT NUMBER: /7- Z-30
PHONE:
PLAN REVIEW INFORMATION
CONSTRUCTION [ ]C/O [ ] FIRE ALARM [I/FIRE SPRINKLER []HOOD [ ]PAINT BOOTH [)TANK
DOES 20% REDUCTION IN FIRE IMPACT FEES APPLY: ( ) YES NO
TOTAL FEES:
Revision 6d I rll- City of Sanford
Response to Comments Building & Fire Prevention Division
Ph: 407.688.5150 Fax: 407.688.5152
Email: building@sanfordfl.gov
Permit # 230 Submittal Date -- a-' I -7
Project Address: 3PLcE SIV
r
MAR 2 7 2017Contact: le- lc( ala5
Ph: q-1 — Fax:
Email: \ o Q e ctC . aM
Trades encompassed in revision:
0 Building
Plumbing
Electrical
Mechanical
Life Safety
Waste Water
Department
Utilities
Waste Water
Planning
Engineering
Fire Prevention
11 Building
BY:
General description of revision:
adb N0,,J q.kJJ- ONs
ROUTING INFORMATION
Approvals
i w NAv'i G i
Revision M q/ City of Sanford
Response to Comments Building & Fire Prevention DivisionP9
Ph: 407.688.5150 Fax: 407.688.5152
Email: building@sanfordfl.gov
Permit # 11- 230
Project Address
Contact:
Ph: L(,-,-1 — 333- 1150
Email: 40`2 e Vv,C-J aeC,
Trades encompassed in revision:
0 Building
14 Plumbing
Electrical
Mechanical
Life Safety
Waste Water
Submittal Date 31 O3"1 I -7
ECEIVE'
r
MAR 21 2011
Fax:
General description of revision:
ROUTING INFORMATION
Department Approvals
Utilities
Waste Water
Planning
Engineering
Fire Prevention
Building
k 6,19
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FIRE SYSTEMS
699 Aero Lane, Sanford, FL 32771
TEL: 407-585-3200 FAX: 407-585-3277
www.wigintonfiresystems.com
PERMIT
2010771
Gafte' sh North "
w
WIGINTON FIRE PROTECTION ENGINEERING, INC.
HYDRANT FLOW TEST FORM
Contract No. 2010771
Name & Location: Ganesh North Buildings One - Five, Monroe Road, Sanford, FL 32771
Description of Property:
Authority Having Juristiction: City of Sanford
FLOW TEST DATA
Test No.: 1 By: WFS Time: 9:00 AM Date: 8/2/2016
STATIC
PRESS.
P.S.I.
RESID.
PRESS.
P.S.I.
PITOT
PRESS.
P.S.I.
FLOW
TABLES
C=
HYDRANT
NOZZLE
COEF.
FLOW
OPENING
INCHES
HYDRANT
NO.
BUTT REMARKS
NUMBER
60 50 1,840 0.9 2 2'/i '
o 1 lllola,a no+ ILi
1111[: 9100 MIp1
1 JlE IO I
Mrs
S1 S I RLL
I RMA, 10 .12
ry¢
1.60114Wrr.) R
RA. 1110iW ,
GAUGE CALIBRATION
TRUE STATIC PITOT CHANGE
WEIGHT RESIDUAL GAUGE OBSERV.
P. S. I. GAUGE
TEST DATA CORRECTED
STATIC
PRESS.
P.S.I.
RESID.
PRESS.
P.S.I.
THEOR.
FLOW
C=
ACTUAL ACTUAL
COEF. FLOW
C= G.P.M.
o
I
1
o
ocm
Ce
o 1 lllola,a no+ ILi
1111[: 9100 MIp1
1 JlE IO I
Mrs
SKETCH OF TEST LOCATION
J I r1A4C1$$U$ AVENUE
o
I
1
o
ocm
Ce
o 1 lllola,a no+ ILi
1111[: 9100 MIp1
1 JlE IO I
Mrs
S1 S I RLL
I RMA, 10 .12
ry¢
1.60114Wrr.) R
RA. 1110iW ,
Elevation of Test Hydrant
Page 1 Form W FPE 500
NOTE CONCERNING FIRE PUMP CURVE USED FOR HYDRAULIC CALCULATIONS:
The proposed electric, vertical in-line fire pump being provided for this project will have a rating of 1,250
gpm at 110 psi. Typically, a factory performance test curve is obtained and input into hydraulic
calculations to reflect the true performance capabilities of the fire pump (in lieu of an NFPA rated
curve). A factory performance test curve was not available for the proposed 110 psi rated fire pump,
but a test curve was available for a similar 105 psi rated fire pump.
Both the 110 psi rated fire pump and the 105 psi rated fire pump having almost identical flow
characteristics, an additional 4 psi has been added to each flow point used from the 105 psi factory
performance test curve that is included with these hydraulic calculations.
mmmmmmmmmmm
mm
mm
mmmmmmm
mmmmmmm
mmmmmm
mmmmmmm
mmmmmmm
mmmmmmm
mm
mm
ORDER INFORMATION
Customer: HYDRO TECHNOLOGIES
Serial No: FP-CO145156-01
Job: 314258
TEST INFORMATION
Positive Pressure Test
Venturi Meter: 8"
Venturi Constant: 192.78
Discharge Dia: 8.00
Suction Dia: 8.00
Discharge Guage Elev.(Zd): 0.00
Suction Guage Elev. (Zs): 0.00
Pressure Ga: 30OPS1
Panel No.: I
WaterTemp
Test Data
No' Pd (PSI) Ps (PSI). kW NI ' h("H20
I, 140.00 16.20 35.20 1,792.00 0.00
2 _ 134_00_ 16.00 64.40 1,788.001 11.00
3 128.00 15.40_ 73.00 1,785.00 27.00
43.004121.00 14.60 79_20 1,784.00
5, 115.00 14.20 83.00 1,784.00 55.00
6. 109.00 13.80 85.40 1,784.00 66.00
7 88.00 12.8_0 89.40_1,778.00 95.0_0
8 83.00 12.60 90.00 1,778.00 100.00
Continents:
UUFM RATING IOOHP
PA'T'TERSON PUMP COMPANY
PUMP DATA
Pump Size & Type:8X8X 18VIPDI
impeller Pattern: D05-104403
Impeller Diameter: 16.375
Vane Tips: .875
Stages: I
TEST DRIVER INFORMATION_.
HP: 100 -
RPM: 1775
Manufacturer: WEG
Serial No.: 1030691230
Volts: 460
Amps: 118
S.F.: 1.15
Eff.(.00): 0.941
Calenlatorl rlar.,
RATING (Design)
GPM. I:5O'
FTHD:2 t3 . IoS-ZZ f%1
RPM (N2); 1780 (-F N Psi)
SECONDARY RATINGS
GPM: 1,875.00, 0.00
FT HD: 157.95, 0.00
Data Collected by: L J
Test Date: Feb -26-2016
Test No.: I
1 Q 1 (GPM)
0.00_1
H I (FT)
285_98
whp i ehp
0.00 47.18_
bhp I i npump
44.401 0.00
639.381
1 1,001.71
272.58
260_11
44.01 86.33
65.801 97.86
81.231 54.18-
92.081 71.45
264.14 245.78 78.46 106.17 99.90 , 78.54
1,429.69
L 1,566.15
232.85
219.91 I
173.7 I
162.62
84.07 _ 111.26
86.97 114.48
104.70 _ 80.3_0
107.72 i 80.74
112.771 _ 73.09 I
1 13.531 69.74
1,878.991
1,927.801
82.42' 119.84
79.17 I 120.64
Calculated Data at Rated Speed
Q2 (GPM) I H2 (FT) bhp2
0,0.9
636.52
F.16 (%%.103.52
270.1-5270.151 80.15
P
r e' .GS /IZ,o091.31 1
ftN1.
8I.I0,
4jD5.-%;99.23
k=V903.99
I 3 9/ e07.00
I 7S V 13.15
j 1,929.971 162.99 113.91
NSIONS IN () ARE FOR PRIMARY
N hM=
Ml PATTERSON PUMP COMPANY
A SUBSIDIARY OF THE GORMAN-RUPP COMPANY
TITLE
DRAWING NUMBER REV
UUFM NAMEPLATE E-15085 6
IN-LINE PUMPS) PATTERN NUMBER
SHEET OF SCALE PART NUMBER
1 1 1:1 23007607DRAWNCHECKEDAPPROVEDGATE
CHILOS AP AP SEP. 27,199%"
5NSIONS ARE IN INCHES AND SECONDARY DIMENSIONS, SHOWN IN ( ], ARE IN MILLIMETER:
e
cl&us
LISTED ® M
ago A SUBSIDIARY OF THE GORMAN-RUPP CO. APPROVED
TOCCOA,GEORGIA
CENTRIFUGAL FIRE PUMP IN-LINE
SIZE -TYPE NO. STGS. SERIAL NO. •
8X8X18VIPD1 FP -C0145156
MAX.B.H.P. 113.9 MAX. SUCT. 178 P.S.I.
1.50 CAP.
G.P.M. R.P.M. PSIG MAX. PSIG PSIG IMP. DIA.
1250 1780 105 122 761 16.375
THIS DOCUMENT CONTAINS DESIGNS AND OTHER PRIMARYINFORMATIONWHICHARETHECONFIDENTIALPROPERTYTOLERANCES
OF PATTERSON PUMP COMPANY. THE RECIPIENT EXCEPTAs NOTE01
ACKNOWLEDGES THAT THIS IS FURNISHED FOR ITS 2 PLC DEC. t.03" PRIVATE USE AND UPON THE EXPRESS AGREEMENT THAT
IT WILL NOT REPRODUCE. COPY, EXHIBIT OR LEND IT IN 3 PLC DEC. t.005"
WHOLE OR IN PART FOR ANY PURPOSE WHAT SO EVER
WITHOUT THE PRIOR WRITTEN CONSENT OF PATTERSON ANGULAR t 1"
PUMP COMPANY.
TORCH C UT t.06"
MACHNIST NOTE:
BREAK ALL SHARP OORNERSTO A.02 X V CHAMFER FABRICATIONtcATtoNUPTos^ t.06"
REV ECR DATE e' 6" TO 24" t.12"
NSIONS IN () ARE FOR PRIMARY
N hM=
Ml PATTERSON PUMP COMPANY
A SUBSIDIARY OF THE GORMAN-RUPP COMPANY
TITLE
DRAWING NUMBER REV
UUFM NAMEPLATE E-15085 6
IN-LINE PUMPS) PATTERN NUMBER
SHEET OF SCALE PART NUMBER
1 1 1:1 23007607DRAWNCHECKEDAPPROVEDGATE
CHILOS AP AP SEP. 27,199%"
5NSIONS ARE IN INCHES AND SECONDARY DIMENSIONS, SHOWN IN ( ], ARE IN MILLIMETER:
e
cl&us
LISTED ® M
ago A SUBSIDIARY OF THE GORMAN-RUPP CO. APPROVED
TOCCOA,GEORGIA
CENTRIFUGAL FIRE PUMP IN-LINE
SIZE -TYPE NO. STGS. SERIAL NO. •
8X8X18VIPD1 FP -C0145156
MAX.B.H.P. 113.9 MAX. SUCT. 178 P.S.I.
1.50 CAP.
G.P.M. R.P.M. PSIG MAX. PSIG PSIG IMP. DIA.
1250 1780 105 122 761 16.375
A Subsidlary of The Gomuw-Rupp Company
HYDROSTATIC PRESSURE TEST REPORT
Serial Number P?(b1y5l!1(,
Pump Model
Test Pressure (Psi) V66
Test Duration (MIN.) 1(;
Test Liquid Water, Temperature ranging from 50 t0 70 degrees F
Test Facility L`Y Small Pump Assy Gauge S/N
Large Pump Assy Gauge S/N
Other Gauge S/N
Test Results L'7 PASS FAIL
COMMENTS:
Tested By: `
Witnessed By:
f
Date: 'L'-'- h -- ( E
N/A
0
400
f-
39,
W
U- 3C
0
a
25
J
0 20
15
10
51
l
20(
U-1
0 15C
w
100
0
Y 50
a
m 0
PATTERSON PUMP COMPANY
A Subsidiary of the Gorman -Rupp Camvany
P. 0. Box 790
Toccoo, Georaia 30577
Telephone 706-886-2101
Fox 706-886-0023
o
14
1" DIA.
I
I I 1 780 RPMq125075
wv- "U, ovi,yunNS. com
GPM PSI to 137 PSI
173' to 317')
I MODEL 8x8x18A VIP
IMP. D05-104403
i CURVE A05-116622
F
DIA.
I
I
82- 5-
83.5%
1
U- I
120
z
18"
40
o
DIA. I
14.'i_QIA_
N P H_
I j
I -
I I
j
400 Ann
r- %J 4 v LOUD GPM
UNIT PPC ORDER No.
JOB CUSTOMER PO No.
Ganesh North
b PUMP -NOW -18102— CAPACITY ilk6010 G.P.M. @92 FT. FT. HD.
MOTOR ODP MANE Weg FRA*S JPV
125 H,P_ 3 PHASE60 CYCLL'60 VdL7$0
John M. Bolin
R.P.M.
t CERTIFIED BY: ger DATE12114/16
UNIT DIMENSIONS
MOTOR
FRAME
C D BG UNIT
WEIGHT
286 JPV 7B1
1 T
348
1:91ft
4
120 Lo
545 KGS
324 JPV 813 151/8 20 7/16131
509.5
SWOWS
384
326 JPV ala
851
151/8
3w-—Wy--0-TO
2013/16 1385 LBS
GS
364 JPV 351/489T.T 177/8 2111116L 8 BS6B5KGS
365 JPV 351/4899-3
17718
77-
2111/16
551
1538 LBS
700 GS
404 JPV 38112
978
177/8
454
235116 1730 LBS
786 NGS92
405 JPV 3181/2978
17718
454
235fflk 185
592
6
3 KG 1113116
405 TCZ 38112 17 7/8 / 6 1890 LBS
300.6
878 054 592 659 KGS
UNIT WEIGHi PUMP AND MOTOR COMBINED. " '"
L
010254.0
S-
Q2 BLAS fF
08 1263.2 SUCTION
013 1/2 / 343 FLANGE
8x 07/8122.2 BOLT HOLES
EO. SP. ON A 011314 / 298.5 B.C.
B.C. STRADDLES 4i
1/4.10 UNC X 1' DI
BOLT HOLES
021b 9 B.C.
D
MOUNTING FOOT DETAILA,
3/4' NPT
c
NOTE:
1) ALL DIMENSIONS ARE N• 1/4'/ 6.4mm (EXCEPT FOR FLANGE DRILLING). 2) PRIMARY DIMENSIONS ARE INCHES.
SECONDARY DIMENSIONS ARE MILLIMETERS.
ROTATION
3/4' NPT
ttt
U 081203.2 DISCHARGE
0151381 FLANGE
8x 07/8 / 22.2 BOLT HOLES
EO. SP. ON A 011 3/44.298.5 B.C.
PLAN VIEW B.C. STRADDLES fL
CLEARANCE RECOMMENDED
TO REMOVE ROTATING ASSY.
5' 150# ANSI FLANGE DIMENSIONS
SEE MOUNTING FOOT DETAIL)
OUTLINE DIMENSIONS LCO2-118338
1Y
BURROW FOR oxA r., DATE
PATTERSON PUMP COMPANY 8 X 8 X 18 VIP mcaudell NOV. 24, 2010ACAIWAIAWIDWAIN
Sc4F AiFAYpW/ VARIOUS MOTORS NONE AP
i
PjagoM L oin
FIRE SYSTEMS
Wiginton Fire Systems
699 Aero Lane
Sanford, FL 32771
407-585-3200
Job Name 2010771 - B1S1RA1'
Drawing FP2/FP3
Location BUILDING ONE
Remote Area B1S1RA1
Contract 2010771
Data File 2010771 - B1S1RA1.WXF
Computer Programs by Hydratec Inc. Revision: 50.52.1
Wiginton Fire Systems
2010771-61 S1RA1
Page 1
Date 5-19-17
Project name: GANESH NORTH
Location: BUILDING ONE
Drawing no: FP2/FP3
Date: 5-19-17
Design
HYDRAULIC CALCULATIONS
for
Remote area number: B1S1RA1
Remote area location: SYSTEM ONE
Occupancy classification: HIGH PILED STORAGE
Density: 52 PSI - Gpm/SgFt
Area of application: 12 HEADS - Sq Ft
Coverage per sprinkler. 100 MAX - SgFt
Type of sprinklers calculated: 16.8K ESFR PENDENT
No. of sprinklers calculated. 12
In -rack demand: N/A - GPM
Hose streams: 250 - GPM
Total water required (including hose streams): 1709.991 - GPM @ 32.419 - Psi
Type of system: WET
Volume of '&Y or preaction system? N/A - Gal '
Water supply information
Date: 8-2-16
Location: ALONG W. 1ST STREET
Source: WFS
Name of contractor. WIGINTON FIRE SYSTEMS
Address: 699 AERO LANE, SANFORD, FL 32771
Phone number: 407-585-3200
Name of designer: W. AMMONS
Authority having jurisdiction: CITY OF SANFORD
Notes: (Include peaking information or gridded systems here.)
Computer Programs by Hydratec Inc. Revision: 50.52.1
Water ply Curve C
Wiginton Fire Systems Page 2
2010771 - 131 S1 RA1 Date 5-19-17
City Water Supply:
C1 - Static Pressure 60
C2 - Residual Pressure: 50
C2 - Residual Flow : 1840
City Water Adjusted to Pump Inlet
for Pf - Elev - Hose Flow
P2 - Pump Rated Flow
Al - Adjusted Static: 54.436
A2 - Adj Resid 33.185 @ 1261.31
A3 - Adj Resid 10.52 @ 1881.1
210
196
182
p 168
R 154
E 140
S 126
S 112
U 98
R 84
E 70
56
42
28
14
Al +1121
1
Pump Data:
P1 - Pump Churn Pressure 126.18
P2 - Pump Rated Pressure 109.95
P2 - Pump Rated Flow 1261.31
P3 - Pump Pressure @ Max Flow 79.39
P3 - Pump Max Flow 1881.1
City Residual Flow @ 0 4846.63
City Residual Flow @ 20 3892.4
City Water @ 150% of Pump 49.58
A2+P2
D2
LUU 41JU bUU 8UU 1000 1200 1400 1600
FLOW N^1.85)
Computer Programs by Hydratec Inc. Revision: 50.52.1
Demand:
01 - Elevation 14.890
D2 - System Flow 1459.99
D2 - System Pressure 110.647
Hose ( Demand)
D3 - System Demand 1459.99
Hose ( Adj City) 250
Safety Margin 18.849
1800
Flow D' -3m
Wiginton Fire Systems
2010771 - 61 S 1 RA1
Page 3
Date 5-19-17
122.7244.5 488.7 793.8 897.7 981.6 1053.5 11223 1196.2 1282.2 1385 1460 1460 1460H3 +-H4 +-100+-101+-103t-105+-107+-109+- III +-113+-115+-117+-119+-121+-123E-125+-127+-129+-131+-133+-135+-137+-139+-141+-143-TR1+-BR1+-PO244.5 244.5 732 848.8 941.7 1018.5 1087.7 1158.1 1237.4 1331.3 1460 1460 1460
1460 1710 1710
PI +- SPIG- UG3+- UG4+- UG5+- UG6e- TEST
1460 1710 1710
1.5 241.7 241.7 728 611.2 518.3 441.5 372.2 301.9 222.6 128.7 75 75
H3 - H2 +- H1 +- 200 +- 201 +- 203 +- 205 +- 207 +- 209 +- 211 +- 213 +- 215 +- 217 +- 219 +- 221 +- 223 +- 225 +- 227 +- 229 i- 231 +- 233 +- 235 +- 237 +- 236 +- 136 +- 137
1198 241.7 484 666.2 562.3 478.4 406.5 337.7 263.8 177.8 75 75
242.2 120.2 122.4 244.2
203 - 202 - H5 -+ H6 H7 +- H8 +- 102 +- 103
1 2422 1.2 244.2 1
1 484 1 488.7
1 244 121.8 121.3 24:13
205 • 204 . H9 - HIO-rH11 H12+- 104 +- 105
1 244 0.2 243.3
1 728
1 61.8 61.8
207 +- 206 +- 106 +- 107
1 61.8 1
1 666.2 1 793.8
1 54.9 54.0
209 +- 208 +- 108 +- 109
1 54.9 1
1 611.2 1 848.8
1 49 491
211+- 210+- 1104- 111
1 49 1
1 562.3 1 897.7
1 43.9 43.0
213+- 212+- 1124- 113
T 43.9 1
1 518.3 1 941.7
1 399 39.0
215+- 214+- 114+- 115
T 39.9 1
1 478.4 1 981.6
1 36.9 36.0
217+- 216+- 116+- 117
T 36.9 1
1 441.5 1 1018.5
1 35 351
219 +- 218 +- 118 +- 119
1 35 1
1 406.5 1 1053.5
1 34.2 34.g
221 +- 220 +- 120+- 121
t 342 1
1 372.2 1 1087.7
1 34.5 34.0
223+- 222 +- 122 +- 123
1 34.5 1
1 337.7 1 1122.3
1 35.9 35.0
225 +- 224 +- 124 +- 125
1 35.9 1
1 301.9 1 11581
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow U 3m
Wiginton Fire Systems
2010771 - B1S1RA1
1 38.1 38.1
227 F- 226 +-126 . 127
T 38.1 T
1 263.8 1 1196.2
1 41.1 41.1
229 228 4-128 <- 129
1 41.1 j
1 222.6 1 1237.4
1 44.8 44 f
231 i 230 +- 130 . 131
1 44.8 1
1 177.8 1 1282.2
1 49.1 49.1
233 <- 232 t 132 e- 133
1 49.1 1
1 128.7 1 1331.3
1 53.7 SIT
235 234 +- 134 t 135
53.7
Computer Programs by Hydratec Inc. Revision: 50.52.1
Page 4
Date 5-19-17
Fittings -d Summary
Wiginton Fire Systems Page 5
2010771 - 61 S1RA1
Date 5-19-17
Fitting Legend
Abbrev. Name '/2 '/. 1 1'% 1 %: 2 2%: 3 3'/2 4 5 6 8 10 12 14 16 18 20 24
B Generic Butterfly Valve 0 0 0 0 0 0 7 10 0 12 9 10 12 19 21 0 0 0 0 0E90' Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61GGenericGateValve00000111122345678101113LLongTurnElbow1122234556891316182427303440SGenericSwingCheckValve4557911141619222732455565768798109130T90' Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121V90'Ell Firelock #001 0 0 0 0. 0 3.5 4.3 5 0 6.8 8.5 10 13 0 0 0 0 0 0 0X90'Tee-BranchFirelock002 0 0 0 0 0 8.5 10.8 13 0 16 _ 21 25 33 0 0 0 0 0 0 0ZafAmes3000SSFittinggeneratesaFixedLossBasedonFlow
Units Summary
Diameter Units Inches
Length Units Feet
Flow Units US Gallons per Minute
Pressure Units Pounds per Square Inch
Computer Programs by Hydratec Inc. Revision: 50.52.1
Pressure / Flow Summary - STANDARD
Wiginton Fire Systems Page 6
2010771 - B1S1RA1 Date 5-19-17
lode Elevation K -Fact Pt Pn Flow Density Area Press
No. Actual Actual Req, _
H3 36.38 16.8 52.0 na 121.15 0.1 100 52.0
H4 35.97 16.8 52.55 na 121.78 0.1 100 52.0
100 32.08 70.23 na
101 29.37 74.25 na
103 29.37 74.26 na
105 29.37 74.32 na
107 29.37 74.45 na
109 29.37 74.6. na
111 29.37 74.77 na
113 29.37 74.96 na
115 29.37 75.16 na
117 29.37 75.38 na
119 29.37 75.62 na
121 29.37 75.87 na
123 29.37 76.14 na
125 29.37 76.42 na
127 29.37 76.72 na
129 29.37 77.04 na
131 29.37 77.37 na
133 29.37 77.74 na
135 29.37 78.12 na
137 29.54 79.96 na
139 -,,29.55 88.25 na
141 29.55 89.88 na
143 29.55 92.31 na
TR1 29.55 93.29 na
BRI 2.0 109.57 na
PO 2.0 110.65 na
PI 2.0 26.46 na
PIG -3.0 29.35 na
G3 -3.0 32.65 na 250.0
UG4 -3.0 43.32 na
UG5 -3.0 48.44 na
UG6 -3.0 52.23 na
TEST 2.0 51.27 na
H2 36.03 16.8 52.15 na 121.32 0.1 100 52.0
H1 35.62 16.8 52.68 na 121.94 0.1 100 52.0
200 32.09 66.13 na
201 29.38 70.09 na
203 29.38 70.2 na
205 29.38 70.61 na
207 29.38 71.47 na
209 29.38 72.21 na
211 29.38 72.83 na
213 29.38 73.37 na
215 29.38 73.83 na
217 29.38 74.23 na
219 29.38 74.57 na
221 29.38 74.87 na
223• 29.38 75.12 na
225 29.38 75.33 na
227 29.38 75.5 na
229 29.38 75.63 na
231 29.38 75.73 na
233 29.38 75.79 na
235 29.38 75.83 na
237 29.38 75.84 na
236 32.09 74.98 na
136 32.25 78.47 na
202 32.09 66.24 na
H5 35.62 16.8 52.74 na 122.01 0.1 100 52.0
H6 36.03 16.8 52.2 na 121.39 0.1 100 52.0
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow Summary - Standard
Wiginton Fire Systems Page 7
2010771 - B1S1RA1 Date 5-19-17
Node Elevation K -Fact Pt Pn Flow Density Area Press
No. - - - Actual Actual Req..
H7 36.38 16.8 52.05 na 121.21 0.1 100 52.0
H8 35.97 16.8 52.6 na 121.84 0.1 100 52.010232.08 70.26 na
204 32.09 66.6 na
H9 35.62 16.8 52.94 na 122.24 0.1 100 52.0H1036.03 16.8 52.4 na 121.61 0.1 100 52.0H1136.38 16.8 52.25 na 121.44 0.1 100 52.0
H12 35.97 16.8 52.79 na 122.06 0.1 100 52.010432.08 70.34 na
206 32.09 70.52 na
106 32.08 73.06 na
208 32.09 71.21 na
108 32.08 73.25 na
210 32.09 71.81 na
110 32.08 73.45 na
212 32.09 72.32 na
112 32.08 73.67 na
214 32.09 72.76 na
114 32.08 73.89 na
216 32.09 73.14 na
116 32.08 74.12 na
218 32.09 73.48 na
118 32.08 74.37 na d
220 32.09 73.77 na
120 32.08 74.62 na
222 32.09 74.02 na
122 32.08 74.89 na
224 32.09 74.24 na
124 32.08 75.16 na
226 32.09 74.42 na
126 32.08 75.45 na
228 32.09 74.56 na
128 32.08 75.76 na
230 32.09 74.68 na
130 32.08 76.08 na
232 32.09 74.76 na
132 32.08 76.42 na
234 32.09 74.82 na
134 32.08 76.78 na
The maximum velocity is 16.05 and it occurs in the pipe between nodes 205 and 207
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 8
2010771 - B1S1RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
EQUIVALENT K'S
REMOTE HEAD TO SUPPLY
H3 122.68 2.703 0.0 10.000 52.000 K Factor = 16.80
to
6.385
120.0 0.0 0.0 0.178
0.0
120.0
H4 122.68 0.0371 0.0 10.000 0.371 Vel = 6.86
H4 121.78 2.703 X 16.786 103.540 52.549 K Factor = 16.80
to 120.0 0.0 16.786 1.685
119 1018.5
100 244.46 0.1330 0.0 120.326 16.000 Vel = 13.67
100 0.0 2.703 T 18.651 2.710 70.234
8.330 76.136
to 120.0 0.0 18.651 1.174
0.0 0.0
101 244.46 0.1330 0.0 21.361 2.840 Vel = 13.67
101 0.0 6.385 0.0 8.330 74.248
8.330 76.418
to 120.0 0.0 0.0 0.0
0.0 0.0
103 244.46 0.0019 0.0 8.330 0.016 _ Vel =
0.299
103 2.44.22 6.385 I'd 0.0 8.330,;,- 74.264
to 120.0 0.0 0.0 0.0
1_05_ 488.68 0.007 - 0073 0.0 8.330_ 0.061 __ Vel = 4.90
105 243.32 6.385 0.0 8.330 74.325
to 120.0 0.0 0.0 0.0
107 732.0_ 0.0154 0.0 8.330 0.128 _ Vel =_ 7.3_3
107 61.83 6.385 0.0 8.330 74.453
to 120.0 0.0 0.0 0.0
109 793.83 0.0179 0.0 8.330 0.149 Vel = 7.95
109 54.92 6.385 0.0 8.330 74.602
to 120.0 0.0 0.0 0.0
Ili--- 848.7.5 0.0202_ 0.0 _ 8.330 0.168 _--_- Vel = 8.50
111 48.96 6.385 0.0 8.330 74.770
to 120.0 0.0 0.0 0.0
113 897.71 0.0224 0.0 8.330 0.187 Vel = 9.00
113
to
115
43.94
941.65
6.385
120.0
0.0246
0.0
0.0
0.0
8.330
0.0
8.330
74.957
0.0
0.205 Vel = 9.44
115 39.92 6.385 0.0 8.330 75.162
to
0.0
120.0 0.0 0.0 0.0
117 981.57 0.0264 0.0 8.330 0.220 Vel = 9.84
117 36.93 6.385 0.0 8.330 75.382 •
to 120.0 0.0 0.0 0.0
119 1018.5 0.0283 0.0 8.330 0.236 Vel = 10.21
119 35.02 6.385 0.0 8.330 75.618
to 120.0 0.0 0.0 0.0
12_1_ _- 10.53.52 0.03_01 - 0.0 8.330 0.251 Vel = 10.56
121 34.22 6.385 0.0 8.330 75.869
to 120.0 0.0 0.0 0.0
123 1087.74 0.0321 0.0 8.330 0.267 Vel = 10.90
123 34.53 6.385 0.0 8.330 76.136
to 120.0 0.0 0.0 0.0
125 11.22.27 0.0339 _ 0.0 8.330 0.282 Vel = 11.25
125 35.85 6.385 0.0 8.330 76.418
to 120.0 0.0 0.0 0.0
127 1158.12 0.0359 0.0 8.330 0.299 Vel = 11.60
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems
2010771 - B1S1RA1
Page 9
Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. C" or Ftng's Pe Pv ""'••` Notes ""'•
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
127 38.11 6.385
18.849
0.0 8.330 76.717 - -
to
Pressure @ Pump Inlet _ _
120.0
PI 0.0 8.249
0.0 0.0 0.0
SPIG 1459.99 0.0158 0.0 45.871 0.726 Vel = 8.76
129 1196.23 0.0382
77.87
0.0 8.330 0.318 Vel = 11.99
129 41.15 6.385 0.0 8.330 77.035
to 120.0 0.0 0.0 0.0
131 1237.38 0.0406 0.0 8.330 0.338 Vel = 12.40
131 44.84 6.385 0.0 8.330 77.373
to 120.0 0.0 0.0 0.0
133 1282.22 0.0435 0.0 8.330 0.362 Vel = 12.85
133 49.07 6.385 0.0 8.330 77.735
to 120.0 0.0 0.0 0.0
135 1331.29 0.0465 0.0 8.330 0.387 Vel = 13.34
135 53.70 6.385 2V 25.691 12.510 78.122
to 120.0 0.0 25.691 0.074
137 1384.99 0.0500 _ L 0.0 38.201 1.911_ Vel = 13.88
137 75.00 6.385
Y
V 12.845 137.500 79.959
to 120.0 0.0 12.845 0.004
139 _ 1459.99 0.0_55_2 0.0 150.345 8.292 _ Vel = 14.63
139 0.0 6.385 V 12.845 16.670 88.247
to 120.0 0.0 12.845 0.0
141 1459.99 0.0552 0.0 29.515 1.628 Vel = 14.63
141 0.0 6.385 V 12.845 31.250 89.875
to 120.0 0.0 12.845 0.0
143 1459.99 0.0552 0.0 44.095 2.432 Vel = 14.63
143 0.0 6.385 V 12.845 4.958 92.307
to 120.0 0.0 12.845 0.0
TR1 1459.99 0.0552 0.0 17.803 0.982 Vel = 14.63
TR1 0.0 6.385 T 38.536 27.500 93.289
to 120.0 B 12.845 51.381 11.932
BR1 1459.99 0.0551 0.0 78.881 4.350 Vel = 14.63
BR1 0.0 8.249 B 13.345 4.500 109.571
to 120.0 S 50.044 63.389 0.0
PO 1459.99 0.0158 0.0 67.889 1.076 Vel = 8.76
0.0
1459.99 110.647 K Factor = 138.80
System Demand Pressure 110.647
Safety Margin 18.849
Continuation Pressure 129.496
Pressure @ Pump Outlet 129.496
Pressure From Pump Curve 103.040
Pressure @ Pump Inlet _ _ 26.456
PI 0.0 8.249 T 38.923 2.500 26.456
to 120.0 G 4.448 43.371 2.166
SPIG 1459.99 0.0158 0.0 45.871 0.726 Vel = 8.76
SPIG 0.0 8.27
to T140.0
UG3 1459.99 0.0118
UG3 250.00 8.27
to
52.413
140.0
UG4 1709.99 0.0158
E 26.955 195.000 29.348
T 52.413 85.358 0.0
G 5.99 280.358 3.299
T 52.413 300.000 32.647
Zaf 0.0 130.283 3.893
4L 77.87 430.283 6.782
Computer Programs by Hydratec Inc. Revision: 50.52.1
Vel = 8.72
Qa = 250
Fixed Loss = 3.893
Vel = 10.21
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 10
2010771 - B1 S1RA1 Date 5-19-17
Hyd. Oa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv '""'"" Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
UG4 0.0 10.28 T 71.092 865.000 43.322
to 140.0 0.0 71.092 0.0
UG5 1709.99 0.0055 0.0 936.092 5.114 Vel = 6.61
UG5 0.0 12.34 T 88.164 1600.000 48.436
to
H3
140.0 0.0 88.164 0.0
UG6 1709.99 0.0022 0.0 1688.164 3.789 Vel = 4.59
UG6 0.0 12.34 T 88.164 450.000 52.225
to
0.0 _
140.0 0.0 88.164 2.166
TEST 1709.99 0.0022 0.0 538.164 1.208 Vel = 4.59
52.152
0.0
to 120.0 0.0 0.0
1709.99
H1 ___
51.267 K Factor = 238.82
NEW PATH
H3 1.53 2.703 0.0 10.000 52.000
to 120.0 0.0 0.0 0.152
d H2 1.53 0.0 _ Q.0 10.000 1.0.0 Vel = 0.09
H2 121.32 2.703 0.0 10.000 52.152 K Factor = 16.80
to 120.0 0.0 0.0 0.178
H1 ___ 119.79 0.0354 _ 0.0 _ 10.000 0.354 _ Vel = 6.70_
H1 121.94 2.703 X 16.786 74.740 52.684 K Factor = 16.80
to 120.0 0.0 16.786 1.529
200 241.73 0.1302 0.0 91.526 11.920 Vel = 13.52
200 0.0 2.703 T 18.651 2.710 66.133
to 120.0 0.0 18.651 1.174
201 _ 241.73 0.1302 _ 0.0 _ _ 21.361 2.782 _ Vel_ = 13.52__
201 0.0 4.304 0.0 8.330 70.089
to 120.0 0.0 0.0 0.0
203 241.73 0.0134 0.0 8.330 0.112 Vel = 5.33
203 242.23 4.304 0.0 8.330 70.201
to 120.0 0.0 0.0 0.0
205 483.96 0.0489 0.0 8.330 0.407 Vel = 10.67
205 244.03 4.304 0.0 8.330 70.608
to 120.0 0.0 0.0 0.0
207 727.99 0.1040 0.0 8.330 0.866 Vel = 16.05
207 61.83 4.304 0.0 8.330 71.474
to 120.0 0.0 0.0 0.0
209 666.16 0.0881 0.0 8.330 0.734 Vel = 14.69
209 54.92 4.304 0.0 8.330 72.208
to 120.0 0.0 0.0 0.0
211 611.24 0.0752 0.0 8.330 0.626 Vel = 13.48
211 48.96 4.304 0.0 8.330 72.834
to 120.0 0.0 0.0 0.0
213_ 562.28 0.0645 0.0 8.330 0.537_ Vel = 12.40
213 43.94 4.304 0.0 8.330 73.371
to 120.0 0.0 0.0 0.0
215 518.34 0.0555 0.0 8.330 0.462 Vel = 11.43
215 39.92 4.304 0.0 8.330 73.833
0 120.0 0.0 0.0 0.0
217 478.42 0.0478 0.0 8.330 0.398 Vel = 10.55
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 11
2010771 - B1S1RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
217 -36.93 4.304 0.0 8.330 74.231
to 120.0 0.0 0.0 0.0
219 441.49 0.0412 0.0 8.330 0.343 Vel = 9.74
219 35.02 4.304 0.0 8.330 74.574
to
to
0.0
120.0 0.0 0.0 0.0
0.0149 0.0
221 406.47 0.0354 0.0 8.330 0.295 Vel = 8.96
221 34.22 4.304 0.0 8.330 74.869
137 75.0
to
0.0
120.0 0.0 0.0 0.0
16.786 1.529
223 372.25 0.0300 0.0 8.330 0.250 Vel = 8.21
223 34.53 4.304 0.0 8.330 75.119
to 120.0 0.0 0.0 0.0
225 337.72 0.0251 0.0 8.330 0.209 Vel = 7.45
225 35.85 4.304 0.0 8.330 75.328
to 120.0 0.0 0.0 0.0
227_ 301:87 0.0204 _ 0.0 - 8.330
w:;
0.170 -_ Vel =
227 38.11 4.304 0.0 8.330 75.498
6.66_
to 120.0 0.0 0.0 0.0
229 263.76 0.0158 0.0 8.330 0.132 Vel = 5.82
229 41.15 4.304 0.0 8.330 75.630
to 120.0 0.0 0.0 0.0
231 222.61 0.0116 0.0 8.330 0.097 Vel = 4.91
231 44.84 4.304 0.0 8.330 75.727
to 120.0 0.0 0.0 0.0
233 177.77 0.0076 0.0 8.330 0.063 Vel = 3.92
233 49.07 4.304 0.0 8.330 75.790
to 120.0 0.0 0.0 0.0
235 128.7 0.0043 _ 0.0 8.330_ 0.036 Vel = 2.84
235 53.70 4.304 0.0 8.330 75.826
to 120.0 0.0 0.0 0.0
237 75.0 0.0014 0.0 8.330 0.012 Vel = 1.65
237 0.0 2.703 T 18.651 2.710 75.838
to 120.0 0.0 18.651 1.174
236 75.0 0.0150 0.0 21.361 0.320 Vel = 4.19
236 0.0 2.703 2X 33.571 204.140 74.984
to 120.0 0.0 33.571 0.069
136, 75.0 0.0149 0.0 237.711 3.551 Vel = 4.19
136 0.0 2.703 T - 18.651 2.710 78.466
to
202 -242.23
120.0 0.0 18.651 1.174
137 75.0 0.0149 0.0 21.361 0.319 Vel = 4.19
0.0
75.00 7.9.959_ K_ Factor= 8.39
NEW PATH
203 -242.23 2.703 T 18.651 2.710 70.201
to 120.0 0.0 18.651 1.174
202 -242.23 0.1307 0.0 21.361 2.792 Vel = 13.54
202 0.0 2.703 X 16.786 74.740 66.235
0 120.0 0.0 16.786 1.529
H5 -242.23 0.1307 0.0 91.526 11.965 Vel = 13.54
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 12
2010771 - B1S1RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv •'••"' Notes '•"•'
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
H5 122.01 2.703
X 16.786
0.0 10.000 52.741 K Factor = 16.80
to
0.0
120.0
1.685
0.0 0.0 0.178
0.0
H6 120.22 0.0358
0.0
0.0 10.000 0.358 Vel = 6.72
H6 121.38 2.703
0.0
0.0 10.000 52.205 K Factor = 16.80
to
0.0 _
120.0
2.815 _ - --- Vel = 13.60
0.0 0.0 0.152
0.004
H7 1.16 0.0001
241.881
0.0 10.000 0.001 Vel = 0.06
H7 121.21 2.703 0.0 10.000 52.054 K Factor = 16.80
to 120.0 0.0 0.0 0.178
H8 122.37 0.0369 0.0 10.000 0.369 Vel = 6.84
H8 121.85 2.703 X 16.786 103.540 52.601 K Factor = 16.80
to 120.0 0.0 16.786 1.685
102 244.22 0.1327 O.0 120.326 15.970 Vel = 13.65
102 0.0 2.703 T 18.651 2.710 70.256
to 120.0 0.0 18.651 1.174
103 244.22,,___9.1327 0.0 21.361 _ 2_834 Vel = 13.65
244.22 74.264 K Factor= 28.34
NEW PATH
205 244.03 2.703 T 18.651 2.710 70.608
to 120.0 0.0 18.651 1.174
204 244.03 0.1325 _ 0.0 - 21.361 2.831 Vel = 13.64
204 0.0 2.703 X 16.786 74.740 66.603
to 120.0 0.0 16.786 1.529
244.03 0_.1325_______ 0.0 91.526 12.130 Vel = 3.64
H9 122.24 2.703 0.0 10.000 52.944
1 -
K Facto = 16.80
to 120.0 0.0 0.0 0.178
H10 121.79 0.0366 0.0 10.000 0.366 Vel = 6.81
H10 121.61 2.703 0.0 10.000 52.400 K Factor = 16.80
to 120.0 0.0 0.0 0.152
H11 0.18 0.0 0.0 10.000 0.0 Vel = 0.01
H11 121.44 2.703 0.0 10.000 52.248 K Factor = 16.80
to 120.0 0.0 0.0 0.178
H12 121.26 0.0363 0.0 10.000 0.363 Vel = 6-78
H12 122.06 2.703 X 16.786 103.540 52.789 K Factor = 16.80
to 120.0 0.0 16.786 1.685
104 243.32 0.1318 0.0 120.326 15.862 Vel = 13.60
104 0.0 2.703 T 18.651 2.710 70.336
to
206 61.83
120.0 0.0 18.651 1.174
105 243.32 0.1318 0.0 _ 21.361--_ 2.815 _ - --- Vel = 13.60
0.0
243.32 74.325 K Factor= 28.22
NEW PATH
207 61.83 2.703 T 18.651 2.710 71.474
to 120.0 0.0 18.651 1.174
206 61.83 0.0104 0.0 21.361 0.223 Vel = 3.46
206 0.0 2.703 2X 33.571 208.310 70.523
to 120.0 0.0 33.571 0.004
106 61.83 0.0105 0.0 241.881 2.529 Vel = 3.46
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 13
2010771 - 61 S1 RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv "••••• Notes '••"•
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
106 0.0 2.703 T 18.651 2.710 73.056
to 120.0 0.0 18.651 1.174
107 61.83 0.0104 0.0 21.361 0.223 Vel = 3.46
0.0
61.83 74.453 K Factor= 7.17
NEW PATH
209 54.92 2.703 T 18.651 2.710 72.208
to
to
48.96
120.0 0.0 18.651 1.174
208 54.92 0.0084 0.0 21.361 0.180 Vel = 3.07
208 0.0 2.703 2X 33.571 208.310 71.214
Vel = 2.74
to
0.0
120.0 0.0 33.571 0.004
241.881'
108 54.92 0.0084 0.0 241.881 2.031 Vel = 3.07_
108 0.0 2.703 T 18.651 2.710 73.249
to
0.0
120.0 0.0 18.651 1.174
0109 _ 54.92 0:0084 _ 0,0,,1____.21,361 0,179 Vel,=! 3.07
111
0.0
0.0067 0.0 21.361
54.92 74.602 K Factor = 6.36
NEW PATH
43.94 2.703 T 18.651 2.710 73.371
to
211 48.96 2.703 --- T 18.651 2.710-- 72.834 ----
to
0.0
120.0 0.0 18.651 1.174
2.703
210 48.96 0.0068 0.0 21.361 0.146 Vel = 2.74
210 0.0 2.703 2X 33.571 208.310 71.806
241.881'
to
112
120.0 0.0 33.571 0.004
73.665
110 _ 48.96 0.0068 _ _ 0.0 241.881 1.642 Vel = 2_._74
110 0.0 2.703 T 18.651 2.710 73.452
to 120.0 0.0 18.651 1.174
111 48.96 0.0067 0.0 21.361 0.144 Vel = 2.74
0.0
48.96 74.770 K Factor = 5-66
NEW PATH
213 43.94 2.703 T 18.651 2.710 73.371
to 120.0 0.0 18.651 1.174
212 43.94 0.0056 0.0 21.361 0.119 Vel = 2.46
212 0.0 2.703 2X 33.571 208.310 72.316
to 120.0 0.0 33.571 0.004
112 43.94 0.0056 0.0 241.881' 1.345 Vel = 2.46
112 0.0 2.703 T 18.651 2.710 73.665
to 120.0 0.0 18.651 1.174
113 43.94 0.0055 0.0 21.361 0.118 Vel = 2.46
0.0
43.94
NEW PATH
2.710 73.83321539.92 2.703
to 120.0
214 - - 39.92 0.0047
214 0.0 2.703
0
241.881
120.0
114 39.92 0.0047
74.957
T 18.651 2.710 73.833
0.0 18.651 1.174
0.0--21.361
33.571
0.100 -
2X- 208.310 72.759
0.0 33.571 0.004
0.0 241.881 1.125
Computer Programs by Hydratec Inc. Revision: 50.52.1
K Factor = 5.08
Vel = 2.23
Vel = 2.23
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 14
2010771 - B1S1RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
114 - - 0.0 - 2.703 T 18.651 2.710 - 73.888 - - - - - - - -
to 120.0 0.0 18.651 1.174
115 39.92 0.0047 0.0 21.361 0.100 Vel = 2.23
0.0
39.92 75.162 K Factor= 4.60
NEW PATH
217 36.93 2.703 T 18.651 2.710 74.231
to 120.0 0.0 18.651 1.174
216 36.93 0.0040 0.0 21.361 0.086 Vel = 2.06
216 0.0 2.703 2X 33.571 208.310 73.143
to 120.0 0.0 33.571 0.004
116 36.93 0.0040 - -_- 0.0 241.881 _- 0.975 Vel = 2.06
116 0.0-_--2.703 T- 18.651 2.710 74.122
to 120.0 0.0 18.651 1.174
117,1 _ 36.93 0.0040• _ 0.0 121.36121.361 0.086 ., ,, Vel = 2.06
Computer Programs by Hydratec Inc. Revision: 50.52.1
0.0
36.93_ 75.382 K Factor = 4.25
NEW PATH
219 35.02 2.703 T 18.651 2.710 74.574
to ' 120.0 0.0 18.651 1.174
218 35.02 0.0037 0.0 21.361 0.078 Vel = 1.96
218 0.0 2.703 2X 33.571 208.310 73.478
to 120.0 0.0 33.571 0.004
118 35.02 0.00_37 0.0 241.881 0.884 Vel = 1.96
118 0.0 2.703 T 18.651 2.710 74.366
to 120.0 0.0 18.651 1.174
119 35.02 0.0037 0.0 21.361 0.078 Vel = 1.96
0.0
35.02 75.618 K Factor = 4.03
NEW PATH
221 34.22 2.703 T 18.651 2.710 74.869
to 120.0 0.0 18.651 1.174
220 34.22 0.0035 0.0 21.361 0.075 Vel = 1.91
220 0.0 2.703 2X 33.571 208.310 73.770
to 120.0 0.0 33.571 0.004
120 _ 34.22 0.0035 0.0_ 241.881 0.84_7 Vel = 1.91
120 0.0 2.703 T 18.651 2.710 74.621
to 120.0 0.0 18.651 1.174
121 34.22 0.003.5 0.0 21.361 0.074 Vel = 1.91
0.0
34.22 75.869 K Factor= 3.93
NEW PATH
223 34.53 2.703 T 18.651 2.710 75.119
to 120.0 0.0 18.651 1.174
222 _ 3.4.53_ 0.0036 0.0 21.361 0.076 Vel = 1.93
222 0.0 2.703 2X 33.571 208.310 74.021
to 120.0 0.0 33.571 0.004
122 34.53 0.0036 0.0 241.881 0.861 Vel = 1.93
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 15
2010771 - B1S1RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv "•"'• Notes ""'•
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
122 0.0 2.703 T 18.651 2.710 74.886
to 120.0 0.0 18.651 1.174
123 34.53 0.0036 0.0 21.361 0.076
0.0
to
34.53 76.136
NEW PATH
Vel = 1.93
K Factor = 3.96
225 35.86 2.703 T 18.651 2.710 75.328
to
to
0.0
120.0
1.174
0.0 18.651 1.174
0.0
224 35.86 0.0038
0.0
0.0 21.361 0.082 Vel = 2.00
224 0.0 2.703 2X 33.571 208.310 74.236
41.15
to
0.0
120.0
1.191 Vel = 2.30
0.0 33.571 0.004
124 35.86 0.0038
44.84
0.0 241.881 0.923 Vel = 2.00
124 0.0 2.703 T 18.651 2.710 75.163
to
44.84
120.0
0.0 _
0.0 18.651 1.174
230
125 35.86 0.0038_ 0.0; r 21_.361 0.081 _ - _ Vel ,= 2.00
120.0
0.0
33.571 0.004
130 44.84 0.0
35.86 76.418 K Factor= 4.10
NEW PATH
227 38.11 2.703 T 18.651 2.710 75.498
to 120.0 0.0 18.651 1.174
226 - 38.11 0.0043 0.0 21.361 0.091 Vel = 2.13
226 0.0 2.703 2X 33.571 208.310 74.415
to 120.0 0.0 33.571 0.004
126 38.11 0.0043 0.0 241.881 1.0_33 Vel =2.13
126 0.0 2.703 T 18.651 2.710 75.452
to 120.0 0.0 18.651 1.174
127 38.11 0.0043 0.0 21.361 0.091 Vel = 2.13
0.0
38.11 76.717 K Factor = 4.35
NEW PATH
229 41.15 2.703 T 18.651 2.710 75.630
to
to
120.0 0.0 18.651 1.174
228 41.15 0.0049 0.0 21.361 0.105 Vel = 2.30
228 0.0 2.703 2X 33.571 208.310 74.561
to 120.0 0.0 33.571 0.004
128 41.15 0.0049 0.0 241.881 1.191 Vel = 2.30
128 0.0 2.703 T 18.651 2.710 75.756
to 120.0 0.0 18.651 1.174
129 41.15 0.0049 0.0 21.361 0.105 Vel = 2.30
0.0
41.15 77.035 K Factor= 4.69
NEW PATH
231 44.84 2.703 T 18.651 2.710 75.727
to 120.0 0.0 18.651 1.174
230 44.84 0.0058 0.0 _ 21.361 0.123 Vel =_ 2.5.1__
230 0.0 2.703 2X 33.571 208.310 74.676
to 120.0 0.0 33.571 0.004
130 44.84 0.0058 0.0 241.881 1.396 Vel = 2.51
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 16
2010771 - 61 S1 RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
130 0.0 2.703 T 18.651 2.710 76.076
to 120.0 0.0 18.651 1.174
131 44.84 0.0058 0.0 21.361 0.123 Vel = 2.51
0.0
44.84 77.373 K Factor= 5.10
NEW PATH
233 49.07 2.703 T 18.651 2.710 75.790
to 120.0 0.0 18.651 1.174
232 49.07 0.0068 0.0 21.361 0.146 Vel = 2.74
232 0.0 2.703 2X 33.571 208.310 74.762
to 120.0 0.0 33.571 0.004
132 49.07 0.0068 0.0 241.881 1.649 Vel = 2.74
132 0.0 2.703 T 18.651 2.710 76.415
to 120.0 0.0 18.651 1.174
133' 49.07 0.0068 0.0 0 21.361 0.146•,; Vel = 2:74 ;r
0.0
49.07___-- 77._73_5 _ - K Factor = 5.57_
NEW PATH
235 53.70 2.703 T 18.651 2.710 75.826
to 120.0 0.0 18.651 1.174
234 53.7 0.0081 0.0 21.361 0.172 Vel = 3.00
234 0.0 2.703 2X 33.571 208.310 74.824
to 120.0 0.0 33.571 0.004
134 53.7 0.0081 0.0 241.881 1.948 Vel = 3.00___
134 0.0 2.703 T 18.651 2.710 76.776
to 120.0 0.0 18.651 1.174
135 53.7 0.0081 0.0 21.361 0.172 Vel = 3.00
0.0
53.70 78.122 K Factor= 6.08
Computer Programs by Hydratec Inc. Revision: 50.52.1
AutoPeaking Summary
Wiginton Fire Systems Page 17
2010771 - B1S1RA1 Date 5-19-17
Auto Peaking Summary - List of Pipes for Area Calculated
Flow
Left
Pressure
Required
Right
Differential
Left 10.000 1 1709.867
Side
0.099
Area Calculated 1 1709.991
Side
0.000
From To Length From To Length
H4 100 103.540 H1 200 74.740
H8 102 103.540 202 H5 74.740
H12 104 103.540 204 H9 74.740
H4 100 103.540 H1 200 74.740
H8 102 103:540 202 H5 74.740
H12 104 103.540 204 H9 74.740
Flow Safety Pressure
Required Margin Differential
Left 10.000 1 1709.867 18.949 0.099
Area Calculated 1 1709.991 18.849 0.000
Right 10.000 1 1710.137 18.876 0.027
Typical Distance Between Heads = 10.000
Split Point Used in Worst Area Peaked = H3
Split Point Used in Area Calculated = H3
Computer Programs by Hydratec Inc. Revision: 50.52.1
W
0 0
omffl am
FIRE SYSTEMS
Wiginton Fire Systems
699 Aero Lane
Sanford, FL 32771
407-585-3200
Job Name 2010771 - B1 S1RA2
Drawing FP10
Location BUILDING ONE
Remote Area B1S1RA2
Contract 2010771
Data File 2010771 - B1S1RA2.WXF
Computer Programs by Hydratec Inc. Revision: 50.52.1
W
Wiginton Fire Systems
2010771 - B1S1RA2
Page 1
Date 5-19-17
Project name: GANESH NORTH
Location: BUILDING ONE
Drawing no: FP10
Date: 5-19-17
Design
HYDRAULIC CALCULATIONS
for
Remote area number: B1S1RA2
Remote area location: SYSTEM ONE - SECOND FLOOR OFFICES
Occupancy classification: OFFICES - LIGHT HAZARD
Density: .10 - Gpm/SgFt
Area of application: 980 - SgFt
Coverage per sprinkler. 225 MAX - SgFt
Type of sprinklers calculated. 5.6K PENDENT
No. of sprinklers calculated. 10
In -rack demand. N/A - GPM
Hose streams: 100 -GPM
Total water required (including hose streams): 287.215 - GPM
Type of system: WET
Volume of dry or pie'action system: N/A - GbI"
Water supply information
Date: 8-2-16
Location: ALONG W. 1ST STREET
Source: WFS
Name of contractor. WIGINTON FIRE SYSTEMS
Address: 699 AERO LANE, SANFORD, FL 32771
Phone number: 407-585-3200
Name of designer. W. AMMONS
Authority having jurisdiction: CITY OF SANFORD
Notes: (Include peaking information or gridded systems here.)
@ 81.622 -Psi
Computer Programs by Hydratec Inc. Revision: 50.52.1
Water )ly Curve C
Wiginton Fire Systems Page 2
2010771 - B1S1RA2
Date 5-19-17
City Water Supply:
C1 - Static Pressure : 60
C2 - Residual Pressure: 50
C2 - Residual Flow : 1840
City Water Adjusted to Pump Inlet
for Pf - Elev - Hose Flow -
Al - Adjusted Static:
A2 - Adj Resid
A3 - Adj Resid
56.432
37.095 @ 1261.31
15.597 @ 1881.1
Pump Data:
P1 - Pump Churn Pressure 126.18
P2 - Pump Rated Pressure 109.95
P2 - Pump Rated Flow 1261.31
P3 - Pump Pressure @ Max Flow 79.39
P3 - Pump Max Flow 1881.1
City Residual Flow @ 0 4846.63
City Residual Flow @ 20 3892.74
City Water @ 150% of Pump 49.58
Demand:
D1 - Elevation 9.239
D2 - System Flow 187.215
D2 - System Pressure 38.207
Hose ( Demand )
D3 - System Demand 187.215
Hose ( Adj City) 100
Safety Margin 141.300
210
196 Al +1131
182
p 168
R 154
E 140
S 126
S 112
U 98 A3 + P3
R 84
E 70 C1
56
42Al
28
14
A3
D1
200 400 600 800 1000 1200 1400 1600 1800
FLOW N^1.85)
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow Diagram
Wiginton Fire Systems Page 3
2010771 - B1 S1RA2 Date 5-19-17
20.3
D1 *- 1
14.8
D2 2
15.2
D3 r- 3
17.9
D4 *- 4
1
1 47.9
19.4
DS 5
18.9
D6 a 6
1
1 18.9
20.?
D7 7
19.8
D8 +- 8
1 19.8
20.a
D9 9
20.4
D10+- 10
20.3
1 +- M1
14.8
2 2A
15.2 47.9
3 +.- 2A 4- 4 F 5 M2
30 67.3
18.9
6 +- 7 +- M3
39.1
1 126.7
19.8 1
8 9 M4
1 40.1
1 40.1 126.7
20.1 1
10 +- M4 I
I
20.3 1 126.7 187.2
M1 +- M2M3 M4 FL2r BR1+- PO
876 187.2 187.2
187.2 287.2 287.2
PI SP/G- UG&- UG4+- UGSi UG6 TEST
187.2 287.2 287.2
Computer Programs by Hydratec Inc. Revision: 50.52.1
Fitting: :d Summary
Wiginton Fire Systems Page 4
2010771 - B1 S1RA2 Date 5-19-17
Fitting Legend
Abbrev. Name _ '/2 ' % 1 1'% 1'% 2 2'/: 3 3'/: 4 5 6 8 10 12 14 16 18 20 24
B Generic Butterfly Valve 0 0 0 0 0 0 7 10 0 12 9 10 12 19 21 0 0 0 0 0E90' Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61GGenericGateValve0000011112 __ 2 3 4 5 6 7 8 10 11 13LLongTurnElbow1122234556891316182427303440SGenericSwingCheckValve4557911141619222732455565768798109130T90' Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121V90' Ell Firelock #001 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 0 0 0 0 0 0 0ZafAmes3000SSFittinggeneratesaFixedLossBasedonFlow
Units Summary
Diameter Units
Length Units
Flow Units
Pressure Units
Inches
Feet
US Gallons per Minute
Pounds per Square Inch
Computer Programs by Hydratec Inc. Revision: 50.52.1
Pressure / Flow Summary - STANDARD
Wiginton Fire Systems Page 5
2010771 - B1 S1RA2 Date 5-19-17
Node Elevation K -Fact Pt Pn Flow Density Area PressNo. Actual Actual Req_
D1 23.333 5.6 13.08 na 20.25 0.1 56 7.0D223.333 5.6 7.0 na 14.82 0.1 124 7.0D323.333 5.6 7.34 na 15.17 0.1 124 7.0D423.333 5.6 10.27 na 17.95 0.1 126 7.0D523.333 5.6 11.97 na 19.37 0.1 70 7.0D623.333 5.6 11.38 na 18.89 0.1 126 7.0D723.333 5.6 13.07 na 20.25 0.1 56 7.0D823.333 5.6 12.53 na 19.82 0.1 30 7.0D923.333 5.6 13.18 na 20.33 0.1 144 7.0D1023.333 5.6 13.23 na 20.37 0.1 144 7.0124.333 13.05 na
2 24.333 6.79 na
3 24.333 7.14 na
2A 24.333 7.72 na
4 24.333 10.48 na
5 24.333 12.05 na
6 24.333 11.64 na
7 24.333 13.44 na
8 24.333 12.86 na
9 24.333 13.55 na
10 24.333 13.2 na
M1 24.333 14.43 na
M2 241333 14.43 na
M3 24.333 14.51 na
M4 24.333 14.87 na
FL2 24.333 28.42 na
BR1 2.0 38.18 na
PO 2.0 38.21 na
PI 2.0 53.79 na
SPIG 3.0 55.97 na
IG3 3.0 56.04 na 100.0
UG4 3.0 61.47 na
UG5 3.0 61.66 na
UG6 3.0 61.8 na
TEST 2.0 59.68 na
The maximum velocity is 14.44 and it occurs in the pipe between nodes 5 and M2
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 6
2010771 - B1S1RA2 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
EQUIVALENT K'S
D1 20.25 1.049 E 2.0 1.000 13.081 K Factor = 5.60
to 120.0 0.0 2.000 -0.433
1 20.25 0.1333 0.0 3.000 0.400 Vel = 7.52
0.0
20.25 13.048 K Factor= 5.61
D2 14.82 1.049 E 2.0 1.000 7.000 K Factor = 5.60
to
19.37
120.0 0.0 2.000 0.433
K Factor = 5.60
2 14.82 0.0747 0.0 3.000 0.224 Vel = 5.50
5
0.0
0.1226 0.0 4.208 0.516
to
14.82
120.0 0.0 5.000
6.791 K Factor= 5.69
D3 15.17 1.049 E 2.0 1.000 7.338 K Factor = 5.60
to
18.89
120.0 0.0 2.000 0.433
K Factor = 5.60
3 15.17 0.0783 0.0 3.000 0.235 Vel = 5.63
0
15.17 7.140 K Factor =_ 5.6_8_
D4 17.95 1.049 T 5.0 1.000 10.272 K Factor = 5.60
to 120.0 0.0 5.000 0.433
4 _ 17.95 0.1065 0.0 6.000 0.639 Vel = 6.66
6
0.0
17.95
0.1170 0.0
10.478 K Factor = 5.55
D5 19.37 1.049 E 2.0 2.208 11.968 K Factor = 5.60
to
18.89
120.0 0.0 2.000 0.433
K Factor = 5.54
5 19.37 0.1226 0.0 4.208 0.516
to
0.0
120.0 0.0 5.000 0.433
Vel _7.19
7
19.37
0.1332 6.000
12.051 K Factor= 5.58
D6 18.89 1.049 T 5.0 1.000 11.376 K Factor = 5.60
to
20.25
120.0 0.0 5.000 0.433
K Factor= 5.52.
6 18.89 0.1170 0.0 6.000 0.702 Vel = 7.01
19.8_2
0.0
6.000
0.0
Vel -=- 7.36
19.82 12.862
18.89
20.33 1.049 13.176
11.645 K Factor = 5.54
D7 20.25 1.049 T 5.0 1.000 13.074 K Factor = 5.60
to 120.0 0.0 5.000 0.433
13.231
7 20.25 0.1332 0.0 6.000 0.799 Vel = 7.52
0.404
0.0
20.25 13.440 K Factor= 5.52.
D8 19.82 1.049
to 0.0120.0
8 19.8_2 0.1280 6.000
0.0
Vel -=- 7.36
19.82 12.862
D9 20.33 1.049
e
D10
to
10
120.0
T
T
20.33 0.1342
0.0
20.33
20.37 1.049 E
120.0
20.37 0.1347
5.0 1.000 12.527 K Factor = 5.60
0.0 5.000 0.433
0.0_ _ 6.000 0.768 Vel -=- 7.36
12.862 K Factor = 5.53
5.0 1.000 13.176 K Factor = 5.60
0.0 5.000 0.433
0.0 6.000 0.805 Vel = 7.55
13.548 K Factor= 5.52
2.0 1.000 13.231 K Factor = 5.60
0.0 2.000 0.433
0.0 3.000 0.404 Vel = 7.56
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 7
2010771 - B1S1RA2 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv •"•"` Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
0.0
20.37 13.202 K Factor= 5.61
1 20.25 1.049 T ' 5.0 5.375 13.048
to 120.0 0.0 5.000 0.0
M1 20.25 0.1332 0.0 10.375 1.382 Vel = 7.52
0.0
20.25 14.430 K Factor= 5.33
2 14.82 1.049 T 5.0 7.500 6.791
19.82
to
9
120.0
1.38
0.0 5.000 0.0
M4
2A 14.82 0.0747
0.0
0.0 12.500 0.934 Vel = 5.50
10
0.0
1.049
to 120.0
M4 20.37 0.1346
14.82 7.725 K Factor = 5.33__
3 15.17 1.049 T 5.0 2.500 7.140
to ,'' 120.0;' 0.0 -;'' 5.000 0.0 -- ;'' 1V '
2A 15.17_ 0.0780 0.0 _ _ 7.500 0.585_ V_el =
2A 14.82 1.049 0.0 10.000 7.725
5_.6.3
to 120.0 0.0 0.0 0.0
4 29.99 0.2753 0.0 10.000 2.753 Vel = 11_.13
4 17.94 1.38 0.0 9.125 10.478
to 120.0 0.0 0.0 0.0
5 --- 47.93 0.1724 0.0 9.125 1.573 Vel = 10.28
5 19.38 1.38 T 6.0 1.375 12.051
to 120.0 0.0 6.000 0.0
M2 _ _ 67.31 0.3231 0.0 - 7.375 2.383 Vel =_14.44
0.0
67.31 14.434 K Factor= 17.72
6 18.89 1.049 2E 4.0 11.333 11.645
to 120.0 0.0 4.000 0.0
7 18.89 0.1171 0.0 15.333 1.795 Vel = 7.01
7 20.25 1.38 T 6.0 3.000 13.440
to 120.0 0.0 6.000 0.0
M3 39.14 0.1184 0.0 9.000 1.066 Vel = 8.40
0.0
39.14 14.506 K Factor= 10.28
8 19.82 1.38
to 9.000120.0
9 19.82 0.0337_
9 20.33 1.38
to 6.000120.0
M4 40.15 0.1242
0.0
40.15
10 20.37 1.049
to 120.0
M4 20.37 0.1346
0.0
E 3.0 11.375 12.862
T 6.0 9.000 0.0
0.0 _____20.375 0.68_6
T 6.0 4.625 13.548
0.0 6.000 0.0
0.0 10.625 1.320
14.868
T 5.0 7.375 13.202
0.0 5.000 0.0
0.0 12.375 1.666
Computer Programs by Hydratec Inc. Revision: 50.52.1
Vel = 4.25
Vet = 8.61
K Factor= 10.41
Vel = 7.56
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 8
2010771 - B1 S1 RA2 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv •"•"` Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
20.37 - _- __14.868 _ K Factor= 5.28
M1 20.25 2.703 0.0 3.375 14.430
to 120.0
to
12.845
120.0 0.0 0.0 0.0
BR1 187.22 0.0012
M2 20.25 0.0012 0.0 3.375 0.004 Vel = 1.13
M2 67.31 2.703 0.0 3.625 14.434
50.044 63.389
to 120.0 0.0 0.0 0.0
67.889 0.024
M3 87.56 0.0199 0.0 3.625 0.072 Vel = 4.90
M3 39.14 2.703 0.0 9.167 14.506
Factor= 30_._29_
System Demand Pressure
to 120.0 0.0 0.0 0.0
Safety Margin
M4 126.7 0.0395 0.0 9.167 0.362 Vel = 7.08
M4 60.52 2.703 6V 40.099 108.208 14.868
to 120.0 T 18.651 58.750 0.0
125.720
FL2 187.22 0.0812 0.0 166.958 13.552 Vel = 10.47
PI 0.0 8.249 T 38.923 2.500 53.787
187.22 28.420 K Factor= 35.12 _
FL2 187.22 6.385 T 38.536 22.333 28.420
to 120.0 B 12.845 51.381 9.672
BR1 187.22 0.0012 0.0 -_ 73.714 0.091_ Vel = 1.88
BRI 0.0 8.249 B 13.345 4.500 38.183
to 120.0 S 50.044 63.389 0.0
PO 187.22 0.0004 0.0 67.889 0.024 Vel = 1.12
0.0
187.22 - - 38.207 _ Factor= 30_._29_
System Demand Pressure 38.207
K_
Safety Margin 141.300
Continuation Pressure 179.507
Pressure @ Pump Outlet 179.507
Pressure From Pump Curve 125.720
Pressure @ Pump Inlet 53.787
PI 0.0 8.249 T 38.923 2.500 53.787
to 120.0 G 4.448 43.371 2.166
SPIG 187.22 0.0003 0.0 45.871 0.015 Vel = 1.12
SPIG 0.0 8.27 E 26.955 195.000 55.968
to 140.0 T 52.413 85.358 0.0
UG3 187.22 0.0003 G 5.99 280.358 0.074 Vel = 1.12
UG3 99.99 8.27 T 52.413 300.000 56.042 Qa = 100
to 140.0 Zaf 0.0 130.283 5.179 Fixed Loss = 5.179
UG4 2.8_7.21 0.000_ _6_ 4L 77.87 430.28_3 0.250 Vel = 1.72
UG4 0.0 10.28 T 71.092 865.000 61.471
to 140.0 0.0 71.092 0.0
UG5 287.21 0.0002 0.0 936.092 0.189 Vel = 1.11
UG5 0.0 12.34 T 88.164 1600.000 61.660
to 140.0 0.0 88.164 0.0
UG6 _ 2.87.21 0.0001_ - 0.0 1688.164 0.139 Vel = 0.77
UG6 0.0 12.34 T 88.164 450.000 61.799
to 140.0 0.0 88.164 2.166
TEST 287.21 0.0001 0.0 538.164 0.045 Vel = 0.77
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 9
2010771 - B1S1RA2 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
0.0
287.21 59.678 K Factor= 37.1
d ,:0 d ,,
Computer Programs by Hydratec Inc. Revision: 50.52.1
ogan:Dm
FIRE SYSTEMS
Wiginton Fire Systems
699 Aero Lane
Sanford, FL 32771
407-585-3200
Job Name 2010771 - B1S2RA1
Drawing FP4/FP5
Location BUILDING ONE
Remote Area B1S2RA1
Contract 2010771
Data File 2010771 - B1S2RA1.WXF
Computer Programs by Hydratec Inc. Revision: 50.52.1
M
Wiginton Fire Systems
2010771 - B1S2RA1
Page 1
Date 5-19-17
Project name: GANESH NORTH
Location: BUILDING ONE
Drawing no: FP4/FP5
Date: 5-19-17
Design
HYDRAULIC CALCULATIONS
for
Remote area number. B1S2RA1
Remote area location: SYSTEM TWO
Occupancy classification: HIGH PILED STORAGE
Density: 52 PSI - Gpm/SgFt
Area of application: 12 HEADS - SgFt
Coverage per sprinkler. 100 MAX - SgFt
Type of sprinklers calculated. 16.81K ESFR PENDENT
No. of sprinklers calculated. 12
In -rack demand. N/A - GPM
Hose streams: 250 - GPM
Total water required (including hose streams): 1709.928 - GPM
Type of system: WET
Volume of dry or preaction system: N/A - Gal
Water supply information
Date: 8-2-16
Location: ALONG W. 1ST STREET
Source: WFS
Name of contractor. WIGINTON FIRE SYSTEMS
Address: 699 AERO LANE, SANFORD, FL 32771
Phone number: 407-585-3200
Name of designer. W. AMMONS
Authority having jurisdiction: CITY OF SANFORD
Notes: (Include peaking information or gridded systems here.)
@ 39.124 -Psi
Computer Programs by Hydratec Inc. Revision: 50.52.1
Water ply Curare C
Wiginton Fire Systems
Page 22010771 - B1S2RA1
Date 5-19-17
City Water Supply:
C1 - Static Pressure : 60
C2 - Residual Pressure: 50
C2 - Residual Flow : 1840
City Water Adjusted to Pump
for Pf - Elev - Hose Flow
Inlet
Al - Adjusted Static:
A2 - Adj Resid
A3 - Adj Resid
54.436 -
33.185 @ 1261.31
10.52 @ 1881.1
Pump Data:
P1 - Pump Churn Pressure 126.18
P2 - Pump Rated Pressure 109.95
P2 - Pump Rated Flow 1261.31
P3 - Pump Pressure @ Max Flow 79.39
P3 - Pump Max Flow 1881.1
City Residual Flow @ 0 4846.63
City Residual Flow @ 20 3892.74
City Water @ 150% of Pump 49.58
Demand:
D1 - Elevation 14.738
D2 - System Flow 1459.93
D2 - System Pressure 117.356
Hose ( Demand )
D3 - System Demand 1459.93
Hose ( Adj City) 250
Safety Margin 12.144
210
196
Al +1121
182
p 168
R 154 A2+P2
E 140
S 126 =
S 112
U 98
R 84
E 70 C1
56
42 Al
28
14 D1
200 400 600 800 1000 1200 1400 1600 1800
FLOW (N^1.85)
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow D IM
Wiginton Fire Systems
2010771 - B1S2RA1
Page 3
Date 5-19-17
121.3 242.7 465.6 729.9 731.3 7383 757.6 796.8 864.4 989,7 1169.4
H3 <-H4 F100F101F103 105f107F 109F111(--113i-115F 117+-119(-121F123F 125+- 127 129f131+-133F135 137 141
242.7 242.7 729.2 730.2 733.7 746 774.2 826.5 911.7 1039.5 1310.2
149.7 1459.9
139 e- 141 TR2+- BR2+- PO
1459.9 1459.9
1459.9 1709.9 1709.9
PI SPIG- UG3(- UG4+- UG5*- UG6 UG7 TEST
1459.9 1709.9
0.2 243.2 243.2 730.7 729.7 726.2 713.9 685.7 633.4 548.2 420.5 149.7 149.7H3 - H2 a H1 200 +- 201 203 F 205 +- 207 *- 209 a 211 F 213 +- 215 t 217 219 +- 221 +- 223 - 225 t 227 a- 229 F- 231 i- 233 i- 235 237 +- 239 +- 238 *- 138 +- 139121.2 243.2 486.6 730 7287 721.6 702.3 663.1 595.5 = 490.3 290.5 149.7 149.7
243.4 121.3 121.4 242.9
203 - 202 - H5 -+ H6 +- H7 F H8 a 102 f 103
t 243.4 0.2 242.9 T
1 486.6 1 485.6
1 244.1 121.7 121.8 2446
205 - 204 - H9 -r H10*-- HI i- H12+- 104 F 105
t 244.1 02 243.6
1 730.7
1 06 0.6
207 206 r- 106 F 107
T 0.6 T
1 730 1 729.9
1 0.4 0.41
209 208 108+- 109
T 0.4 T
1 729.7 1 730.2
I 1 1 I
211-210-110<- 111
T t T
1 728.7 1 731.3
1 2.4 2.41
213e 212- 112+- 113
T 2.4 T
1 726.2 1 733.7
1 4.6 4,61
2151 214+- 114E 115
T 4.6 T
1 721.6 1 738.3
1 7.7 7.71
217 216 116 i- 117
T 7.7 T
1 713.9 1 746
1 11.6 11.6
219 r- 218 r- 118(.- 119
T 11.6 T
1 702.3 1 757.6
1 16.6 16.6
221 f.. 220 120 +- 121
T 16.6 T
1 685.7 1 774.2
1 22.6 22.6
223 f 222 f- 122 (- 123
T 22.6 T
1 663.1 1 796.8
Computer. Programs by Hydratec Inc. Revision: 50.52.1
Flow [ am
Wiginton Fire Systems
2010771 - B1S2RA1
Page 4
Date 5-19-17
1 29.7 29.1
225 t- 224 i- 124 r- 125
T 29.7 t
1 633.4 1 826.5
1 37.9 37.¢
227 226 <- 126 r- 127
T 37.9 t
1 595.5 1 864.4
1 47.3 47.8
229*- 228 . 128 129
T 47.3 t
1 548.2 1 911.7
1 57.9 57.¢
231 a 230 +- 130 +- 131
T 57.9 t
1 490.3 1 969.7
1 69.8 69.8
233 232 +- 132 i- 133
1 69.8 t
1 420.5 1 1039.5
1 130 13Q
235 +- 234 +- 134 F 135
T 130 t
1 290.5 1 1169.4
1 140.7 14%7
237 < 236 e- 136 f- 137
140.7
Computer Programs by Hydratec Inc. Revision: 50.52.1
Fitting: d Summary
Wiginton Fire Systems Page 5
2010771 - B1S2RA1 Date 5-19-17
Fitting Legend
Abbrev. Name '/: '/. 1 1'/. 1'/: 2 _ 2%: 3 3%z 4 _5 6 8 10 12 14 16 18 20 24
B Generic Butterfly Valve 0 0 0 0 0 0 7 10 0 12 __ 9 10 12 19 21 0 0 0 0 0
E 90' Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61GGenericGateValve00000111122345678101113LLongTumElbow1122234556891316182427303440SGenericSwingCheckValve4557911141619222732455565768798109130T90' Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121
V 90' Ell Firelock #001 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 0 0 0 0 0 0 0X90'Tee-BranchFirelock002 0 ' 0 0 0 0 8.5 10.8 13 0 16 21 25 33 0 0 0 0 0 0 0
Zaf Ames 3000SS Fitting generates a Fixed Loss Based on Flow
Units Summary
Diameter Units Inches
Length Units Feet
Flow Units US Gallons per Minute
Pressure Units Pounds per Square Inch
Computer Programs by Hydratec Inc. Revision: 50.52.1
Pressure / Flow Summary - STANDARD
Wiginton Fire Systems Page 6
2010771 - B1S2RA1 Date 5-19-17
Node Elevation K -Fact Pt Pn Flow Density Area Press
No.Actual Rte'-- - ---
H3 36.03 16.8 52.0 na 121.15 0.1 100 52.0
H4 36.38 16.8 52.21 na 121.39 0.1 100 52.0
100 32.42 67.31 na
101 29.72 71.28 na
103 29.72 71.4 na
105 29.72 71.8 na
107 29.72 72.67 na
109 29.72 73.54 na
111 29.72 74.41 na
113 29.72 75.29 na
115 29.72 76.16 na
117 29.72 77.05 na
119 29.72 77.96 na
121 29.72 78.89 na
123 29.72 79.86 na
125 29.72 80.88 na
127 29.72 81.98 na
129 29.72 83.17 na
131 29.72 84.48 na
133 29.72 85.95 na
135 29.02 95.06 na
137 29.02 97.14 na
939 29.02 X1198.88 na
141 29.02 98.91 na
TR2 29.02 99.66 na
BR2 2.0 115.69 na
PO 2.0 117.36 na
PI 2.0 26.46 na
SPIG -3.0 29.35 na
UG3 -3.0 32.65 na 250.0
1G4 -3.0 43.32 na
UG5 -3.0 48.44 na
UG6 -3.0 52.23 na
TEST 2.0 51.27 na
H2 35.62 16.8 52.18 na 121.35 0.1 100 52.0
Hl 35.2 16.8 52.72 na 121.98 0.1 100 52.0
200 32.09 67.44 na
201 29.38 71.42 na
203 29.38 71.54 na
205 29.38 71.95 na
207 29.38 72.82 na
209 29.38 73.69 na
211 29.38 74.56 na
213 29.38 75.43 na
215 29.38 76.29 na
217 29.38 77.14 na
219 29.38 77.97 na
221 29.38 78.78 na
223 29.38 79.56 na
225 29.38 80.29 na
227 29.38 80.96 na
229 29.38 81.55 na
231 29.38 82.06 na
233 29.38 82.48 na
235 29.38 82.8 na
237 29.38 82.95 na
239 29.38 83.0 na
238 32.09 82.97 na
138 31.73 96.56 na
202 32.09 67.55 na
H5 35.2 16.8 52.81 na 122.09 0.1 100 52.0
H6 35.62 16.8 52.26 na 121.45 0.1 100 52.0
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow Summary - Standard
Wiginton Fire Systems Page 7
2010771 - B1S2RA1 Date 5-19-17
Node Elevation K -Fact Pt Pn Flow Density Area Press
No. Actual-- Actual Req: --
H7 36.03 16.8 52.09 na 121.25 0.1 100 52.0
H8 36.38 16.8 52.3 na 121.5 0.1 100 52.0
102 32.42 67.42 na
204 32.09 67.94 na
H9 35.2 16.8 53.13 na 122.46 0.1 100 52.0
H10 35.62 16.8 52.58 na 121.82 0.1 100 52.0
H11 36.03 16.8 52.4 na 121.62 0.1 100 52.0
H12 36.38 16.8 52.62 na 121.87 0.1 100 52.0
104 32.42 67.81 na
206 32.09 71.65 na
106 32.42 71.5 na
208 32.09 72.52 na
108 32.42 72.37 na
210 32.09 73.39 na
110 32.42 73.24 na
212 32.09 74.25 na
112 32.42 74.12 na
214 32.09 75.11 na
114 32.42 74.99 na
216 32.09 75.97 na
116 32.42 75.88 na
218 32.09 76.81 na
118 32:42 76.78 na-11
220 32.09 77.63 na
120 32.42 77.7 na
222 32.09 78.42 na
122 32.42 78.66 na
224 32.09 79.17 na
124 32.42 79.66 na
226 32.09 79.87 na
26 32.42 80.72 na
228 32.09 80.52 na
128 32.42 81.86 na
230 32.09 81.09 na
130 32.42 83.11 na
232 32.09 81.59 na
132 32.42 84.5 na
234 32.09 82.5 na
134 31.73 93.0 na
236 32.09 82.8 na
136 31.73 94.94 na
The maximum velocity is 25.79 and it occurs in the pipe between nodes 135 and 137
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 8
2010771 - B1S2RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv *'*'•'• Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
EQUIVALENT K'S
REMOTE HEAD TO SUPPLY
H3 121.31 2.703 0.0 10.000 52.000 K Factor = 16.80
to 120.0 0.0 0.0 0.152
H4 121.31 0.0364 0.0 10.000 0.364 Vel = 6.78
H4 121.39 2.703 X 16.786 85.210 52.212 K Factor = 16.80
to 120.0 0.0 16.786 1.715
100 242.7 0.1312 0.0 101.996 13.383 Vel = 13.57
100 0.0 2.703 T 18.651 2.710 67.310
to 120.0 0.0 18.651 1.169
101 242.7 0.1312 0.0 21.361 2.803 Vel = 13.57
101 0.0 4.304 0.0 8.330 71.282
to 120.0 0.0 0.0 0.0
103 242.7 0.0136 0.0 8.330 0.113 Vel = 5.35
103 242.91 114.304 0.0 8.330 71:1395
to 120.0 0.0 0.0 0.0
105 _- 485.61 0.0491 0_0 _____8.330 0.409 Vel = 10.71
105 243.64 4.304 0.0 8.330 71.804
to 120.0 0.0 0.0 0.0
107 729.25 0.1043 0.0 _ 8.330 0.869 _ 16.08_-
107 0.63 4.304 0.0 8.330 72.673
Vel
to 120.0 0.0 0.0 0.0
109 729.88 0.1043 _ 0.0 8.330 0.869 16.10
109 0.37 4.304 0.0 8.330 73.542
Vel .=.
to 120.0 0.0 0.0 0.0
111 730.25 0.1046 0.0 _ 8.330 0.871 _ -__ Vel = 16.10_
111 1.03 4.304 0.0 8.330 74.413
to 120.0 0.0 0.0 0.0
113 731.28 0.1048 0.0 8.330 0.873 Vel = 16.13
113 2.43 4.304 0.0 8.330 75.286
to 120.0 0.0 0.0 0.0
115 733.71 0.1054 0.0 8.330 0.878 Vel = 16.18
115 4.62 4.304 0.0 8.330 76.164
to 120.0 • 0.0 0.0 0.0
117 738.33 0.1066 0.0 8.330 0.888 Vel = 16.28
117 7.66 4.304 0.0 8.330 77.052
to 120.0 0.0 0.0 0.0
119 745.99 0.1088 0.0 8.330 0.906 Vel = 16.45
119 11.63 4.304 0.0 8.330 77.958
to 120.0 0.0 0.0 0.0
121 757.62 0.1118_ 0.0 8.330---- 0.931 Vel = 16.71
121 16.59 4.304 0.0 8.330 78.889
to 120.0 0.0 0.0 0.0
123 774.21 0.1164 0.0 8.330 0.970 Vel = 17.07
123 22.59 4.304 0.0 8.330 79.859
to 120.0 0.0 0.0 0.0
125 796.8 0.1228 0.0 8.330 1.023 Vel = 17.57
125 29.68 4.304 0.0 8.330 80.882
to 120.0 0.0 0.0 0.0
127 826.48 0.1315 0.0 8.330 1.095 Vel = 18.23
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems
129.500
Page 9
2010771 - B1S2RA1
103.042
Pressure Rump Inlet
Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
26.458-
26.458
Ref.
G
C" or
2.166
Ftng's Pe Pv Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
to 140.0
127 37.91 4.304
0.0
0.0 8.330 81.977
280.358
to
UG3 250.00 8.27
120.0
52.413
0.0 0.0 0.0
Zaf
129 864.39 0.1427
UG4 1709.93 0.0158
0.0 8.330 1.189 Vel = 19.06
129 47.32 4.304 0.0 8.330 83.166
to 120.0 0.0 0.0 0.0
131 911.71 0.1575 0.0 8.330 1.312 Vel = 20.10
131 57.94 4.304 0.0 8.330 84.478
to 120.0 0.0 0.0 0.0
133 969.65 0.1766 0.0 8.330 1.471 Vel = 21.38
133 69.81 4.304 2V 18.826 25.010 85.949
to 120.0 0.0 18.826 0.303
135 1039.46 0.2008 0.0 - 43.836 8.803 Vel =_22.92
135 129.97 4.304 0.0 8.330 95.055
to 120.0 0.0 0.0 0.0
137 1169.43 0.2498 0_0
J ,,
8.330 2.081 Vel = 25.79
137 140.75 6.385 X 32.113 7.250 97.136
to 120.0 0.0 32.113 0.0
141 1310.18_ 0.0451 0.0 39.363 1.776 Vel = 13.13
0.0
1310.18 98.912 K Factor = 131.74
139 149.74 6.385 X 32.113 1.083 98.885
to 120.0 0.0 32.113 0.0
141 149.74 0.0008 0.0 33.196 0.027 Vel = 1.50
141 1310.19 6.385 V 12.845 0.792 98.912
to 120.0 0.0 12.845 0.0
TR2 _ 1459.93 0.0551 0.0 13.637 0.752 14.63
TR2 0.0 6.385 T 38.536 27.020 99.664
Vel
to 120.0 B 12.845 51.381 11.702
BR2 1459.93 0.0552 0.0 78.401 4.325 Vel = 14.63
BR2 0.0 8.249 2V 28.914 12.833 115.691
to 120.0 B 13.345 92.303 0.0
PO 1459.93 0.0158 S 50.044 105.136 1.665 Vel = 8.76 _
0.0
1459.93 117.356 K Factor = 134.77
System Demand Pressure 117.356
Safety Margin 12.144
Continuation Pressure 129.500
Pressure @ Pump Outlet 129.500
Pressure From Pump Curve 103.042
Pressure Rump Inlet
PI 0.0 8.249 T 38.923 2.500
26.458-
26.458
to 120.0 G 4.448 43.371 2.166
SPIG 1459.93 0.0158 0.0 45.871 0.726
SPIG 0.0 8.27 E 26.955 195.000 29.350
to 140.0 T 52.413 85.358 0.0
UG3 1459.93 0.0118 G 5.99 280.358 3.298
UG3 250.00 8.27 T 52.413 300.000 32.648
to 140.0 Zaf 0.0 130.283 3.893
UG4 1709.93 0.0158 4L 77.87 430.283 6.782
Computer Programs by Hydratec Inc. Revision: 50.52.1
Vel = 8.76
Vel = 8.72
Qa = 250
Fixed Loss = 3.893
Vel = 10.21
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 10
2010771 - B1S2RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv ••""' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
UG4 0.0 10.28 T 71.092 865.000 43.323
to
to
140.0 0.0 71.092 0.0
UG5 1709.93 0.0055 0.0 936.092 5.113 Vel = 6.61
UG5 0.0 12.34 T 88.164 1600.000 48.436
to
0.37
140.0 0.0 88.164 0.0
UG6 1709.93 0.0022 0.0 1688.164 3.790 Vel = 4.59
UG6 0.0 12.34 T 88.164 450.000 52.226
to
to
140.0 0.0 88.164 2.166
0.0
TEST 1709.93 0.0022 0.0 538.164 1.208 Vel = 4.59
0.870
0.0
16.10
209 0.37 4.304 0.0 8.330
1709.93
to
51.268 K Factor = 238.81
NEW PATH
0.0 0.0
211
H3 0.16 2.703 0.0 10.000 52.000
16_.0_9___
to
1.03
120.0 0.0 0.0 0.178
H2 _ ; 0.16_ 0.0 I'd 0.0 _ 10:000 0.0 ; Vel = 0.01,_a
H2 121.35 2.703 0.0 10.000 52.178 K Factor = 16.80
to
Vel =
120.0 0.0 0.0 0.182
0.0
H1 _ 121.19 0.0362 0.0 _ 10.000 _ 0.362 _ _ Vel _ 6.78
H1 121.99 2.703 X 16.786 84.730 52.722 K Factor = 16.80
to
0.0
120.0 0.0 16.786 1.347
215
200 243.18 0.1317 0.0 _ 101.516 13.368 Vel = 13.60
200 0.0 2.703 T 18.651 2.710 67.437
i
to
217
120.0 0.0 18.651 1.174
0.852
201 _ 243.18 _ 0.1316 0.0_ 21.361 ____.__._2.812 Vel = 1.3.60_
201 0.0 4.304 0.0 8.330 71.423
to 120.0 0.0 0.0 0.0
203 243.18 0.0137 0.0 8.330 0.114 Vel = 5.36
203 243.38 4.304 0.0 8.330 71.537
to 120.0 0.0 0.0 0.0
205 486.56 0.0493 0.0 8.330 0.411 Vel = 10.73
205 244.12 4.304 0.0 8.330 71.948
to 120.0 0.0 0.0 0.0
207 730.68 0.1046 0.0 8.330 0.871 Vel = 16.11
207 0.63 4.304 0.0 8.330 72.819
to 120.0 0.0 0.0 0.0
209 730.05 0.1044 0.0 8.330 0.870 Vel = 16.10
209 0.37 4.304 0.0 8.330 73.689
to 120.0 0.0 0.0 0.0
211 729.68 0.1044 0.0 8.330 0.870 Vel = 16_.0_9___
211 1.03 4.304 0.0 8.330 74.559
to 120.0 0.0 0.0 0.0
213 728.65 0.1041 0.0 8.330 0.867 Vel = 16.07
213 2.43 4.304 0.0 8.330 75.426
to 120.0 0.0 0.0 0.0
215 726.22 0.1034 0.0 8.330 0.861 Vel = 16.01
215 4.62 4.304 0.0 8.330 76.287
to 120.0 0.0 0.0 0.0
217 721.6 0.1023 0.0 8.330 0.852 Vel = 15.91
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 11
2010771 - B1S2RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes ""••
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
217 7.66 4.304 0.0 8.330 77.139 - ---
to
1.174
120.0 0.0 0.0 0.0
1.146 Vel = 8.37
0.0
219 713.94 0.1002 0.0 8.330 0.835 Vel = 15.74
219 11.64 4.304 0.0 8.330 77.974
203 -243.38 2.703
to
2.710
120.0 0.0 0.0 0.0
18.651 1.174
221 702.3 0.0971 0.0 8.330 0.809 Vel = 15.49
221 16.58 4.304 0.0 8.330 78.783
to 120.0 0.0 0.0 0.0
223 685.72 0.0930 0.0 8.330 0.775 Vel = 15.12
223 22.59 4.304 0.0 8.330 79.558
to 120.0 0.0 0.0 0.0
225 663.13 0.0874 0.0 8.330 0.728 Vel = 14.62
225 29.69 4.304 0.0 8.330 80.286
to 120.0 0.0 0.0 0.0
227 633.44 0.0804 0.0 8.330 0.670;;____ Vel = 13.97
227 37.91 4.304 0.0 8.330 80.956
f
to 120.0 0.0 0.0 0.0
229 595.53 0.0717 0.0 8.330 0.597 Vel = 13.13
229 47.31 4.304 0.0 8.330 81.553
to 120.0 0.0 0.0 0.0
231 548.22 0.0615 0.0 8.330 0.512 Vel = 12.09
231 57.94 4.304 0.0 8.330 82.065
to 120.0 0.0 0.0 0.0
233 490.28 0.0499 0.0 8.330 0.416 Vel = 10.81
233 69.82 4.304 0.0 8.330 82.481
to 120.0 0.0 0.0 0.0
235 420.46 0.0377 0.0 8.330 0.314 Vel = 9.2.7_
235 129.97 4.304 0.0 8.330 82.795
to 120.0 0.0 0.0 0.0
237 290.49 0.0190 0.0 8.330 0.158 Vel = 6.41
237 140.75 4.304 0.0 8.330 82.953
to 120.0 0.0 0.0 0.0
239 149.74 0.0055 0.0 8.330 0.046 Vel = 3.30
239 0.0 2.703 T 18.651 2.710 82.999
to 120.0 0.0 18.651 1.174
238 149.74 0.0537 0.0 21.361 1.148 Vel = 8.37
238 0.0 2.703 2X 33.571 216.640 82.973
to 120.0 0.0 33.571 0.156
138 149.74 0.0537 0.0 250.211 13.436 Vel = 8.37
138 0.0 2.703 T 18.651 2.710 96.565
to 120.0 0.0 18.651 1.174
139 1.49.74 0.0536 0.0 21.361 1.146 Vel = 8.37
0.0
149.74 98.885 K Factor= 15.06
NEW PATH
203 -243.38 2.703 T 18.651 2.710 71.537
to 120.0 0.0 18.651 1.174
202 -243.38 0.1319 0.0 21.361 2.817 Vel = 13.61
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 12
2010771 - B1S2RA1 Date 5-19-17
Hyd. Oa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
202 0.0 2.703 X 16.786 84.730 67.546
to 120.0 0.0 16.786 -1.347
H5 -243.38 -0.1319 0.0 101.516 -13.388 Vel = 13.61
H5 122.09 2.703 0.0 10.000 52.811 K Factor = 16.80
to 120.0 0.0 0.0 -0.182
H6 -121.29 -0.0364 0.0 10.000 -0.364 Vel = 6.78
H6 121.45 2.703
0.0
0.0 10.000 52.265 K Factor = 16.80
to
120.0
120.0
0.0
0.0 0.0 0.178
121.67
H7 0.16 0.0001
0.366
0.0 10.000 0.001 Vel = 0.01
H7 121.25 2.703
K Factor = 16.80
0.0 10.000 52.088 K Factor = 16.80
to
0.178
120.0
H11
0.0 0.0 0.152
10.000
H8 121.41 0.0364
243.64
0.0 10.000 0.364 Vel = 6.79
H8 121.50 2.703 X 16.786 85.210 52.300 K Factor = 16.80
to
243.64
120.0 0.0 16.786 1.715
NEW PATH
102 ;,, 242.91 0.1314._:,) 0.0 101.996
T
13.404 , Vel = 13.58.;,
T
102 0.0 2.703 T 18.651 2.710 67.419
0.0
to
1.174
120.0
206
0.0 18.651 1.169
21.361
103 242.91 0.1314 0.0 21.361 ------- 2.807 _ - Vel = 13.58
0.0
242.91 71_._395 _ K Facto_ r = 28.75
NEW PATH
205 244.12 2.703 T 18.651 2.710 71.948
to 120.0 0.0 18.651 1.174
204 244.12 0.1326 0.0 21.361 ----- 2.833--- _ Vel = 13.65
204 0.00.0 2.703 X 16.786 84.730 67.941
to 120.0 0.0 16.786 1.347
H9 244.12 0.1326 0.0 101.516 13.464 Vel = 13.65
H9 122.45 2.703 0.0 10.000 53.130 K Factor = 16.80
to
121.87
120.0 0.0 0.0 0.182
K Factor = 16.80
H10 121.67 0.0366 0.0 10.000 0.366 Vel = 6.80
H10 121.82 2.703 0.0 10.000 52.582 K Factor = 16.80
to
0.0
120.0 0.0 0.0 0.178
H11 0.15 0.0001 0.0 10.000 0.001 Vel = 0.01
H11
to
H12
121.62
121.77 .
2.703
120.0
0.0367
0.0
0.0
0.0
10.000
0.0
10.000
52.405
0.152
0.367
K Factor = 16.80
Vel = 6.81
H12 121.87 2.703 X 16.786 85.210 52.620 K Factor = 16.80
to 120.0 0.0 16.786 1.715
104 243.64 0.1321 0.0 101.996 13.477 Vel = 13.62
104 0.0 2.703 T 18.651- 2.710 67.812 -
to 120.0 0.0 18.651 1.169
105 243.64 0.1322 0.0 21.361 2.823 Vel = 13.62
0.0
243.64 71.804 K Factor= 28.75
NEW PATH
207 0.63 2.703 T 18.651 2.710 72.819
0 120.0 0.0 18.651 1.174
206 0.63 0.0 0.0 21.361 0.001 Vel = 0.04
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 13
2010771 - B1S2RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """` Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
206 0.0 2.703 2X 33.571 199.970 71.646
to
to
120.0 0.0 33.571 0.143
106 0.63 0.0 0.0 233.541 0.0 Vel = 0.04
106 0.0 2.703 T 18.651 2.710 71.503
to
199.970
120.0 0.0 18.651 1.169
107 0.63 0.0 0.0 21.361 0.001 Vel = 0.04
0.0
0.63 72.673 K Factor= 0.07
NEW PATH
209 0.37 2.703 T 18.651 2.710 73.689
to
211
120.0 0.0 18.651 1.174
2.710
208 0.37 0.0 0.0 21.361 0.001 Vel = 0.02
208 0.0 2.703 2X 33.571 199.970 72.516
to
21.361
120.0 0.0 33.571 0.143
2.703
108 0.37 0.0 _ 0.0 _ 233.54,1"il 0.0 1, Vel = 0.02_
108 0.0 2.703 T 18.651 2.710 72.373
110
to
0.0
120.0 0.0 18.651 1.169
Vel = 0.06
109 -__ 0.37 0.0 0.0 21.361 0.0 _ Vel =
0.0
120.0 0.0 18.651 1.169
0.37
111 1.03 0.0
73.542 K Factor= 0 04
NEW PATH
211 1.03 2.703 T 18.651 2.710 74.559
to 120.0 0.0 18.651 1.174
210 -_ 1.03 0.0 __- 0.0_ 21.361 0.0 _ Vel = 0.0_6_
210 0.0 2.703 2X 33.571 199.970 73.385
to 120.0 0.0 33.571 0.143
110 1.03 0.0 0.0 233.541 0.001 Vel = 0.06
110 0.0 2.703 T 18.651 2.710 73.243
to 120.0 0.0 18.651 1.169
111 1.03 0.0 0.0 21.361 0.001 Vel = 0.06
0.0
1.03 74.413 K Factor= 0.12
NEW PATH
213 2.43 2.703 T 18.651 2.710 75.426
to 120.0 0.0 18.651 1.174
212 2.43 0.0 • 0.0 21.361 0.0 • Vel = 0.14
212 0.0 2.703 2X 33.571 199.970 74.252
to 120.0 0.0 33.571 0.143
112 2.43_ 0.00.0 233.541_ 0.007 - Vel = 0.14
112 0.0 2.703 T 18.651 2.710 74.116
to 120.0 0.0 18.651 1.169
113 2.43 0.0 0.0 21.361 0.001 Vel = 0.14
0.0
2.43 75.286 K Factor = 0.28
NEW_ PATH__
215 4.62 2.703 T 18.651 2.710 76.287 _---
to 120.0 0.0 18.651 1.174
214 4.62 0.0001 0.0 21.361 0.002 Vel = 0.26
Computer Programs by Hydratec Inc. Revision: 50.52.1
C
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 14
2010771 - B1S2RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes "*"*
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
214 0.0 2.703 2X 33.571 199.970 75.115
to 120.0 0.0 33.571 0.143
114 4.62 0.0001 0.0 233.541 0.020 Vel = 0.26
114 0.0 2.703 T 18.651 2.710 74.992
to 120.0 0.0 18.651 1.169
115 4.62 0.0001 0.0 21.361 0.003 Vel = 0.26
0.0
4.62 76.164 K Factor = 0.53
NEW PATH
217 7.66 2.703 T 18.651 2.710 77.139
to 120.0 0.0 18.651 1.174
216 7.66 0.0002 0.0 21.361 0.005 Vel = 0.43
216 0.0 2.703 2X 33.571 199.970 75.970
to 120.0 0.0 33.571 0.143
116 Z66 0.0002 _ 0.0 233.541 0.051 -_ Vel = 0.4.3_-
116 0.0 2.703 T 18.651 2.710 75.878
to 120.0 0.0 18.651 1.169
117 7.66 0.0002_ _ 0.0 21.361 _ 0.005 _ Vel = 0.43
0.0
7.66 77.052 K Factor = 0.87
NEW PATH
219 11.63 2.703 T 18.651 2.710 77.974
to 120.0 0.0 18.651 1.174
218 11.63 0.0005 0.021.361 0.010 _ Vel =
218 0.0 2.703 2X 33.571 199.970 76.810
to 120.0 0.0 33.571 0.143
118 11.63 0.0005. 0.0 233.541 0.111 Vel = 0.65
118 0.0 2.703 T 18.651 2.710 76.778
to 120.0 0.0 18.651 1.169
119 11.63 0.0005 0.0 21.361 0.011 Vel = 0.65
0.0
11.63 77.958 K Factor = 1.32
NEW PATH
221 16.59 2.703 T 18.651 2.710 78.783
to 120.0 0.0 18.651 1.174
220 16.59 0.0009 0.0 21.361 0.020 Vel = 0.93
220 0.0 2.703 2X 33.571 199.970 77.629
to 120.0 0.0 33.571 0.143
120 --_ 16_59 _ 0.0009 - -- 0.0 233.541
2.710
0.214 Vel = 0.93
120 0.0 2.703 T 18.651 77.700 -
to 120.0 0.0 18.651 1.169
121 16.59 0.0009 0.0 21.361 0.020 Vel = 0.93
0.0
16.59 78.889 K Factor = 1.87
NEW PATH
223 22.59 2.703 T 18.651 2.710 79.558
0 120.0 0.0 18.651 1.174
222 22.59 0.0016 0.0 21.361 0.035 Vel = 1.26
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 15
2010771 - B1S2RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv ""••• Notes '•"'*
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
222 0.0 2.703 2X 33.571 199.970 78.419
to 120.0 0.0 33.571 0.143
122 22.59 0.0016 0.0 233.541 0.379 Vel = 1.26
122 0.0 2.703 T 18.651 2.710 78.655
to
Vel =
120.0 0.0 18.651 1.169
123 22.59 0.0016 0.0 21.361 0.035 Vel = 1.26
to
0.0
120.0
2X
0.0 33.571 0.143
22.59
124 ; d 29.68_
79.859 K Factor = 2.53
NEW PATH
0.0 233.5.41 0.628 ; Vel_= 01.66 _0
225 29.68 2.703 T 18.651 2.710 80.286
to
47.32
120.0
T
0.0 18.651 1.174
224 29.68 0.0027 0.0 21.361 0.058 Vel = 1.66
224 0.0 2.703 2X 33.571 199.970 79.170
Vel'-_ - 2.65
to
0.0
120.0
2X
0.0 33.571 0.143
124 ; d 29.68_ 0.0027 r 0.0 233.5.41 0.628 ; Vel_= 01.66 _0
124 0.0 2.703 T 18.651 2.710 79.655
2.65
to .
0.0
120.0
T
0.0 18.651 1.169
125 _ -29.68 0.0027 0.0 - 21.361 0.058 Vel = 1.66
129
0.0
0.0064 0.0 21.361 0.137 Vel = 2.65
29.68 80.882 K Factor = 3.30
NEW PATH
47.32 83.166 K Factor= 5.19
227 37.91 2.703 T 18.651 2.710 80.956
to
57.94
120.0
T
0.0 18.651 1.174
226 37.91 0.0042 O.0 21.361 _ 0.090 Vel = 2.12_
226 0.0 2.703 2X 33.571 199.970 79.872
3.24
to 120.0 0.0 33.571 0.143
126 37.91 0.0042 0.0 233.541 0.988 Vel = 2.12
126 0.0 2.703 T 18.651 2.710 80.717
to 120.0 0.0 18.651 1.169
127 37.91 0.0043 0.0 21.361 0.091 Vel = 2.12
0.0
37.91 81.977 K Factor = 4.19
NEW PATH
229 47.32 2.703 T 18.651 2.710 81.553
to 120.0 0.0 18.651 1.174
228 47.32 0.0064 0.0, - 21.361 0.136 Vel'-_ - 2.65
228 0.0 2.703 2X 33.571 199.970 80.515
to 120.0 0.0 33.571 0.143
128_ 47.32 0.0064 0.0 233.541 1.488 Vel = 2.65
128 0.0 2.703 T 18.651 2.710 81.860
to 120.0 0.0 18.651 1.169
129 47.32 0.0064 0.0 21.361 0.137 Vel = 2.65
0.0
47.32 83.166 K Factor= 5.19
NEW PATH
231 57.94 2.703 T 18.651 2.710 - 82.065
0 120.0 0.0 18.651 1.174
230 57.94 0.0093 0.0 21.361 0.198 Vel = 3.24
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 16
2010771 - B1S2RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
230 - 0.0 2.703 - ----_ 2X 33.571 199.970 81.089 - - - - -- -- _ --- - - - -- - -_---- -
to
0.0
120.0 0.0 33.571 0.143
130 57.94 0.0093 0.0 233.541 2.165 Vel = 3.24
130 0.0 2.703 T 18.651 2.710 83.111
to
0.0
120.0 0.0 18.651 1.169
131 57.94 0.0093. 0.0 21.361 0.198 Vel = 3.24
0.0
0.0
2X 33.571 199.970 81.587
57.94
to 120.0
84.478 K Factor= 6.30
NEW PATH
140.75
140.75
2.703
120.0
0.0479
T 18.651
0.0
0.0
2.710
18.651
21.361
82.953
1.174
1.023
236 0.0
233 69.81 2.703 T 18.651 2.710 82.481
0.0 33.571
to
136
120.0
0.0479
0.0 18.651 1.174
136 0.0
232 69.81 0.0131 0.0 21.361 0.280 Vel = 3.90
232 0.0 2.703 2X 33.571 199.970 81.587
0.0
to 120.0 0.0 33.571 0.143
132 69.81 0.0131 0.0 233.541 ,, ;__ 3.056 Vel = 3.90
132 0.0 2.703 T 18.651 2.710 84.500
to 120.0 0.0 18.651 1.169
133 69.81 0.0131 0.0 21.361 0.280 Vel = 3.90
0.0
69.81 85.949 -- K Factor = 7.53
NEW PATH
235 129.97 2.703 T 18.651 2.710 82.795
to 120.0 0.0 18.651 1.174
2_3_4 129.9_7_ 0.041_3_ -_ 0.0 - 21.361 _ 0.883 _ Vel = 7.2.7_-
234 0.0 2.703 2X 33.571 216.640 82.504
to 120.0 0.0 33.571 0.156
134 129.97 0.0413 0.0 250.211 10.339 Vel = 7.27
134 0.0 2.703 T 18.651 2.710 92.999
to 120.0 0.0 18.651 1.174
135 129.97 0.0413 0.0 21.361 0.882 Vel = 7.27
0.0
129.97 95.055 K Factor= 13.33
NEW PATH
237
to
236
140.75
140.75
2.703
120.0
0.0479
T 18.651
0.0
0.0
2.710
18.651
21.361
82.953
1.174
1.023
236 0.0 2.703 2X 33.571 216.640 82.802
to 120.0 0.0 33.571 0.156
136 140.75 0.0479 0.0 250.211 11.981
136 0.0 2.703 T 18.651 2.710 94.939
to 120.0 0.0 18.651 1.174
137 140.75 0.0479 0.0 21.361 1.023
0.0
140.75 97.136
Computer Programs by Hydratec Inc. Revision: 50.52.1
Vel = 7.87
Vel = 7.87
Vel = 7.87
K Factor= 14.28
AutoPeaking Summary
Wiginton Fire Systems Page 17
2010771 - B1S2RA1 Date 5-19-17
Auto Peaking Summary - List of Pipes for Area Calculated
Left Right
Side Side
From To Length From To Length
H4 100 85.210 H1 200 84.730
H8 102 85.210 202 H5 84.730
H12 104 85.210 204 H9 84.730
H4 100 85.210 H1 200 84.730
H8 102 85.210 202 H5 84.730 '
H12 104 85.210 204 H9 84.730
Flow Safety Pressure
Required Margin Differential
Left 10.000 1709.930 12.212 0.067
Area Calculated 1709.928 12.145 0.000
Right 10.000 1709.970 12.210 0.066
Typical Distance Between Heads = 10.000
Split Point Used in Worst Area Peaked = H3
Split Point Used in Area Calculated = H3
Computer Programs by Hydratec Inc. Revision: 50.52.1
H'Dg)'0MRqM
FIRE SYSTEMS
Wiginton Fire Systems
699 Aero Lane
Sanford, FL 32771
407-585-3200
Job Name 2010771 - B1S3RA1
Drawing FP6
Location BUILDING ONE
Remote Area B1S3RA1
Contract 2010771
Data File 2010771 - B1S3RA1.WXF
Computer Programs by Hydratec Inc. Revision: 50.52.1
W
Wiginton Fire Systems
2010771-B1S3RA1
Page 1
Date 5-19-17
Project name: GANESH NORTH
Location: BUILDING ONE
Drawing no: FP6
Date: 5-19-17
Design
HYDRAULIC CALCULATIONS
for
Remote area number: B1S3RA1
Remote area location: SYSTEM THREE
Occupancy classification: HIGH PILED STORAGE
Density: 52 PSI - Gpm/SgFt
Area of application: 12 HEADS - SgFt
Coverage per sprinkler: 100 MAX - SgFt
Type of sprinklers calculated: 16.81K ESFR PENDENT
No. of sprinklers calculated: 12
In -rack demand: N/A - GPM
Hose streams: 250 - GPM
Total water required (including hose streams): 1713.391 - GPM @ 42.677 - Psi
Type of,system: WET
Volume' of dry or preaction syst6m: N/A - Gal
Water supply information
Date: 8-2-16
Location: ALONG W. 1ST STREET
Source: WFS
Name of contractor: WIGINTON FIRE SYSTEMS
Address: 699 AERO LANE, SANFORD, FL 32771
Phone number: 407-585-3200
Name of designer: W. AMMONS
Authority having jurisdiction: CITY OF SANFORD
Notes: (Include peaking information or gridded systems here.)
Computer Programs by Hydratec Inc. Revision: 50,52.1
Water ply Curve C
Wiginton Fire Systems
Page 2
2010771 - B1S3RA1
Date 5-19-17
City Water Supply:
C1 - Static Pressure : 60
C2 - Residual Pressure: 50
C2 - Residual Flow : 1840
City Water Adjusted to Pump Inlet
for Pf - Elev - Hose Flow
Al - Adjusted Static:
A2 - Adj Resid
A3 - Adj Resid
54.436
33.185 @ 1261.31
10.52 @ 1881.1
Pump Data:
P1 - Pump Churn Pressure 126.18
P2 - Pump Rated Pressure 109.95
P2 - Pump Rated Flow 1261.31
P3 - Pump Pressure @ Max Flow 79.39
P3 - Pump Max Flow 1881..x,
City Residual Flow @ 0 4846.63
City Residual Flow @ 20 3892.74
City Water @ 150% of Pump 49.58
Demand:
01 - Elevation 14.197
D2 - System Flow 1463.39
D2 - System Pressure 120.681
Hose ( Demand )
D3 - System Demand 1463.39
Hose ( Adj City) 250
Safety Margin 8.559
210
196
182
Al +1P1
p 168
R 154 A2+P2
E 140
S 126
S 112
U 98
R 84
E 70 C1
56
42 Al AZ
28
14 D1
200 400 600 800 1000 1200 1400 1600 1800
FLOW (N^1.85)
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow Diagram
Wiginton Fire Systems
2010771 - B1S3RA1
118.7240.8 481.5 807.3 972 1133 1295.6 1463.4 1463.4 1463.4
H3 +-H4 +-100+-101+-103-105+-107+-109+-111+-113+-115+-117+-119+-121+-123+- 125+- 127+-TR3+-8R3+-PO
240.8 240.8 721.8 890.4 1052.6 1213.9 1378.6 1463.4 1463.4
1463.4 1713.4 1713.4
PI +- SPIG- UG3+- UG4+- UG5+- UG6*- TEST
1463.4 1713.4 1713.4
2.4 246.6 246.6 741.6 573 410.8 249.5 84.8 84.8
H3 +- H2 +- H1 +- 200 +- 201 +- 203 +- 205 +- 207 +- 209 +- 211 +- 213 +- 215 +- 217 +- 219 +- 221 +- 223 +- 222 +- 122 +- 123
123.7 246.6 493.5 656.1 491.4 330.3 167.8 84.8 84.8
Page 3
Date 5-19-17
246.9 124 118.6 240.7
203 - 202 - H5 -* H6 - H7 +- H8 +- 102 +- 103
t 246.9 26 240.7 1
1 493.5 1 481.5
1 248.1 124.9 118 24%3
205 -a 204 - H9 -+ H10 H11 H12+- 104 105
1 248.1 34 240.3
1 741.6
1 85.5 85.5
207 +- 206 +- 106 +- 107
t 85.5 t
1 656.1 1 807.3
1 83.1 83.1
209 +- 208 i- 108 +- 109
1 83.1 1
1 573 1 890.4
1 81.5 81.5
211*- 210+- 110+- 111
1 • 81.5 1
1 095.4 1 972 "
1 80.6 80.0
213+- 212+- 112+- 113
1 80.6 1
1 410.8 1 1052.6
1 80.4 80.4
215 +- 214 +- 114 +- 115
1 80.4 1
1 330.3 1 1133
1 80.8 80.0
217 +- 216 +- 116 +- 117
1 80.8 t
1 249.5 1 1213.9
1 81.7 81.T
219+- 218+- 118+- 119
1 81.7 t
1 167.8 1 1295.6
1 83.1 83.1
221 +- 220 +- 120 +- 121
83.1
Computer Programs by Hydratec Inc. Revision: 50.52.1
Fittings d Summary
Wiginton Fire Systems Page 4
2010771 - 61 S3RA1 Date 5-19-17
Fitting Legend
Abbrev. Name : %: '/. 1 1'/. 1'/: 2 _ 2%x 3 3'/: 4 5 6 8 10 12 14 16 18 20 24
B Generic Butterfly Valve 0 0 0 0 0 0 7 10 0 12 9 10 12 19 21 0 0 0 0 0E90' Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61GGenericGateValve00000111122345678101113LLongTurnElbow1122234556891316182427303440SGenericSwingCheckValve4557911141619222732455565768798109130T90' Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121V90'Ell Firelock #001 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 0 0 0 0 0 0 0X90'Tee-BranchFirelock002 0 0 0 0 0 8.5 10.8 13 0 16 21 25 33 0 0 0 0 0 0 0ZafAmes3000SSFittinggeneratesaFixedLossBasedonFlow
Units Summary
Diameter Units
Length Units
Flow Units
Pressure Units
Inches
Feet
US Gallons per Minute
Pounds per Square Inch
Computer Programs by Hydratec Inc. Revision: 50.52.1
Pressure / Flow Summary - STANDARD
Wiginton Fire Systems Page 5
2010771 - B1S3RA1 Date 5-19-17
Node Elevation K -Fact Pt Pn Flow Density Area Press
No.__ Actual Actual Req.
H3 34.78 16.8 52.0 na 121.15 0.1 100 52.0
H4 35.2 16.8 52.76 na 122.03 0.1 100 52.0
100 34.16 86.53 na
101 31.45 93.43 na
103 31.45 93.44 na
105 31.45 93.5 na
107 31.45 93.63 na
109 31.45 93.78 na
111 31.45 93.96 na
113 31.45 94.18 na
115 31.45 94.43 na
117 31.45 94.72 na
119 31.45 95.04 na
121 31.45 95.41 na
123 31.45 95.83 na
125 31.45 97.23 na
127 29.12 102.06 na
TR3 29.12 102.94 na
BR3 2.0 119.03 na
PO 2.0 120.68 na
PI 2.0 26.34 na
SPIG -3.0 29.23 na
UG3• '' -3.0 32.54'' na 250:0''
UG4 -3.0 43.25 na
UG5 -3.0 48.39 na
UG6 -3.0 52.19 na
TEST 2.0 51.24 na
H2 34.41 16.8 52.16 na 121.33 0.1 100 52.0
H1 33.95 16.8 53.48 na 122.86 0.1 100 52.0
00 32.09 74.89 na
01 29.38 82.04 na
203 29.38 82.16 na
205 29.38 82.58 na
207 29.38 83.48 na
209 29.38 84.19 na
211 29.38 84.75 na
213 29.38 85.16 na
215 29.38 85.46 na
217 29.38 85.67 na
219 29.38 85.78 na
221 29.38 85.84 na
223 29.38 85.86 na
222 32.09 85.51 na
122 34.16 93.82 na
202 32.09 74.99 na
H5 33.95 16.8 53.54 na 122.92 0.1 100 52.0
H6 34.41 16.8 52.21 na 121.39 0.1 100 52.0
H7 34.78 16.8 52.05 na 121.2 0.1 100 52.0
H8 35.2 16.8 52.81 na 122.09 0.1 100 52.0
102 34.16 86.55 na
204 32.09 75.36 na
H9 33.95 16.8 53.73 na 123.14 0.1 100 52.0
H10 34.41 16.8 52.38 na 121.59 0.1 100 52.0
H11 34.78 16.8 52.22 na 121.4 0.1 100 52.0
H12 35.2 16.8 52.98 na 122.28 0.1 100 52.0
104 34.16 86.62 na
206 32.09 83.15 na
106 34.16 91.61 na
208 32.09 83.82 na
108 34.16 91.81 na
210 32.09 84.34 na
110 34.16 92.02 na
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow Summary - Standard
Wiginton Fire Systems Page 6
2010771 - B1S3RA1 Date 5-19-17
Node Elevation K -Fact Pt Pn Flow Density Area Press
No. ActualActual Req.
212 32.09 84.75 na
112 34.16 92.25 na
214 32.09 85.04 na
114 34.16 92.5 na
216 32.09 85.25 na
116 34.16 92.79 na
218 32.09 85.39 na
118 34.16 93.1 na
220 32.09 85.47 na
120 34.16 93.44 na
The maximum velocity is 20.88 and it occurs in the pipe between nodes 205 and 204
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 7
2010771 - B1S3RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
EQUIVALENT_ K'S
REMOTE HEAD TO SUPPLY
H3 118.74 2.203 0.0 10.000 52.000 K Factor = 16.80
to 120.0 0.0 0.0 0.182
H4 118.74 0.0947 0.0 10.000 0.947 Vel = 9.99
H4 122.04 2.203 X 11.593 83.570 52.765 K Factor = 16.80
to 120.0 0.0 11.593 0.450
100 240.78 0.3501 0.0 95.163 33.314 Vel = 20.27
100 0.0 2.203 T 13.639 2.710 86.529
to 120.0 0.0 13.639 1.174
101 240.78 0.3501_ 0.0 16.349 5.723 Vel = 20.27
101 0.0 6.385 0.0 8.330 93.426
to 120.0 0.0 0.0 0.0
103 240.780.0020 0.0 8._330 0.017 Vel = 2.41.
103 240.68 6.385 0.0 8.330-i 93.443
to 120.0 0.0 0.0 0.0
105 481.46 0.0071 0.0 8.330 0.059 Vel = 4.82
105 240.32 6.385 0.0 8.330 93.502
to 120.0 0.0 0.0 0.0
107 721.78 0.0150 0.0 8.330 0.125 Vel = 7.23
107 85.52 6.385 0.0 8.330 93.627
to 120.0 0.0 0.0 0.0
109 807.3 0.0184 0.0 8.330 0.153 Vel = 8.09
109 83.14 6.385 0.0 8.330 93.780
to 120.0 0.0 0.0 0.0
111 890.44 0.0221 0.0 8.330 0.184 _ Vel = 8.92
111 81.53 6.385 0.0 8.330 93.964
to 120.0 0.0 0.0 0.0
113 971.97 0.0261 _ 0.0 8.330 0.217 Vel = 9.74
113 80.65 6.385 0.0 8.330 94.181
to 120.0 0.0 0.0 0.0
115 1052.62 0.0301 0.0 8.330 0.251 Vel = 10.55
115 80.43 6.385 0.0 8.330 94.432
to 120.0 0.0 0.0 0.0
117 1133.05 0.0345 0.0 8.330 0.287 Vel = 11.35
117 80.81 6.385 0.0 8.330 94.719
to 120.0 0.0 0.0 0.0
119 1213.86 0.0391 0.0 _ 8.330 0.326 Vel = 12.16
119 81.72 6.385 0.0 8.330 95.045
to 120.0 0.0 0.0 0.0
121 1295.58 0.0443 0.0 8.330 0.369 Vel = 12.98
121 83.06 6.385 0.0 8.330 95.414
to 120.0 0.0 0.0 0.0
123 1378.64 0.0496 0.0 8.330 0.413 Vel = 13.81
123 84.75 6.385 V 12.845 12.500 95.827
to 120.0 0.0 12.845 0.0
125 1463.39 0.0554 0.0 25.345 1.404 Vel = 14.66
125 0.0 6.385 V 12.845 56.040 97.231
to 120.0 0.0 12.845 1.009
127 1463.39 0.0554 0.0 68.885 3.816 Vel = 14.66
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 8
2010771 - B1S3RA1 Date 5-19-17
Hyd, Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
127 0.0 6.385 V 12.845 3.080 102.056
to 120.0
120.681
0.0 12.845 0.0
TR3 1463.39 0.0554
0.0
0.0 15.925 0.882 Vel = 14.66
TR3 0.0 6.385 T 38.536 27.120 102.938
to
1713.39
120.0 B 12.845 51.381 11.746
BR3 1463.39 0.0554 0.0 78.501 4.347 Vel = 14.66
BR3 0.0 8.249 2V 28.914 11.375 119.031
to
38.923
120.0 B 13.345 92.303 0.0
PO 1463.39 0.0159 S 50.044 103.678 1.650 Vel = 8.79
0.0
0.0 12.34 T 88.164 450.000 52.189
1463.39
to 140.0
120.681 K Factor = 133.21
System Demand Pressure
TEST 1713.39
120.681
0.0
Safety Margin
1.213 Vel = 4.60
8.559
Continuation Pressure 129.240
1713.39
Pressure @ Pump,Outlet
51.236
129.240 a
Pressure From Pump Curve 102.903
H3
Pressure @ Pump Inlet
2.203 0.0 9.000
26.337
PI 0.0 8.249 T 38.923 2.500 26.337
0.160
to 120.0 G 4.448 43.371 2.166
9.000
SPIG 14_63.39_ _0.0159 0.0 45.871_ 0.729
29.232 -----
Vel = 8.79
SPIG 0.0 8.27 E 26.955 195.000
to 140.0 T 52.413 85.358 0.0
123.74
UG3 1463.39 _ 0.0118_ G 5.99 280.358 3.313 Vel = 8.74_
UG3 250.00 8.27 T 52.413 300.000 32.545 Qa = 250
to 140.0 Zaf 0.0 130.283 3.901 Fixed Loss = 3.901
UG4 1713.39 0.0158 _ 4L 77.87 430.283 6.807 Vel = 10.23
UG4 0.0 10.28 T 71.092 865.000 43.253
to 140.0 0.0 71.092 0.0
UG5 1713.39 0.0055 0.0 936.092 5.133 Vel = 6.62
UG5 0.0 12.34 T 88.164 1600.000 48.386
to 140.0 0.0 88.164 0.0
UG6 1713.39 0.0023 0.0 1688.164 3.803 Vel = 4.60
UG6 0.0 12.34 T 88.164 450.000 52.189
to 140.0 0.0 88.164 2.166
TEST 1713.39 0.0023 0.0 538.164 1.213 Vel = 4.60
0.0
1713.39 51.236 K Factor = 239.37
NEW PATH
H3 2.40 2.203 0.0 9.000 52.000
to 120.0 0.0 0.0 0.160
H2 2.4 0.0001 0.0 9.000 0.001 Vel = 0.20
H2 121.34 2.203 0.0 11.000 52.161 K Factor = 16.80
to 120.0 0.0 0.0 0.199
H1 123.74 0.1022 0.0 11.000 1.124 Vel = 10.42
H1 122.86 2.203 X 11.593 44.700 53.484 K Factor = 16.80
to 120.0 0.0 11.593 0.806
200 246.6 0.3659 0.0 56.293 20.597 Vel = 20.76
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems
2010771 - B1S3RA1
Page 9
Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. C" or Ftng's Pe Pv "••••• Notes "•"`
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
200 0.0 2.203 T 13.639 2.710 74.887
to
to
0.0
120.0 0.0 13.639 1.174
0.0507 0.0 _
201 246.6 0.3659 0.0 16.349 5.982 Vel = 20.76
201. 0.0 4.304 0.0 8.330 82.043
123 84.75
to
0.0
120.0 0.0 0.0 0.0
203 246.6 0.0140 0.0 8.330 0.117 Vel = 5.44
203 246.92 4.304 0.0 8.330 82.160
to 120.0 0.0 0.0 0.0
205 493.52 0.0505 0.0 8.330 0.421 Vel = 10.88
205 248.09 4.304 0.0 8.330 82.581
to 120.0 0.0 0.0 0.0
207 741.61 0.1076 0.0 8.330 0.896 Vel = 16.35
207 85.51 4.304 0.0 8.330 83.477
to 120.0 0.0 0.0 0.0
209 656.1 0.0857 0.0 8.330 0.71_4 Vel = 14.47
209 83.14 4.304 0.0 8.330 84.191
to 120.0 0.0 0.0 0.0
211 572.96 _-0.0667 0.0 8.330 0.556 Vel = 12.63
211 81.54 4.304 0.0 8.330 84.747
to 120.0 0.0 0.0 0.0
213 _ _ 491.42 0.0502 _ _ 0.0_ - 8.330 0.418 _ Vel = 10.84
213 80.65 4.304 0.0 8.330 85.165
to 120.0 0.0 0.0 0.0
215 410.77 0.0360_ 0.0 8.330 0.3_00 Vel = 9.06_
215 80.43 4.304 0.0 8.330 85.465
to 120.0 0.0 0.0 0.0
217 ----- 330.34 0.0241 -- 0.0 8.330 0.201 Vel = 7.28
217 80.81 4.304 0.0 8.330 85.666
to 120.0 0.0 0.0 0.0
219 249.53 0.0143 0.0 8.330 0.119 Vel = 5.50
219 81.72 4.304 0.0 8.330 85.785
to 120.0 0.0 0.0 0.0
221 167.81 0.0070 0.0 8.330 0.058 Vel = 3.70
221 83.06 4.304 0.0 8.330 85.843
to 120.0 0.0 0.0 0.0
223 84.75 0.0019 0.0 8.330 0.016 Vel = 1.87
223 0.0 2.203 T 13.639 2.710 85.859
to 120.0 0.0 13.639 1.174
222 84.75 0.0507 0.0 16.349 0.829 Vel = 7.13
222 0.0 2.203 2X 23.186 158.300 85.514
to 120.0 0.0 23.186 0.897
122. 84.75 0.0507 0.0 _ 181.486 9.207 Vel = 7.13
122 0.0 2.203 T 13.639 2.710 93.824
to 120.0 0.0 13.639 1.174
123 84.75 0.0507 0.0 16.349 0.829 Vel = 7.13
0.0
84.75 95.827 K Factor= 8.66
NEW PATH
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 10
2010771 - B1S3RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv rrrrrrr Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
203 -246.92 2.203 T 13.639 2.710 82.160
to 120.0 0.0 13.639 -1.174
202 -246.92 -0.3668 0.0 16.349 -5.997 Vel = 20.78
202 0.0 2.203 X 11.593 44.700 74.989
82.581
to
to
120.0 0.0 11.593 0.806
13.639
H5 246.92 0.3668 0.0 56.293 20.647 Vel = 20.78
H5 122.92 2.203 0.0 11.000 53.536 K Factor = 16.80
to
44.700
120.0 0.0 0.0 0.199
120.0
H6 124.0 0.1025 0.0 11.000 1.128 Vel = 10.44
H6 121.39 2.203 0.0 9.000 52.209 K Factor = 16.80
to
2.203
120.0 0.0 0.0 0.160
K Factor = 16.80
H7 ___ 2.61 0.0001 0.0 _ 9.000 0.00_1 _ _ Vel = 0.22
H7 121.20 2.203 0.0 10.000 52.048 K Factor = 16.80
to
Vel = 10.52
120.0 0.0 0.0 0.182
0.0
H8 118.59,_ 0.0944 L0.0_ 10.000 0.944 Vel = 9.98
H8 122.09 2.203 X 11.593 83.570 52.810 K Factor = 16.80
to
0.0
120.0 0.0 11.593 0.450
121.40
102 240.68 0.3498 0.0 95.163 33.290 Vel = 20.26
102 0.0 2.203 T 13.639 2.710 86.550
to
118.05
120.0 0.0 13.639 1.174
0.936
103 240.68 0.3498 0.0 16.349 5.719 Vel = 20.26
52.975
0.0
to 120.0 0.0 11.593
240.68
104 240.33
93.443 K Fnr-tnr = 7d Un
NEW PATH
205 248.08 2.203 T 13.639 2.710 82.581
to 120.0 0.0 13.639 1.174
204 248.08 0.3699 0.0 16.349 6.048 Vel = 20.88_
204 0.0 2.203 X 11.593 44.700 75.359
to 120.0 0.0 11.593 0.806
H9 248.08 0.3700 0.0 56.293 20.827 Vel = 20.88
H9 123.14 2.203 0.0 11.000 53.726 K Factor = 16.80
to 120.0 0.0 0.0 0.199
H10 124.94 0.1041 0.0 11.000 1.145 Vel = 10.52
H10 121.59 2.203 0.0 9.000 52.382 K Factor = 16.80
to 120.0 0.0 0.0 0.160
H11 3.35 0.0001 0.0 9.000 0.001 Vel = 0.28
H11 121.40 2.203 0.0 10.000 52.221 K Factor = 16.80
to 120.0 0.0 0.0 0.182
H12 _ 118.05 0.093_6 0.0 10.000 0.936 Vel = 9.94
H12 122.28 2.203 X 11.593 83.570 52.975 K Factor = 16.80
to 120.0 0.0 11.593 0.450
104 240.33 0.3489 0.0 95.163 33.200 Vel = 20.23
104 0.0 2.203 T 13.639 2.710 86.625
to 120.0 0.0 13.639 1.174
105 240.33 0.3488 0.0 16.349 5.703 Vel = 20.23
0.0
240.33 93.502 K Factor = 24.85
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 11
2010771 - B1S3RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
NEW PATH
207 85.51 2.203 T 13.639 2.710 83.477
84.191
to 120.0 0.0 13.639 1.174
0..0.)
206 85.51 0.0516 0.0 16.349. 0.843 Vel = 7.20
206 0.0 2.203 2X 23.186 158.300 83.146
208
to
2.203
120.0 0.0 23.186 0.897
106 85.51 0.0516 0.0 181.486 9.361 Vel = 7.20
106 0.0 2.203 T 13.639 2.710 91.610
0.0
to
181.486
120.0 0.0 13.639 1.174
0.0
107 85.51 0.0516 0.0 16.349 0.843 Vel = 7.20
to
0.0
120.0 0.0 13.639 1.174
85.51
109 _ 83.14 0.0489
93.627 K Factor= 8.84
NEW PATH
0.800 Vel = V 7.00
0.0
209 83.14 2.203 T 13.639 2.710 84.191
alto 1,20.0 0..0.) 13.639 1;174 d
208 _ _ 83.14 0.0490 0.0 ------ 16.349 0.801 Vel = 7.00
208 0.0 2.203 2X 23.186 158.300 83.818
to 120.0 0.0 23.186 0.897
108 83.14 0.0490 _ 0.0 181.486 8.885 Vel = 7.00
108 0.0 2.203 T 13.639 2.710 91.806
to 120.0 0.0 13.639 1.174
109 _ 83.14 0.0489 0.0 16.349 0.800 Vel = V 7.00
0.0
83.14 93.780 _ _ _ K Factor = 8.59
NEW PATH
211 81.53 2.203 T 13.639 2.710 84.747
to 120.0 0.0 13.639 1.174
210 81.53 0.0472 0.0 16.349 0.772 Vel = 6.86
210 0.0 2.203 2X 23.186 158.300 84.345
to 120.0 0.0 23.186 0.897
110 81.53 0.0472 0.0 181.486 8.570 Vel = 6.86
110 0.0 2.203 T 13.639 2.710 92.018
to 120.0 0.0 13.639 1.174
111 81.53 0.0472 0.0 16.349 0.772 Vel = 6.86
0.0
81.53 93.964 K Factor = 8.41 , .
NEW PATH
213 80.65 2.203 T 13.639 2.710 85.165
to 120.0 0.0 13.639 1.174
212 80.65 0.0463 _ 0.0 16.349 0.757 Vel = 6.79
212 0.0 2.203 2X 23.186 158.300 84.748
to 120.0 0.0 23.186 0.897
112 80.65 0.0463 0.0 181.486 8.399 Vel = 6.79
112 0.0 2.203 T 13.639 2.710 92.250
to 120.0 0.0 13.639 1.174
113 80.65 0.0463 0.0 16.349 _ 0.757 Vel = 6.79
0.0
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 12
2010771 - B1S3RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv '•""' Notes •""'
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
80.65 94.181 K Factor= 8.31
NEW PATH
215 80.43 2.203 T 13.639 2.710 85.465
16.349
120.0
to
23.186
120.0
118
0.0 13.639 1.174
181.486 8.606 Vel = 6.88
214 80.43 0.0461
T 13.639
0.0 16.349 0.753 Vel = 6.77
214 0.0 2.203 2X 23.186 158.300 85.044
16.349 0.775 Vel = 6.88
to
0.0
120.0 0.0 23.186 0.897
81.72
114 80.43 0.0461 0.0 181.486 8.358 Vel = 6.77
114 0.0 2.203 T 13.639 2.710 92.505
to 120.0 0.0 13.639 1.174
115 80.43 0.0461 0.0 16.349 0.753 Vel = 6.77
0.0
80.43 94.432 K Factor= 8.28
NEW PATH
217 80.81 2.203 T 13.639• '' 2.710 85.6661
to 120.0 0.0 13.639 1.174
216 _ _ 80.81 0.0465 -------0.0 1_6.349_______ 0.760 - 6_._8.0_
216 0.0 2.203 2X 23.186 158.300 85.252
Vel
to 120.0 0.0 23.186 0.897
116 80.81 0.0465 0.0 181.486 8.431 Vel = 6.80
116 0.0 2.203 T 13.639 2.710 92.786
to 120.0 0.0 13.639 1.174
1-17 80.81 0.0464 ------- 0.0 16.349 0.759 Vel = 6.80
0.0
80.81_- 94.719 -__ K Factor= 8.30_
NEW PATH
219 81.72 2.203 T 13.639 2.710 85.785
to 120.0 0.0 13.639 -1.174
218 81.72 0.0475 0.0 16.349 0.776 Vel = 6.88
218 0.0 2.203 2X 23.186 158.300 85.387
to
16.349
120.0 0.0 23.186 0.897
118 81.72 0.0474 0.0 181.486 8.606 Vel = 6.88
118 0.0 2.203 T 13.639 2.710 93.096
to
16.349
120.0 0.0 13.639 1.174
119 81.72 0.0474 0.0 16.349 0.775 Vel = 6.88
0.0
81.72 95.045 K Factor = 8.38
NEW PATH
2.710 _- 221 83.06 2.203
to
16.349
120.0
220 83.06 0.0489
220 0.0 2.203
to
181.486
120.0
120 83.06 0.0489
120 0.0 2.203
0
16.349
120.0
121 83.06 0.0489
T - - 13.639 2.710 _- 85.843 - -- ---
0.0 13.639 1.174
0.0 16.349 0.799
2X 23.186 158.300 85.468
0.0 23.186 0.897
0.0 181.486 8.870
T 13.639 2.710 93.441
0.0 13.639 1.174
0.0 16.349 0.799
Computer Programs by Hydratec Inc. Revision: 50.52.1
Vel = 6.99
Vel = 6.99
Vel = 6.99
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 13
2010771 - B1S3RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv "•••'• Notes '•'•"
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
0.0
83.06 95.414 K Factor= 8.50
Computer Programs by Hydratec Inc. Revision: 50.52.1
AutoPeaking Summary
Wiginton Fire Systems Page 14
2010771 - B1S3RA1 Date 5-19-17
Auto Peaking Summary - List of Pipes for Area Calculated
Left Right
Side Side
From To Length From To Length
H4 100 83.570 H1 200 44.700
H8 102 83.570 202 H5 44.700
H12 104 83.570 204 H9 44.700
H4 100 83.570 H1 200 44.700
H8 102 '''' 83.570 202 H5 44700
H12 104 83.570 204 H9 44.700
Flow Safety Pressure
Required Margin Differential
Left 10.000 1713.168 8.703 0.145
Area Calculated 1713.391 8.559 0.000
Right 10.000 1713.787 8.854 0.295
Typical Distance Between Heads = 10.000
Split Point Used in Worst Area Peaked = H3
Split Point Used in Area Calculated = H3
Computer Programs by Hydratec Inc. Revision: 50.52.1
M
0 0
Rom
FIRE SYSTEMS
Wiginton Fire Systems
699 Aero Lane
Sanford, FL 32771
407-585-3200
Job Name 2010771'- B1S4RA1
Drawing FP7/FP8
Location BUILDING ONE
Remote Area B1S4RA1
Contract 2010771
Data File 2010771 - B1S4RA1.WXF
Computer Programs by Hydratec Inc. Revision: 50.52.1
M
Wiginton Fire Systems
2010771 - B1S4RA1
Page 1
Date 5-19-17
HYDRAULIC CALCULATIONS
for
Project name: GANESH NORTH
Location: BUILDING ONE
Drawing no: FP7/FP8
Date: 5-19-17
Design
Remote area number. B1S4RA1
Remote area location: SYSTEM FOUR
Occupancy classification: HIGH PILED STORAGE
Density: 52 PSI - Gpm/SgFt
Area of application: 12 HEADS - SgFt
Coverage per sprinkler: 100 MAX - SgFt
Type of sprinklers calculated: 16.8K ESFR PENDENT
No. of sprinklers calculated: 12
In -rack demand. N/A - GPM
Hose streams: 250 - GPM
Total water required (including hose streams): 1710.737 - GPM
Type of system: WET-
Volume of dry or preaction system: N/A - Gal
Water supply information
Date: 8-2-16
Location: ALONG W. 1ST STREET
Source: WFS
Name of contractor. WIGINTON FIRE SYSTEMS
Address: 699 AERO LANE, SANFORD, FL 32771
Phone number. 407-585-3200
Name of designer. W. AMMONS
Authority having jurisdiction: CITY OF SANFORD
Notes: (Include peaking information or gridded systems here.)
@ 33.655 - Psi
Computer Programs by Hydratec Inc. Revision: 50.52.1
Water )ly Curve C
Wiginton Fire Systems Page 2
2010771 - B1S4RA1 Date 5-19-17
City Water Supply:
C1 - Static Pressure 60
C2 - Residual Pressure: 50
C2 - Residual Flow 1840
City Water Adjusted to Pump Inlet
for Pf - Elev - Hose Flow
1261.31
Al - Adjusted Static: 54.436
A2 - Adj Resid
A3 - Adj Resid
33.185 @ 1261.31
10.52 @ 1881.1
Pump Data:
P1 - Pump Churn Pressure 126.18
P2 - Pump Rated Pressure 109.95
P2 - Pump Rated Flow 1261.31
P3 - Pump Pressure @ Max Flow 79.39
P3 - Pump Max Flow 1881.1
City Residual Flow @ 0 4846.63
City Residual Flow @ 20 3892.74
City Water @ 150% of Pump 49.58.
Demand:
D1 - Elevation 14.890
D2 - System Flow 1460.74
D2 - System Pressure 111.833
Hose ( Demand )
D3 - System Demand 1460.74
Hose ( Adj City) 250
Safety Margin 17.606
210
196
AI+P1
182
p 168
R 154 A2+P2
E 140
S 126
D2
S 112
U 98
R 84
E 70 C1
56
42 AZ
28
14 D1
200 400 600 800 1000 1200 1400 1600 1800
FLOW N^1.85)
Computer Programs by Hydratec Inc. Revision:; 50.52.1
Flow D am
Wiginton Fire Systems
2010771 - B1S4RA1
119.6 241.3 483.4 787.2 893.9 982.6 1061.1 1137.6 1219.9 1314.1 1460.7 1460.7 1460.7
H3 +- H4 +- 100 +- 101 + 103 +- 105 +- 107 + 109 +- 111 +- 113 + 115 +- 117 119 +- 121 +- 123 +- 125 +- 127 t 129 +- 131 +-"133 i- 135 +- 137 139 F TR4<- BR4F PO
241.3 241.3 724.7 843.3 940 10226 1099.1 1177.6 1265.2 1366.9 1460.7 1460.7
1460.7 1710.7 1710.7
PI +- SPlr- UG3+- UG4+- UG5i- UG6+- TEST
1460.7 1710.7 1710.7
1.6 244.9 244.9 736.1 617.4 520.7 438.1 361.6 283.1 195.5 93.8 93.8
H3 +- H2 +- Hi F 200 +- 201 203 +- 205 +- 207 +- 209 F 211 +- 213 +- 215 +- 217 +- 219 + 221 +- 223 +- 225 +- 227 <- 229 F 231 +- 233 +- 235 +- 234 +- 134 135
122.9 2449 489.6 6735 566.8 478.1 399.6 323.1 240.8 146.7 93.8 93.8
244.7 122.6 120.2 242.1
203 - 202 H5 -+ H6 H7 H8 +- 102 + 103
T 244.7 1.1 242.1 t
1 489.6 1 483.4
1 246.4 124.1 119.1 24143
205 - 204 -+ H9 - H10- H/1 e- H12+ 104+- 105
T 246.4 2.4 241.3
1 736.1
1 62.5 625
207+- 206+- 106+- 107
t 62.5 t
1 673.5 1 787.2
1 56.1 56.1
209+ 208(.- 108+ 109
T 56.1 t
1 617.4 1 843.3
1 50.6 50.6
211 210+- 110+- 111
T 50.6 t
1 566.8 1 893.9
1 46.1 46.1
213+ 212+- 112+ 113
T 461 t
1 520.7 1 940
1 42.6 42.6
215+- 214+- 114+ 115
T 42.6 t
1 478.1 1 982.6
1 40 401
217+- 216+- 116+- 117
t 40 t
1 438.1 1 1022.6
1 38.5 38.$
219+- 218+- 118+- 119
T 38.5 t
1 399.6 1 1061.1
1 38 381
221 + 220 +- 120+- 121
t 38 t
1 361.6 1 10991
1 38.5 38.5
223+- 222 + 122*- 123
t 38.5 t
1 323.1 1 1137.6
1 40 401
225+- 224 F 124+- 125
T 40 t
1 283.1 1 1177.6
Computer Programs by Hydratec Inc. Revision: 50.52.1
Page 3
Dafe 5-19-17
Flow [ am
Wiginton Fire Systems
2010771 - 61 S4RA1
Page 4
Date 5-19-17
1 42.3 42.0
227 F 226 +-126 +- 127
T 42.3 T
1 240.8 1 1219.9
1 45.3 45.}
229 +- 228 128 +- 129
T 45.3 T
1 195.5 1 1265.2
1 48.8 48.a
231 230. 130. 131
T 48.8 T
1 146.7 1 1314.1
1 52.9 52 V
233 +- 232 +- 132 E- 133
52.9
Computer Programs by Hydratec Inc. Revision: 50.52.1
Fitting d Summary
Wiginton Fire Systems
Page 5
2010771 - 131S4RA1
Date 5-19-17
Fitting Legend
Abbrev_ Name _ '/: '/. 1 1'/. 1 %: 2 2'% 3 3'/: 4 5 6 8 10 12 14 16 18 20 24
B Generic Butterfly Valve 0 0 0 0 0 0 7 10 0 12 9 10 12 19 21 0 0 0 0 0E90' Standard Elbow 2 2 2 3 4 5 6 7 8 10 _ 12 14 18 22 27 35 40 45 50 61GGenericGateValve00000111122345678101113LLongTumElbow1122234 * 5 5 6 8 9 13 16 18 24 27 30 34 40SGenericSwingCheckValve4557911141619222732455565768798109130T90' Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121V90'Ell Firelock #001 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 0 0 0 0 0 0 0X90'Tee-BranchFirelock002 0 0 0 0 0 8.5 10.8 13 0 16 21 25 33 0 0 0 0 0 0 0ZafAmes3000SSFittinggeneratesaFixedLossBasedonFlow
Units Summary
Diameter Units
Length Units
Flow Units
Pressure Units
Inches
Feet
US Gallons per Minute
Pounds per Square Inch
Computer Programs by Hydratec Inc. Revision: 50.52.1
Pressure / Flow Summary - STANDARD
Wiginton Fire Systems Page 6
2010771 - B1S4RA1 Date 5-19-17
lode Elevation K -Fact Pt Pn Flow Density Area Press
No. - - Actual Actual
H3 36.38 16.8 52.0 na 121.15 0.1 100 52.0
H4 35.97 16.8 52.53 na 121.76 0.1 100 52.0
100 32.03 68.95 na
101 29.37 76.34 na
103 29.37 76.36 na
105 29.37 76.42 na
107 29.37 76.55 na
109 29.37 76.69 na
111 29.37 76.86 na
113 29.37 77.04 na
115 29.37 77.25 na
117 29.37 77.47 na
119 29.37 77.71 na
121 29.37 77.96 na
123 29.37 78.23 na
125 29.37 78.52 na
127 29.37 78.83 na
129 29.37 79.16 na
131 29.37 79.51 na
133 29.37 79.89 na
135 29.37 83.59 na
137 29.37 90.11 na
139 • 29.55 93.38 na
TR4 29.55 94.14 na
BR4 2.0 110.46 na
PO 2.0 111.83 na
PI 2.0 26.43 na
SPIG -3.0 29.32 na
UG3 -3.0 32.62 na 250.0
IG4 -3.0 43.31 na
iG5 -3.0 48.43 na
UG6 -3.0 52.22 na
TEST 2.0 51.26 na
H2 36.03 16.8 52.15 na 121.32 0.1 100 52.0
H1 35.62 16.8 52.7 na 121.96 0.1 100 52.0
200 32.09 67.77 na
201 29.38 71.8 na
203 29.38 71.91 na
205 29.38 72.33 na
207 29.38 73.21 na
209 29.38 73.96 na
211 29.38 74.6 na
213 29.38 75.14 na
215 29.38 75.61 na
217 29.38 76.0 na
219 29.38 76.34 na
221 29.38 76.63 na
223 29.38 76.87 na
225 29.38 77.06 na
227 • 29.38 77.21 na
229 29.38 77.32' na
231 29.38 77.4 na
233 29.38 77.44 na
235 29.38 77.46 na
234 32.09 76.77 na
134 33.76 80.6 na
202 32.09 67.89 na
H5 35.62 16.8 52.83 na 122.11 0.1 100 52.0
H6 36.03 16.8 52.29 na 121.48 0.1 100 52.0
H7 36.38 16.8 52.13 na 121.3 0.1 100 52.0
H8 35.97 16.8 52.67 na 121.92 0.1 100 52.0
102 32.03 68.93 na
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow Summary - Standard
Wiginton Fire Systems Page 7
2010771 - B1S4RA1 Date 5-19-17
lode Elevation K -Fact Pt Pn Flow Density Area Press
No. Actual Actual Req_
204 32.09 68.27 na
H9 35.62 16.8 53.04 na 122.35 0.1 100 52.0
H10 36.03 16.8 52.48 na 121.7 0.1 100 52.0
H11 36.38 16.8 52.33 na 121.53 0.1 100 52.0
H12 35.97 16.8 52.86 na 122.14 0.1 100 52.0
104 32.03 69.03 na
206 32.09 72.26 na
106 32.03 74.88 na
208 32.09 72.97 na
108 32.03 75.12 na
210 32.09 73.58 na
110 32.03 75.36 na
212 32.09 74.1 na
112 32.03 75.6 na
214 32.09 74.55 na
114 32.03 75.84 na
216 32.09 74.93 na
116 32.03 76.09 na
218 32.09 75.26 na
118 32.03 76.35 na
220 32.09 75.55 na
120 32.03 76.6 na
222 32.09, ' 75.79 na
122 32.03 76.87 na
224 32.09 75.98 na
124 32.03 77.15 na
226 32.09 76.15 na
126 32.03 77.43 na
228 32.09 76.27 na
128 32.03 77.73 na
30 32.09 76.37 na
130 32.03 78.04 na
232 32.09 76.44 na
132 32.03 78.36 na
The maximum velocity is 16.23 and it occurs in the pipe between nodes 205 and 207
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems
2010771 - B1S4RA1
Page 8
Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. C" or Ftng's Pe Pv "'•"' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
EQUIVALENT K'S
REMOTE HEAD TO SUPPLY
H3 119.56 2.703 0.0 10.000 52.000 K Factor = 16.80
to
120.0
120.0 0.0 0.0 0.178
1137.65 0.0348_
H4 119.56 0.0354 0.0 10.000 0.354 Vel = 6.68
H4 121.76 2.703 T 18.651 94.650 52.532 K Factor = 16.80
to
1177.65
120.0 0.0 18.651 1.706
100 241.32 0.1298 0.0 113.301 14.710 Vel = 13.49
100 0.0 2.703 T 18.651 29.450 68.948
to 120.0 0.0 18.651 1.152
101 241.32 0.1298 0.0 48.101 6.245 Vel = 13.49
101 0.0 6.385 0.0 8.330 76.345
to 120.0 0.0 0.0 0.0
103 241.32 0.0019 _ 0.0 8.330_ 0.016 Vel = 2.42
1,103 242.09 6:385 0.0, ; 8.330 76.3.61 a
to 120.0 0.0 0.0 0.0
105 _ 483.41 0.0072 __ 0.0 8_330 0.060 _ Vel = 4.84
105 241.27 6.385 0.0 8.330 76.421
to 120.0 0.0 0.0 0.0
107 724.68 0.0150 0.0 _ 8.330 0.125 _ _ Vel = 7.26
107 62.51 6.385 0.0 8.330 76.546
to 120.0 0.0 0.0 0.0
10-9-787.19 0.0176 --
6.385 _ -
0.0
0.0 -
8.330 _ 0.147 Vel = 7.89
109 56.11 8.330 76.693to120.0 0.0 0.0 0.0
111 843.3 0.0199 0.0 8.33_0 0.166 _ Vel = 8.45_
111 50.64 6.385 0.0 8.330 76.859
to 120.0 0.0 0.0 0.0
113 893.94 0.0223 0.0 8.330 0.186 Vel = 8.96
113 46.11 6.385 0.0 8.330 77.045
to 120.0 0.0 0.0 0.0
115 940.05 0.0244 0.0 8.330 0.203 Vel = 9.42
115 42.55 6.385 0.0 8.330 77.248
to 120.0 0.0 0.0 0.0
117 982.6 0.0265 0.0 8.330 0.221 Vel = 9.85
117 40.00 6.385 0.0 8.330 • 77.469
to 120.0 0.0 0.0 0.0
119 1022.6 0.0286 0.0 8.330 0.238 Vel = 10.25
119 38.49 6.385 0.0 8.330 77.707
to 120.0 0.0 0.0 0.0
121 1061.09 _ 0.03_05_ _ 0.0 8.330 0.254 Vel = 10.63
121 38.01 6.385 0.0 8.330 77.961
to 120.0 0.0 0.0 0.0
123 1099.1 0.0327 0.0 8.330 0.272 Vel = 11.01
123 38.55 6.385 0.0 8.330 78.233
to 120.0 0.0 0.0 0.0
125 1137.65 0.0348_ 0.0 8.330 0.290 Vel = 11.40
125 40.00 6.385 0.0 8.330 78.523
to 120.0 0.0 0.0 0.0
127 1177.65 0.0370 0.0 8.330 0.308 Vel = 11.80
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems
2010771 - B1S4RA1
Page 9
Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv ""••` Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
127 42.29 6.385 0.0 8.330 78.831 - - - - -- - -
to
129.439
120.0 0.0 0.0 0.0
129 1219.94 0.0396 0.0 8.330 0.330 Vel = 12.22
129 45.27 6.385 0.0 8.330 79.161
to
Vel =
120.0 0.0 0.0 0.0
131 1265.21 0.0423 0.0 8.330 0.352 Vel = 12.68
131 48.85 6.385
17.606
0.0 8.330 79.513
129.439
Pressure From Pump Curve
to
Pressure @ Pump Inlet
120.0
PI 0.0• 8.249
0.0 0.0 0.0
SPIG 1460.74 0.0158 0.0 45.871 0.727 Vel = 8.77
133 1314.06 0.0455
280.358 _
0.0 8.330 0.379 Vel = 13.17
133 52.87 6.385 2V 25.691 50.000 79.892
140.0 Zaf
to
130.283
120.0
Fixed Loss = 3.896
0.0 25.691 0.0
4L 77.87
135 1366.93 0.0488
UG4
0.0 75.691 3.695 Vel = 13.70
135 93.81 6.385 V 12.845 105.350 83.587
71.092 0.0
to
UG5
120.0
0.0055
0.0 12.845 0.0
5.118 Vel = 6_.6.1
137 ;,, 14.60.74 0.0552, 0.0 118.195 _ 6.525 Vel = 14.64-
137 0.0 6.385 V 12.845 47.710 90.112
UG6 1710.74
to 120.0
1688.164
0.0 12.845 0.078
139 1460.74 0.0552 0.0 60.555 3.343 Vel = 14.64
139 0.0 6.385 V 12.845 1.000 93.377
to 120.0 0.0 12.845 0.0
TR4 1460.74 0.0552 0.0 13.845 0.764 Vel = 14.64
TR4 0.0 6.357 T 37.72 27.500 94.141
to 120.0 B 12.573 50.293 11.932
BR4 146.0.74 0.0564 0.0
14.457 -
77_.793 4.3_88
110.461 -_ - - -_
Vel = 14.77
BR4 0.0 8.249 V 8.666
to 120.0 B 13.345 77.846 0.0
PO 1460.74 0.0159 S 50.044 86.512 1.372 Vel = 8.77
0.0
1460.74 111.833 K Factor = 138.13
System Demand Pressure 111.833
Safety Margin 17.606
Continuation Pressure 129.439
Pressure @ Pump Outlet 129.439
Pressure From Pump Curve 103.010
Pressure @ Pump Inlet 26.429
PI 0.0• 8.249 T • 38.923 2.500 26.429
to 120.0 G 4.448 43.371 2.166
SPIG 1460.74 0.0158 0.0 45.871 0.727 Vel = 8.77
SPIG 0.0 8.27 E 26.955 195.000 29.322
to 140.0 T 52.413 85.358 0.0
UG3 1460.74 0.0118 G 5.99 280.358 _ 3.302 Vel = 8.72
UG3 250.00 8.27 T 52.413 300.000 32.624 Qa = 250
to 140.0 Zaf 0.0 130.283 3.896 Fixed Loss = 3.896
UG4 1710.74 0.0158 4L 77.87 430.283 6.787 Vel = 10.22
UG4 0.0 10.28 T 71.092 865.000 43.307
to 140.0 0.0 71.092 0.0
UG5 1710.74 0.0055 0.0 93_6.092 5.118 Vel = 6_.6.1
UG5 0.0 12.34 T 88.164 1600.000 48.425
to 140.0 0.0 88.164 0.0
UG6 1710.74 0.0022 0.0 1688.164 3.792 Vel = 4.59
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 10
2010771 - B1S4RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv '•"•" Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
UG6 0.0 12.34 T 88.164 450.000 52.217
to 140.0 0.0 88.164 -2.166
TEST 1710.74 0.0022 0.0 538.164 1.210 Vel = 4.59
0.0
1710.74 51.261 K Factor = 238.94
NEW PATH
H3 1.59 2.703 0.0 10.000 52.000
to 120.0 0.0 0.0 0.152
H2 1.59 0.0 0.0 10.000 0.0 Vel = 0.09
H2 121.32 2.703 0.0 10.000 52.152 K Factor = 16.80
to 120.0 0.0 0.0 0.178
H1 122.91 0.0372 0.0 10.000 0.372 Vel = 6.87
H1 121.96 2.703 X 16.786 84.740 52.702 K Factor = 16.80
to 120.0 0.0 16.786 1.529
o 200 244.87 0.1334 - 0.0:1- _ 101.526_ 13.542 _- Vel = 13.6.9_
200 0.0 2.703 T 18.651 2.710 67.773
to 120.0 0.0 18.651 1.174
201__- 244_87 0.1333 0.0 21.361 2.848 Vel = 13.69
201 0.0 4.304 0.0 8.330 71.795
to 120.0 0.0 0.0 0.0
203 244.87 0.0139 0.0 - 8.330 0.116 Vel = 5.40_
203 244.73 4.304 0.0 8.330 71.911
to 120.0 0.0 0.0 0.0
2_05 489._6 0.049_8_ 0.0 8.330 _ 0.415 Vel =_10_.8.0_
205 246.45 4.304 0.0 8.330 72.326
to 120.0 0.0 0.0 0.0
207 736.05 0.1061 0.0 8.330 0.884 Vel = 16.23
207 62.50 4.304 0.0 8.330 73.210
to 120.0 0.0 0.0 0.0
209 673.55 0.0899 0.0 8.330 0.749 Vel = 14.85
209 56.11 4.304 0.0 8.330 73.959
to 120.0 0.0 0.0 0.0
211 617.44 0.0766 0.0 8.330 0.638 Vel = 13.62
211 50.64 4.304 0.0 8.330 74.597
to 120.0 0.0 0.0 0.0
213 566.8 0.0654 0.0 8.330 0.545 Vel = 12.50
213 46.11 4.304 0.0 8.330 75.142
to 120.0 0.0 0.0 0.0
215 520.69 0.0559 - 0.0 _- 8.330 0.466 Vel = 11.48
215 42.56 4.304 0.0 8.330 75.608
to 120.0 0.0 0.0 0.0
217 478.13 0.0477 0.0 8.330 0.397 Vel = 10.54
217 40.00 4.304 0.0 8.330 76.005
to 120.0 0.0 0.0 0.0
219 438.13 0.0407 0.0 8.330 0.339 Vel = 9.66
219 38.48 4.304 0.0 8.330 76.344
0 120.0 0.0 0.0 0.0
221 399.65 0.0342 0.0 8.330 0.285 Vel = 8.81
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 11
2010771 - B1S4RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. C" or Ftng's Pe Pv Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
221 38.02 4.304 0.0 8.330 76.629
to 120.0 0.0 0.0 0.0
223 361.63 0.0285 0.0 8.330 0.237 Vel = 7.97
223 38.54 4.304 0.0 8.330 76.866
to 120.0 0.0 0.0 0.0
225 323.09 0.0232 0.0 8.330 0.193 Vel = 7.12
225 40.00 4.304 0.0 8.330 77.059
to 120.0 0.0 0.0 0.0
227 283.09 0.0181 0.0 8.330 0.151 Vel = 6.24
227 42.29 4.304 0.0 8.330 77.210
to 120.0 0.0 0.0 0.0
229 240.8 _ 0.0133_ 0.0 8.330 0.111 Vel = 5.3.1
229 45.28 4.304 0.0 8.330 77.321
to 120.0 0.0 0.0 0.0
231, _ 195.52 0.0091_ 0.0 8.330 0.0_76 ; Vel_ =_ 4.31
231 48.84 4.304 0.0 8.330 77.397
I _
to 120.0 0.0 0.0 0.0
233 146.68 0.0054 0.0 8.330 0.045 Vel = 3.23
233 52.87 4.304 0.0 8.330 77.442
to 120.0 0.0 0.0 0.0
235 93.81 0.0024 0.0 8.330 0.020 Vel = 2.07
235 0.0 2.703 T 18.651 2.710 77.462
to 120.0 0.0 18.651 1.174
234 93.81 0.0226 0.0 21.361 0.483 Vel_= 5.25
234 0.0 2.703 2X 33.571 167.750 76.771
to 120.0 0.0 33.571 0.723
134 93.81 0.0226 0.0 201.321 4.550 - Vel = 5.25
134 0.0 2.703 T 18.651 29.450 80.598
to 120.0 0.0 18.651 1.901
135 93.81 0.0226 0.0 48.101 1.088 5.25
0.0
Vel
93.81 83.587 K Factor= 10.26
NEW PATH
203 244.73 2.703 T 18.651 2.710 71.911
to 120.0 0.0 18.651 1.174
202 244.73 0.1332 0.0 21.361 2.846 Vel = 13.68
202 0.0 2.703 X 16.786 84.740 67.891
to 120.0 0.0 16.786 1.529
H5 _- 244.73_ 0_1332 0.0 101.526_ 13.528 _ _ Vel = 1_3.68
H5 122.11 2.703 0.0 10.000 52.834 K Factor = 16.80
to 120.0 0.0 0.0 0.178
H6 122.62 0.0370 0.0 10.000 0.370 Vel = 6.86
H6 121.48 2.703 0.0 10.000 52.286 K Factor 16.80
to 120.0 0.0 0.0 0.152
H7 1.14 0.0 0.0 10.000 0.0 Vel = 0.06
H7 121.30 2.703 0.0 10.000 52.134 K Factor 16.80
0 120.0 0.0 0.0 0.178
H8 120.16 0.0357 0.0 10.000 0.357 Vel = 6.72
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 12
2010771 - B1S4RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv ••""• Notes '•""
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
H8 121.93 2.703 X 16.786 94.650 52.669 K Factor = 16.80
to 120.0 0.0 16.786 1.706
102 242.09 0.1306 0.0 111.436 14.553 Vel = 13.54
102 0.0 2:703 T 18.651 29.450 68.928
to
207
120.0
2.703
0.0 18.651 1.152
73.210
103 242.09 0.1306 0.0 48.101 6.281 Vel = 13.54
1.174
0.0
206 62.5 0.0107 0.0 . 21.361
242.09
Vel = 3.49
206 0.0
76.361 K Factor= 27.70
NEW PATH
209.420 72.264
to
205 246.45 2.703 T 18.651 2.710 72.326
106
to
0.0107
120.0
0.0
0.0 18.651 1.174
3.49
204 246.45 0.1350
T
0.0 _ 21.361 2.883 Vel = 13.78
204 0.0 2.703 X 16.786 84.740 68.269
1.152
to 120.0
62.5
0.0 16.786 1.529
48.101
H9, 246.45 0.13_50 ,, , 0.0 101..526 _ 13.7_03 Vel = 13.78
H9 122.35 2.703 0.0 10.000 53.037 K Factor = 16.80
to 120.0
K Factor = 7.14
0.0 0.0 0.178
H10 124.1_ 0.0379 _ _ 0.0 10.000 0.3_79 Vel = 6.94_
H10 121.70 2.703
73.959
0.0 10.000 52.480 K Factor = 16.80
to 120.0
18.651
0.0 0.0 0.152
208
H11 2.4 _ 0.0
0.0
0.0_---l-0.000 0.0 _ Vel = 0.13_
H11 121.53 2.703 0.0 10.000 52.328 K Factor = 16.80
to 120.0 0.0 0.0 0.178
H12 119_13 0.0352 0.0 10.000 0.352 _ _ _ Vel = 6.66
H12 122.14 2.703 X 16.786 94.650 52.858 K Factor = 16.80
to 120.0 0.0 16.786 1.706
104 241.27 0.1298 0.0 111.436 14.462 Vel = 13.49
104 0.0 2.703 T 18.651 29.450 69.026
to 120.0 0.0 18.651 1.152
105 241.27 0.1298 0.0 48.101 6.243 Vel = 13.49
0.0
241.27 76.421 K Factor= 27.60
NEW PATH
207 62.50 2.703 T 18.651 2.710 73.210
to 120.0 0.0 18.651 1.174
206 62.5 0.0107 0.0 . 21.361 0:228 Vel = 3.49
206 0.0 2.703 2X 33.571 209.420 72.264
to 120.0 0.0 33.571 0.026
106 62.5 0.0107 0.0 242.991 2.591 Vel = 3.49
106 0.0 2.703 T 18.651 29.450 74.881
to 120.0 0.0 18.651 1.152
107 62.5 0.0107 0.0 48.101 0.513 Vel = 3.49
0.0
62.50 76.546 K Factor = 7.14
NEW PATH
209 56.11 2.703 T 18.651 2.710 73.959
0 120.0 0.0 18.651 1.174
208 56.11 0.0088 0.0 21.361 0.187 Vel = 3.14
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 13
2010771 - B1S4RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv "•"•' Notes "•'•'
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
208 0.0 2.703 - 2X 33.571 209.420 72.972 --
to 120.0 0.0 33.571 0.026
108 56.11 0.0087 0.0 242.991 2.123 Vel = 3.14
108 0.0 2.703 T 18.651 29.450 75.121
to 120.0 0.0 18.651 1.152
109 56.11 0.0087 0.0 48.101 0.420 Vel = 3.14
0.0
56.11 76.693 K Factor = 6.41
NEW PATH
211 50.64 2.703 T 18.651 2.710 74.597
to 120.0 0.0 18.651 1.174
210_ 50.64 0.0073 - 0.0 _ 21.361 0.155 _-_ Vel =_ 2.83---- 83-
210 210 0.0 2.703 2X 33.571 209.420 73.578
to 120.0 0.0 33.571 0.026
110 50.64 0.0072_ _ 0.0 242.991,,,- 1.756 Vel =2_.83
110 0.0 2.703 T 18.651 29.450 75.360
to 120.0 0.0 18.651 1.152
111 50.64 0.0072 0.0- 48.101 0.347 Vel = 2.83
0.0
5.0.64 76._859 - K Factor= 5.78
NEW PATH
213 46.11 2.703 T 18.651 2.710 75.142
to 120.0 0.0 18.651 1.174
212 46.11 0.0061 0.0 21.361 0.130 Vel = 2.58
212 0.0 2.703 2X 33.571 209.420 74.098
to 120.0 0.0 33.571 0.026
112 46.11 0.0061 0.0 242.991 1.476 Vel = 2.58
112 0.0 2.703 T 18.651 29.450 75.600
to 120.0 0.0 18.651 1.152
113 46.11 0.0061 0.0 48.101 0.293 Vel = 2.58
0.0
46.11 77.045 K Factor = 5.25
NEW PATH
215 42.55 2.703 T 18.651 2.710 75.608
to 120.0 0.0 18.651 1.174
214 42.55 0.0052 0.0 21.361 0.112 Vel = 2.38
214 0.0 2.703 2X 33.571 209.420 74.546
to 120.0 0.0 33.571 0.026
114 42.55 0.0052 0.0 242.991 1.272 Vel = 2.38
114 0.0 2.703 T 18.651 29.450 75.844
to 120.0 0.0 18.651 1.152
115 42.55 0.0052 0.0 48.101 0.252 Vel = 2.38
0.0
42.55 77.248 K Factor= 4.84
NEW PATH
217 40.00 2.703 T 18.651 2.710 76.005
0 120.0 0.0 18.651 1.174
216 40.0 0.0047 0.0 21.361 0.100 Vel = 2.24
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 14
2010771 - B1S4RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv ***'*" Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
216 0.0 2.703 2X 33.571 209.420 74.931
to
Vel =
120.0 0.0 33.571 0.026
116 40.0 0.0047 0.0 242.991 1.135 Vel = 2.24
116 0.0 2.703 T 18.651 29.450 76.092
to
Vel =
120.0 0.0 18.651 1.152
117 40.0 0.0047 0.0 48.101 0.225 Vel = 2.24
to
0.0
120.0
T
0.0 33.571 0.026
40.00
118 ,, ; 38.49
77.469 K Factor= 4.54
NEW PATH
0.0 242!991 1.057.--.-,,,,, 2_._1.5., d
219 38.49 2.703 T 18.651 2.710 76.344
Vel = 2.15
to
0.0
120.0
2X
0.0 18.651 1.174
218 38.49 0.0044 _ 0.0 _ 21.361 0.093 Vel = 2.15
218 0.0 2.703 2X 33.571 209.420 75.263
2.15
to
0.0
120.0
T
0.0 33.571 0.026
118 ,, ; 38.49 0.0043, -;i. 0.0 242!991 1.057.--.-,,,,, 2_._1.5., d
118 0.0 2.703 T 18.651 29.450 76.346
Vel ..=
to
0.0
120.0 0.0 18.651 1.152
119 38.49 0.0043 0.0 48.101 0.209 Vel = 2.15
0.0
225
38.49 77.707 _ K Factor= 4.37_
NEW PATH___
120.0 0.0 18.651 1.174
221 38.01 2.703 T 18.651 2.710 76.629
Vel = 2.24
to 120.0 0.0 18.651 1.174
220 38.01 0.0043 0.0 21.361 0.091 Vel = 2.13
220 0.0 2.703 2X 33.571 209.420 75.546
to 120.0 0.0 33.571 0.026
120 38.01 0.0043 0.0 242.991 1.033 Vel = 2.13
120 0.0 2.703 T 18.651 29.450 76.605
to 120.0 0.0 18.651 1.152
121 38.01 0.0042 0.0 48.101 0.204 Vel = 2.13
0.0
38.01 77.961 K Factor= 4.30
NEW PATH
223
to
222
38.54
38.54
2.703
120.0
0.0044
T 18.651
0.0
6.0
2.710
18.651
21.361
76.866
1.174
0:094 Vel = 2.15
222 0.0 2.703 2X 33.571 209.420 75.786
to 120.0 0.0 33.571 0.026
122 38.54 0.0044 0.0 242.991 1.059 Vel = 2.15
122 0.0 2.703 T 18.651 29.450 76.871
to 120.0 0.0 18.651 1.152
123 38.54 0.0044 0.0 48.101 0.210 Vel = 2.15
0.0
38.54 78.233 K Factor= 4.36
NEW PATH
225 40.00 2.703 T 18.651 2.710 77.059
to 120.0 0.0 18.651 1.174
224 40.0 0.0047 0.0 21.361 0.100 Vel = 2.24
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 15
2010771 - B1S4RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv ***"'• Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
224 0.0 2.703 2X 33.571 209.420 75.985
to
48.84
120.0 0.0 33.571 0.026
124 40.0 0.0047 0.0 242.991 1.135 Vel = 2.24
124 0.0 2.703 T 18.651 29.450 77.146
to
Vel =
120.0 0.0 18.651 1.152
125 40.0 0.0047 0.0 48.101 0.225 Vel = 2.24
to
0.0
120.0 0.0 33.571 0.026
40.00
126 42.29
78.523 K Factor = 4.51
NEW PATH
227 42.29 2.703 T 18.651 2.710 77.210
48.84 0.0068_
to
0.0
120.0
to
0.0 18.651 1.174
48.84 0.0068
226 42.29 0.0051 0.0 21.361 0.110 Vel = 2.36
226 0.0 2.703 2X 33.571 209.420 76.146
52.87 0.0079
to 120.0 0.0 33.571 0.026
126 42.29 0.0052 0.0 242.99.1; } 1.258 d Vel = 2.36 "d
126 0.0 2.703 T 18.651 29.450 77.430
to 120.0 0.0 18.651 1.152
127 42.29 0.0052 --- 0.0 48.101 0.249 Vel = 2.36
0.0
42.29 78.831 K Factor= 4.76
NEW PATH
229 45.28 2.703 T 18.651 2.710 77.321
to 120.0 0.0 18.651 1.174
228 _ 45.28 0.0059 0.0 21.361 0.126 - Vel = 2.53
228 0.0 2.703 2X 33.571 209.420 76.273
to 120.0 0.0 33.571 0.026
128 45.28 0.0059 0.0 242.991 1.427 Vel = 2.53
128 0.0 2.703 T 18.651 29.450 77.726
to 120.0 0.0 18.651 1.152
129 45.28 0.0059 0.0 48.101 0.283 Vel = 2.53
0.0
45.28 79.161 K Factor = 5.09
NEW PATH
231 48.84 2.703 T 18.651 2.710 77.397
to 120.0 0.0 18.651 -1.174
230 48.84 0.0068 0.0 21.361 0.146- Vel = '233
230 0.0 2.703
to 33.571120.0
130 48.84 0.0068_
130 0.0 2.703
to 18.651120.0
131 48.84 0.0068
0.0
48.8.4
NEW PATH
233 52.87 2.703
0 120.0
232 52.87 0.0079
2X 33.571 209.420 76.368
0.0 33.571 0.026
0.0 2.42.9_91 1.6_42 Vel = 2_.73
T 18.651 29.450 78.036
0.0 18.651 1.152
0.0 48.101 0.325 Vel = 2.73
79.513 K Factor = 5.48
T 18.651 2.710 77.442 -- --- ------ -
0.0 18.651 -1.174
0.0 21.361 0.168 Vel = 2.96
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 16
2010771 - B1S4RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. C" or Ftng's Pe Pv Notes '•""
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
209.4202320.0 2.703 2X 33.571 76.436
to 120.0 0.0 33.571 0.026
132 52.87 0.0078 0.0 242.991 1.901 Vel = 2.96
132 0.0 2.703 T 18.651 29.450 78.363
to 120.0 0.0 18.651 1.152
133 52.87 0.0078 0.0 48.101 0.377 Vel = 2.96
0.0
52.87 79.892 K Factor= 5.92
Computer Programs by Hydratec Inc. Revision: 50.52.1
AutoPeaking Summary
Wiginton Fire Systems
2010771 - B1S4RA1
Auto Peaking Summary - List of Pipes for Area Calculated
Left Right
Side Side
From To Length From To Length
Page 17
Date 5-19-17
H4 100 94.650 H1 200 84.740
H8 102 94.650 202 H5 84.740
H12 104 94.650 204 H9 84.740
H4 100 94.650 H1 200 84.740
H8 102' 94.650 202 H5 184.740
H12 104 94.650 204 H9 84.740
Flow Safety Pressure
Required Margin Differential
Left 10.000 1 1710.707 17.642 0.036
Area Calculated 1 1710.737 17.606 0.000
Right 10.000 1710.811 17.681 0.075
Typical Distance Between Heads = 10.000
Split Point Used in Worst Area Peaked = H3
Split Point Used in Area Calculated = H3
Computer Programs by Hydratec Inc. Revision: 50.52.1
M
0g)'D 90 R (D M
FIRE SYSTEMS
Wiginton Fire Systems
699 Aero Lane
Sanford, FL 32771
407-585-3200
Job Name 2010771 - 61S5RA1'
Drawing FP9
Location BUILDING ONE
Remote Area B1S5RA1
Contract 2010771
Data File 2010771 - B1S5RA1.WXF
Computer Programs by Hydratec Inc. Revision: 50.52.1
W
Wiginton Fire Systems
2010771 - B 1 S5RA1
Project name: GANESH NORTH
Location: BUILDING ONE
Drawing no: FP9
Date: 5-19-17
Design
HYDRAULIC CALCULATIONS
for
Remote area number. B1S5RA1
Remote area location: SYSTEM FIVE
Occupancy classification: HIGH PILED STORAGE
Density: .37 - Gpm/SgFt
Area of application: 2,044 - Sq Ft
Coverage per sprinkler: 100 MAX - SgFt
Type of sprinklers calculated. 11.2K STANDARD RESPONSE UPRIGHT
No. of sprinklers calculated. 22
In -rack demand: N/A - GPM
Hose streams: 500 - GPM
Total water required (including hose streams): 1394.581 - GPM @
Type of system: WET
Volume of'dry or preaction system:' N/A - Gal
Water supply information
Date: 8-2-16
Location: ALONG W. 1ST STREET
Source: WFS
Name of contractor. WIGINTON FIRE SYSTEMS
Address: 699 AERO LANE, SANFORD, FL 32771
Phone number: 407-585-3200
Name of designer: W. AMMONS
Authority having jurisdiction: CITY OF SANFORD
Notes: (Include peaking information or gridded systems here.)
Computer Programs by Hydratec Inc. Revision: 50.52.1
41.223 - Psi
Page 1
Date 5-19-17
Water )ly Curve C
Wiginton Fire Systems = Page 2
2010771 - BIS5RA1 Date 5-19-17
City Water Supply:
C1 - Static Pressure 60
C2 - Residual Pressure: 50
C2 - Residual Flow 1840
City Water Adjusted to Pump Inlet
for Pf - Elev - Hose Flow
P3 - Pump Pressure @ Max Flow
Al - Adjusted Static: 52.437
A2 - Adj Resid 25.858 @ 1261.31
A3 - Adj Resid 1.391 @ 1881.1
210
196
182
p 168
R 154
E 140
S 126
S 112
U 98
R 84
E 70
56
42
28
14
Pump Data:
P1 - Pump Churn Pressure 126.18
P2 - Pump Rated Pressure 109.95
P2 - Pump Rated Flow 1261.31
P3 - Pump Pressure @ Max Flow 79.39
P3 - Pump Max Flow 1881.1
City Residual Flow @ 0 4846.63
City Residual Flow @ 20 3892.74
City Water @ 150% of Pump 49.58
Demand:
D1 - Elevation 11.503
D2 - System Flow 894.58
D2 - System Pressure 142.838
Hose ( Demand )
D3 - System Demand 894.58
Hose ( Adj City) 500
Safety Margin 12.789
200 400 600 800 1000 1200 1400 1600 1800
FLOW N^1.85)
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow Diagram
Wiginton Fire Systems
2010771 - B1S5RA1
Page 3
Date 5-19-17
38.31132 154.4 309.3 475.8 542.4 627.2 739.5 894.6 894.6 894.6H54- H6 4- H7 +- H8 _ 100 101 +- 103 105 - 107 109 111 113 +- 115 117 +- 119 +- 121 +- 125 +- 127 129 131 +- TR5+- BR5+- PO75154.4 154.4 445.8 507.5 5819 679.5 808.4 894.6 894.6 894.6
894.6 1394.6 1394.6
Pl « SPIG- UG3 UG44- UGSi UG6e- TEST
894.6 1394.6 1394.6
1.9 72.1 153.5 153.5 448.8 387 312.7 215.1 86.2 86.2 86.2H5 -+ H4 H3 +- H2 +- H1 +- 200 F 201 203 +- 205 r- 207 209 +- 211 +- 213 F 215 t 217 F 219 221 +- 223 4- 222 122 123 F- 125
34.8 111.1 153.5 307.5 418.7 352.2 267.3 155 86.2 86.2
154 111.5 34.9 38.4 113.5 154.9
203 -+ 202- H9 -* H10 -a H11- H12+- H134- H14r. H15r- H16+- 1024- 103
T 154 72.3 1.9 75.2 154.9
1 307.5
1 141.3 92.9 1.4 89.2 136.4
205-i 204- H17 H18- H19 -i H2O+- H214- H224- 1044_ 105
1 141.3 46.7 43.7 136.4
I 448.8
1 30.1 30.1
2074 206+- 106+- 107
t 30.1 1
1 418.7 1 475.8
1 31.7 31J
209 4 208 4 108 4- 109
t 31.7 1
I 387 1 507.5
1 34.9 34.V
211 +- 210 4- 110 4- 111
i34.9 ?
352.2 1 542.4
1 39.5 39.5
2134- 2124 1124- 113
1 39.5 1
I 312.7 1 581.9
1 45.3 45.1
215+- 214+- 114- 115
1 45.3 1
267.3 1 627.2
1 522 52.g
2174_ 216-. 116 117
1 52.2 1
1 215.1 1 679.5
1 601 60.1
2194- 2184- 1184- 119
60.1 1
155 1 739.5
1 68.9 68.0
221+- 220 4 120 4- 121
68.9
Computer Programs by Hydratec Inc. Revision: 50.52.1
Fittings 3d Summary
Wiginton Fire Systems Page 4
2010771 - B1S51RA1
Date 5-19-17
Fitting Legend
Abbrev. Name '/: _ % 1 1'/. 1'/: 2 2'/: 3 3'/: 4 5 6 8 10 12 14 16 18 20 24
B Generic Butterfly Valve 0 0 0 0 0 0 7 10 0 12 9 10 12 19 21 0 0 0 0 0E90' Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61GGenericGateValve00000111122345678101113J90'Tee-Branch Gry Vic #20 0 0 4.5 6 8 8.5 10.8 13 17 16 '= 21 25 33 41 50 65 78 88 98 120LLongTumElbow1122234556891316182427303440SGenericSwingCheckValve4557911141619222732455565768798109130T90' Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121V90'Ell Firelock #001 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 0 0 0 0 0 0 0ZafAmes3000SSFittinggeneratesaFixedLossBasedonFlow
Units Summary
Diameter Units
Length Units
Flow Units
Pressure Units
Inches
Feet
US Gallons per Minute
Pounds per Square Inch
Computer Programs by Hydratec Inc. Revision: 50.52.1
Pressure / Flow Summary - STANDARD
Wiginton Fire Systems Page 5
2010771 B1S5RA1 Date 5-19-17
Node Elevation K -Fact Pt Pn Flow Density Area PressNo-. Actual Actual Req.
H5 28.56 11.2 10.59 na 36.45 0.37 98.5 7.0H628.88 11.2 10.74 na 36.7 0.37 98.5 7.0H729.19 11.2 11.59 na 38.13 0.37 98.5 7.0H829.5 11.2 13.58 na 41.27 0.37 98.5 7.010027.833 27.89 na
101 27.833 48.36 na
103 27.833 48.62 na
105 27.833 49.58 na
107 27.833 51.46 na
109 27.833 53.59 na
111 27.833 55.98 na
113 27.833 58.69 na
115 27.833 61.77 na
117 27.833 65.32 na
119 27.833 69.42 na
121 27.833 74.23 na
125 27.833 85.01 na
127 31.292 96.18 na
129 31.292 117.2 na
131 29.167 127.28 na
TR5 29.167 128.86 na
BR5. 2.0 142.39 na
Po". 2.0 142,84 na
PI 2.0 37.75 na
SPIG 3.0 40.21 na
UG3 3.0 41.54 na 500.0
UG4 3.0 49.24 na
UG5 3.0 52.75 na
UG6 3.0 55.35 na
TEST 2.0 54.01 na
14 28.25 11.2 10.72 na 36.67 0.37 98.5 7.0H327.94 11.2 11.1 na 37.31 0.37 98.5 7.0H227.63 11.2 12.15 na 39.04 0.37 98.5 7.0H127.31 11.2 14.34 na 42.41 0.37 98.5 7.020026.18 37.72 na
201 23.47 45.85 na
203 23.47 46.11 na
205 23.47 47.06 na
207 23.47 48.97 na
209 23.47 50.64 na
211 23.47 52.09 na
213 23.47 53.31 na
215 23.47 54.29 na
217 23.47 55.02 na
219 23.47 55.51 na
221 23.47 55.78 na
223 23.47 55.86 na
222 26.18 57.08 na
122 30.47 76.68 na
123 27.833 84.78 na
202 26.18 37.94 na
H9 27.31 11.2 14.42 na 42.53 0.37 98.5 7.0H1027.63 11.2 12.22 na 39.16 0.37 98.5 7.0H1127.94 11.2 11.16 na 37.42 0.37 98.5 7.0H1228.25 11.2 10.79 na 36.78 0.37 98.5 7.0H1328.56 11.2 10.65 na 36.56 0.37 98.5 7.0H1428.88 11.2 10.8 na 36.81 0.37 98.5 7.0H1529.19 11.2 11.66 na 38.25 0.37 98.5 7.0H1629.5 11.2 13.66 na 41.4 0.37 98.5 7.010230.47 26.9 na
204 26.18 39.92 na
H17 27.42 11.2 18.65 na 48.37 0.37 98.5 7.0
Computer Programs by Hydratec Inc. Revision: 50.52.1
Flow Summary - Standard
Wiginton Fire Systems Page 6
2010771 - B1S5RA1 Date 5-19-17
Node Elevation K -Fact Pt Pn Flow Density Area Press
No. - --- Actual- - Actual Req._
H18 27.75 11.2 16.96 na 46.13 0.37 98.5 7.0
H19 28.08 11.2 16.39 na 45.34 0.37 98.5 7.0
H2O 28.41 11.2 16.24 na 45.14 0.37 98.5 7.0
H21 28.73 11.2 16.49 na 45.48 0.37 98.5 7.0
H22 29.06 11.2 17.78 na 47.23 0.37 98.5 7.0
104 30.47 32.17 na
206 26.18 48.13 na
106 30.47 49.33 na
208 26.18 49.84 na
108 30.47 51.36 na
210 26.18 51.37 na
110 30.47 53.54 na
212 26.18 52.7 na
112 30.47 55.91 na
214 26.18 53.84 na
114 30.47 58.51 na
216 26.18 54.79 na
116 30.47 61.42 na
218 26.18 55.56 na
118 30.47 64.71 na
220 26.18 56.18 na
120 30.47 68.49 na
The maximum velocity is 30.14 and it occurs in the pipe between nodes 121 and 125
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 7
2010771 - B1S5RA1 Date 5-19-17
Hyd, Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv ••**••• Notes *`••`*
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
EQUIVALENT K'S
REMOTE HEAD TO SUPPLY - - -
H5 38.34 1.728 0.0 7.500 10.589 K Factor = 11.20
to. 120.0 0.0 0.0 -0.139
H6 38.34 0.0381 0.0 7.500 0.286 Vel = 5-25
H6 36.70 1.728 0.0 7.500 10.736 K Factor = 11.20
to 120.0 0.0 0.0 -0.134
H7 75.04 0.1321 0.0 7.500 0.991 Vel = 10 27
H7 38.14 1.728 0.0 7.500 11.593 K Factor = 11.20
to
39.50
120.0 0.0 0.0 0.134
H8 113.18 0.2827 0.0 7.500 2.120 Vel = 15.48
H8 41.27 1.728 J 11.29 15.760 13.579 K Factor = 11.20
to
45.32
120.0 0.0 11.290 0.722
100 154.45_ 0.502_4 0.0 27.050 - 13.590_ Vel = 21.13
100 d 0.0 1.728 r T 11.29 29.450 27.891to
Vel = 23.39
117 52.21
120.0 0.0 11.290 0.0
101 154.45 0.5024 0.0 40.740 20.468 Vel = 21.13
101 0.0 3.31 0.0 12.500 48.359
Vel = 25.33
to
60.10
120.0 0.0 0.0 0.0
103 - 154.45 0.0212 0.0 - 12.5_00 0_.265
48.624
Vel = 5.76
103 154.89 3.31 0.0 12.500
to
68.86
120.0 0.0 0.0 0.0
10_5 309.34 0.0766 0.0 12.500 0.958 Vel =_ 11._53
105 136.44 3.31- 0.0 12.500 49.582
Vel = 30.14
to 120.0 0.0 0.0 0.0
107 445.78 0.1506 0.0 12.500 -- --- 1.883 Vel = 16.62
107 30.07 3.31 0.0 12.500 51.465
to 120.0 0.0 0.0 0.0
109 475.85 0.1700 0.0 12.500 2.125 Vel = 17.74_
109 31.68 3.31 0.0 12.500 53.590
to 120.0 0.0 0.0 0.0
111 507.53 0.1915 0.0 12.500 2.394 Vel = 1R-92
111
to
113
34.89
542.42
3.31
120.0
0.2166
0.0
0.0
0.0
12.500
0.0
12.500
55.984
0.0
2.707 Vel = 20.22
1.13 39.50 3.31 0.0 12.500 58.691
to 120.0 0.0 0.0 0.0
115 581.92 0.2466 0.0 12.500 3.083 Vel = 21.70
115 45.32 3.31 0.0 12.500 61.774
to 120.0 0.0 0.0 0.0
117 627.24 0.2834 0.0 12.500 3.542 Vel = 23.39
117 52.21 3.31 0.0 12.500 65.316
to 120.0 0.0 0.0 0.0
119 679.45 0.3286 0.0 12.500 4.107 Vel = 25.33
119 60.10 3.31 0.0 12.500 69.423
to 120.0 0.0 0.0 0.0
121 739.55 0.3843 0.0 12.500 4.804 Vel = 27.57
121 68.86 3.31 T 21.71 2.080 74.227
to 120.0 0.0 21.710 0.0
125 808.41 0.4531 0.0 23.790 10.779 Vel = 30.14
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 8
2010771 - B1S5RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
125 86.17 4.304 0.0 83.330 85.006
to 120.0 0.0 0.0 1.498
127 894.58 0.1521 0.0 83.330 12.677 Vel = 19.73
127 0.0 4.304 2V 18.826 119.330 96.185
to 120.0 0.0 18.826 0.0
129 894.58 0.1521 0.0 138.156 21.016 Vel = 19.73
129 0.0 4.304 V 9.413 50.790 117.201
to 120.0 0.0 9.413 0.920
131 894.58 0.1521 0.0 60.203 9.159 Vel = 19.73
131 0.0 4.304 V 9.413 1.000 127.280
to 120.0 0.0 9.413 0.0
TR5 - 894.58 0.1521 __ 0.0 10.413 _ 1.584 Vel = 19.73
TR5 0.0 6.357 T 37.72 27.167 128.864
to 120.0 B 12.573 50.293 11.766
BRS
l_ _
894.58 0.0228 _ 0.0 77.460 1.763 ,, _ _ Vel = 9.04 -
BR5 0.0 8.249 B 13.345 6.000 142.393
to 120.0 S 50.044 63.389 0.0
PO 894.58 0.0064_ 0.0 69.389 0.445 Vel = 5.37
0.0
894.58 _ 142.838_ _ Factor= 74.85
System Demand Pressure 142.838
K
Safety Margin 12.789
Continuation Pressure 155.627
Pressure @ Pump Outlet 155.627
Pressure From Pump Curve 117.880
Pressure @Pump Inlet
PI 0.0 8.249 T 38.923 2.500
37.747
37.747
to 120.0 G 4.448 43.371 2.166
SPIG 894.58 0.0_064 0.0 45.871 0.294 Vel =
SPIG 0.0 8.27 E 26.955 195.000 40.207
5.37__
to 140.0 T 52.413 85.358 0.0
UG3 894.58 0.0048 G 5.99 280.358 1.332 Vel = 5.34
UG3 500.00 8.27 T 52.413 300.000 41.539 Qa = 500
to 140.0 Zaf 0.0 130.283 3.053 Fixed Loss = 3.053
UG4 1394.58 0.0108 4L 77.87 430.283 4.651 Vel = 8.33
UG4 0.0 • 10.28 T 71.092 865.000 49.243
to 140.0 0.0 71.092 0.0
UG5 1394.58 0.0037 0.0 936.092 3.507 Vel = 5.39
UG5 0.0 12.34 T 88.164 1600.000 52.750
to 140.0 0.0 88.164 0.0
UG6 1394.58 0.0015 0.0 1688.164 2.599 Vel = 3.74
UG6 0.0 12.34 T 88.164 450.000 55.349
to 140.0 0.0 88.164 2.166
TEST 1394.58 0.0015 0.0 538.164 0.829 Vel = 3.74
0.0
1394.58 54.012 K Factor = 189.76
NEW PATH
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 92010771 - B1S5RA1 Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C' or Ftng's Pe Pv ""••` Notes '••`••
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
H5 1.90 1.728 0.0 7.500 10.589
to
to
120.0 0.0 0.0 0.134
0.0
H4 1.9 0.0001 0.0 7.500 0.001 Vel = 0.26
H4 36.68 1.728 0.0 . 7.500 10.722 K Factor = 11.20to
52.093
120.0 0.0 0.0 0.134
120.0
H3 34.78 0.0319 0.0 7.500 0.239 Vel = 4.76
H3 37.30 1.728 0.0 7.500 11.095 K Factor = 11.20to
3.31
120.0 0.0 0.0 0.134
H2 72.08 0.1227 0.0 7.500 0.920 Vel = 9.86
H2 39.04 1.728 0.0 7.500 12.149 K Factor = 11.20to
11.66
120.0 0.0 0.0 0.139
12.500
H1 111.12 0.2732 0.0 7.500 2.049 Vel = 15.20
H1 42.41 1.728 J 11.29 34.780 14.337 K Factor = 11.20to
2,500
120.0 0.0 11.290 0.489
52.22
200 153.53 0.4969 0.0 46.070 22.893 Vel 21.00
200 0.0 1.728 T 11.29 2.710 37.719
to
215.13
120.0 0.0 11.290 1.174
Vel =
201_ 153.53 0.4969 _ 0.0 14.000 6.956 Vel = 21.00
201 0.0 3.31 0.0 12.500 45.849 ----
to 120.0 0.0 0.0 0.0
0.0
203 153.53 0.0210 0.0 - 12.500 _ 0.262 Vel_ =_ 5.72
203 154.02 3.31 0.0 12.500 46.111
to 120.0 0.0 0.0 0.0
205 307.55 0.0758 0.0 12.500 0.948 Vel = 11.47
205 141.25 3.31 0.0 12.500 47.059
to 120.0 0.0 0.0 0.0
207 448.8 0.1526 0.0 12.500 1.907 Vel = 16.7_3_
207 30.07 3.31 0.0 12.500 48.966
to 120.0 0.0 0.0 0.0
209 418.73 0.1342 0.0 12.500 1.677 Vol = 1 r, a1
209 31.68 3.31 0.0 12.500 50.643
to 120.0 0.0 0.0 0.0
211 387.05 0.1160 0.0 12.500 1.450 Vel = 14.43
211 34.89 3.31 0.0 12.500 52.093
to 120.0 0.0 0.0 0.0
213 352.16 0.0974 0.0 12.500 1.217 Vel = 13.13
213 39.50 3.31 0.0 ' 12.500 53.310
to 120.0 0.0 0.0 0.0
215 312.66 0.0782 0.0 12.500 0.977 Vel = 11.66
215 45.31 3.31 0.0 12.500 54.287
to 120.0 0.0 0.0 0.0
217 267.35 0.0585 0.0 -1 2,500 0.731 Vel = 9.97
217 52.22 3.31 0.0 1.500 55.018
to 120.0 0.0 0.0 0.0
219 215.13 0.0392_ 0.0 12.500 0.490 Vel = 8.02
219 60.10 3.31 0.0 12.500 55.508
to 120.0 0.0 0.0 0.0
221 155.03 0.0214 0.0 12.500 0.267 Vel = 5.78
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems
Page 102010771 - B1S5RA1
Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv •"'•" NotesPointQtPf/Ft Eqv. Ln. Total Pf Pn
221 68.86 3.31 0.0 12.500 - 55.775 - - - - - - -- -
to 120.0 0.0 0.0 0.0
223 86.17 0.0072 0.0 12.500 0.090 Vel = 3-21
223 0.0 1.728 T 11.29 2.710 55.865
to
86.17
to
0.0
120.0
85.006
0.0 11.290 1.174
0.0001 0.0
222 86.17 0.1707
154.02
0.0 14.000 2.390 Vet = 11.79
222 0.0 1.728 2J 22.58 103.110 57.081
202 _ 154.02
to
0.0
120.0
6.997
0.0 22.580 1.858
1.728 J 11.29
122 86.17 0.1707
to
0.0 125.690 21.455 Vel = 11.79
122 0.0 1.728 J 11.29 29.450 76.678
Vel = 21.07
H9
to
1.728
120.0
7.500
0.0 11.290 1.142
to
120.0
123 86.17 0.1707
0.134
0.0 _ _ 40.740 6.955 Vel = 11.79_
123 0.0 3.31 T 21.71 10.420 84.775
Vel = 15.25
to
39.15
120.0
0.0
0.0 21.710 0.0
to
102
125 86-17 0.0072
l
0.0 A2.130,,-_ 0.231 Vel = 3.21
7.500 0.926 Vel = 9.90
H11 37.42 1.728 0.0 7.500 11.162
H12
0.0
1.728 0.0 7.500 10.787 K Factor = 11.20to
86.17
120.0 0.0 0.0
85.006 K Factor = 9.35
NEW PATH
1.88 0.0001 0.0 0.001
203 154.02 1.728 T 11.29 2.710 46.111
to
to
120.0 0.0 11.290 1.174
0.139
202 _ 154.02 0.4998_ 0.0 14.000 6.997 Vel 21.07
202 0.0 1.728 J 11.29 34.780 37.940
to
to
120.0 0.0 11.290 0.489
0.134
H9 154.02 0.4998_ 0.0 4.6.070 23.028 Vel = 21.07
H9 42.54 1.728 0.0 7.500 14.423 K Factor = 11.20to
to
120.0 0.0 0.0 0.139
0.134
H10 111.48 0.2749 0.0 7.500
7.500 2.131
H16 41.39 1.728 T 11.29
2.062 Vel = 15.25
H10 39.15 1.728 0.0 7.500 12.222 K Factor = 11.20to
102
120.0 0.0 0.0 0.134
13.662
H11 72.33 0.1235 0.0 7.500 0.926 Vel = 9.90
H11 37.42 1.728 0.0 7.500 11.162 K Factor = 11.20to120.0 0.0 0.0 0.134
H12 34.91 0.0321 0.0 7.500 0.241 Vel = 4.78
H12 36.79 1.728 0.0 7.500 10.787 K Factor = 11.20to120.0 0.0 0.0 0.134
H13 1.88 0.0001 0.0 7.500 0.001 Vel = • 0.26
H13 36.55 1.728 0.0 7.500 10.654 K Factor = 11.20to120.0 0.0 0.0 0.139
H14 38.43 0.0384 0.0 7.50_0 _ 0.2_88 Vel =
H14 36.81 1.728 0.0 7.500 10.803
5.26
K Factor = 11.20to120.0 0.0 0.0 0.134
H15 75.24 0.1328 0.0 7.500 0.996 Vel = 10.29
H15 38.26 1.728 0.0 7.500 11.665 K Factor = 11.20to120.0 0.0 0.0 0.134
H16 113.5 0.2841 0.0 7.500 2.131 Vel = 15.53
H16 41.39 1.728 T 11.29 15.760 13.662 K Factor = 11.20
0 120.0 0.0 11.290 0.420
102 154.89 0.5051 0.0 27.050 13.662 Vel = 21.19
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems
Page 112010771 - B1S5RA1
Date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt PtRef. "C" or Ftng's Pe Pv '*""'• NotesPointQtPf/Ft Eqv. Ln. Total Pf pn
102 0.0 1.728 J 11.29 29.450 26.904
to
30.06
120.0 0.0 11.290 1.142
103 154.89 0.5051 0.0 40.740 20.578 Vel = 21.19
206
0.0
0.0243' 0.0 14.000 0.340 Vel = 4.11
206
154.89
1.728 2J 22.58 103.040
48.624 K Factor = 22.21
NEW PATH
120.0 0.0 22.580 1.858
205 141.25 1.728 T 11.29 2.710 47.059
3.058
to
106
120.0 0.0 11.290 1.174
49.332
204 141.25 0.4259 0.0 14.000 5.962 Vel = 19.32
204 0.0 1.728 J 11.29 37.390 39.923
0.991
to 120.0 0.0 11.290 0.537H17 ___-_141.25 0.4259_ 0.0 48.680 20.733_ Vel = 19.32
H17
to
48.37 1.728 0.0 7.880 18.653 K Factor = 11.20120.0 0.0 0.0 0.143H1892.88
0.
1961 0.0 7.880 1.545 Vel = 12.71
H18
to
46.13 1.728 0.0 7.880 16.965 K Factor = 11.20120.0 0.0 0.0 0.143H1946.75 0.0551 0.0 7.880 0.434 Vel = 6.40
H19
to
45.34 1.728 0.0 7.880 16.388 K Factor = 11.20120.0 0.0 0.0 0.143H2O1.41
to
1.728 0.0 7.880 16.245 K Factor = 11.20120.0 0.0 0.0 0.139H2143.73 0.0487 0.0 7.880 0.384 Vel = 5.98
H21
to
45.48 1.728 0.0 7.880 16.490 K Factor = 11.20120.0 0.0 0.0 0.143H22 _ 89.21 0.1820 0.0 7.88_0 1.434_Vel 12.20H22
to
47.23 1.728 J 11.29 26.250 17.781 - K Factor = 11.20 _ - 120.0 0.0 11.290 0.611104136.44 0.3995 _ 0.0 37.540_ 14.996 Vel = 18.67
104 0.0 1.728 T 11.29 29.450 32.166to120.0 0.0 11.290 1.142
105 136.44 0.3995 0.0 40.740 16.274 Vel = 18.67
0.0
136.44 49.582 K Factor= 19.38NEWPATH
207 30.06 1.728 T 11.29 2.710 48.966to120.0 0.0 11.290 1.174
206 30.06 0.0243' 0.0 14.000 0.340 Vel = 4.11
206 0.0 1.728 2J 22.58 103.040 48.132
to 120.0 0.0 22.580 1.85810630.06 0.0243 0.0 125.620 3.058 Vel = 4.11
106 0.0 1.728 T 11.29 29.450 49.332
to 120.0 0.0 11.290 1.142
107 30.06 0.0243 0.0 40.740 0.991 Vel = 4.11
0.0
30.06 51.465 K Factor= 4.19
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems
7r11n771 - R1_Qr,RA1
12 =
R-10-17
109 31.69 0.0268 0.0 40.740 1.093 Vel - 4.34
0.0
31.69 53.590 K Factor = 4.33
NEW PATH
211 34.89 1.728 T 11.29 2.710 52.093 -
to 120.0 0.0 11.290 1.174
Hyd. Qa Dia. Fitting Pipe Pt Pt
0.0 ------
Ref.
0.449
C" or Ftng's Pe Pv """" Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
to
NEW PATH
120.0 0.0
209 31.69 1.728 T 11.29 2.710 50.643
4.026
to 120.0 0.0 11.290 1.174
11.29
208 31.69 0.0268 0.0 14.000 0.375 Vel = 4.34
208 0.0 1.728 2J 22.58 103.040 49.844
111
to
0.0321
120.0 0.0 22.580 1.858
Vel = 4.77
108 31.69 0.0268 0.0 125.620 3.369 Vel = 4.34
108 0.0 1.728 T 11.29 29.450 51.355
to
55.984
120.0 0.0 11.290 1.142
109 31.69 0.0268 0.0 40.740 1.093 Vel - 4.34
0.0
31.69 53.590 K Factor = 4.33
NEW PATH
211 34.89 1.728 T 11.29 2.710 52.093 -
to 120.0 0.0 11.290 1.174
210 34.89 0.0321 0.0 ------ 14.000 0.449 Vel = 4.77
210 0.0 1.728 2J 22.58 103.040 51.368
to 120.0 0.0 22.580 1.858
110 0.0320' 0.0 125.620 4.026 Vel = 34.89
110 0.0 1.728 T 11.29 29.450 53.536
4.77
I
0 120.0 0.0 11.290 1.142
111 34.89 0.0321 0.0 40.740 1.306 Vel = 4.77
0.0
34.89 55.984 K Factor = 4.66
NEW PATH
213 39.49 1.728 T 11.29 2.710 53.310
to 120.0 0.0 11.290 1.174
212 39.49 0.0404 0.0 14.000 0.565 Vel = 5.40
212 0.0 1.728 2J 22.58 103.040 52.701
to 120.0 0.0 22.580 1.858
112 39.49 0.0403 0.0 125.620 5.064 Vel = 5.40
112 0.0 1.728 T 11.29 29.450 55.907
to 120.0 0.0 11.290 1.142
113 39.49 0.0403 0.0 40.740 1.642 Vel = 5.40
0.0
39.49 58.691 K Factor = 5.15
NEW PATH
215 45.32 1.728 T 11.29 2.710 54.287
to 120.0 0.0 11.290 1.174
214 45.32 0.0520 0.0 14.000 0.728 Vel = 6.20
214 0.0 1.728 2J 22.58 103.040 53.841
to 120.0 0.0 22.580 1.858
114 45.32_ 0.0520 0.0 125.620 6.531 Vel = 6.20
114 0.0 1.728 T 11.29 29.450 58.514
to 120.0 0.0 11.290 1.142
115 45.32 0.0520 0.0 40.740 2.118 Vel = 6.20
0.0
Computer Programs by Hydratec Inc. Revision: 50.52.1
Final Calculations - Hazen -Williams
Wiginton Fire Systems Page 13-
2010771 - B1S5RA1 date 5-19-17
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv """' Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
45.32
NEW PATH
61.774
217 52.22 1.728 T 11.29 2.710 55.018
to 120.0 0.0 1.1.290 -1.174
216 52.22 0.0676 0.0 14.000 0.947
216 0.0 1.728 2J 22.58 103.040 54.791
to
52.22
120.0 0.0 22.580 1.858
116 52.22 0.0676 0.0 125.620 8.488
116 0.0 1.728 T 11.29 29.450 61.421
to
68.86
120.0 0.0 11.290 1.142
117 52.22 0.0676 0.0 40.740 2.753
K Fact Ir = 5.77
Vel = 7.14
T_
Vel = 7.14
Vel = 7.14
K Factor
Vel = 8.22
Vel = 8.22
1 1 _ O Tri
0.0
52.22
60.09
65.316
NEW PATH
69.423 K Factor 7.21
NEW PATH
219 60.09 1.728 T• : ; 11.29 2.710 55.508
to
68.86
120.0 0.0 11.290 1.174
2_18 _ _ 60.09_ 0.0876 0.0 14.000 1.227
218 0.0 1.728 2J 22.58 103.040 55.561
to
0.0
120.0 0.0 22.580 1.858
118 60.09 0.0876 0.0 125.620 11.008
118 0.0 1.728 T 11.29 29.450 64.711
to
1.858
120.0 0.0 11.290 1.142
110 rn n0 n AG7R A A AA 7AA G7A
K Fact Ir = 5.77
Vel = 7.14
T_
Vel = 7.14
Vel = 7.14
K Factor
Vel = 8.22
Vel = 8.22
1 1 _ O Tri
0.0
60.09 69.423 K Factor 7.21
NEW PATH
221 68.86 1.728 T 11.29 2.710 55.775
to 120.0 0.0 11.290 1.174
220 68.86 0.1127 0.0 14.000 1.578 Vel = 9.42
220 0.0 1.728 2J 22.58 103.110 56.179
to 120.0 0.0 22.580 1.858
120 68.86 0.1127 0.0 125.690 14.171 Vel = 9.42
120 0.0 1.728 T 11.29 29.450 68.492
to 120.0 0.0 11.290 1.142
121 68.86 0.1127 0.0 40.740 4.593 Vel = 9.42
0.0
68.86 74.227 K Factor 7.99
1 Computer Programs by Hydratec Inc. Revision: 50.52.1
r
AutoPeaking Summary
Wiginton Fire Systems Page 14
2010771 - B1S5RA1 Date 5-19-17
kuto Peaking Summary - List of Pipes for Area Calculated
Left Right
Side Side
From To Length From To Length
H8 100 15.760 H1 200 34.780
12.789
H16 102 15.760 202 H9 34.780
H22 104 26.250 204 H17 37.390
H8 100 15.760 H1 200 34.780
H16 102 15.760 202 H9 34.780
H22 104 26.250 204 H17 37.390
Flow Safety Pressure
Required Margin Differential
Left 7.500 i 1394.109 13.125 0.336
Area Calculated 1394.581 12.789 0.000
Right 7.500 i 1395.026 12.882 0.093
Typical Distance Between Heads = 7.500
Split Point Used in Worst Area Peaked = H5
Split Point Used in Area Calculated = H5
Computer Programs by Hydratec Inc. Revision: 50.52.1
MP
N
F
Z
W
d
a
W
d
m
W
C
M
Wigint el
FIRE SYSTEMS
699 Aero Lane, Sanford, FL 32771
TEL: 407-585-3200 - FAX: 407-585-3277
www.wigintonfiresystems.com
2010771
Ganesh North -
Monroe Road
Sanford, FL 32771
Submittal: One
Dated: May 19, 2017
Building One
The materials submitted in this package...
are intended to describe the type and quality of all materials to be used on this
project. This submittal intends that all materials, appliances, pieces, parts; and
craftsmanship, will be equal to.and/or better than the specific item shown and that
actual per foot friction losses will be equal to and/or less than indicated herein.
Some of the items included may be substituted due to common procurement,
stocking and supply procedures, scheduling requirements, etc. at the option of
WFS, however ALL supplied and installed materials will meet the requirements of
the applicable NFPA code in effect at the time of installation.
UNIT PPC ORDER No.
JOB CUSTOMER PO No.
Ganesh North
PUMP 8 X 8 X 18 VIP CAPACITY 1250 G.P.M. Q 254 FT. HD.
MOTOR OOP MAKE Weg FRAM JPV
125 H.P. 3 PHASE 60 CYCLE60 VdL7P R.P.M.
CERTIFIED BY- John M. Bolinger DAT02114/16
UNIT DIMENSIONS
MOTOR
FRAME
C D BG UNIT
WEIGHT
286 JPV
31
787.4 13111991184 7
00 LBS
545 KGS
324 JPV 2?-
813
151/8 201/16
509.5
1318 BS
600 KGS384
326 JPV 338585 15T 20 LBS
630KGTS
364 JPV 351/4895.3
177/8
454
2111116
3
1508 LBS
685 KGS
365 JPV 351/483
17718 2111/16 1538 LBS
700 KGS17- 3T-
404 JPV 38112978
17718
454
235116
592
1730 LBS
786 KGS
405 JPV 38 112978
177/8
454
235/16 1855 LBS
843 KGS592
405 TCZ 38 1/2
978
17 7/8 23 5116`
592
1890 LBS
859 KGS454
UNIT WEIGHT = PUMP AND MOTOR COMBINED.
010254.0
S-
NOTE:
1) ALL DIMENSIONS ARE +1- 1/4' / 6Amm (EXCEPT FOR FLANGE DRILLING).
2) PRIMARY DIMENSIONS ARE INCHES.
SECONDARY DIMENSIONS ARE MILLIMETERS.
ROTATION
125 CLASS F.F.
08 / 203.2 SUCTION
013 1/2 J 343 FLANGE
8x 07/8 / 22.2 BOLT HOLES
EO. SP. ON A 011 3/4 / 298.5 B.C.
B.C. STRADDLES
14-JU VNt; A V U
BOLT HOLES
0215 B.C.
0
MOUNTING FOOT DETAIL Qj
PLAN VIEW _kk
CLEARANCE RECOMMENDED
TO REMOVE ROTATING ASSY.
125 CLASS F.F.
08 / 203.2 DISCHARGE
0151381 FLANGE
8x 07/8 / 22.2 BOL•T•HOLES
EO. SP. ON A 011 3/4 1298.5 B.C.
B_C. STRADDLES(i
O
PATTERSON PUMP COMPANY
AGORVXMWCWAlrr
5' 1504 ANSI FLANGE DIMENSIONS
SEE MOUNTING FOOT DETAIL)
OUTLINE DIMENSIONS
FOR
8X8X18VIP
W/ VARIOUS MOTORS
N4i N0. rRY
CO2 -118338 1
PAWN DATE
mcaudell NOV, 24, 2010
CALF APPRVo
NONE AP
400
35C
LU
LU
u- 30C
0
25C
J
2S 200
0
150
100
50
200
w
0 150
a
w
100
0
Y 50
m 0
Iii7iii
PATTERSON PUMP COMPANY
A Subsidiary of The Gormon-Rupp C*Gny
P. 0. Box 790
Toccoa, Georgio 30577
Telephone 706-886-2101
Fox 706-886-0023
www.pattersonpunps.com
11
DIA. 1780 RPM 1250 GPM 75 PSI to 137 PSI
173 to 317')
MODEL 8x8x18A VIP
IMP. D05-104403
CURVE A05-116622
2r o
14" DIA,
83.6%
v
20
0-
N.RS
U)
CL
z
18"1 DIA.
0 400 800 - 1200 1600 2000 2400 2800 GPM
SUCTION GAUGE
0-30# VAC 0-300# PRESS.
o 120 150
180
60
210
30
240
0
Cv 30 300
270/
VAC PRESS/ .
DIAL SUCTION GAUGE
DISCHARGE GAUGE
0-300# PRESS
120
150
180
90
210 '
60 w 240
30 v
270
WATER
300
DIAL DISCHARGE GAUGE
w
PATTERSON PUMP COMPANY
x A SMIDIARY OF TIC OORNw+•RUPP COMPANY
1/4" N.P T
1/4" N.P.T.
SUCTION & DISCHARGE
DIAL GAUGES
CO2 -99432
VN DATE
MEALOR 8/26/05
LE APPRvo.
NONE AP
3 r --I 15
n
FTA1 000
FULL VOLTAGE FIRE PUMP
CONTROLLERS
STANDARD SUBMITTAL PACKAGE
rairetror
NOTE: The drawings included herein are for standard controllers.
Actual "as built" drawings may differ from those seen here.
ASCOPower
Technologies® SBP1000-51(A)
Description - Firetrol® FTA1000 Full Voltage Fire Pump
Controllers are intended for use with electric motor
driven fire pumps where the capacity of the power
source permits full voltage starting. Full voltage is ap-
plied to the motor as soon as the controller is actuated.
The controller monitors, displays and records fire pump
system information.
Full voltage starting is simple and low cost and is pre-
ferred whenever the utility or emergency generator set
will permit this type of starting.
Approvals - Firetrol fire pump controllers are listed by
Underwriters' Laboratories, Inc., in accordance with
UL218, Stondord for Fire Pump Controllers, CSA, Standard
forindustrial Control Equipment, and approved by Factory
Mutual. They are built to meet or exceed the require-
ments of the approving authorities as well as NEMA and
the latest editions of NFPA 20, Instollotion of Centrifugal
Fire Pumps, and NFPA 70, National Electrical Code.
Standard Features—The following are included as stan-
dard with each controller:
Voltage surge protector
Main Disconnect Switch sized for connected motor
horsepower and voltage
Fire pump Circuit Breaker
Single handle Isolating Disconnect Switch/Circuit
Breaker mechanism
Motor contactor
Emergency Manual Run Mechanism to mechanically
close motor contactor contacts in an emergency con-
dition
Built-in Start and Stop push -buttons to bypass auto-
matic start circuits
Minimum Run Timer Off Delay Timer
Daylight Savings Time Option
Weekly Test Timer
Elapsed Time Meter
LrIbr 'fin §
0
Door mounted display interfacepanel featuring a 128
x 64 pixel backlit LED Graphical Display, Membrane
Type User Control Push -buttons and easy to read LED
Indicators for:
POWER AVAILABLE
ALARM
TRANSFER SWITCH NORMAL (If unit ordered with
Automatic Power Transfer Switch)
TRANSFER SWITCH EMERGENCY (If unit ordered with
Automatic Power Transfer Switch)
SYSTEM PRESSURE LOW
PUMP RUNNING
DELUGE OPEN
REMOTE START
INTERLOCK ON
FAIL TO START
MOTOR OVERLOAD
EMERGENCY ISO SWITCH OFF (If unit ordered with
Automatic Power Transfer Switch)
PHASE FAILURE
PHASE REVERSAL
AUTOMATIC SHUTDOWN DISABLED
OVERVOLTAGE
UNDERVOLTAGE
Digital Pressure Display
USB Host Controller and Port
Solid State Pressure Transducer
Data Log
Event Log (3000 Events)
True RMS Metering with simultaneous 3 Phase Display
of Amps, Volts, Frequency, Pressure and Alarm Mes-
sages
Disk Error message
Disk Near Full message
Pressure Error message
Motor Over 320% message
Local Start message
Remote Start message
Emergency Start message
Fail To Start message
Undervoltage message
Overvoltage message
NEMA Type 2 enclosure
Suitable for use as Service Equipment
Each standard controller comes with user configurable
options for:
Interlock Alarm • Low Pressure Audible
Low Suction • Pump Run
User Defined Input • Weekly Test
O
EMERSON -
Network Power
Main Fire Pump Controller
The main fire pump controllershall be a factory assembled,
wired and tested unit and shall conform to all the requirements
of the latest edition of NFPA 20, Standard for the Installation
of Stationary Pumps for Fire Protection and NFPA 70, National
Electrical Code.
The controller shall be listed by Underwriters Laboratories,
Inc., in accordance with UL218, Standard for Fire Pump Con-
trollers, CSA, and Canadian Standards Association CSA -C22.2,
Standard for Industrial Control Equipment (cULus), approved
by Factory Mutual and approved by the City of New York for
fire pump service.
Starting Method
The controller shall be of the combined manual and auto-
matic type designed for:
XFull Volta e Starting 1.
D Wye (Star -Delta Open Transition Starting
D Wye (Star) -Delta Closed Transition Starting
I Part Winding Starting
I Primary Resistance Reduced Voltage Starting
I Autotransformer Reduced Voltage Starting
I Digital Soft Start Reduced Current Starting
of the Fre pump motor having the horsepower, voltage, phase
and frequency rating shown on the plans and drawings. The
controller components shall be housed in a NEMA Type 2 (IEC
IP11) drip -proof, wall mounted enclosure.
Withstand Ratings (Short Circuit Current Ratings)
All controller components shall be front mounted, wired
and front accessible for maintenance. The minimum withstand
rating of the controllers shall not be less than 100,000 Amps
RMS Symmetrical at 200-600 Volts'. If the available system
fault current exceeds these ratings, the controllers shall be
supplied with a withstand rating of 150,000 or 200,000 Amps
RMS Symmetrical, as required.
Note: 100,000 Amp withstand rating not available in
some larger horsepowers. Consult factory for
details.
Isolation Switch and Circuit Breaker
The controller shall include a motor rated combination
isolating disconnect switch/circuit breaker, mechanically inter-
locked and operated with a single, externally mounted handle.
When moving the handle from OFF to ON, the interlocking
mechanism shall sequence the isolating disconnect switch ON
first, and then the circuit breaker. When the handle is moved
from ON to OFF, the interlocking mechanism shall sequence
the circuit breaker OFF first, and then the isolating disconnect
switch.
The isolating disconnect switch/circuit breaker shall be
mechanically interlocked so that the enclosure door cannot be
opened with the handle in the ON position exceptby a hidden
tool operated defeater mechanism. The isolating disconnect
switch circuit breaker shall be capable of being padlocked in
the OFF position for installation and maintenance safety, and
shall also be capable of being locked in the ON position without
affecting the tripping characteristics of the circuit breaker.
The controller door shall have a locking type handle and three
point cam and roller vault type hardware. The circuit breaker
trip curve adjustment shall be factory set, tested and sealed for
the full load amps of the connected motor. The circuit breaker
shall be capable of being field tested to verify actual pick up,
locked rotor, and instantaneous trip points after field installa-
tion without disturbing incoming line and load conductors.
Operator Interface
The fire pump controller shall feature an operator interface
with user keypad. The interface shall monitor and display motor
operating conditions, including all alarms, events, and pressure
conditions. All alarms, events, and pressure conditions shall be
displayed with a time and date stamp. The display shall be a
128x64 Backlit LED capable of customized graphics and Cyrillic
type character display. The display and interface shall be NEMA
rated for Type 2, 3R, 4, 4X, and.12 protection and shall be fully
accessible without opening the controller door. Thedisplayand
user interface shall utilize multiple levels of password protection
for system security. A minimum of 3 password levels shall be
provided.
AmmeterlVoltmeter
The fire pump controller operator interface shall be
capable of displaying true RMS digital motor voltage and
current measurements for all three phases simultaneously.
Displays requiring push-button and selector switches to
toggle between phases or current and voltage shall not be
accepted.
Voltage and current shall be measured by True RMS
technology to provide the most accurate measurement for
all sine waves, including non -sinusoidal waveforms. Average
responding meters will not be accepted.
Digital Status/Alarm Messages
The digital display shall indicate text messages for the
status and alarm conditions of:
Motor On Sequential Start Time
Minimum Run Time Local Start
Off Delay Time Remote Start
Fail to Start System Battery Low
Under Voltage Over Voltage
Locked Rotor Trip Over Frequency
Emergency Start Motor Over 320%
Drive Not Installed Motor Overload
Disk Error Printer Error'
Disk Near Full Pressure Error
The Sequential Start Timerand Minimum Run Timer/Off Delay
Timersimershall be displayed as numeric values reflecting the value
of the remaining time.
LED Visual Indicators
LED indicators, visible with the door closed, shall indi-
cate:
Power Available • Alarm
Pump Running • System Pressure Low
O
EMERSON_
Network Power