1200 Albright Rd - #22181 (1987) (METAL MANUFACTURING) (ADDITION) DOCUMENTSNAME
DATE' OcT_ Z i98-1 `
LOCATION zoo D S o O' Ft
BUILDING New 1°a'I A-aoiT.o
S SYSTEM NO:`777
CONTRACTOR u wl S T g T 1 f1 P ; ,. , o CN
CALCULATED BY CON7RAGT. N0. R,'ri`
CONSTRUCTION. COMBUSTIBLE NON COMBUSTIBLE77
DRAWING NQ
CEILING HEIGHT a l FT: OCCUPANCY
NFPA ix.. LT.. HAZ. ORD HAZ. GR
NFPA 231 Lj 1 2 , 3 ., EX HAZ;
Z NFPA 231C: FIGUR E --__.
OTHER
y ,
CURVE
t7 Specify)
w SPECIFIC RULING` MADE DATEp
BY
ui
w
77777-7777
AREA OF SPRINKLER OPERATION 1 500 . SYSTEM
N DENSITY i 9
AREA: PER SPRINKLER 1 3Q Mpx
WET_ DRY DELUGE, PRE:ACTION
HOSE ALLOWANCE:GPM.:. "INSIDE cN7r,z.o
SPRINK ER RN ZZ E
HOSE ALLOWANOE GPM:.'OUTSIDE ,.`': Sa
MAKE
SIZE
MODEL,': UPR 6+T:
RACK SPRINKLER ALLOWANCE .' TEMPERATURE''RATING ' .2 2
CALCULATION
SUMMARY
GPM REQUIRED L366ji PSI REQUIRED 42 a I' AT BASE; OF RISER C" FACTOR USED OVERHEAD 1 20 11NDERGROUND L4o WATER
FLOW TEST y
DATE 8 TIME PUMP
DATA RATED
CAPACITY TANK
OR R 4 RVOIR CAPACITY
a
STATIC PSI .. l AT PSf ELE VAT,I N
RESIDUAL PSI S 5 ELEVATION GPM
FLOWING o ELEVATION
M T WELL
Fww- PROOF FLOW GPM :- LOCATION
QSs ME'' QVAILi4 LE,: AT A Pr,r' n %''n Au0 SOURCE
OF INFORMATION LTY OF K1l1 ORD COMMODITY
CLASS LOCATIONkw w
STORAGE HEIGHT AREA AISLEnWIDTH STORAGE.
METHOD: SOLID PILED % .PALLETIZED q, RACK °10 SINGLE
ROW CONVENTIONAL PALLET AUTOMATIC STORAGE ENCAPSULATED DOUBLE
ROW. SLAVE PALLET. - SOLIDSHELVING NON - o Y
MULTIPLE ROW . ;
OPEN ENCAPSULATED.. c FLUE
SPACING
1N I NCkESI. CLEARANCE FROM TOP OF STORAGE TO CEILING O vLONGITUDINAL
TRANSVERSE FT IN. HORIZONTAL BARRIERS
PROVIDED E45-ISO
vI (10-76)
HYDRAULIC CALCULATIONS
Abbreviations
Hazen & Williams Flow. Value
tine Calc " Branch Line :Being Calculated`
Spkl." 3 Number of Sprinklers Being Calculated,
E:H.P.
11 End Head Pressure
K11 K Factor
Q" Gallons .Per Minute ._@ Specific Locati on
Flow" Total Gallons..Flowing
Diam" Inside Diameter of Piping
L/ft" Friction Loss Per. Foot
FF" Friction Loss Per Foot
Lgth" Length of Piping Plus Fitting Loss
Len". Length of Piping Plus Fitting Loss
Loss" Friction Loss for Total Length.
PT" Pressure Total
End P" Starting Pressure for Main Calculations
P E," Pipe Elevation Loss
Stat". Static Pressure
Resd" Residual Pressure
Avail" Pressure Available.@ System Demand
VVA I EK I- LUVV TEST SUMMARY SHEET
Hydrant
No.
Outlet I.D.
inches
Pitot Press.
psi
Flow
gpm
Residual
psi
Date: Time: Cont. No, b tzl
Cont. Name: R i m m1
2 Address: l20o A Rono• r.
3
Total Flow Static Press: psi Flow 9 20 psi gpm
I
Scale A 100 200 300 400 S00 600 700 800 900 1000
Scale B 200 400 600 800 1000 1200 1400 1600 1800 2000
Scale- C. 400 800 1200 1600 2000 2400 2800 3200 3600 The Viking Co,DorJlion 4000
CONTRACT NO. 8 7 12 1 SHEET NO I OF Z
NAME R t M M Fa DATE _ O--t 9 - 19 8-,
LOCATION SRNFoa 1'LpF2,p 1
NOZZLE
TYPE a
LOCATION
FLOW
IN
G.P.M..
PIPE
SIZE
FITTING
81
DEVICES
PIPE EQUIV.
LENGTH
FRICTION
LOSS
PS-I./FT
REQUIRED
P.S.I.
HYD.
REF.PT
Q
ELEV. NOTES
K= 5-c-
I
LGTH. to-o
IrolB
PT 16.sl I
Q 22.8
FTG. — PF 1.(.I a
TOT 10-o PE- .359
14
LGTH.10-o
1 663
PT Z
FT G'• PF 1. r.cs
Q 46.31 OT• 10-0 PE - . 359
Q 7-4.50
12
LGTH- to-o
I`8F
PT .13.3
FTG. — PF .684
Q,o.B T. to-o PE •-.35
Q 25.33
1,2
LGTH. wo-o
29t4
PT 20.458 14
FTG. — PF t•942
Q U-14 T. 10-0 PE - .35
t
2
T lo.o GTH. -1-o PT 23.o41 5
k` too TG• o•o PF 3.-12.
Q IZ3.02 TOT. PE -5
Q LGTH- PT 26• % A-8 RS9 AT TOP
of alseR
NPP e • K= z3.8S
FTG. PF
Q TOT. PE
Q GTH. PT
T • PF
Q TOT PE
Q
I„
LGTH- l0-o PT lo.
022.5
FTG- - PF .616
TOT. PE -. S9
Q
23.0
1 4
LGTH- Io-o
1
PT
FTG. - PF
0 4ra.31 TOT 10 0 PE - •35-1
o Q
1'Z
LGTH• zo-o
o as
PT 19.133
FTG- — PF . 1• S
Q 46.31 TOT Zo-o PE - .116
K= . n
LGTH. ,-o
0232
PT .985
Q 4(..31
2e= ,o-o FTG- 20-o PF .62G
TOT. 2,-o PE - .zzs
Q L H. PT 2o.3e` I C REq AT lop
CC: RIS 4MR
N,PPLE- K- o . z c- Q
FTG- PF
TOT • PE
Q LGTH- PT
0
F T PF
TOT. PE
Q
2
LGTH z-o
jo3
PT zc.53 RsER t.1.Pr E
PTS- A R
23.68
T FTG. to-O PF 1.243
01z3.o2 TOT. 1z-o PE —
QLGTH- PT 21•1-79 A Base 5F R• 1J.
K = 23.339
FTG- PF
0 TOT. PE
oLGTH- z-o PT 7.o.36 Rl segz hl,orLe
PTS- C
14= c.ze-
FTG- I e - PF 204
Q v1..31 TOT. 12-0 PE —
Q LGTH. PT Zo.s9 c BRSE or
Risea N,Pr«
K= 10.2-o9
O
FTG- PF
TOT. PE
o LGTH.
JPE
PT
Q
FTG- PF
T T. I
PT
r --rvc, P1{„V I GU IN U.J.H.
CONTRACT NO. 8-1 1 Z 1 SHEET NO 2 OF Z
NAME FZ M N1 F DATE coc-s o1 - 19a-i
j LOCATION F-Lorevoa
NOZZLE
TYPE 81
LOCATION
FLOW
IN
G.P.M.
PIPE
SIZE
FITTING
a
DEVICES
PIPE EQUIV.
LENGTH
FRICTION
LOSS
P.S•I./FT
REQUIRED
P.S.I.
HYD•
REF.PT
Q
ELEV. NOTES
1<= 23.339
L'w'
y
Ll z-o
o o3s
AQcRossMAL"
Q 123. 01
FTG. — PF .04
TOT 1'L-o PE —
23.339 A 123.10
4
LGTH. 1z-3
o1z9
PT 21•622 5
FTG• — PF .Isa
Q 246.12 TOTIZ-3 PE —
1<. lo.zo9 0 54•o s- LGTH. o - '
oz lz
T -.98 c
FTG• 30-0 PF .9 b9
Q 300-1z T• 234-1' PE —
LGTH. o a
o2tz
PT 32.943 ToP cr R,sg¢
Q 3oo•1Z
t-T -to FTG• 44-0 PF 1-s-),+
Cr va= 22•o TOT. -14-3 PE 6.3o
G GTH. PT Li Z.8n Bgse oc
Rise2
TG- PF
Q TOT. IPE
C= }o A L H. 68-0
003o
PT 42.8 1 UMME.R CROU 0Z1>
2.E FTG- Ie-o PF seQ3oo• 12 TOT. 281;-o PE --
0
O1
T.?30-0 TH. 1-o
0030
3.e-1s A1a T
R t_BRG tT
ArC Coµw. TO
G•.: 3-0 T •3-0 2.892
Q 300.i2 TOT. 64 kPELGTH• s(.j-
6.sz cot
F1 a e SPRi--AWLEQ
TG•
TOT•
p LGTH. PT Svsi c.
FTG• PF
Q TOT PE
Wrw No ti 0 550.1
L
T o So-o LGTH• 31-o
009 1
PT 43.615
Q
s-o FTG• 33-o PF 11Z
TOT gtoy-o PE
a LGTH. PT s2.44-I
Ar Aka-Pot-r
4. ALL8R14 uQ
FTG• PF
TOT- PE
9 L TH. PT 6 S. 5z1 PT.
O
FTG• PF
TOT PE
p LGTH• PT
Q
FTG• PF
TOT. PE
Q L TH PT
0
FT . PF
TOT. PE
Q FTGH PF
Q TOT PE
Q GTH• PT
Q
FTG• PF
TOT. PE
o LGTH. PT
FTG• PF
TOT. PE
0 LGTH_
IPE
PT
Q FTG• PF
T T• I
PT
1
f HYDRAULIC DESIGN INFORMATION SHEET
i
NAME R
LOCATION 1200 DATE' OCT. i2, 198"I
s
BUILDING New`". q8 A--aoiT gu
CONTRACTOR r` R P'sa 1 w 9 SYSTEM No. N
LE0
CALCULATED BY CONTRACT NO.,. Z i>
CONSTRUCTION: COMBUSTIBLE NON-COMBUSTIBLE
OCCUPANCY "
DRAWING NO; is o F 1.
CEILING HEIGHT aR e`s
M T A rat
a Z
ji
NFPA 13 LT. HA ORD HAZ. GP. ' }' U 1 2 3 EX HAZ. NFPA 231 NFPA 231C•r FIGURE
OTHER (Specify)77777777 CURVE ,.
W SPECIFIC RULING MADE BY DATE .. , o
W AREA OF SPRINKLER OPERATIONa
N
j N
DENSITY I "9
AREA PER SPRINKLERSPRINK
WET :
SYSTEM TYP
DRY DELUGE . PRE -ACTION_`
HOSE ALLOWANCE GPM: INSIDE MAKE CCuTsia
ER R N ZZ E ;
HOSE ALLOWANCE GPM: OUTSIDE "' "2 So SIZE %z"
MO DEL uPa 6+T.'
RACK SPRINKLER ALLOWANCE- K-FACTOR s
r TEMPERATURE''RATING
CALCULATION GPM REQUIRED 30o i2 PSI REQUIRED 'tz. 8) AT: BASEOF RISERSUMMARY "C" FACTOR USED OVERHEAD I Zo UNDERGROUND I ' 4a'
i
a
WATER FLOW TFS T_
DATE & TIME
PL)MP DATA
4
TANK Oft RFS RVOIR
d
J RATED CAPACITY CAPACITY'
d
i
STATIC PSI ': 01
F3ESIDUAL PSI 5 5
AT PSI E LEVATION a
9NELEVATION
GPM .FLOWING o
w ELEVATIONWELLMATE
PROOF FLOW GPM:.
i
LOCATION FaSSuMED' QVii Ri . .."4T IRPot2T` ono Auk
SOURCE OF INFORMATION STY OF Sq L4:*
L R 1 r
P
I COMMODITY C LASS LOCAT:'ION'
Uj STORAGE HEIGHT ' AREA AISLE WIDTH
Q STORAGE METHOD: SOLID PILED % PALLETIZED y, RACK % o
SINGLE ROW CONVENTIONAL PALLET AUTOMATIC STORAGE ENCAPSULATEDDOUBLEROW SLAVE PALLET S OLID SHELVING NON-
C) Y MULTIPLE ROW OPEN ENCAPSULATED_
g
v
cc
Q FLUE SPACING IN INCHES CLEARANCE FROM TOP OF STORAGE TO CEILINGO
v LONGITUDINAL TRANSVERSE FT IN.
i HORIZONTAL r BARRIERS PROVIDED
E45-ISO W1 (10-76)
qa
HYDRAULIC CALCULATIONS
9
Abbreviations
C.'= Hazen & Williams Flow. Value
Line Calc " Branch Line Being Calculated
Spkl." 3 Number of Sprinklers Being Calculated,
E.H.P." End Head Pressure
i K" K Factor
Gallons Per Minute ,@ Specific .Location
Flow" Total Gallons -Flowing
Diam" Inside Diameter of Piping
a
Friction Loss Per Foot
FF" Friction Loss Per Foot
Lgth" Length.of Piping Plus Fitting Loss
i
T.en" TPnvth of . Pi nl nn Pl inn F1 tti ncr T.n:ca
L-_-.- 1 ..
VV<-1 I F-1-f F- f ()W 1 1= -I 1 IAAAAAQN1 C1-1 1=T
Hydrant Outlet I.D. Pitot Press. Flow Residual Date: Time: Cont. No, 81121No. Inches psi gpm psi
1 Cont. Name: R I± m m
2 Address: i RoAo• SAF 3
Total
Flow Static Press: psi Flow 20 psi m 9P12(
V
11f
1(
10(
c
90
E
80
a
70
E
Lna`
60 50
40
30
20
1
10
0
Scale
A Scale
B Scale-
C. 4UU SUU I LUU 1 6UU LUUU L9UU L?JUU IzUU -'6UU The Viking Corporalion 4000 t
CONTRACT NO. B -1 121 SHEET NO I OF 2
NAME;_ R M m Fa DATE opt 9-19 n
LOCATION __ SAwFoao F'Lprsp
NOZZLE
TYPE 81
LOCATION
FLOW
IN
G.P.M..
PIPE
SIZE
FITTING
81
DEVICES
PIPE EQUIV.
LENGTH
FRICTION
LOSS
P.S.I./FT
REQUIRED
P.S.I.
HYD.
REFPT
Q
ELEV. NOTES
0
I "
LGTH. PT 1G.sl I
Q 22. a rFTG. PF
TOT PE- .3s9
0
14
LGTH. 10-o
I663
PT Z
Q yG.31
FTG. PF 1. cca
TOT Io-o PE -.359
0 2.4.50
z
LGTH. io _o
s,
T .13.3
Q i0.8
FTG. - PF 1.484
T. 1 o-o PE - . 359
Q 25.33 LGTH. o-o
29'+2
PT 20.458
Q 94.14
FTG. - PF 2.942
TO12T. l o - o PE - .359
LGTH. -I-o
13l a
PT 23.041 5
Q Izs.o2
t = iooFTG. o•o PF 3.12.
TOT. 2-o PE -. s
0 LGTH. PT 26. A-g Req AT Top
ov R seR
hl.PPLC • x=z3.aa
FTG • PF
0 TOT. PE
0 GTH. PT
Q
T - PF
TOT. PE
a
1"
LGTH.10-o PT .
Q 22 6
FTG. — PF . ara
TOT. PE -. s9
0
23.G4
14
GTH.Io-o
I l,63
PT n.929
FTG. - PF I - a1:3
Q 4io.31 TOT Io-o PE-.359
I< = o 0
I Z
LGTH.2o-b
o-las
PT 19.133
Q 4c.z1
FTG. — PF I. s
TOT 20-o PE
0 T = ,o-o LGTH. ,-o
0232
PT i .°185
Q 4.31
2e= 10-0 FTG- zo-o PF .tu.
TOT. 2'1-0 PE - .2z5
0 LGTH. T 2o.3e` c RE9 AT Tof>
ov Rls4aR
uPP e- It= 0.24Q
FTG• PF
TOT. PE
0 LGTH. PT
Q
FTG. F
TOT. rp E
0
2
LGTH z-o
103r-
PT 2G.53G Rise¢
PTS- A 4 Bf
23.ta8Q123.o2
T FTG. to-O PF 1.243
TOT. Iz-o PE —
0 LGTH. P 2-I.Tj9 A - 5 Bgse eF R.1.1.
K = 23.339
FTG. PF
Q TOT. PE
0
2
LGTH. 2 o
01
PT 2o.lal. RISER N,PrLe
PTS- C
1<= I o. 2e-
FTG. e-o PF .z04
Q 46.31 TOT. z-o PE -
0 LGTH. PT 20.s9 c qse oR
Rise¢ NkLe K=
1o.zor9 Q
FTG-
PF TOT.
PE 0
LGTH. PT Q
FTG.
PF T
T. p PT
CONTRACT NO. 81I2 SHEET NO 2 OF 2 g
c
NAME cT M n ti= DATE ocT d - LOCATION
FLor,,oa NOZZLE
TYPE
a LOCATION
FLOW
IN
G.
P.M. PIPE
SIZE
FITTING
sk
DEVICES
PIPE
EQUIV. LENGTH
I
FRICTION
LOSS
P.
S.I./FT REQUIRED
P.
S.I. HYD•
REF -
PT ELEV. NOTES 1<'
23.399 o LA.l. 4
MH.
12-o oo3s
T
z1.119 A CROSS Mate4 Q
Mol FTG. —
PF . 043 TOT
i PE — 1<'
2 3.339 0 123. o 4„
LGTH.
iz-3 t9
PT
Z.622 d Q
246.12TOT. FTG- -
PF 12
3 PE - 1<=
Io.Zo9 54.0 t •.
5-
LGTH- o- - ozlz
T -?
mb c Q3oo.
zTOT. FTG-
3o-o PF 9fo z3Li-
1'z, PE _ Q c:,=
z LGTH. io 3 o21Z PT
3Z.
943 Top or Rse2 Q 3oo.
lz 40 FTG.
6ti-o PF 1.s14 cr VRr
z2-o T. ,4-3 PE 6.30 q GTH.
PT ti. e Bast o c Ri s
r2 Q 3oo.z OT PE C= 0
e 011 L
H.
6s-o 003o PT
42.
gi uuo RCRou e 2.E
FTG. la-o PF sa Q 300.2 TOT 286-0 PE — C Q
3oo.
12 T.= 3_
cro T . I-o 003o PT
43.
61s A a ,eT ; Al - LEA
IG HT Ar. r-
04 . TQ c..: 3-
o T 33 0 PF 2.8gz TOT. 64
PE — LGTH. PT
4c.sG1' AVA a6le . Re sPR,
Q TG.
PF
TOT. PE
pLGTH- PT
SYST r. Q FTG-
PF
TOT PE
ITK Hose
sso.i2 L T=
ao-
o LGTH-31-0, 0091 PT
43.`-
is Q b
3 -o
v c.. FTG- 33-0 PF. .-11Z TOT PE _
e LGTH.
PT 52.4'61 Av^«we c. AT AMPor-
r ALL IIR.
G u Q FTG- PF
TOT. PE
L TH.
PT c S. 5zi Pr. Q FTG-
PF
TOT• PE
p LGTH
PT Q FTG.
PF
TOT: PE
0 LGTH
PT Q FTG.
PF
TOT PE
o LGTH.
p Q FTG-
PF
TOT. PE
o LdTH.
PT Q FTG.
PF
TOT. PE
o LGTH.
PT Q FTG-
PF
TOT. PE
o LGTH.
PT FTG- PF
TOT. P
PT J
I
DATE
COMMERCIAL
VALUATION ' ^ PERMIT FEE
1im