HomeMy WebLinkAbout1200 Albright Rd #22181 (from 1987)NAME
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 C
N
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
L j 1 2 ❑ , 3 ., ❑ EX HAZ;
Z
NFPA 231C: FIGUR
❑ E --__.
OTHER
y ,
CURVE
t7
❑ (Specify)
w
,❑ SPECIFIC RULING` MADE
DATE
p
,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
.v
LONGITUDINAL 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 m
1
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
AQ
cRoss MAL"
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 se
Q 3oo• 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
'—
kPE
LGTH•
(.•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 u
Q
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 OPERATION
a
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 RISER
SUMMARY "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
9
N
ELEVATION
¢
GPM .FLOWING ► o
w
ELEVATIONWELL
M ATE
¢
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 ❑ ENCAPSULATED
.
❑ DOUBLE ROW ❑ 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 CEILING
O
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, 81121
No. 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
9P
12(
V
11f
1(
10(
c
90
E
80
a
70
E
Ln
a`
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
—TO12
T. 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= ►0.24
Q
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.ta8
Q123.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
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