Autec_HYDRAULIC_CALCULATIONS.pdf

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Interior and Exterior Alterations of the existing AUTEC Federal Building in West Palm Beach, Florida
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GS-04P-15-BV-C-0013
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JENSEN HUGHES

725 PRIMERA BOULEVARD, SUITE 215

LAKE MARY, FL 32746

HYDRAULIC CALCULATIONS

FOR

AUTEC FEDERAL BUILDING

DRAWING NUMBER: FP104

HYDRAULIC REMOTE AREA #1

DATE: 06-18-15

-DESIGN DATA-

OCCUPANCY CLASSIFICATION: LIGHT HAZARD

DENSITY: 0.10 gpm/sq. ft.

AREA OF APPLICATION: 1,500 sq. ft.

COVERAGE PER SPRINKLER: 225 sq. ft. max.

NUMBER OF SPRINKLERS CALCULATED: 26 sprinklers

TOTAL SPRINKLER WATER FLOW REQUIRED: 644.7 gpm

TOTAL WATER REQUIRED (including hose): 744.8 gpm

FLOW AND PRESSURE (@ BR): 57 psi @ 645 gpm

SPRINKLER NOMINAL K-FACTOR: 5.6

CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 27050933 )

HRS SYSTEMS, INC.

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2

DATE: 6/18/2015 C:\PROGRAM FILES\HRS SYSTEMS\GSA AUTEC\GSA AUTEC.SDF

JOB TITLE:

WATER SUPPLY DATA

SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D

NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS.

TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI)

SOURCE 80.0 74.0 1250.0 77.7 744.8 67.2

AGGREGATE FLOW ANALYSIS:

TOTAL FLOW AT SOURCE 744.8 GPM

TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM

OTHER HOSE STREAM ALLOWANCES 0.0 GPM

TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 644.8 GPM

NODE ANALYSIS DATA

NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE

(FT) (PSI) (GPM)

A 10.0 K= 5.26 25.1 26.4 B 10.0 K= 5.26 25.1 26.4 C 10.0 K= 5.26 25.3 26.5 D 10.0 K= 5.26 23.6 25.6 E 10.0 K= 5.26 21.9 24.6 F 10.0 K= 5.26 22.6 25.0 G 10.0 K= 5.26 20.1 23.6 H 10.0 K= 5.26 19.8 23.4 I 10.0 K= 5.26 19.9 23.5 J 10.0 K= 5.26 18.7 22.8 K 10.0 K= 5.26 18.3 22.5 L 10.0 K= 5.26 18.9 22.9 M 10.0 K= 5.26 24.7 26.2 N 10.0 K= 5.26 24.7 26.1 O 10.0 K= 5.26 25.7 26.6 P 10.0 K= 5.26 24.6 26.1 Q 10.0 K= 5.26 24.1 25.8 R 10.0 K= 5.26 19.3 23.1 S 10.0 K= 5.26 20.4 23.8 T 10.0 K= 5.26 19.3 23.1 U 10.0 K= 5.26 19.7 23.3 V 10.0 K= 5.26 20.9 24.0 W 10.0 K= 5.26 25.6 26.6 X 10.0 K= 5.26 24.3 25.9 Y 10.0 K= 5.26 24.3 25.9 Z 10.0 K= 5.26 22.7 25.1 E1 17.5 - - - - 19.8 - - - G1 17.5 - - - - 18.7 - - - H1 17.5 - - - - 18.7 - - - I1 17.5 - - - - 18.7 - - - J1 17.5 - - - - 17.5 - - - K1 17.5 - - - - 16.8 - - - L1 17.5 - - - - 16.1 - - -

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3

JOB TITLE:

NODE ANALYSIS DATA

NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE

(FT) (PSI) (GPM)

Q1 17.5 - - - - 21.2 - - - S1 17.5 - - - - 18.6 - - - T1 17.5 - - - - 18.6 - - - U1 17.5 - - - - 18.9 - - - V1 17.5 - - - - 20.3 - - - X1 17.5 - - - - 21.3 - - - Z1 17.5 - - - - 22.5 - - - 99 17.5 - - - - 22.6 - - - 98 17.5 - - - - 22.7 - - - 97 17.5 - - - - 22.7 - - - 96 17.5 - - - - 22.8 - - - 95 17.5 - - - - 23.0 - - - 94 17.5 - - - - 23.9 - - - 1 17.5 - - - - 25.0 - - - 2 10.5 - - - - 29.0 - - - 3 10.5 - - - - 29.0 - - - 4 10.5 - - - - 29.1 - - - 5 10.5 - - - - 29.1 - - - 6 10.5 - - - - 29.2 - - - 7 10.5 - - - - 29.3 - - - 8 10.5 - - - - 29.3 - - - 9 10.5 - - - - 29.4 - - - 10 -3.0 - - - - 63.9 - - - 12 17.5 - - - - 24.7 - - - 13 15.0 - - - - 25.7 - - - 14 15.0 - - - - 25.6 - - - 15 15.0 - - - - 25.6 - - - 16 15.0 - - - - 25.5 - - - 17 15.0 - - - - 25.4 - - - 18 15.0 - - - - 25.3 - - - 19 15.0 - - - - 25.2 - - - 20 17.5 - - - - 24.3 - - - 21 10.5 - - - - 28.4 - - - 22 10.5 - - - - 28.5 - - - 23 10.5 - - - - 28.9 - - - 24 17.5 - - - - 24.8 - - - 25 10.5 - - - - 29.0 - - - 26 10.5 - - - - 29.0 - - - 27 10.5 - - - - 29.0 - - - 28 10.5 - - - - 29.0 - - - 29 17.5 - - - - 24.7 - - - 30 15.0 - - - - 25.7 - - - 31 15.0 - - - - 25.7 - - - 32 15.0 - - - - 25.7 - - - 33 15.0 - - - - 25.7 - - - 35 17.5 - - - - 24.7 - - - 36 17.5 - - - - 24.8 - - - 37 17.5 - - - - 25.8 - - - 39 17.5 - - - - 24.7 - - - 40 17.5 - - - - 24.8 - - - 41 17.5 - - - - 24.7 - - - 42 17.5 - - - - 24.7 - - -

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4

JOB TITLE:

NODE ANALYSIS DATA

NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE

(FT) (PSI) (GPM)

43 17.5 - - - - 24.6 - - - 44 17.5 - - - - 24.6 - - - 45 17.5 - - - - 24.5 - - - 46 17.5 - - - - 24.5 - - - 47 10.5 - - - - 29.0 - - - 48 15.0 - - - - 25.1 - - - 49 17.5 - - - - 23.9 - - - 50 17.5 - - - - 23.4 - - - 51 15.0 - - - - 24.4 - - - 52 15.0 - - - - 25.1 - - - 53 15.0 - - - - 25.0 - - - 54 15.0 - - - - 24.9 - - - 55 15.0 - - - - 24.9 - - - 56 15.0 - - - - 24.9 - - - 57 15.0 - - - - 24.9 - - - 58 15.0 - - - - 24.9 - - - 59 15.0 - - - - 24.9 - - - 60 15.0 - - - - 24.9 - - - 61 17.5 - - - - 23.7 - - - 62 17.5 - - - - 22.8 - - - 63 15.0 - - - - 23.8 - - - 64 15.0 - - - - 23.8 - - - 65 15.0 - - - - 23.8 - - - 66 15.0 - - - - 23.7 - - - 67 15.0 - - - - 23.7 - - - 68 15.0 - - - - 23.7 - - - 69 15.0 - - - - 23.9 - - - 70 15.0 - - - - 24.9 - - - 71 17.5 - - - - 23.4 - - - 72 17.5 - - - - 19.4 - - - 73 17.5 - - - - 23.2 - - - 74 17.5 - - - - 20.6 - - - 75 17.5 - - - - 23.7 - - - 76 17.5 - - - - 22.6 - - - 77 17.5 - - - - 23.7 - - - 78 17.5 - - - - 22.8 - - - 79 17.5 - - - - 23.7 - - - 80 17.5 - - - - 22.8 - - - 81 17.5 - - - - 23.7 - - - 82 17.5 - - - - 22.8 - - -

TR1 10.5 - - - - 50.6 - - -

BR1 3.0 - - - - 57.3 - - -

BS 3.0 - - - - 64.6 - - -

BD 3.0 - - - - 61.8 - - -

SOURCE 0.0 SOURCE 67.2 644.8

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5

JOB TITLE:

PIPE DATA

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 1000 -0.2 1.610 PL 14.00 PF 0.0

A 10.0 5.3 25.1 26.4 0.0 120 FTG ---- PE 0.0

B 10.0 5.3 25.1 26.4 0.000 TL 14.00 PV

Pipe: 999 -26.6 1.610 PL 8.00 PF 0.2

B 10.0 5.3 25.1 26.4 4.2 120 FTG ---- PE 0.0

C 10.0 5.3 25.3 26.5 0.027 TL 8.00 PV

Pipe: 998 -53.0 1.610 PL 1.42 PF 0.9

C 10.0 5.3 25.3 26.5 8.4 120 FTG T PE -3.2

95 17.5 0.0 23.0 0.0 0.098 TL 9.42 PV

Pipe: 997 -25.0 1.610 PL 9.00 PF 0.4

F 10.0 5.3 22.6 25.0 3.9 120 FTG 2E PE -3.2

E1 17.5 0.0 19.8 0.0 0.024 TL 17.00 PV

Pipe: 996 -24.6 1.049 PL 1.17 PF 1.2

E 10.0 5.3 21.9 24.6 9.1 120 FTG T PE -3.2

E1 17.5 0.0 19.8 0.0 0.191 TL 6.17 PV

Pipe: 995 -49.6 1.610 PL 6.33 PF 0.5

E1 17.5 0.0 19.8 0.0 7.8 120 FTG ---- PE 3.2

D 10.0 5.3 23.6 25.6 0.087 TL 6.33 PV

Pipe: 994 -75.2 1.610 PL 6.17 PF 2.7

D 10.0 5.3 23.6 25.6 11.8 120 FTG T PE -3.2

95 17.5 0.0 23.0 0.0 0.187 TL 14.17 PV

Pipe: 993 -23.6 1.049 PL 1.58 PF 1.9

G 10.0 5.3 20.1 23.6 8.8 120 FTG 2ET PE -3.2

G1 17.5 0.0 18.7 0.0 0.177 TL 10.58 PV

Pipe: 992 -23.4 1.049 PL 3.00 PF 2.1

H 10.0 5.3 19.8 23.4 8.7 120 FTG 2ET PE -3.2

H1 17.5 0.0 18.7 0.0 0.174 TL 12.00 PV

Pipe: 991 -23.5 1.049 PL 2.50 PF 2.0

I 10.0 5.3 19.9 23.5 8.7 120 FTG 2ET PE -3.2

I1 17.5 0.0 18.7 0.0 0.175 TL 11.50 PV

Pipe: 990 13.2 1.610 PL 8.83 PF 0.1

G1 17.5 0.0 18.7 0.0 2.1 120 FTG ---- PE 0.0

H1 17.5 0.0 18.7 0.0 0.007 TL 8.83 PV

Pipe: 989 -10.2 1.610 PL 10.08 PF 0.0

H1 17.5 0.0 18.7 0.0 1.6 120 FTG ---- PE 0.0

I1 17.5 0.0 18.7 0.0 0.005 TL 10.08 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 988 -33.7 1.610 PL 7.92 PF 0.7

I1 17.5 0.0 18.7 0.0 5.3 120 FTG T PE 0.0

72 17.5 0.0 19.4 0.0 0.042 TL 15.92 PV

Pipe: 987 -22.9 1.610 PL 12.00 PF 0.4

L 10.0 5.3 18.9 22.9 3.6 120 FTG 2E PE -3.2

L1 17.5 0.0 16.1 0.0 0.021 TL 20.00 PV

Pipe: 986 -22.5 1.049 PL 1.25 PF 1.0

K 10.0 5.3 18.3 22.5 8.4 120 FTG T PE -3.2

L1 17.5 0.0 16.1 0.0 0.162 TL 6.25 PV

Pipe: 985 -45.4 1.610 PL 2.25 PF 0.8

L1 17.5 0.0 16.1 0.0 7.1 120 FTG T PE 0.0

K1 17.5 0.0 16.8 0.0 0.073 TL 10.25 PV

Pipe: 984 -45.4 1.610 PL 10.00 PF 0.7

K1 17.5 0.0 16.8 0.0 7.1 120 FTG ---- PE 0.0

J1 17.5 0.0 17.5 0.0 0.073 TL 10.00 PV

Pipe: 983 -22.8 1.049 PL 3.50 PF 2.1

J 10.0 5.3 18.7 22.8 8.5 120 FTG 2ET PE -3.2

J1 17.5 0.0 17.5 0.0 0.165 TL 12.50 PV

Pipe: 982 -68.1 1.610 PL 3.75 PF 1.8

J1 17.5 0.0 17.5 0.0 10.7 120 FTG T PE 0.0

72 17.5 0.0 19.4 0.0 0.156 TL 11.75 PV

Pipe: 981 -26.2 1.049 PL 1.17 PF 1.3

M 10.0 5.3 24.7 26.2 9.7 120 FTG T PE -3.2

96 17.5 0.0 22.8 0.0 0.214 TL 6.17 PV

Pipe: 980 -26.1 1.049 PL 1.17 PF 1.3

N 10.0 5.3 24.7 26.1 9.7 120 FTG T PE -3.2

97 17.5 0.0 22.7 0.0 0.213 TL 6.17 PV

Pipe: 979 -26.6 1.610 PL 1.17 PF 0.3

O 10.0 5.3 25.7 26.6 4.2 120 FTG T PE -3.2

98 17.5 0.0 22.7 0.0 0.027 TL 9.17 PV

Pipe: 978 -25.8 1.610 PL 5.83 PF 0.4

Q 10.0 5.3 24.1 25.8 4.1 120 FTG T PE -3.2

Q1 17.5 0.0 21.2 0.0 0.026 TL 13.83 PV

Pipe: 977 -25.8 1.610 PL 5.33 PF 0.1

Q1 17.5 0.0 21.2 0.0 4.1 120 FTG ---- PE 3.2

P 10.0 5.3 24.6 26.1 0.026 TL 5.33 PV

Pipe: 976 -51.9 1.610 PL 6.00 PF 1.3

P 10.0 5.3 24.6 26.1 8.2 120 FTG T PE -3.2

98 17.5 0.0 22.7 0.0 0.094 TL 14.00 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 975 -23.1 1.049 PL 7.00 PF 1.2

R 10.0 5.3 19.3 23.1 8.6 120 FTG ---- PE 0.0

S 10.0 5.3 20.4 23.8 0.170 TL 7.00 PV

Pipe: 974 -46.9 1.610 PL 1.75 PF 1.4

S 10.0 5.3 20.4 23.8 7.4 120 FTG 2ET PE -3.2

S1 17.5 0.0 18.6 0.0 0.078 TL 17.75 PV

Pipe: 973 -7.3 1.610 PL 9.00 PF 0.0

S1 17.5 0.0 18.6 0.0 1.2 120 FTG ---- PE 0.0

T1 17.5 0.0 18.6 0.0 0.003 TL 9.00 PV

Pipe: 972 -23.1 1.049 PL 5.83 PF 2.5

T 10.0 5.3 19.3 23.1 8.6 120 FTG 2ET PE -3.2

T1 17.5 0.0 18.6 0.0 0.170 TL 14.83 PV

Pipe: 971 -30.4 1.610 PL 10.00 PF 0.4

T1 17.5 0.0 18.6 0.0 4.8 120 FTG ---- PE 0.0

U1 17.5 0.0 18.9 0.0 0.035 TL 10.00 PV

Pipe: 970 -23.3 1.049 PL 5.58 PF 2.5

U 10.0 5.3 19.7 23.3 8.7 120 FTG 2ET PE -3.2

U1 17.5 0.0 18.9 0.0 0.173 TL 14.58 PV

Pipe: 969 -53.8 1.610 PL 8.00 PF 1.6

U1 17.5 0.0 18.9 0.0 8.5 120 FTG T PE 0.0

74 17.5 0.0 20.6 0.0 0.101 TL 16.00 PV

Pipe: 968 -24.0 1.049 PL 5.67 PF 2.7

V 10.0 5.3 20.9 24.0 8.9 120 FTG 2ET PE -3.2

V1 17.5 0.0 20.3 0.0 0.183 TL 14.67 PV

Pipe: 967 -24.0 1.610 PL 3.75 PF 0.3

V1 17.5 0.0 20.3 0.0 3.8 120 FTG T PE 0.0

74 17.5 0.0 20.6 0.0 0.023 TL 11.75 PV

Pipe: 966 -26.6 1.610 PL 1.17 PF 0.3

W 10.0 5.3 25.6 26.6 4.2 120 FTG T PE -3.2

99 17.5 0.0 22.6 0.0 0.027 TL 9.17 PV

Pipe: 965 -25.9 1.610 PL 6.17 PF 0.3

Y 10.0 5.3 24.3 25.9 4.1 120 FTG E PE -3.2

X1 17.5 0.0 21.3 0.0 0.026 TL 10.17 PV

Pipe: 964 -25.9 1.610 PL 1.00 PF 0.2

X 10.0 5.3 24.3 25.9 4.1 120 FTG T PE -3.2

X1 17.5 0.0 21.3 0.0 0.026 TL 9.00 PV

Pipe: 963 -51.9 1.610 PL 6.17 PF 1.3

X1 17.5 0.0 21.3 0.0 8.2 120 FTG T PE 0.0

99 17.5 0.0 22.6 0.0 0.094 TL 14.17 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 962 -25.1 1.049 PL 6.33 PF 3.0

Z 10.0 5.3 22.7 25.1 9.3 120 FTG 2ET PE -3.2

Z1 17.5 0.0 22.5 0.0 0.198 TL 15.33 PV

Pipe: 961 -8.5 1.610 PL 11.00 PF 0.1

Z1 17.5 0.0 22.5 0.0 1.3 120 FTG 2ET PE 0.0

76 17.5 0.0 22.6 0.0 0.003 TL 27.00 PV

Pipe: 960 26.2 1.610 PL 69.00 PF 2.0

94 17.5 0.0 23.9 0.0 4.1 120 FTG T PE 3.2

A 10.0 5.3 25.1 26.4 0.027 TL 77.00 PV

Pipe: 1 -15.5 1.610 PL 81.04 PF 1.0

1 17.5 0.0 25.0 0.0 2.4 120 FTG 3ET PE 3.0

2 10.5 0.0 29.0 0.0 0.010 TL 101.04 PV

Pipe: 2 -76.3 4.260 PL 18.00 PF 0.0

2 10.5 0.0 29.0 0.0 1.7 120 FTG ---- PE 0.0

3 10.5 0.0 29.0 0.0 0.002 TL 18.00 PV

Pipe: 3 -92.4 4.260 PL 16.00 PF 0.0

3 10.5 0.0 29.0 0.0 2.1 120 FTG ---- PE 0.0

4 10.5 0.0 29.1 0.0 0.002 TL 16.00 PV

Pipe: 4 -109.0 4.260 PL 17.67 PF 0.1

4 10.5 0.0 29.1 0.0 2.5 120 FTG ---- PE 0.0

5 10.5 0.0 29.1 0.0 0.003 TL 17.67 PV

Pipe: 5 -125.9 4.260 PL 18.33 PF 0.1

5 10.5 0.0 29.1 0.0 2.8 120 FTG ---- PE 0.0

6 10.5 0.0 29.2 0.0 0.004 TL 18.33 PV

Pipe: 6 -143.7 4.260 PL 15.67 PF 0.1

6 10.5 0.0 29.2 0.0 3.2 120 FTG ---- PE 0.0

7 10.5 0.0 29.3 0.0 0.005 TL 15.67 PV

Pipe: 7 -154.5 4.260 PL 8.50 PF 0.1

7 10.5 0.0 29.3 0.0 3.5 120 FTG ---- PE 0.0

8 10.5 0.0 29.3 0.0 0.006 TL 8.50 PV

Pipe: 8 -166.1 4.260 PL 2.34 PF 0.0

8 10.5 0.0 29.3 0.0 3.7 120 FTG ---- PE 0.0

9 10.5 0.0 29.4 0.0 0.007 TL 2.34 PV

Pipe: 9 -644.7 4.260 PL 139.78 PF 21.3

9 10.5 0.0 29.4 0.0 14.5 120 FTG 6ET PE 0.0

TR1 10.5 0.0 50.6 0.0 0.087 TL 243.78 PV

Pipe: 10 -644.7 4.260 PL 10.00 PF 3.4

TR1 10.5 0.0 50.6 0.0 14.5 120 FTG EB PE 3.2

BR1 3.0 0.0 57.3 0.0 0.087 TL 39.00 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 11 -644.7 4.240 PL 7.82 PF 4.0

BR1 3.0 0.0 57.3 0.0 14.7 150 FTG 3E PE 2.6

10 -3.0 0.0 63.9 0.0 0.059 TL 67.82 PV

Pipe: 12 -644.7 6.080 PL 10.00 PF 0.6

10 -3.0 0.0 63.9 0.0 7.1 150 FTG 2E PE -2.6

BD 3.0 0.0 61.8 0.0 0.010 TL 54.00 PV

Pipe: 12A FIXED PRESSURE LOSS DEVICE BS 3.0 0.0 64.6 0.0 2.8 psi, 644.7 gpm

BD 3.0 0.0 61.8 0.0

Pipe: 12B -644.8 6.080 PL 26.00 PF 1.3

BS 3.0 0.0 64.6 0.0 7.1 150 FTG 2ET2G PE 1.3

SOURCE 0.0 SRCE 67.2 (N/A) 0.010 TL 126.00 PV

Pipe: 14 15.5 1.610 PL 2.50 PF 0.1

12 17.5 0.0 24.7 0.0 2.4 120 FTG T PE 1.1

13 15.0 0.0 25.7 0.0 0.010 TL 10.50 PV

Pipe: 15 76.3 4.260 PL 18.00 PF 0.0

13 15.0 0.0 25.7 0.0 1.7 120 FTG ---- PE 0.0

14 15.0 0.0 25.6 0.0 0.002 TL 18.00 PV

Pipe: 16 92.4 4.260 PL 18.00 PF 0.0

14 15.0 0.0 25.6 0.0 2.1 120 FTG ---- PE 0.0

15 15.0 0.0 25.6 0.0 0.002 TL 18.00 PV

Pipe: 17 109.0 4.260 PL 18.00 PF 0.1

15 15.0 0.0 25.6 0.0 2.5 120 FTG ---- PE 0.0

16 15.0 0.0 25.5 0.0 0.003 TL 18.00 PV

Pipe: 18 125.9 4.260 PL 18.00 PF 0.1

16 15.0 0.0 25.5 0.0 2.8 120 FTG ---- PE 0.0

17 15.0 0.0 25.4 0.0 0.004 TL 18.00 PV

Pipe: 19 143.7 4.260 PL 18.00 PF 0.1

17 15.0 0.0 25.4 0.0 3.2 120 FTG ---- PE 0.0

18 15.0 0.0 25.3 0.0 0.005 TL 18.00 PV

Pipe: 20 166.1 4.260 PL 18.00 PF 0.1

18 15.0 0.0 25.3 0.0 3.7 120 FTG ---- PE 0.0

19 15.0 0.0 25.2 0.0 0.007 TL 18.00 PV

Pipe: 21 -19.6 1.610 PL 2.50 PF 0.2

19 15.0 0.0 25.2 0.0 3.1 120 FTG T PE -1.1

20 17.5 0.0 24.3 0.0 0.016 TL 10.50 PV

Pipe: 22 -19.6 1.610 PL 54.33 PF 1.1

20 17.5 0.0 24.3 0.0 3.1 120 FTG 2ET PE 3.0

21 10.5 0.0 28.4 0.0 0.016 TL 70.33 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 23 -5.7 1.610 PL 51.63 PF 0.1

21 10.5 0.0 28.4 0.0 0.9 120 FTG ET PE 0.0

22 10.5 0.0 28.5 0.0 0.002 TL 63.63 PV

Pipe: 24 -464.8 4.260 PL 8.00 PF 0.4

22 10.5 0.0 28.5 0.0 10.5 120 FTG ---- PE 0.0

23 10.5 0.0 28.9 0.0 0.048 TL 8.00 PV

Pipe: 25 -478.7 4.260 PL 8.99 PF 0.5

23 10.5 0.0 28.9 0.0 10.8 120 FTG ---- PE 0.0

9 10.5 0.0 29.4 0.0 0.050 TL 8.99 PV

Pipe: 26 15.5 1.610 PL 18.00 PF 0.2

1 17.5 0.0 25.0 0.0 2.4 120 FTG ---- PE 0.0

24 17.5 0.0 24.8 0.0 0.010 TL 18.00 PV

Pipe: 27 15.5 1.610 PL 1.42 PF 0.1

24 17.5 0.0 24.8 0.0 2.4 120 FTG T PE 0.0

12 17.5 0.0 24.7 0.0 0.010 TL 9.42 PV

Pipe: 28 60.8 4.260 PL 18.33 PF 0.0

2 10.5 0.0 29.0 0.0 1.4 120 FTG ---- PE 0.0

25 10.5 0.0 29.0 0.0 0.001 TL 18.33 PV

Pipe: 29 45.7 4.260 PL 2.70 PF 0.0

25 10.5 0.0 29.0 0.0 1.0 120 FTG ---- PE 0.0

26 10.5 0.0 29.0 0.0 0.001 TL 2.70 PV

Pipe: 30 31.0 4.260 PL 6.97 PF 0.0

26 10.5 0.0 29.0 0.0 0.7 120 FTG ---- PE 0.0

27 10.5 0.0 29.0 0.0 0.000 TL 6.97 PV

Pipe: 31 15.5 4.260 PL 14.33 PF 0.0

27 10.5 0.0 29.0 0.0 0.3 120 FTG ---- PE 0.0

28 10.5 0.0 29.0 0.0 0.000 TL 14.33 PV

Pipe: 32 15.5 1.610 PL 99.43 PF 1.2

28 10.5 0.0 29.0 0.0 2.4 120 FTG 2E2T PE -3.0

29 17.5 0.0 24.7 0.0 0.010 TL 123.43 PV

Pipe: 33 15.5 1.610 PL 2.50 PF 0.1

29 17.5 0.0 24.7 0.0 2.4 120 FTG T PE 1.1

30 15.0 0.0 25.7 0.0 0.010 TL 10.50 PV

Pipe: 34 15.5 4.260 PL 14.33 PF 0.0

30 15.0 0.0 25.7 0.0 0.3 120 FTG ---- PE 0.0

31 15.0 0.0 25.7 0.0 0.000 TL 14.33 PV

Pipe: 35 31.0 4.260 PL 4.97 PF 0.0

31 15.0 0.0 25.7 0.0 0.7 120 FTG ---- PE 0.0

32 15.0 0.0 25.7 0.0 0.000 TL 4.97 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 36 45.7 4.260 PL 9.00 PF 0.0

32 15.0 0.0 25.7 0.0 1.0 120 FTG ---- PE 0.0

33 15.0 0.0 25.7 0.0 0.001 TL 9.00 PV

Pipe: 37 60.8 4.260 PL 13.00 PF 0.0

33 15.0 0.0 25.7 0.0 1.4 120 FTG ---- PE 0.0

13 15.0 0.0 25.7 0.0 0.001 TL 13.00 PV

Pipe: 39 14.7 1.610 PL 2.50 PF 0.1

35 17.5 0.0 24.7 0.0 2.3 120 FTG T PE 1.1

32 15.0 0.0 25.7 0.0 0.009 TL 10.50 PV

Pipe: 40 -14.7 1.610 PL 1.42 PF 0.1

35 17.5 0.0 24.7 0.0 2.3 120 FTG T PE 0.0

36 17.5 0.0 24.8 0.0 0.009 TL 9.42 PV

Pipe: 41 -14.7 1.610 PL 97.00 PF 1.0

36 17.5 0.0 24.8 0.0 2.3 120 FTG ET PE 0.0

37 17.5 0.0 25.8 0.0 0.009 TL 109.00 PV

Pipe: 42 -14.7 1.610 PL 7.00 PF 0.2

37 17.5 0.0 25.8 0.0 2.3 120 FTG ET PE 3.0

26 10.5 0.0 29.0 0.0 0.009 TL 19.00 PV

Pipe: 44 15.1 1.610 PL 2.50 PF 0.1

39 17.5 0.0 24.7 0.0 2.4 120 FTG T PE 1.1

33 15.0 0.0 25.7 0.0 0.010 TL 10.50 PV

Pipe: 45 -15.1 1.610 PL 1.42 PF 0.1

39 17.5 0.0 24.7 0.0 2.4 120 FTG T PE 0.0

40 17.5 0.0 24.8 0.0 0.010 TL 9.42 PV

Pipe: 46 -15.1 1.610 PL 102.31 PF 1.2

40 17.5 0.0 24.8 0.0 2.4 120 FTG 3ET PE 3.0

25 10.5 0.0 29.0 0.0 0.010 TL 122.31 PV

Pipe: 47 -15.5 1.610 PL 2.50 PF 0.1

31 15.0 0.0 25.7 0.0 2.4 120 FTG T PE -1.1

41 17.5 0.0 24.7 0.0 0.010 TL 10.50 PV

Pipe: 48 -15.5 1.610 PL 99.43 PF 1.2

41 17.5 0.0 24.7 0.0 2.4 120 FTG 2E2T PE 3.0

27 10.5 0.0 29.0 0.0 0.010 TL 123.43 PV

Pipe: 49 -16.1 1.610 PL 2.50 PF 0.1

14 15.0 0.0 25.6 0.0 2.5 120 FTG T PE -1.1

42 17.5 0.0 24.7 0.0 0.011 TL 10.50 PV

Pipe: 50 -16.1 1.610 PL 100.46 PF 1.3

42 17.5 0.0 24.7 0.0 2.5 120 FTG 2E2T PE 3.0

3 10.5 0.0 29.0 0.0 0.011 TL 124.46 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 51 -16.6 1.610 PL 2.50 PF 0.1

15 15.0 0.0 25.6 0.0 2.6 120 FTG T PE -1.1

43 17.5 0.0 24.6 0.0 0.011 TL 10.50 PV

Pipe: 52 -16.6 1.610 PL 100.40 PF 1.4

43 17.5 0.0 24.6 0.0 2.6 120 FTG 2E2T PE 3.0

4 10.5 0.0 29.1 0.0 0.011 TL 124.40 PV

Pipe: 53 -17.0 1.610 PL 2.50 PF 0.1

16 15.0 0.0 25.5 0.0 2.7 120 FTG T PE -1.1

44 17.5 0.0 24.6 0.0 0.012 TL 10.50 PV

Pipe: 54 -17.0 1.610 PL 100.73 PF 1.5

44 17.5 0.0 24.6 0.0 2.7 120 FTG 3E2T PE 3.0

5 10.5 0.0 29.1 0.0 0.012 TL 128.73 PV

Pipe: 55 -17.8 1.610 PL 2.50 PF 0.1

17 15.0 0.0 25.4 0.0 2.8 120 FTG T PE -1.1

45 17.5 0.0 24.5 0.0 0.013 TL 10.50 PV

Pipe: 56 -17.8 1.610 PL 100.40 PF 1.7

45 17.5 0.0 24.5 0.0 2.8 120 FTG 3E2T PE 3.0

6 10.5 0.0 29.2 0.0 0.013 TL 128.40 PV

Pipe: 57 -22.3 1.610 PL 2.50 PF 0.2

18 15.0 0.0 25.3 0.0 3.5 120 FTG T PE -1.1

46 17.5 0.0 24.5 0.0 0.020 TL 10.50 PV

Pipe: 58 -22.3 1.610 PL 54.33 PF 1.5

46 17.5 0.0 24.5 0.0 3.5 120 FTG E2T PE 3.0

47 10.5 0.0 29.0 0.0 0.020 TL 74.33 PV

Pipe: 59 -11.5 1.610 PL 50.30 PF 0.4

47 10.5 0.0 29.0 0.0 1.8 120 FTG ET PE 0.0

8 10.5 0.0 29.3 0.0 0.006 TL 62.30 PV

Pipe: 60 185.7 4.260 PL 18.00 PF 0.2

19 15.0 0.0 25.2 0.0 4.2 120 FTG ---- PE 0.0

48 15.0 0.0 25.1 0.0 0.009 TL 18.00 PV

Pipe: 61 10.2 1.610 PL 2.50 PF 0.0

48 15.0 0.0 25.1 0.0 1.6 120 FTG T PE -1.1

49 17.5 0.0 23.9 0.0 0.005 TL 10.50 PV

Pipe: 62 10.2 1.610 PL 96.30 PF 0.5

49 17.5 0.0 23.9 0.0 1.6 120 FTG 3E PE 0.0

50 17.5 0.0 23.4 0.0 0.005 TL 108.30 PV

Pipe: 63 10.2 1.610 PL 2.50 PF 0.1

50 17.5 0.0 23.4 0.0 1.6 120 FTG ET PE 1.1

51 15.0 0.0 24.4 0.0 0.005 TL 14.50 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 64 -459.1 4.260 PL 19.84 PF 2.1

51 15.0 0.0 24.4 0.0 10.3 120 FTG 2E PE 1.9

22 10.5 0.0 28.5 0.0 0.047 TL 45.84 PV

Pipe: 65 175.5 4.260 PL 1.17 PF 0.0

48 15.0 0.0 25.1 0.0 3.9 120 FTG ---- PE 0.0

52 15.0 0.0 25.1 0.0 0.008 TL 1.17 PV

Pipe: 66 153.4 4.260 PL 10.00 PF 0.1

52 15.0 0.0 25.1 0.0 3.5 120 FTG ---- PE -1.1

94 17.5 0.0 23.9 0.0 0.006 TL 10.00 PV

Pipe: 66A 127.2 4.260 PL 5.67 PF 0.0

94 17.5 0.0 23.9 0.0 2.9 120 FTG ---- PE 1.1

53 15.0 0.0 25.0 0.0 0.004 TL 5.67 PV

Pipe: 67 90.4 4.260 PL 18.13 PF 0.0

53 15.0 0.0 25.0 0.0 2.0 120 FTG ---- PE 0.0

54 15.0 0.0 24.9 0.0 0.002 TL 18.13 PV

Pipe: 68 50.9 4.260 PL 11.87 PF 0.0

54 15.0 0.0 24.9 0.0 1.1 120 FTG ---- PE 0.0

55 15.0 0.0 24.9 0.0 0.001 TL 11.87 PV

Pipe: 69 34.3 4.260 PL 9.67 PF 0.0

55 15.0 0.0 24.9 0.0 0.8 120 FTG ---- PE 0.0

56 15.0 0.0 24.9 0.0 0.000 TL 9.67 PV

Pipe: 70 19.7 4.260 PL 16.67 PF 0.0

56 15.0 0.0 24.9 0.0 0.4 120 FTG ---- PE 0.0

57 15.0 0.0 24.9 0.0 0.000 TL 16.67 PV

Pipe: 71 5.7 4.260 PL 12.80 PF 0.0

57 15.0 0.0 24.9 0.0 0.1 120 FTG ---- PE 0.0

58 15.0 0.0 24.9 0.0 0.000 TL 12.80 PV

Pipe: 72 27.8 4.260 PL 1.20 PF 0.0

58 15.0 0.0 24.9 0.0 0.6 120 FTG ---- PE 0.0

59 15.0 0.0 24.9 0.0 0.000 TL 1.20 PV

Pipe: 73 13.7 4.260 PL 26.00 PF 0.0

59 15.0 0.0 24.9 0.0 0.3 120 FTG ---- PE 0.0

60 15.0 0.0 24.9 0.0 0.000 TL 26.00 PV

Pipe: 74 13.7 1.610 PL 2.50 PF 0.1

60 15.0 0.0 24.9 0.0 2.2 120 FTG T PE -1.1

61 17.5 0.0 23.7 0.0 0.008 TL 10.50 PV

Pipe: 75 13.7 1.610 PL 97.63 PF 1.0

61 17.5 0.0 23.7 0.0 2.2 120 FTG 2E2T PE 0.0

62 17.5 0.0 22.8 0.0 0.008 TL 121.63 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 76 13.7 1.610 PL 2.50 PF 0.1

62 17.5 0.0 22.8 0.0 2.2 120 FTG T PE 1.1

63 15.0 0.0 23.8 0.0 0.008 TL 10.50 PV

Pipe: 77 13.7 4.260 PL 18.00 PF 0.0

63 15.0 0.0 23.8 0.0 0.3 120 FTG ---- PE 0.0

64 15.0 0.0 23.8 0.0 0.000 TL 18.00 PV

Pipe: 78 27.8 4.260 PL 18.00 PF 0.0

64 15.0 0.0 23.8 0.0 0.6 120 FTG ---- PE 0.0

65 15.0 0.0 23.8 0.0 0.000 TL 18.00 PV

Pipe: 79 41.8 4.260 PL 15.47 PF 0.0

65 15.0 0.0 23.8 0.0 0.9 120 FTG ---- PE 0.0

66 15.0 0.0 23.7 0.0 0.001 TL 15.47 PV

Pipe: 80 56.4 4.260 PL 6.67 PF 0.0

66 15.0 0.0 23.7 0.0 1.3 120 FTG ---- PE 0.0

67 15.0 0.0 23.7 0.0 0.001 TL 6.67 PV

Pipe: 81 47.9 4.260 PL 8.58 PF 0.0

67 15.0 0.0 23.7 0.0 1.1 120 FTG ---- PE -1.1

99 17.5 0.0 22.6 0.0 0.001 TL 8.58 PV

Pipe: 81A -30.6 4.260 PL 5.42 PF 0.0

99 17.5 0.0 22.6 0.0 0.7 120 FTG ---- PE 1.1

68 15.0 0.0 23.7 0.0 0.000 TL 5.42 PV

Pipe: 82 -108.4 4.260 PL 1.75 PF 0.0

68 15.0 0.0 23.7 0.0 2.4 120 FTG ---- PE -1.1

98 17.5 0.0 22.7 0.0 0.003 TL 1.75 PV

Pipe: 82A -186.9 4.260 PL 7.00 PF 0.1

98 17.5 0.0 22.7 0.0 4.2 120 FTG ---- PE 0.0

97 17.5 0.0 22.7 0.0 0.009 TL 7.00 PV

Pipe: 82B -213.0 4.260 PL 7.50 PF 0.1

97 17.5 0.0 22.7 0.0 4.8 120 FTG ---- PE 0.0

96 17.5 0.0 22.8 0.0 0.011 TL 7.50 PV

Pipe: 82C -239.2 4.260 PL 1.58 PF 0.0

96 17.5 0.0 22.8 0.0 5.4 120 FTG ---- PE 1.1

69 15.0 0.0 23.9 0.0 0.014 TL 1.58 PV

Pipe: 83 -341.0 4.260 PL 6.83 PF 0.2

69 15.0 0.0 23.9 0.0 7.7 120 FTG ---- PE -1.1

95 17.5 0.0 23.0 0.0 0.027 TL 6.83 PV

Pipe: 83A -469.3 4.260 PL 7.25 PF 0.4

95 17.5 0.0 23.0 0.0 10.6 120 FTG ---- PE 1.1

51 15.0 0.0 24.4 0.0 0.048 TL 7.25 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 84 22.1 3.260 PL 155.15 PF 0.1

52 15.0 0.0 25.1 0.0 0.8 120 FTG 2ET PE 0.0

70 15.0 0.0 24.9 0.0 0.001 TL 195.15 PV

Pipe: 85 22.1 3.260 PL 13.83 PF 0.0

70 15.0 0.0 24.9 0.0 0.8 120 FTG T PE 0.0

58 15.0 0.0 24.9 0.0 0.001 TL 33.83 PV

Pipe: 86 36.8 1.610 PL 2.50 PF 0.5

53 15.0 0.0 25.0 0.0 5.8 120 FTG T PE -1.1

71 17.5 0.0 23.4 0.0 0.050 TL 10.50 PV

Pipe: 87 36.8 1.610 PL 77.00 PF 4.6

71 17.5 0.0 23.4 0.0 5.8 120 FTG 2ET PE 0.0

G1 17.5 0.0 18.7 0.0 0.050 TL 93.00 PV

Pipe: 88 -101.8 1.610 PL 2.50 PF 3.4

72 17.5 0.0 19.4 0.0 16.0 120 FTG T PE 1.1

69 15.0 0.0 23.9 0.0 0.328 TL 10.50 PV

Pipe: 89 39.5 1.610 PL 2.50 PF 0.6

54 15.0 0.0 24.9 0.0 6.2 120 FTG T PE -1.1

73 17.5 0.0 23.2 0.0 0.057 TL 10.50 PV

Pipe: 90 39.5 1.610 PL 66.00 PF 4.7

73 17.5 0.0 23.2 0.0 6.2 120 FTG 2ET PE 0.0

S1 17.5 0.0 18.6 0.0 0.057 TL 82.00 PV

Pipe: 91 -77.8 1.610 PL 2.50 PF 2.1

74 17.5 0.0 20.6 0.0 12.3 120 FTG T PE 1.1

68 15.0 0.0 23.7 0.0 0.199 TL 10.50 PV

Pipe: 92 16.6 1.610 PL 2.50 PF 0.1

55 15.0 0.0 24.9 0.0 2.6 120 FTG T PE -1.1

75 17.5 0.0 23.7 0.0 0.011 TL 10.50 PV

Pipe: 93 16.6 1.610 PL 84.42 PF 1.2

75 17.5 0.0 23.7 0.0 2.6 120 FTG E2T PE 0.0

Z1 17.5 0.0 22.5 0.0 0.011 TL 104.42 PV

Pipe: 94 -8.5 1.610 PL 2.50 PF 0.0

76 17.5 0.0 22.6 0.0 1.3 120 FTG ET PE 1.1

67 15.0 0.0 23.7 0.0 0.003 TL 14.50 PV

Pipe: 95 14.6 1.610 PL 2.50 PF 0.1

56 15.0 0.0 24.9 0.0 2.3 120 FTG T PE -1.1

77 17.5 0.0 23.7 0.0 0.009 TL 10.50 PV

Pipe: 96 14.6 1.610 PL 92.43 PF 1.0

77 17.5 0.0 23.7 0.0 2.3 120 FTG 2T PE 0.0

78 17.5 0.0 22.8 0.0 0.009 TL 108.43 PV

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 16

JOB TITLE:

PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.

END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.

NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)

Pipe: 97 14.6 1.610 PL 2.50 PF 0.1

78 17.5 0.0 22.8 0.0 2.3 120 FTG T PE 1.1

66 15.0 0.0 23.7 0.0 0.009 TL 10.50 PV

Pipe: 98 14.0 1.610 PL 2.50 PF 0.1

57 15.0 0.0 24.9 0.0 2.2 120 FTG T PE -1.1

79 17.5 0.0 23.7 0.0 0.008 TL 10.50 PV

Pipe: 99 14.0 1.610 PL 93.63 PF 1.0

79 17.5 0.0 23.7 0.0 2.2 120 FTG 2E2T PE 0.0

80 17.5 0.0 22.8 0.0 0.008 TL 117.63 PV

Pipe: 100 14.0 1.610 PL 2.50 PF 0.1

80 17.5 0.0 22.8 0.0 2.2 120 FTG T PE 1.1

65 15.0 0.0 23.8 0.0 0.008 TL 10.50 PV

Pipe: 101 14.1 1.610 PL 2.50 PF 0.1

59 15.0 0.0 24.9 0.0 2.2 120 FTG ET PE -1.1

81 17.5 0.0 23.7 0.0 0.008 TL 14.50 PV

Pipe: 102 14.1 1.610 PL 95.23 PF 0.9

81 17.5 0.0 23.7 0.0 2.2 120 FTG 2ET PE 0.0

82 17.5 0.0 22.8 0.0 0.008 TL 111.23 PV

Pipe: 103 14.1 1.610 PL 2.50 PF 0.1

82 17.5 0.0 22.8 0.0 2.2 120 FTG T PE 1.1

64 15.0 0.0 23.8 0.0 0.008 TL 10.50 PV

Pipe: 104 -10.8 1.610 PL 48.40 PF 0.3

47 10.5 0.0 29.0 0.0 1.7 120 FTG ET PE 0.0

7 10.5 0.0 29.3 0.0 0.005 TL 60.40 PV

Pipe: 105 -13.9 1.610 PL 46.57 PF 0.5

21 10.5 0.0 28.4 0.0 2.2 120 FTG ET PE 0.0

23 10.5 0.0 28.9 0.0 0.008 TL 58.57 PV

NOTES (HASS):

(1) Calculations were performed by the HASS 8.5 computer program under license no. 27050933 granted by HRS Systems, Inc.

208 Southside Square Petersburg, TN 37144

(931) 659-9760

(2) The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.077 gpm.

(3) Total pressure at each node is used in balancing the system.

Maximum water velocity is 16.0 ft/sec at pipe 88.

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 17

JOB TITLE:

(4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report.

(5) Available pressure at source node SOURCE under full flow conditions is

77.37 psi compared to the minimum required pressure of 20.00 psi.

(6) PIPE FITTINGS TABLE

Pipe Table Name: STANDARD.PIP

PAGE: A MATERIAL: S40 HWC: 120

Diameter Equivalent Fitting Lengths in Feet

(in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee

1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00

1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 8.00

PAGE: B MATERIAL: THNWL HWC: 120

Diameter Equivalent Fitting Lengths in Feet

(in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee

3.260 10.00 20.00 7.00 22.00 14.00 1.00 18.00 18.00 20.00

4.260 13.00 26.00 8.00 29.00 16.00 3.00 26.00 26.00 26.00

PAGE: E MATERIAL: PVC150 HWC: 150

Diameter Equivalent Fitting Lengths in Feet

(in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee

4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.00

6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 18

WA

TE

R

SU

PP

LY

A

NA

LY

SI

S St at ic

.0 ps i

Re si d:

4.

p si

F lo w:

0.

gp m

-1 4.

0.

.0

.0

.0

.0

0.

FLOW (GPM) (Note: Dashed Lines indicate extrapolated values from Test Results)

G A U G E P R E S S U R E ( p s i )

A 1 2

B

LE

GE

ND

C

Av ai la bl e pr es su re

.7 ps i

4.

gp m

Re qu ir ed p re ss ur e

.2 ps i

4.

gp m A.

S ou rc e

Su pp ly C ur ve

B.

S ys te m De ma nd

C ur ve C.

A va il ab le a t So ur ce

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 19

JOB TITLE:

WATER SUPPLY CURVE

84+ 77+ 0 \\\\\\\ | * <-74.0 psi @ 1250 gpm | Flow Test Point 70+ | X 63+ P 56+ R | E | S | S 49+ U | R | E | 42+ P | S | I 35+ 28+ 21+

14+ LEGEND "

| X = Required Water Supply " | 67.22 psi @ 744.8 gpm " 7+ " | 0 = Available Water Supply " | 77.70 psi @ 744.8 gpm " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000

FLOW (GPM)

SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 20

Utility Report:

Equivalent K-Factor Calculator

Node Sprinkler Pres. Dia. Pipe Ftgs. Total H-W Equivalent Name K-Factor (psi) (in) Len.(ft) Len.(ft) coef. K-factor Drop 5.60 7.00 1.049 7.50 T 12.50 120.00 5.26

File details come from the government source that posted it. Updated .