HomeMy WebLinkAboutWater ReportD
Indian Lakes SubdivIsio
Phase XVII i
MCCLURE & BROWNE, ENGINEERING/SURVEYING, INC.
1008 Woodcreek Dr., Suite 103 College Station, Tx. 77845 (979) 693-3838 Engineer Reg. No. F-458
1314 10th Street, Suite 210 Huntsville, Tx. 77320 (936) 294-9749 Survey Reg. No. 101033-00
WATER SYSTEM ANALYSIS
for
INDIAN LAKES PHASE 17
General Information
Anticipated land use:
Residential
Anticipated number of lots:
19 lots
Notes on surrounding development:
This development is located near the existing Phase
12 of Indian Lakes in South Brazos County.
Water System Analysis
Primary water supply line:
Existing 8" line on Matoska Ridge Drive
Software model:
PIPE2000 (Kentucky Pipe Network Model)
Average daily flow:
28.5 gpd (all lots combined)
Estimated fire demand:
1,000 gpm (at Junction J-12)
Pipe material:
PVC (C909)
Regulated1tems
Desigmed
j Requirement Notes
Min. Pressure (psi) _ _1
88.59
; 20(min) j Fire flow conditions (J-12)
Max. Velocity (fps)
6.58
j 12 (max) i Fire flow conditions (P-14)
Conclusion: The proposed water system exceeds the requirements of TCEQ
and the City of College Station
Applicable Exhibits.
Exhibit A Schematic Water System Layout
Exhibit B Static Flow Model Output
Exhibit C Fire Flow Model Output
Indian Lakes, Phase 17
MBESI #10620039
Exhibit B
Static Flow Conditions
K Y P I P E 5 * * + + * * + + * +
--- * Pipe Network Modeling Software
* Copyrighted by KYPIPE LLC
* Version 5 - February 2010
* *
Date & Time: Fri Sep 20 15:59:54 2013
Master File : f:\1062 - clarke & wyndham inc\0039 - indian lakes phase xvii\docs\water
report\static.KYP\static.P2K
S U M M A R Y O F O R I G I N A L D A T A
U N I T S S P E C I F I E D
FLOWRATE ............ = gallons/minute
HEAD (HGL) .......... = feet
PRESSURE ............ = psig
P I P E L I N E D A T A
STATUS CODE: XX -CLOSED PIPE
CV -CHECK VALVE
P I P E
NODE
NAMES
LENGTH
DIAMETER
ROUGHNESS
MINOR
N A M E
R1
42
(ft)
(in)
COEFF.
LOSS
COEFF.
____________________
-- P-1
VP-2
J-1
7830.00
_---___------_-___-----
8.00
140.0000
0.00
P-2
J-1
J-7
2199.52
12.00
140.0000
0.00
..._. P-3
J-2
J-3
3660.00
12.00
140.0000
0.00
P-4
VP-1
J-3
1690.00
12.00
140.0000
0.00
P-5
J-4
J-2
1590.00
8.00
140.0000
0.00
P-6
J-5
J-4
5614.00
6.00
140.0000
0.00
P-7
J-6
J-5
220.00
6.00
140.0000
0.00
P-8
J-3
J-6
3088.00
6.00
140.0000
0.00
P-9
J-7
J-2
4360.48
12.00
140.0000
0.00
P-10
J-7
J-8
3387.00
8.00
140.0000
0.00
P-11
J-8
J-9
621.00
6.00
140.0000
0.00
...... P-12
J-8
J-10
356.00
6.00
140.0000
0.00
P-13
J-9
J-11
322.00
6.00
140.0000
0.00
P-14
J-3
J-12
635.00
8.00
140.0000
0.00
P-15
7-12
J-13
656.00
8.00
140.0000
0.00
P-16
7-12
J-19
66.16
8.00
140.0000
0.00
P-17
J-13
J-17
565.00
6.00
140.0000
0.00
P-16
J-13
J-14
807.00
8.00
140.0000
0.00
" P-19
J-14
J-15
182.00
4.00
125.0000
0.00
P-20
J-14
J-16
302.00
4.00
125.0000
0.00
P U M P/L O S S
E L E M E
N T D A
T A
THERE IS A DEVICE
AT NODE
VP-1
DESCRIBED
BY THE FOLLOWING DATA: (ID= 1)
HEAD
FLOWRATE
EFFICIENCY
(ft) (gpm)
219.23 0.00
180.00 1500.00
77.61 3000.00
THERE IS A DEVICE AT NODE
HEAD FLOWRATE
(ft) (gpm)
219.23 0.00
180.00 1500.00
77.61 3000.00
N O D E D A T A
(8)
75.00
75.00
75.00
VP-2 DESCRIBED BY THE FOLLOWING DATA: (ID= 2)
EFFICIENCY
(5)
75.00
75.00
75.00
NODE
NODE
EXTERNAL
JUNCTION
EXTERNAL
NAME
TITLE
DEMAND
ELEVATION
GRADE
----------------------------------------------
(gpm)
(ft)
(ft)
J-1
0.00
267.00
J-2
0.00
278.00
J-3
0.00
263.00
J-4
0.00
266.00
J-5
15.00
247.00
J-6
0.00
246.00
J-7
0.00
285.00
J-8
0.00
294.00
J-9
0.00
292.00
J-10
6.00
296.00
J-il
6.00
294.00
J-12
4.50
253.00
J-13
7.50
250.00
J-14
4.50
242.00
J-15
6.00
240.00
J-16
4.50
252.00
J-17
4.50
240.00
J-19
0.00
251.00
VP-1
----
258.00
258.00
VP-2
----
285.00
285.00
O U T P U T
O P T I O N
D A T A
OUTPUT SELECTION: ALL RESULTS
ARE INCLUDED
IN THE
TABULATED OUTPUT
MAXIMUM AND MINIMUM
PRESSURES
= 5
MAXIMUM AND MINIMUM
VELOCITIES
= 5
MAXIMUM AND MINIMUM
HEAD LOSS/1000
= 5
S Y S T E M
C O N F I G U
R A T I O N
NUMBER OF
PIPES ...................(p)
= 20
NUMBER OF
END NODES ...............(j)
= 18
NUMBER OF
PRIMARY LOOPS
...........(1)
= 1
NUMBER OF
SUPPLY NODES
............(f)
= 2
NUMBER OF
SUPPLY ZONES
............(z)
= 1
Case: 0
RESULTS OBTAINED AFTER 20 TRIALS: ACCURACY = 0.00001
S I M U L A T I O N D E S C R I P T I O N (L A B E L)
P I P E L I N E
R E S U L
T S
STATUS CODE:
XX -CLOSED
PIPE
CV -CHECK VALVE
P I P E
NODE NUMBERS
FLOWRATE
HEAD
MINOR
LINE
HL+ML/
HL/
N A M E
41
02
LOSS
LOSS
VELD.
1000
1000
---------------------------------------------------------------------------_
(gpm)
(ft)
(ft)
(ft/s)
(ft/ft)
(ft/ft)
P-1
VP-2
J-1
58.50
0.65
0.00
0.37
0.08
0.08
P-2
J-1
J-7
58.50
0.03
0.00
0.17
0.01
0.01
P-3
J-2
J-3
39.02
0.02
0.00
0.11
0.01
0.01
P-4
VP-1
J-3
0.00
0.00
0.00
0.00
0.00
0.00
P-5
J-4
J-2
-7.48
0.00
0.00
0.05
0.00
0.00
P-6
J-5
J-4
-7.48
0.04
0.00
0.08
0.01
0.01
P-7
J-6
J-5
7.52
0.00
0.00
0.09
0.01
0.01
2-6
J-3
J-6
7.52
0.02
0.00
0.09
0.01
0.01
P-9
J-7
J-2
46.50
0.03
0.00
0.13
0.01
0.01
P-10
J-7
J-8
12.00
0.01
0.00
0.08
0.00
0.00
P-11
J-8
J-9
6.00
0.00
0.00
0.04
0.00
0.00
P-12
J-6
J-10
6.00
0.00
0.00
0.07
0.00
0.00
P-13
J-9
J-11
6.00
0.00
0.00
0.07
0.00
0.00
P-14
J-3
J-12
31.50
0.02
0.00
0.20
0.03
0.03
P-15
J-12
17-13
27.00
0.01
0.00
0.17
0.02
0.02
P-16
J-12
J-19
0.00
0.00
0.00
0.00
0.00
0.00
P-17
J-13
J-17
4.50
0.00
0.00
0.05
0.00
0.00
P-18
J-13
J-14
15.00
0.01
0.00
0.10
0.01
0.01
P-19
J-1e
J-15
6.00
0.01
0.00
0.15
0.04
0.04
P-20
J-14
J-16
4.50
0.01
0.00
0.11
0.03
0.03
P U M P/L 0 S S E L E M E N T R E S U L T S
INLET
OUTLET
PUMP
EFFIC-
USEFUL
INCREMTL
TOTAL
*PUMPS
#PUMPS
NPSH
NAME
FLOWRATE
HEAD
HEAD
HEAD
ENCY
POWER
COST
COST
PARALLEL
SERIES
Avail.
(gpm)
(ft)
(ft)
(ft)
(%)
(Hp)
(S)
(S)
(ft)
-----------------------------------------------------------------------------------------------
Device "VP-1" is
closed
VP-1
0.00
0.00
245.41
0.0
75.00
0.
0.0
0.0
**
**
33.2
VP-2
56.50
0.00
219.13
219.1
75.00
0.
0.0
0.0
**
**
33.2
N 0 D E R E S U L T S
NODE NODE
NAME TITLE
___________
J-1
J-2
J-3
J-4
J-5
J-6
J-7
EXTERNAL
HYDRAULIC
NODE
PRESSURE
NODE
DEMAND
GRADE
ELEVATION
HEAD
PRESSURE
(gpm)
(ft)
(ft)
(ft)
(psi)
------------------------------------------------
0.00
503.48
287.00
216.48
93.61
0.00
503.43
278.00
225.43
97.68
0.00
503.41
263.00
240.41
104.18
0.00
503.42
266.00
237.42
102.88
15.00
503.38
247.00
256.38
111.10
0.00
503.38
246.00
257.38
111.53
0.00
503.46
265.00
218.46
94.67
J-8
0.00
503.44
294.00
209.44
90.76
J-9
0.00
503.44
292.00
211.44
91.63
J-10
6.00
503.44
296.00
207.44
69.89
J-11
6.00
503.44
294.00
209.44
90.76
J-12
4.50
503.39
253.00
250.39
108.50
J-13
7.50
503.38
250.00
253.38
109.80
J-14
4.50
503.37
242.00
261.37
113.26
J-15
6.00
503.36
240.00
263.36
114.12
J-16
4.50
503.36
252.00
251.36
108.92
J-17
4.50
503.38
240.00
263.38
114.13
J-19
0.00
503.39
251.00
252.39
109.37
VP-1
----
503.41
258.00
245.41
106.34
VP-2
----
504.13
285.00
219.13
94.96
M A X I M U M A
N
D M I N I
M U M
V A L U
E S
P R E S S U R
E
S
JUNCTION
MAXIMUM
JUNCTION
MINIMUM
NUMBER
PRESSURES
NUMBER
PRESSURES
---------------------
(Psi)
---------------------
(Psi)
J-17
114.13
J-10
89.89
J-15
114.12
J-11
90.76
J-14
113.26
J-8
90.76
J-6
111.53
J-9
91.63
J-5
111.10
J-1
93.81
V E L O C I T
I
E S
PIPE
MAXIMUM
PIPE
MINIMUM
NUMBER
VELOCITY
NUMBER
VELOCITY
(ft/s)
(ft/s)
P-1
---
0.37
---------------------
P-11
0.04
P-14
0.20
P-5
0.05
P-15
0.17
P-17
0.05
P-2
0.17
P-12
0.07
P-19
0.15
P-13
0.07
H L+ M L /
1
0 0 0
PIPE
MAXIMUM
PIPE
MINIMUM
NUMBER
HL+ML/1000
NUMBER
HL+ML/1000
---------------------
(ft/ft)
(ft/ft)
P-1
0.06
-------------------__
P-11
0.00
P-19
0.04
P-5
0.00
P-14
0.03
P-17
0.00
P-20
0.03
P-10
0.00
P-15
0.02
P-12
0.00
H L / 1 0 0
0
PIPE
MAXIMUM
PIPE
MINIMUM
NUMBER
HL/1000
NUMBER
HL/1000
--"'----------------
(ft/ft)
------------"'------
(ft/£t)
P-1
0.08
P-11
0.00
P-19
0.04
P-5
0.00
P-14
0.03
P-17
0.00
P-20
0.03
P-10
0.00
P-15
0.02
P-12
0.00
S U M M A R Y 0
F
I N F L O
W S A
N D O
U T
F L O W S
W INFLOWS INTO THE SYSTEM FROM SUPPLY NODES
(-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES
NODE FLOWRATE NODE
NAME (gpm) TITLE
------------------------------------------
VP-2 58.50
NET SYSTEM INFLOW = 58.50
NET SYSTEM OUTFLOW = 0.00
NET SYSTEM DEMAND = 58.50
***** HYDRAULIC ANALYSIS COMPLETED *****
Exhibit C
Fire Flow Conditions
* * * * * * * * * * K Y P I P E 5
* Pipe Network Modeling Software
* Copyrighted by KYPIPE LLC
* Version 5 - February 2010
*
Date & Time: Fri Sep 20 16:20:36 2013
Master File : f:\1062 - clarke & wyndham inc\0039 - indian lakes phase xvii\dots\water
report\fire.KYP\fire.P2K
S U M M A R Y O F O R I G I N A L D A T A
U N I T S S P E C I F I E D
FLOWRATE ............ = gallons/minute
HEAD (HGL) .......... = feet
PRESSURE ............ = psig
P I P E L I N E D A T A
STATUS CODE: XX -CLOSED PIPE
P I P E
NODE
NAMES
NAM E
$1
$2
______P-
-1
VP 2
--
17-1
P-2
J-1
J-7
P-3
J-2
J-3
P-4
VP-1
J-3
P-5
J-4
J-2
P-6
J-5
J-4
P-7
J-6
J-5
P-8
J-3
J-6
P-9
J-7
J-2
P-10
J-7
J-8
P-11
J-8
J-9
P-12
J-8
J-10
P-13
J-9
J-11
P-14
J-3
J-12
P-15
J-12
J-13
P-16
J-12
J-19
P-17
J-13
J-17
P-18
J-13
J-14
P-19
J-14
J-15
P-20
J-14
J-16
CV -CHECK VALVE
LENGTH DIAMETER ROUGHNESS I
(ft) (in) COEFF. LOST
------------------------------"'---
7830.00 6.00 140.0000
2199.52 12.00 140.0000
3660.00 12.00 140.0000
1690.00 12.00 140.0000
1590.00 8.00 140.0000
5614.00 6.00 140.0000
220.00 6.00 140.0000
3088.00 6.00 140.0000
4360.48 12.00 140.0000
3387.00 6.00 140.0000
621.00 8.00 140.0000
356.00 6.00 140.0000
322.00 6.00 140.000C
635.00 8.00 140.000C
656.00 8.00 140.0000
66.16 8.00 140.0000
565.00 6.00 140.000C
807.00 8.00 140.000C
182.00 4.00 125.000C
302.00 4.00 125.000C
IINOR
COEFF.
i 00
1.00
1.00
1.00
1.00
1.00
.00
i.00
1.00
1.00
1.00
I.00
1.00
1.00
I.00
).00
i.00
1.00
i.00
1.00
P U M P/L 0 S S E L E M E N T D A T A
THERE IS A DEVICE AT NODE VP-1 DESCRIBED BY THE FOLLOWING DATA: (ID= 1)
HEAD FLOWRATE
(£t) (g=m)
219.23 0.00
180.00 1500.00
77.61 3000.00
THERE IS A DEVICE AT NODE
HEAD FLOWRATE
(ft) (gpm)
219.23 0.00
160.00 1500.00
77.61 3000.00
N 0 D E D A T A
EFFICIENCY
(6)
75.00
75.00
75.00
VP-2 DESCRIBED BY THE FOLLOWING DATA: (ID= 2)
EFFICIENCY
M
75.00
75.00
75.00
NODE NODE
EXTERNAL
JUNCTION
EXTERNAL
NAME TITLE
DEMAND
ELEVATION
GRADE
__-------___
(gpm)
_________________________________
(ft)
(ft)
J-1
0.00
287.00
J-2
0.00
278.00
J-3
0.00
263.00
J-4
0.00
266.00
J-5
15.00
247.00
J-6
0.00
246.00
J-7
0.00
285.00
J-8
0.00
294.00
J-9
0.00
292.00
J-10
6.00
296.00
J-11
6.00
294.00
J-12
1004.50
253.00
J-13
7.50
250.00
J-14
4.50
242.00
J-15
6.00
240.00
J-16
4.50
252.00
J-17
4.50
240.00
J-19
0.00
251.00
VP-1
----
258.00
258.00
VP-2
----
265.00
265.00
O U T P U T O P T I O N
D A T A
OUTPUT SELECTION: ALL RESULTS
ARE INCLUDED
IN
THE
TABULATED OUTPUT
MAXIMUM AND MINIMUM
PRESSURES
=
5
MAXIMUM AND MINIMUM
VELOCITIES
=
5
MAXIMUM AND MINIMUM
HEAD LOSS/1000
=
5
S Y S T E M C O N F I G U
P. A T I O N
NUMBER OF PIPES
=20
NUMBER OF END NODES ...............(j)
=
18
NUMBER OF PRIMARY LOOPS
=
NUMBER OF SUPPLY NODES
............(f)
=
2
NUMBER OF SUPPLY ZONES
............(z)
=
1
------ ___O ----------------------------------- _____________-----------------------
Case:
RESULTS OBTAINED AFTER 6 TRIALS: ACCURACY = 0.00007
S I M U L A T I O N D E S C R I P T I O N (L A B E L)
P I P E L I N E
R E S U L
T S
STATUS CODE:
XX -CLOSED
PIPE
CV -CHECK VALVE
P I P E
NODE
NUMBERS
FLOWRATE
HEAD
MINOR
LINE
HL+ML/
HL/
N A M E
#1
#2
LOSS
LOSS
VELD.
1000
1000
---_-----__
_---___
(gpm)
(ft)
(ft)
(ft/s)
(ft/ft)
(ft/ft)
-- P-1
VP-2
J-1
------_-__
442.13
27.51
0.00
2.82
3.51
___-___---
3.51
P-2
J-1
J-7
442.13
1.07
0.00
1.25
0.49
0.49
P-3
J-2
J-3
387.57
1.40
0.00
1.10
0.38
0.38
P-4
VP-1
J-3
616.37
1.52
0.00
1.75
0.90
0.90
P-5
J-4
J-2
-42.56
0.07
0.00
0.27
0.05
0.05
P-6
J-5
J-4
-42.56
1.05
0.00
0.48
0.19
0.19
P-7
J-6
J-5
-27.56
0.02
0.00
0.31
0.08
0.08
P-8
J-3
J-6
-27.56
0.26
0.00
0.31
0.08
0.08
P-9
J-7
J-2
430.13
2.02
0.00
1.22
0.46
0.46
-- P-10
J-7
J-8
12.00
0.01
0.00
0.08
0.00
0.00
P-11
J-8
J-9
6.00
0.00
0.00
0.04
0.00
0.00
.... P-12
J-8
J-10
6.00
0.00
0.00
0.07
0.00
0.00
P-13
J-9
J-11
6.00
0.00
0.00
0.07
0.00
0.00
P-14
J-3
J-12
1031.50
10.71
0.00
6.58
16.87
16.87
P-15
J-12
J-13
27.00
0.01
0.00
0.17
0.02
0.02
P-16
J-12
J-19
0.00
0.00
0.00
0.00
0.00
0.00
P-17
J-13
J-17
4.50
0.00
0.00
0.05
0.00
0.00
P-18
J-13
J-14
15.00
0.01
0.00
0.10
0.01
0.01
--- P-19
J-14
J-15
6.00
0.01
0.00
0.15
0.04
0.04
P-20
J-14
J-16
4.50
0.01
0.00
0.11
0.03
0.03
P U M P/L O S S E L E M E N T R E S U L T S
INLET
OUTLET
PUMP
EFFIC-
USEFUL INCREMTL TOTAL
#PUMPS #PUMPS
NPSH
.-..
NAME
FLOWRATE
HEAD
HEAD
HEAD
ENCY
POWER COST
COST
PARALLEL SERIES
Avail.
..._..
(gpm)
(ft)
(ft)
(ft)
(%)
(Hp) (S)
(S)
(ft)
-----------------------------------------------------------------------------------------------
VP-1
616.37
0.00
211.67
211.7
75.00
0. 0.0
0.0
** **
33.2
VP-2
442.13
0.00
215.15
215.1
75.00
0. 0.0
0.0
** **
.-. 33.2
N O
D E R
E S U L T S
NODE
NODE
EXTERNAL
HYDRAULIC
NODE PRESSURE
NODE
"
NAME
TITLE
DEMAND
GRADE
ELEVATION HEAD
PRESSURE
--------------
(gpm)
-------"----_------------------------------
(ft)
(ft) (ft)
(psi)
,..._
J-1
0.00
472.64
287.00
185.64
80.44
.. _.
J-2
0.00
469.55
278.00
191.55
83.00
J-3
0.00
468.15
263.00
205.15
88.90
J-4
0.00
469.48
266.00
203.48
88.17
J-5
15.00
468.43
247.00
221.43
95.95
J-6
0.00
468.41
246.00
222.41
96.38
---
J-7
0.00
471.57
285.00
186.57
80.85
J-8
0.00
471.55
294.00
177.55
76.94
J-9
0.00
471.55
292.00
179.55
77.61
J-10
6.00
471.55
296.00
175.55
76.07
J-11
6.00
471.55
294.00
177.55
76.94
J-12
1004.50
457.44
253.00
204.44
68.59
J-13
7.50
457.43
250.00
207.43
89.88
J-14
4.50
457.42
242.00
215.42
93.35
J-15
6.00
457.41
240.00
217.41
94.21
J-16
4.50
457.41
252.00
205.41
89.01
J-17
4.50
457.43
240.00
217.43
94.22
J-19
0.00
457.44
251.00
206.44
89.46
VP-1
----
469.67
256.00
211.67
91.73
VP-2
----
500.15
285.00
215.15
93.23
M A X I M U M A
N D M I N I
M U M
V A L U
E S
P R E S S U R
E S
JUNCTION
MAXIMUM
JUNCTION
MINIMUM
NUMBER
PRESSURES
NUMBER
PRESSURES
(psi)
(psi)
J-6
96.38
J-10
76.07
J-5
95.95
J-11
76.94
J-17
94.22
J-8
76.94
J-15
94.21
J-9
77.81
J-14
93.35
J-1
80.44
V E L O C I T
I E S
PIPE
MAXIMUM
PIPE
MINIMUM
NUMBER
VELOCITY
NUMBER
VELOCITY
(ft/s)
(ft/s)
P-14
6.58
P-11
0.04
2-1
2.82
P-17
0.05
P-4
1.75
P-12
0.07
P-2
1.25
P-13
0.07
P-9
1.22
P-10
0.08
H L + M L /
1 0 0 0
PIPE
MAXIMUM
PIPE
MINIMUM
NUMBER
HL+ML/1000
NUMBER
HL+ML/1000
(ft/ft)
-------
(ft/ft)
P-14
16.87
-------------------
P-il
0.00
P-1
3.51
P-17
0.00
P-4
0.90
P-10
0.00
P-2
0.49
P-12
0.00
P-9
0.46
P-13
0.00
H L / 1 0 0
0
PIPE
MAXIMUM
PIPE
MINIMUM
NUMBER
HL/1000
NUMBER
HL/1000
---------------------
(ft/ft)
(ft/ft)
P-14
16.87
P-11
_-----_---
0.00
P-1
3.51
P-17
0.00
P-4
0.90
P-10
0.00
P-2
0.49
P-12
0.00
P-9
0.46
P-13
0.00
S U M M A R Y 0
F I N F L O
W S A
N D O
U T
F L O W S
(+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES
(-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES
NODE FLOWRATE NODE
NAME (gpm) TITLE
_.--__--____-------___ ___-
VP-1 616.37
-- VP-2 aa2.13
NET SYSTEM INFLOW = 1058.50
NET SYSTEM OUTFLOW = 0.00
NET SYSTEM DEMAND = 1058.50
***** HYDRAULIC ANALYSIS COMPLETED *****