Upload
hasanadel88
View
221
Download
0
Embed Size (px)
Citation preview
7/27/2019 Chilled Water Pump Head Calculation-port-214f
1/6
HYDRAULIC CALCULATION
FOR
CHILLED W ATER PUMPS
TOTAL DYNAMIC HEAD
7/27/2019 Chilled Water Pump Head Calculation-port-214f
2/6
Head loss calculation using ( 1 ) COLBROOK Formula For CHILLED WATER PUMPS
no. mm m mm GPM l/s 0 . 2
0 . 2
8 . 0
2 . 0
0 . 2
0 . 3
0 . 9
0 . 5
2 . 0
1 . 0 1/1 m m/s 1
A - B 6" GI 154 2 0.1 680 42.8 1 1 1 1 1 5.4 2.29756 35400B - C 8" GI 203 22 0.1 1360 85.7 4 1 2.1 2.65406 53808
C - D 6" GI 154 8 0.1 679 42.8 5 1.5 2.29418 35348D - E 8" GI 203 42 0.1 756.23 47.6 4 1 2.1 1.47579 29920E - F 6" GI 154 32 0.1 491.41 31 2 1 1.5 1.66036 25582F - G 4" GI 102 20 0.1 293.96 18.5 2 2 2.4 2.2549 230G - H 2 1/2" GI 62.7 13 0.1 99.22 6.25 1 4 3.9 2.02578 12697H - I 2" GI 52.5 20 0.1 77.18 4.86 4 3.6 2.24785 11796I - J 1 1/2" GI 40.9 16 0.1 44.58 2.81 4 3.6 2.13351 87345
J - K 1 1/4" GI 35.1 17 0.1 25.04 1.58 3 1 1.8 1.63217 57256K - FCU 3/4" GI 21 19 0.1 5.5 0.35 1 3 1 1 1 12.3 1.00422 21048
TOTAL 211 1 1 1 25 20 1 2
Pressure drop in chiller =
Pressure drop in FCU =two way valve loss =
total friction loss =
Total dynamic head supply = 33
Total dynamic head return = 21
n o .
p a r t o
f p
i p e
D N N o m
i n a
l d i a m e
t e r
F l e x i
b l e
I D P i p e
I n n e r
d i a m e
t e r
L P i p e
l e n g
t h
K P i p e r o u g
h n e s s
Q
F l o w r a
t e
S t r a
i n e r
d i s c h a r g e o u
t l e t
V
M e a n
V e
l o c i
t y
T o
t a l l o c a
l f a c t o r s
DN
c h e c k v a
l v e
G H
S t a t i c h e a
l
G l o b e v a
l v e
Local factors of fittings
e l b o w
( 4 5 l e g . )
e l b o w
( 9 0 l e g . )
t e e
r e d u c e r
g a
t e v a
l v e
7/27/2019 Chilled Water Pump Head Calculation-port-214f
3/6
no. mm m mm GPM l/s 0 . 2
0 . 2
8 . 0
2 . 0
0 . 2
0 . 3
0 . 9
0 . 5
2 . 0
1 . 0 1/1 m m/s 1
n o .
p a r t o
f p
i p e
D N N o m
i n a
l d i a m e
t e r
F l e x i
b l e
I D P i p e
I n n e r
d i a m
e t e r
L P i p e
l e n g
t h
K P i p e r o u g
h n e s s
Q
F l o w r a
t e
S t r a
i n e r
d i s c h a r g e o u
t l e t
V M e a n
V e
l o c i
t y
T o
t a l l o c a
l f a c t o r s
DN
c h e c k v a
l v e
G H
S t a t i c h e a
l
G l o b e v a
l v e
Local factors of fittings
e l b o w
( 4 5 l e g . )
e l b o w
( 9 0 l e g . )
t e e
r e d u c e r
g a
t e v a
l v e
Safty factor 20% =
total dynamic head =
7/27/2019 Chilled Water Pump Head Calculation-port-214f
4/6
CHILLED WATER PUMPS
Project : Agriculture Bank - Gizan Page ( 1 )
Head Loss Calculations:
The total friction loss Hs Consist of:
Hs = Hs1 + Hs2 . (1)
Where: Hs1 : Friction loss Inside pipesHs2 : Friction loss inside fittings
Linear friction loss equation:
Hs = J . L ... .... (2)
J = l . V / ( 2 g D ) .... (3)
Where: J : linear loss factor L : length Of the pipe (m.)l : friction loss factor (COLBROOK-WHITE formula)V : velocity of water (m/s)g : gravity acceleration (9.81 m/s)D : pipe inside diameter (m.)
COLBROOK WHITE formula:.. ( 4 )
1sqr( l)
Where: K : pipe inside Surface roughness (m.)
D : pipe inside diameter (m.)RE : REYNOLDS no. is given as follows: (1/1)
RE = V x D / n . ( 5 )
Where: n : water viscosity= ( n = 1E-06 m 2/s)V : velocity of water (m/s)D : pipe inside diameter (m.)
V = Q / A .... ( 6 )
Where: Q : flow rate (m/s) A : cross section are of the pipe (m)
Data for the first pipe : 6" GI Pipe type & size 6"
168.3 mm Out side diameter (mm)7.11 mm Wall thickness (mm)
D = 0.1541 m : pipe inside diameter (m.)K = 0.0001 m : pipe inside Surface roughness (m.)
= - 2 x log [ +k
)2.51
3.7 x D Re x sqr( l )
7/27/2019 Chilled Water Pump Head Calculation-port-214f
5/6
Project : Agriculture Bank - Gizan Page ( 2 )
Flow : Q = 680.0 GPM = 42.84 l/s = 0.04284 m/sec
A = p x D 2 / 4 = 3.14 x 0.154 / 4 = 0.01865 m
V = Q / A = 2.298 m/s
Re = V x D / n = 2.298 x 0.1541 / 0.000001 = 354008.19
1sqr( l) x sqr( l )
By solving above equation :
l = 0.01882
Loss m per 100 m = J x 100 = 0.03286 x 100 m = 3.286 m / 100m
Pipe length L = 2.0 m
dh(1) Liner loss = J x L = 0.03286 x 2.0 = 0.066 m
Local losses equation is given as follows:
HS2 = SUM ZE . V / ( 2 . G ) .... (7)
Where: G : Gravity acceleration (9.81 m/s)V : Velocity of water (m/s)
SUM ZE : Sum of local loss factors
SUM ZE = gate valve 1 x 0.2 = 0.2Flexible 0 x 0.2 = 0Globe valve 0 x 8 = 0check valve 1 x 2 = 2elbow ( 45 leg.) 0 x 0.2 = 0elbow ( 90 leg.) 1 x 0.3 = 0.3tee 1 x 0.9 = 0.9reducer 0 x 0.5 = 0Strainer 1 x 2 = 2discharge outlet 0 x 1 = 0Total local factors =
HS2 = SUM ZE . V / ( 2 . g )
DH Total loss = HS1 + HS2 = 0.066 + 1.453 = 1.519 m
Total heal (DH+GH) / pipe = Static head + Friction losses . ( 8 )
= 0.0 + 1.519 = 1.519 m
= - 2 log [0.0001
+2.51
3.7 x 0.154
J = l . V / ( 2 g D ) =
HS(2) = SUM ZE.x V / ( 2 g ) = 5.4 x 2.2976 X 2.29762 x 9.81
5.40
]
= 0.03286 m/m
= 1.4529 m
0.01882 x 2.2976 x 2.2982 x 9.81 x 0.1541
354008.2
7/27/2019 Chilled Water Pump Head Calculation-port-214f
6/6
Project : Agriculture Bank - Gizan Page ( 3 )
Data for the second pipe : 8" GI Pipe type & size 8"219.1 mm Out side diameter (mm)
8.18 mm Wall thickness (mm)
D = 0.2027 m : pipe inside diameter (m.)K = 0.0001 m : pipe inside Surface roughness (m.)
Flow : Q = 1360.0 GPM = 85.68 l/s = 0.08568 m/sec
A = p x D 2 / 4 = 3.14 x 0.203 / 4 = 0.03228 m
V = Q / A = 2.654 m/s
Re = V x D / n = 2.654 x 0.2027 / 0.000001 = 538084.07
1sqr( l) x sqr( l )
By solving above equation : l =
Loss m per 100 m = J x 100 = 0.03108 x 100 m = 3.108 m / 100m
Pipe length L = 22.0 m
dh(1) Liner loss = J x L = 0.03108 x 22.0 = 0.684 m
Local losses equation is given as follows:
HS2 = SUM ZE . V / ( 2 . G )
SUM ZE = gate valve 0 x 0.2 = 0Flexible 0 x 0.2 = 0Globe valve 0 x 8 = 0check valve 0 x 2 = 0elbow ( 45 leg.) 0 x 0.2 = 0elbow ( 90 leg.) 4 x 0.3 = 1.2tee 1 x 0.9 = 0.9reducer 0 x 0.5 = 0Strainer 0 x 2 = 0discharge outlet 0 x 1 = 0Total local factors =
HS2 = SUM ZE . V / ( 2 . g )
DH Total loss = HS1 + HS2 = 0.684 + 0.754 = 1.438 m
Total heal (DH+GH) / pipe = Static head + Friction losses
= 0.0 + 1.438 = 1.438 m
Total Head for pipe 1 & 2 = 1.519 + 1.438 = 2.956 m
Other pipes are calculated same as above, All data and results are arranged in the following table :
]
= 0.03108 m/m
= 0.7539 m
J = l . V / ( 2 g D ) =
2.10
HS(2) = SUM ZE.x V / ( 2 g ) = 2.1 x 2.6541 X 2.65412 x 9.81
0.01755
538084.1= - 2 log [
0.01755 x 2.6541 x 2.6542 x 9.81 x 0.2027
3.7 x 0.2030.0001
+2.51