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Pipeline Hydraulics: Day 1 (Solutions) 1
PIPELINE DESIGN COURSE
DAY 1
PIPELINE HYDRAULICS
CONTINUING PROFESSIONAL DEVELOPMENT RESULTS SHEET
PIPELINE HYDRAULICS – HAND CALCULATION
Derive a relationship for the flowrate relationship for the threedifferent pipes.
Derive a relationship for therequired effective diameter toreplace the three parallel pipes.
Flow rate relationship
321 QQQQTotal ++= ………………….(1)
321 f f f hhh == and VAQ =
1
2
1111
2 gD
V Lh f
λ = thus
11
11
1
2
L
h gDV
f
λ = ………………….(2)
2
2
2222
2 gD
V Lh f
λ = thus
22
22
2
2
L
h gDV
f
λ = ………………….(3)
3
2
3333
2 gD
V Lh f
λ = thus
33
33
3
2
L
h gDV
f
λ = ………………….(4)
Substitute (2), (3) and (4) into (1)
+
+
=
4
2
4
2
4
2 2
3
33
332
2
22
222
1
11
11 D
L
h gD D
L
h gD D
L
h gDQ
f f f
Total
π
λ
π
λ
π
λ
SOLUTIONS
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Pipeline Hydraulics: Day 1 (Solutions) 2
PIPELINE HYDRAULICS – HAND CALCULATION
Effective diameter
321 f f f fE hhhh ===
3
2
333
2
2
222
1
2
111
2
2222 gD
V L
gD
V L
gD
V L
gD
V L
E
E E E λ λ λ λ ===
21
11
1
2
1
=
E
E E E
D L
DV LV
λ
λ ………………….(1)
21
22
2
2
2
=
E
E E E
D L
DV LV
λ
λ ………………….(2)
2
1
33
32
3
= E
E E E
D L
DV LV
λ
λ ………………….(3)
E QQQQ =++ 321
E E AV AV AV AV =++ 332211 ………………….(4)
Substitute (1), (2) and (3) into (4)
=
+
+
4444
223
2
1
33
322
2
1
22
22
12
1
11
1 E E
E
E E E
E
E E E
E
E E E
DV D
D L
D LV D
D L
D LV D
D L
D LV π π
λ
λ π
λ
λ π
λ
λ
( ) ( ) ( ) 22
3
21
33
32
2
21
22
22
1
21
11
1 E
E
E E
E
E E
E
E E D D D L
D L D
D L
D L D
D L
D L=
+
+
λ
λ
λ
λ
λ
λ
+
+
=33
2
5
3
22
2
5
2
11
2
5
12
5
L
D
L
D
L
D L D E E E
λ λ λ λ
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Pipeline Hydraulics: Day 1 (Solutions) 3
NETWORK ANALYSIS – HAND CALCULATION
Assume Hazen-Williamsroughness value of C=130 for allthe pipes.
VAQ =
85.1165.1
85.178.6
C D
V Lh f =
∑
∑−=
i
fi
fi
q
h
hq
2
δ
Pipe nrFlow
(l/s)
Head loss
(m) ∑i
fi
q
h
2 100 6.432 0.064
4 30 1.040 0.035
5 -100 -6.432 0.064
Total 1.040 0.163
Calculated correction factor for Loop 1 -3.185 l/s
( )( )
( ) ( ) mh f 432.6
1303.0
3.0
1.0100078.6
85.1165.1
85.1
2
2 =
= π
( )( )
( ) ( ) mh f 040.1
1303.0
3.0
03.0150078.6
85.1165.1
85.1
2
4 =
= π
( )( )
( ) ( ) mh f 432.6
1303.0
3.0
1.0100078.6
85.1165.1
85.1
2
5 =
= π
( ) sl q /185.3
163.02
040.1−=−=δ
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Pipeline Hydraulics: Day 1 (Solutions) 4
ECONOMIC ANALYSIS – HAND CALCULATION
1. Evaluate which of the future income streams S1 or S2 is more favourable if the costof capital is 10% on a yearly basis.
2. Determine the current investment that should be made for the replacement of a R1.5mil installation (current cost) after 15 years, if the expected CPIX is 15 % and thereturn on a fixed investment is 8% pa.
3. Determine the Internal Rate of Return (IRR) for the following cash flow.
Question 1
If you assume year 1 to be the base year than the NPV of the two income streams are: NPVS1 = R1 412.39 NPVS2 = R1 374.43
Resulting in income stream S1 being the most favourable when comparing the Net PresentValues (NPV).
This was calculated using the following formula:
( )n
i
F NPV
+
=
1
Where:F = future valuei = interest raten = periodsEach future value was brought back to present values and accumulated to obtain the total
NPV for each income stream
Year S1 S21 250 100
2 350 400
3 600 350
4 100 600
5 400 250
Year Cash flow
0 -1300
1 250
2 350
3 600
4 100
5 400
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Pipeline Hydraulics: Day 1 (Solutions) 5
ECONOMIC ANALYSIS – HAND CALCULATION
Question 2
First the future value of the investment should be determined. The current installation isworth R1 500 000 and the escalation will be 15 % for a 15 year period
( )ni P F += 1 ( ) 592205R1215.01000500115
=+= F
Now the current investment should be calculated by discounting the future required valuewith 8% per annum for the 15 year period.
( )ni
F P
+=
1
( )712847R3
08.01
5922051215 =
+= P
Question 3
The internal rate of return is the rate where the NPVincome = NPVexpenditure
( ) ( ) ( ) ( ) ( )543211
400
1
100
1
600
1
350
1
250
iiiii NPV income
++
++
++
++
+= ………………….(1)
( )0exp1
1300
i NPV enditure
+= ………………….(2)
Equation (1) = Equation (2)
( ) ( ) ( ) ( ) ( ) ( )0543211
1300
1
400
1
100
1
600
1
350
1
250
iiiiii +=
++
++
++
++
+
Solving from this equation for “i”
IRR = 9.525%
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Pipeline Hydraulics: Day 1 (Solutions) 6
Question Description Solution
NETWORK ANALYSES - PRACTICAL
D1Q1 Which nodes in the New York tunnel systemdo not adhere to the minimum pressure
requirement?
Node 16 (64.47 m) Node 17 (80.90 m)
Node 18 (48.35 m) Node 19 (30.10 m) Node 20 (64.05 m)
D1Q2 What is the pressure drop in pipe 14 ? ∆h = 2.45 m (difference between pressures of node15 and 14)
D1Q3 What would the corresponding friction factor(λ ) in pipe 14 be, as used in the DarcyWeisbach equation?
λ = 0.0192
D1Q4 If you had to add any parallel pipes to thesystem, where would you place these and why?
(Engineering gut feel)
Adding pipes close to thesupply reservoir usually
improves the pressure in theentire network. Anotheroption is to place parallel pipes along side pipes whichhave high unit head lossvalues such as pipes 17, 18,19 and 21.
OPTIMIZATION - PRACTICAL
D1Q5 How many possible solutions does the smallnetwork below have if with there are 5different pipe diameters to select from?
Possible solutions= 56 = 15 625
Pipe DiameterD1Q6 List the additional pipes (diameters) that
should be installed in the network to solve the pressure problems and indicate where these pipes should be installed.
3141617181921
2133.62133.62438.42438.42133.61828.81828.8
D1Q7 What is the cheapest solution for the abovesystem?
$41 219 821
D1Q8 Does the system meet the necessary pressure
and velocity criteria (Yes/No)?
Yes, there are no pressure or
velocity penalties
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Pipeline Hydraulics: Day 1 (Solutions) 7
Question Description Solution
LIFE CYCLE COSTING ANALYSIS - PRACTICAL
D1Q9 What is the maximum flow rate for
Alternative 1 at the end of the design life(Ml/day)?
10.263 Ml/day in year 2019
D1Q10 What and where is the lowest pressure (m) inthe pipeline (year 1) for alternative 1? At chainage 1650 m the
pressure is 4.115 m
D1Q11 What is the capital cost of Alternative 2?Total capital cost =R5 079 261
D1Q12 What is the IRR of Alternative 2?IRR = 62.511 %
D1Q13 What is the annual operating cost in year 15for alternative 2? Total operation cost =
R291 374.30
D1Q14 Which alternative would you recommend andwhy?
Alternative 1 cannot providethe total demand of 10.345Ml/day in year 2019 whilstAlternative 2 still has somespare capacity. The totalcapital cost of Alternative 1is however less than that ofAlternative 2 by ±R363 000.The IRR of alternative 1 isalso higher than that ofAlternative 2.
D1Q15 What other options do you have that willimprove the system, providing you with a
better alternative?
Use pipes with less internalfriction.
Other pipe materials.Obtain the best combinationas shown in Alternative 2.Could add a booster pump.Different route.Provide greater headdifference between thereservoirs by lifting thesupply level or lowering theend reservoir level.
The two entered alternatives are provided electronically on the website:
Practical Example (Gravity system – Alternative 1).lccPractical Example (Gravity system – Alternative 2).lcc