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Series-parallel pipes with control valve

Short answer

Solving the pipe network yields head at C = 75.48 m, total system discharge = 0.102 m³/s (102.0 L/s), and valve opening n = 38.7%.

A system of pipes conveying water is connected in parallel and in series as shown in figure below. The section DE represents the resistance of a valve for controlling the flow, which has a resistance coefficient KDE=(4000n)2K_{DE} = \left(\frac{4000}{n}\right)^2, where n is the percentage valve opening. [Figure: pipe A to B splits into two parallel pipes AA1B and AA2B, continues as BC, then at C branches into CD (with the valve, leading to E) and CF (leading to F)]

The friction factor f in the Darcy formula is 0.024 for all pipes, and their lengths and diameters are given by

PipeLength (m)Diameter (m)
AA1B300.1
AA2B300.125
BC600.15
CD150.1
CF300.1

The head at A is 100 m, at E is 40 m and at F is 60 m. If the valve is adjusted to give equal discharge rates at E and F, calculate the head at C, the discharge through the system and percentage valve opening. Neglect all losses except those due to friction.

Method. Use hf=rQ2h_f = rQ^2 for each pipe, with r=8fLπ2gD5r = \dfrac{8fL}{\pi^2gD^5} (f=0.024f = 0.024). Only friction is considered. Heads: HA=100H_A = 100 m, HE=40H_E = 40 m, HF=60H_F = 60 m. For equal discharge let QE=QF=qQ_E = Q_F = q, so the flow in BCBC is 2q2q.

Resistance coefficients (s²/m⁵)

PipeL (m)D (m)r=8fL/(π2gD5)r = 8fL/(\pi^2gD^5)
AA1B300.1005949.1
AA2B300.1251949.4
BC600.1501566.9
CD150.1002974.6
CF300.1005949.1

Parallel pair A to B (same head loss in both): Q=h/r1+h/r2Q = \sqrt{h/r_1} + \sqrt{h/r_2}, so

1rAB=1r1+1r2  ⇒  rAB=788.4\frac{1}{\sqrt{r_{AB}}} = \frac{1}{\sqrt{r_1}} + \frac{1}{\sqrt{r_2}} \;\Rightarrow\; r_{AB} = 788.4

Discharge

Energy balance from A to F (pair AB, then BC carrying 2q2q, then CF carrying qq):

HA−HF=rAB(2q)2+rBC(2q)2+rCFq2H_A - H_F = r_{AB}(2q)^2 + r_{BC}(2q)^2 + r_{CF}q^2 100−60=q2[4(788.4+1566.9)+5949.1]=15370.2 q2  ⇒  q=0.05101 m3/s100 - 60 = q^2\left[4(788.4 + 1566.9) + 5949.1\right] = 15370.2\,q^2 \;\Rightarrow\; q = 0.05101\ \text{m}^3/\text{s} Q=2q=0.10203 m3/s=102.0 l/sQ = 2q = 0.10203\ \text{m}^3/\text{s} = 102.0\ \text{l/s}

Head at C

HC=HF+rCFq2=60+5949.1(0.002602)=75.48 mH_C = H_F + r_{CF}q^2 = 60 + 5949.1(0.002602) = 75.48\ \text{m}

(Check from A: HB=HC+rBC(2q)2=91.79H_B = H_C + r_{BC}(2q)^2 = 91.79 m; the two parallel pipes then carry 0.03714 and 0.06489 m³/s, which add to 0.10203 m³/s.)

Valve opening

Branch C to E has pipe CD and the valve DE in series, carrying qq with head loss HC−HE=75.48−40=35.48H_C - H_E = 75.48 - 40 = 35.48 m:

(rCD+KDE)q2=35.48  ⇒  KDE=35.480.002602−2974.6=10659.7(r_{CD} + K_{DE})q^2 = 35.48 \;\Rightarrow\; K_{DE} = \frac{35.48}{0.002602} - 2974.6 = 10659.7 KDE=(4000n)2  ⇒  n=400010659.7=38.7 %K_{DE} = \left(\frac{4000}{n}\right)^2 \;\Rightarrow\; n = \frac{4000}{\sqrt{10659.7}} = 38.7\ \%

Answer: Head at C =75.48= 75.48 m; total discharge =0.1020= 0.1020 m³/s (102.0102.0 l/s); valve opening n≈38.7 %n \approx 38.7\ \%.

✓ Answer checked by Claude Sonnet 5.5

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