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The pressure difference between points 1 and 2 in the series pipe system of the figure below is 20 psi. All the pipes are galvanized iron with roughness value of 0.0005 ft. The loss coefficient at the sudden contraction is 0.05. Determine the flow: rate in the system. The prevailing temperature is 70°F. 6inda OE nda | ooo son ———— 13001 a iven data: = 0.0005 ft Now, apply the energy equation between 1 k = 0.05 nd 2 v2 v2 w-w) WW =F LRN: BP PPA IRL A pg 29 pg 2 29 29 ‘e have to determine the flow rate The frictional head loss in the pipes will be rough the pipe hy = hy, + hy, + hy, Now, apply the continuity equation CALE ph fh = AV = MoV = AgVy FR Ta Tr f 2 PR I. a C8 Vh = I S107. 002-1000 ($2) 018.130. vz 0017-850 (23) —_— ee 2.9-% 2.9 2.9.3 6Vi = 64V; = 100V3 ” : 25.0521; 16 = ————=The head loss due to sudden i=—=W 9 [) xpansion will be 1 wy, Ly)’ vi = oy, vy (3% §w) 25 5 7 0.647V2 ———2 From the energy equation Ihe continuity equation is the conservation ? ) f 2 p ass flow Pp (Bw) py VE psn? 0edTv? v2 Lp 202 hy + ——2 + 0.055 Pg 29 2 9 9 2 2 e roughness in the pipes is Pp 204 Pg 9 ky = 0.0005 ft . 20-144 _ 24.60; = 0.006 inAssume the flow through the 230 5 ipe is turbulent a The friction factor for each pipe will be 1 d y 5 PF — — 2log( —— X ie weight density of water at 70°F is 77 ox +) +1 2 0 1 6 \e Reynolds number of the flow will be —— = 2log( -——— | + 1.74 Vd 77 (ams) * pV 1 " 1 = 0.02 va v 1 8 Ea 208) +174 7m. 4 2-0. — Vi, 0.008 05842810" f2 = 0.018 6.148 - 10° > 4000The discharge through the pipe 1 = 210g 10 ) +17 be Vi 20.006 er ] BH 3 = 0.017 x (8). =i (g) wm = 2.713 f%/s he value of the friction factor is obtained y using the Nikuradse equation.

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Uploaded ImageUploaded ImageThe pressure difference between points 1 and 2 in the series pipe system of the figure below is 20 psi. All the pipes are galvanized iron with roughness value of 0.0005 ft. The loss coefficient at the sudden contraction is 0.05. Determine the flow: rate in the system. The prevailing temperature is 70°F. 6inda OE nda | ooo son ———— 13001 a iven data: = 0.0005 ft Now, apply the energy equation between 1 k = 0.05 nd 2 v2 v2 w-w) WW =F LRN: BP PPA IRL A pg 29 pg 2 29 29 ‘e have to determine the flow rate The frictional head loss in the pipes will be rough the pipe hy = hy, + hy, + hy, Now, apply the continuity equation CALE ph fh = AV = MoV = AgVy FR Ta Tr f 2 PR I. a C8 Vh = I S107. 002-1000 ($2) 018.130. vz 0017-850 (23) —_— ee 2.9-% 2.9 2.9.3 6Vi = 64V; = 100V3 ” : 25.0521; 16 = ————=The head loss due to sudden i=—=W 9 [) xpansion will be 1 wy, Ly)’ vi = oy, vy (3% §w) 25 5 7 0.647V2 ———2 From the energy equation Ihe continuity equation is the conservation ? ) f 2 p ass flow Pp (Bw) py VE psn? 0edTv? v2 Lp 202 hy + ——2 + 0.055 Pg 29 2 9 9 2 2 e roughness in the pipes is Pp 204 Pg 9 ky = 0.0005 ft . 20-144 _ 24.60; = 0.006 inAssume the flow through the 230 5 ipe is turbulent a The friction factor for each pipe will be 1 d y 5 PF — — 2log( —— X ie weight density of water at 70°F is 77 ox +) +1 2 0 1 6 \e Reynolds number of the flow will be —— = 2log( -——— | + 1.74 Vd 77 (ams) * pV 1 " 1 = 0.02 va v 1 8 Ea 208) +174 7m. 4 2-0. — Vi, 0.008 05842810" f2 = 0.018 6.148 - 10° > 4000The discharge through the pipe 1 = 210g 10 ) +17 be Vi 20.006 er ] BH 3 = 0.017 x (8). =i (g) wm = 2.713 f%/s he value of the friction factor is obtained y using the Nikuradse equation.

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Asked by: MD ISRARUL HAQUE
Created at: 2025-08-27 20:14:39

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Here’s a summary and breakdown of the solution steps for the given pipe flow problem: --- ### **Given Data** - Pressure difference (\( \Delta P \)) = 20 psi - Roughness (\( k_s \)) = 0.0005 ft - Loss coefficient at contraction (\( k \)) = 0.05 - Temperature (\( T \)) = 70°F - Pipe details: - 6 in diameter, 1000 ft - 10 in diameter, 850 ft - 8 in diameter, 1300 ft --- ## **Step 1: Continuity Equation** **Conservation of mass flow:** \[ Q = A_1 V_1 = A_2 V_2 = A_3 V_3 \] - \( \frac{\pi}{4} \cdot 6^2 \cdot V_1 = \frac{\pi}{4} \cdot 8^2 \cdot V_2 = \frac{\pi}{4} \cdot 10^2 \cdot V_3 \) - Simplifying: - \( 36 V_1 = 64 V_2 = 100 V_3 \) - \( V_1 = \frac{16}{9} V_2 \) - \( V_3 = \frac{16}{25} V_2 \) --- ## **Step 2: Friction Factor Calculation** **Roughness and turbulent flow:** - Assume turbulent flow. - Use Nikuradse equation: \[ \frac{1}{\sqrt{f}} = 2 \log_{10} \left( \frac{d}{2 k_s} \right) + 1.74 \] - For 6 in (\( f_1 \)): \( f_1 = 0.02 \) - For 8 in (\( f_2 \)): \( f_2 = 0.018 \) - For 10 in (\( f_3 \)): \( f_3 = 0.017 \) --- ## **Step 3: Energy Equation Application** **Apply energy equation between points 1 and 2:** \[ \frac{P_1}{\rho g} + \frac{V_1^2}{2g} + Z_1 = \frac{P_2}{\rho g} + \frac{V_2^2}{2g} + Z_2 + h_f \] - \( h_f = h_{f1} + h_{f2} + h_{f3} \) - Calculate each head loss: - \( h_{f1} = \frac{f_1 L_1 V_1^2}{2gd_1} \) - \( h_{f2} = \frac{f_2 L_2 V_2^2}{2gd_2} \) - \( h_{f3} = \frac{f_3 L_3 V_3^2}{2gd_3} \) - Include minor loss (sudden contraction): \( k \frac{(V_1 - V_3)^2}{2g} \) - Substitute velocities in terms of \( V_2 \). **Combine all terms and solve for \( V_2 \):** - Substitute known values: - Pressure difference in ft: \( \frac{P_1 - P_2}{\rho g} = \frac{20 \times 144}{62.3} = 46.25 \) ft - Equation: \[ \frac{P_1 - P_2}{\rho g} = 25.052 \frac{V_2^2}{g} + 0.647 \frac{V_2^2}{g} + 0.05 \frac{V_2^2}{g} \] \[ 46.25 = 25.749 \frac{V_2^2}{g} \] \[ V_2 = 7.772 \text{ ft/s} \] --- ## **Step 4: Flow Rate Calculation** \[ Q = A_2 V_2 = \frac{\pi}{4} \left(\frac{8}{12}\right)^2 \cdot 7.772 = 2.713 \text{ ft}^3/\text{s} \] --- ## **Step 5: Reynolds Number Check** \[ Re = \frac{V d}{\nu} = \frac{7.772 \times \frac{8}{12}}{0.8428 \times 10^{-5}} = 6.148 \times 10^5 \] - Confirms turbulent flow (>4000). --- ## **Final Answer** ### **The flow rate in the system is:** \[ \boxed{Q = 2.713 \ \text{ft}^3/\text{s}} \] --- **All calculations and steps are shown clearly in the provided solution image. If you need a detailed explanation of any step, let me know!**

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