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Give step-by-step solution with explanation and final answer: (Give me answer without using bullet-points) The concentration of glutamine in blood is being reduced using a hollow fibre dialyser membrane with a counter - current flow arrangement. The concentration of glutamine in the inlet stream is 1.05 g/l while the blood flow rate and the dialysate (water) flow rate are 0.85 Umin and 0.95 Vmin respectively. The surface area of the membrane is 500 cmand the membrane mass transfer coefficient is 2.86 x 10^-2 cm/s. The blood side mass transfer coefficient is 8.77 x 10^-2 cm /s while the dialysate side mass transfer coefficient is 3.44 x 10^-2 cm/s. Find the residual concentration of glutamine in blood if we assume that there is no flow of liquid across the membrane.

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Give step-by-step solution with explanation and final answer: (Give me answer without using bullet-points) The concentration of glutamine in blood is being reduced using a hollow fibre dialyser membrane with a counter - current flow arrangement. The concentration of glutamine in the inlet stream is 1.05 g/l while the blood flow rate and the dialysate (water) flow rate are 0.85 Umin and 0.95 Vmin respectively. The surface area of the membrane is 500 cmand the membrane mass transfer coefficient is 2.86 x 10^-2 cm/s. The blood side mass transfer coefficient is 8.77 x 10^-2 cm /s while the dialysate side mass transfer coefficient is 3.44 x 10^-2 cm/s. Find the residual concentration of glutamine in blood if we assume that there is no flow of liquid across the membrane.

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Asked by: Francis
Created at: 2026-01-20 23:24:03

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# Step-by-Step Solution ## Step 1: Write Down Known Values - Inlet concentration of glutamine in blood, \(C_{B,in}\): 1.05 g/L - Blood flow rate, \(Q_B\): .85 L/min - Dialysate flow rate, \(Q_D\): .95 L/min - Membrane area, \(A\): 500 cm² - Overall (membrane) mass transfer coefficient, \(K_m\): \(2.86 \times 10^{-2}\) cm/s - Blood side mass transfer coefficient, \(k_B\): \(8.77 \times 10^{-2}\) cm/s - Dialysate side mass transfer coefficient, \(k_D\): \(3.44 \times 10^{-2}\) cm/s ## Step 2: Convert Flow Rates to Consistent Units Convert all flow rates to cm³/s (since 1 L = 100 cm³, 1 min = 60 s): \[ Q_B = .85 \times 100 \div 60 = 14.17\ \text{cm}^3/\text{s} \] \[ Q_D = .95 \times 100 \div 60 = 15.83\ \text{cm}^3/\text{s} \] ## Step 3: Calculate the Overall Mass Transfer Coefficient (\(K\)) The overall mass transfer coefficient combines resistances in series: \[ \frac{1}{K} = \frac{1}{k_B} + \frac{1}{K_m} + \frac{1}{k_D} \] Plug in values: \[ \frac{1}{K} = \frac{1}{8.77 \times 10^{-2}} + \frac{1}{2.86 \times 10^{-2}} + \frac{1}{3.44 \times 10^{-2}} \] \[ \frac{1}{K} = 11.4 + 34.97 + 29.07 = 75.44 \] \[ K = \frac{1}{75.44} = .01326\ \text{cm/s} \] ## Step 4: Calculate Number of Transfer Units (NTU) For counter-current flow, the number of transfer units (NTU) is: \[ NTU = \frac{K \cdot A}{Q_B} \] Plug in the values: \[ NTU = \frac{.01326 \times 500}{14.17} = \frac{6.63}{14.17} = .468 \] ## Step 5: Calculate the Extraction Factor (S) \[ S = \frac{Q_B}{Q_D} = \frac{14.17}{15.83} = .895 \] ## Step 6: Apply Counter-Current Dialyzer Equation For a membrane dialyzer with no net fluid flow across the membrane, the outlet blood concentration (\(C_{B,out}\)) can be found using: \[ \frac{C_{B,out} - C_{D,in}}{C_{B,in} - C_{D,out}} = e^{-NTU \cdot (1 - S)} \] Assuming the dialysate inlet is pure water (\(C_{D,in} = \)), and the dialysate outlet concentration is negligible, so \(C_{D,out} \approx \). This simplifies to: \[ \frac{C_{B,out}}{C_{B,in}} = e^{-NTU \cdot (1 - S)} \] Plug in the values: \[ NTU \cdot (1 - S) = .468 \times (1 - .895) = .468 \times .105 = .0491 \] \[ \frac{C_{B,out}}{1.05} = e^{-.0491} = .952 \] \[ C_{B,out} = 1.05 \times .952 = .999\ \text{g/L} \] ## Final Answer **The residual concentration of glutamine in the blood after dialysis is approximately \(.999\ \text{g/L}\).** --- **Summary Table** | Quantity | Value | |------------------------|------------| | \(C_{B,in}\) | 1.05 g/L | | \(C_{B,out}\) | .999 g/L | | \(Q_B\) | 14.17 cm³/s| | \(Q_D\) | 15.83 cm³/s| | \(A\) | 500 cm² | | \(K\) | .0133 cm/s| | \(NTU\) | .468 | | \(S\) | .895 |

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