A CSTR is used to carry out liquid-phase reactions as described below. 2A + B -> 3C + D -r1A = k1A C2ACB A + 2 D -> E r2E = k2E CAC2D B + D -> 2E -r3B = k3B CBCD The reaction conditions are determined to be: T = 313 K; k1A = 5.5 dm6 /(mol2•min); k2E = 1.8 dm6 /(mol2•min); k3B = 1.2 dm3 /(mol•min) At steady state, the concentrations of A, B, C, and D are measured to be: 0.7, 0.8, 0.6, and 0.08 mol/dm3, while E is not measured. 1. Write the net formation rate of every species involved; 2. For species A, give your own values of its volumetric flowrate, and initial concentration, then calculate the volume of the reactor.
A CSTR is used to carry out liquid-phase reactions as described below.
2A + B -> 3C + D -r1A = k1A C2ACB
A + 2 D -> E r2E = k2E CAC2D
B + D -> 2E -r3B = k3B CBCD
The reaction conditions are determined to be:
T = 313 K; k1A = 5.5 dm6 /(mol2•min); k2E = 1.8 dm6 /(mol2•min); k3B = 1.2 dm3 /(mol•min)
At steady state, the concentrations of A, B, C, and D are measured to be: 0.7, 0.8, 0.6, and 0.08 mol/dm3, while E is not measured.
1. Write the net formation rate of every species involved;
2. For species A, give your own values of its volumetric flowrate, and initial concentration, then calculate the volume of the reactor.
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