This quiz contains multiple-choice problems on CSTRS design.
Using a number of CSTRs in series is preferable to achieve a specific conversion than a single CSTR. True or false?
True
False
For very low conversion, the value of the Damkohler number is
≤ 0.1
> 10
≥ 0.1
= 10
For different sized CSTRs in series, the best system is one having a minimum volume for a specific conversion. True or false?
True
False
In terms of conversion, half-life is the time taken for
50% conversion
75% conversion
20% conversion
30% conversion
For a second-order reaction, t.0.5 is directly proportional to the initial concentration. True or false?
True
False
For equal-sized CSTRs in series carrying out first-order reactions, the concentration at the outlet of the nth reactor is
C{N} = 1/(1 + τk)^N
C{N} = C{0}/(1 + τ)^N
C{N} = C{0}/(1 + k)^N
C{N} = C{0}/(1 + τk)^N
What is the mole balance of a component in a CSTR (where F0 is the molar flow rate of reactant entering and F is the exit molar flow rate)?
F{0} = FX + F
F{0} = FX + F{0}
F{0} = F{0}X + F
F{0} = X + F
For ‘i’ CSTRs of variable volume in series, the residence time in the [i]th reactor is
τ{i} = C{i}/r{i}
τ{i} = (C{i} - C{i-1})/r{i}
τ{i} = -C{i}/r{i}
τ{i} = -C{i-1}/r{i}
For equal-sized CSTRs in series carrying out 1st order reactions of constant density, which of the following is true (k{i} is the rate constant in a reactor ‘i’ in series)?
k{1} ≠ k{2} ≠ … ≠ k{n}, τ{1} = τ{2} = … = τ{n}
k{1} = k{2} = … = k{n}, τ{1} = τ{2} = … = τ{n}
k{1} = k{2} = … = k{n}, τ{1} ≠ τ{2} ≠ … ≠ τ{n}
k{1} < k{2} < …
What is the concentration C4 at the end of the fourth reactor for n unequal sized CSTRs in series, where X{4} is the conversion in the fourth reactor?
C{4} = (1 – X{4})
C{4} = C{0}X{4}
C{0} = C{4} (1 – X{4})
C{4} = C{0}(1 – X{4})