1988-7-b-iv-cre Liquid \(A\) decomposes by first order kinetics in an isothermal batch reactor. Fifty percent of \(A\) is converted in 300 seconds. The time required for a conversion of 75 percent is
1989-7-i-b-cre For the following reaction, the rate constant at 373 K is 0.5 per minute. \[ 0.5A + B \rightarrow C \] The overall order of the reaction is
1992-2-c-cre A gaseous reaction \(A\rightarrow 2B+C\) takes place isothermally in a constant pressure reactor. Starting with a gaseous mixture containing 50% \(A\) (rest inerts), the ratio of final to initial volume is found to be 1.6. The percentage conversion of
\(A\) is
1992-8-a-cre
The conversion of a reactant, undergoing a first order reaction, at a time equal to three times the half life of the reaction is
1999-2-14-cre Consider the n\(^{th}\) order irreversible liquid phase reaction \(A \rightarrow B\). Which one of the following plots involving half-life of the reaction \((t_{1/2})\) and the initial reactant concentration \((C_{A0})\) gives a straight line plot?
2000-1-19-cre The reaction \(A\rightarrow B\) is conducted in an isothermal batch reactor. If the conversion of \(A\) increases linearly with holding time, then the order of the reaction is
2000-2-17-cre The following half-life data are available for the irreversible liquid phase reaction, \[ A \rightarrow \text { Products} \] The overall order of the reaction is
Initial concentration
(kmol/m3)Half-life
(min)
2
2
8
1
2001-1-14-cre The conversion for a second order, irreversible reaction (constant volume), \(A \stackrel {k_2}{\longrightarrow } B\), in batch mode is given by
2001-2-17-cre The first-order, gas phase reaction \(A \stackrel {k_1}{\rightarrow } 2B\) is conducted isothermally in batch mode. The rate of change of conversion with time is given by
2004-73-cre For an isothermal second order aqueous phase reaction \(A \rightarrow B\), the ratio of the time required for 90% conversion to the time required for 45% conversion is
2005-26-cre For the liquid phase reaction \(A \rightarrow P\), in a series of experiments in a batch reactor, the half-life \(t_{1/2}\) was found to be inversely proportional to the square root of the initial concentration of \(A\). The order of the reaction is
2006-16-cre A first order reversible reaction \(A\xrightleftharpoons [k_2]{k_1} B\) occurs in a batch reactor. The exponential decay of the concentration of \(A\) has the time constant
2009-14-cre
The half-life of a first order liquid phase reaction is 30 seconds. Then the rate constant, in min-1, is
2012-19-cre The half-life of an \(n^{\text {th}}\) order reaction in a batch reactor depends on
2015-18-cre
For which reaction order, the half-life of the reactant is half of the full lifetime (time for 100% conversion) of the reactant?
2015-19-cre An irreversible, homogeneous reaction \(A\rightarrow \text {products}\), has the rate expression: \[ \text {Rate} = \frac {2C_A^2+0.1C_A}{1+50C_A}, \qquad \text {where \(C_A\) is the concentration of \(A\).} \] \(C_A\) varies in the range 0.5 - 50 mol/m3.
For very high concentrations of \(A\), the reaction order tends to:
2007-58-cre The following rate-concentration data are calculated from experiment. Find the activation energy temperature (\(E/R\)) of the first order reaction.
\(d_p\)
\(C_A\)
\(-r_A\)
\(T\)
1
20
1
480
2
40
2
480
2
40
3
500
2014-37-cre A homogeneous reaction (\(R\rightarrow P\)) occurs in a batch reactor. The conversion of the reactant \(R\) is 67% after 10 minutes and 80% after 20 minutes. The rate equation for this reaction is
The concentration versus batch time data for a constant volume, isothermal batch reactor is given in the table below. Assuming the reaction to be first order in \(A\), the best value of \(k\) by least squares regression is found to be = _______________ \(\times 10^{-3}\) s\(^{-1}\)
\(t\) (s)
0
30
60
90
120
150
180
\(C_A\) (kmol/m\(^3\))
1.00
0.92
0.89
0.81
0.76
0.72
0.70
BT-2016-48-cre Decimal reduction of bacterial spores is 23 min at 121oC and the death kinetics follow first order. One litre medium containing \(10^5\) spores per mL was sterilized for 10 min at 121oC in a batch sterilizer. The number of spores
in the medium after sterilization (assuming destruction of spores in heating and cooling period is negligible) will be ____________\(\times 10^7\).
BT-2018-48-cre Mammalian cells in active growth phase were seeded at a density of \(1\times 10^5\) cells/mL. After 72 hours, \(1\times 10^6\) cells/mL were obtained. The population double time of the cells in hours is (up to two decimal places) ____________
0700-3-cre Consider the reaction \(A+2B\rightarrow R\). This reaction was carried out and the following initial-rate data were reported. Determine the overall order of reaction and the reaction rate constant.
Run No.
\(C_{A0}\) (mol/litre)
\(C_{B0}\) (mol/litre)
Initial rate (mol/litre.s)
1
0.10
0.10
1.01
2
0.15
0.10
1.51
3
0.10
0.20
2.01
Last Modified on: 01-May-2024
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