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Chemical Engineering Gate 2013 Questions with Answer
Ques 1 GATE 2013
A gaseous system contains H2, I2, and HI, which participate in the gas-phase reaction
2 HI ↔ H2+I2
At a state of reaction equilibrium, the number of thermodynamic degrees of freedom is
Ques 2 GATE 2013
The thermodynamic state of a closed system containing a pure fluid changes from (T1,p1) to (T2, p2). where T and p denote the temperature and pressure, respectively. Let Q denote the heat absorbed (> 0 if absorbed by the system) and W the work done (> 0 if done by the system). Neglect changes in kinetic and potential energies. Which one of the following is CORRECT?
Ques 3 GATE 2013
An equation of state is explicit in pressure p and cubic in the specific volume v. At the critical point 'c', the isotherm passing through 'c' satisfies
Ques 4 GATE 2013
The units of the isothermal compressibility are
Ques 5 GATE 2013
In a process occurring in a closed system F, the heat transferred from F to the surroundings E is 600 J. If the temperature of E is 300 K and that of F is in the range 380-400 K, the entropy changes of the surroundings (ΔSE) and system (ΔSF), in J/K, are given by
Ques 6 GATE 2013
A binary liquid mixture is in equilibrium with its vapor at a temperature T=300 K. The liquid mole fraction x1 of species 1 is 0.4 and the molar excess Gibbs free energy is 200 J/mol. The value of the universal gas constant is 8.314 J/mol-K and γi denotes the liquid-phase activity coefficient of species i. If ln(γ1)=0.09, then the value of ln(γ2) up to 2 digits after the decimal point, is
Ques 7 GATE 2013
Calculate the heat required (in kJ, up to 1 digit after the decimal point) to raise the temperature of 1 mole of a solid material from 100°C to 1000°C. The specific heat (Cp) of the material (in J/mol-K) is expressed as Cp=20+0.005T where T is in K. Assume no phase change.
Ques 8 GATE 2013
The exit age distribution for a reactor is given by E(t)=δ(t-4), where t is in seconds. A first order liquid phase reaction (k=0.25 s-1) is carried out in this reactor under steady state and isothermal conditions. The mean conversion of the reactant at the exit of the reactor, up to 2 digits after the decimal point, is
Ques 9 GATE 2013
An isothermal liquid phase zero order reaction A→B (k=0.5 mol/m3-s) is carried out in a batch reactor. The initial concentration of A is 2 mol/m3. At 3 seconds from the start of the reaction, the concentration of A in mol/m3 is
Ques 10 GATE 2013
The overall rates of an isothermal catalytic reaction using spherical catalyst particles of diameters 1 mm and 2 mm are rA1 and rA2 (in mol (kg-catalyst)-1h-1), respectively. The other physical properties of the catalyst particles are identical. If pore diffusion resistance is very high, the ratio rA2/rA1 IS
Ques 11 GATE 2013
The gas phase decomposition of azomethane to give ethane and nitrogen takes place according to the following sequence of elementary reactions. (CH3)2N2+(CH3)2N2 → k1 (CH3)2N2+[(CH3)2N2]*
[(CH3)2N2]*+(CH3)2N2 → k2 (CH3)2N2+ (CH3)2N2
[(CH3)2N2]* → k3 C2H6+N2
Using the pseudo-steady-state-approximation for [(CH3)2N2]* the order with respect to azomethane in the rate expression for the formation of ethane, in the limit of high concentrations of azomethane, is
Ques 12 GATE 2013
A first order liquid phase reaction is carried out isothermally at a steady state in a CSTR and 90% conversion is attained. With the same inlet conditions and for the same overall conversion, if the CSTR is replaced by two smaller and identical isothermal CSTRs in series, the % reduction in total volume, to the nearest integer, is
Ques 13 GATE 2013
Liquid reactant A decomposes as follows

If the conversion of A is 80%, the concentration of R in the exit stream in mol/m3 to the nearest integer, is
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