Related Questions
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4
All gases above its inversion temperature, in a throttling process will show
B. No change in temperature
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4
Co-efficient of performance for a reversed Carnot cycle working between temperatures T1 and T2 (T1 > T2) is
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4
For the gaseous phase chemical reaction, C2H4(g) + H2O(g) ↔ C2H5OH(g), the equilibrium conversion does not depend on the
A. Steam to ethylene ratio
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4
Fugacity is a measure of the
A. Escaping tendencies of the same substance in different phases of a system
B. Relative volatility of a mixture of two miscible liquids
C. Behaviour of ideal gases
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4
What is the value of maximum COP in case of absorption refrigeration, if refrigeration provided is at temperature, TR (where, T1 and T2 are source & surrounding temperatures respectively.)?
A. TR/(T2 - TR) × (T1 - T2)/T1
B. TR/(T2 - TR) × T1/(T1 - T2)
C. TR/(T1 - TR) × (T1 - T2)/T1
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4
Forward reaction will be favoured for the exothermic reaction, represented by CO + H2O CO2 + H2, by
A. Low temperature and high pressure
B. Low temperature and low pressure
C. High temperature and high pressure
D. High temperature and low pressure
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4
In an ideal solution, the activity of a component equals its
B. Fugacity at the same temperature and pressure
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4
In polytropic process (PVn = constant), if n = 1; it means a/an __________ process.
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4
Pick out the undesirable property for a good refrigerant.
A. High thermal conductivity
C. Large latent heat of vaporisation
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4
If an ideal solution is formed by mixing two pure liquids in any proportion, then the __________ of mixing is zero
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4
Free energy change at equilibrium is
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4
A Carnot cycle consists of the following steps:
A. Two isothermal and two isentropic
B. Two isobaric and two isothermal
C. Two isochoric and two isobaric
D. Two isothermals and two isochoric
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4
Consider the process A & B shown in the figure given below: In this case, it is possible that
A. Both the processes are adiabatic
B. Both the processes are isothermal
C. Process A is isothermal while B is adiabatic
D. Process A is adiabatic while B is isothermal
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4
Degree of freedom of a system consisting of a gaseous mixture of H2 and NH3 will be
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4
One ton of refrigeration is defined as the heat rate corresponding to melting of one ton of ice in one
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4
Internal energy change of a system over one complete cycle in a cyclic process is
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4
Grams of butane (C4H10) formed by the liquefaction of 448 litres of the gas (measured at (STP) would be
D. Data insufficient; can't be computed
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4
The equilibrium constant for a chemical reaction at two different temperatures is given by
A. Kp2/Kp1 = - (ΔH/R) (1/T2 - 1/T1)
B. Kp2/Kp1 = (ΔH/R) (1/T2 - 1/T1)
C. Kp2/Kp1 = ΔH (1/T2 - 1/T1)
D. Kp2/Kp1 = - (1/R) (1/T2 - 1/T1)
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4
The reaction A (l) → R(g) is allowed to reach equilibrium conditions in an autoclave. At equilibrium, there are two phases, one a pure liquid phase of A and the other a vapor phase of A, R and S. Initially A alone is present. The numbers of degrees of freedom are:
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4
Which of the following diagrams does not represent an Otto cycle?
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4
The adiabatic throttling process of a perfect gas is one of constant enthalpy
A. In which there is a temperature drop
B. Which is exemplified by a non-steady flow expansion
C. Which can be performed in a pipe with a constriction
D. In which there is an increase in temperature
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4
Solubility of a substance which dissolves with an increase in volume and liberation of heat will be favoured by the
A. Low pressure and high temperature
B. Low pressure and low temperature
C. High pressure and low temperature
D. High pressure and high temperature
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4
The value of gas constant 'R' is
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4
__________ functions are exemplified by heat and work.
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4
The number of degree of freedom for an Azeotropic mixture of ethanol and water in vapourliquid equilibrium, is
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4
In jet refrigerators, the refrigerating fluid is practically always
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4
Which of the following is not affected by temperature changes?
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For a stable phase at constant pressure and temperature, the fugacity of each component in a binary system __________ as its mole fraction increases.
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4
Dry ice is
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For an irreversible process involving only pressure-volume work