Related Questions
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The temperature at the eutectic point of the system is the __________ temperature that can be attained in the system.
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The principle applied in liquefaction of gases is
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Charles' law for gases states that
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An isentropic process is carried out at constant
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The theoretical minimum work required to separate one mole of a liquid mixture at 1 atm, containing 50 mole % each of n- heptane and noctane into pure compounds each at 1 atm is
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4
In an ideal refrigeration cycle, the change in internal energy of the fluid is
D. Either of the above three; depends on the nature of refrigerant
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For an ideal gas, the enthalpy
A. Increases with rise in pressure
B. Decreases with rise in pressure
C. Is independent of pressure
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The melting point of paraffin wax (which contracts on solidification) __________ with pressure rise.
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The necessary condition for phase equilibrium in a multiphase system of N components is that the
A. Chemical potentials of a given component should be equal in all phases
B. Chemical potentials of all components should be same in a particular phase
C. Sum of the chemical potentials of any given component in all the phases should be the same
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Enthalpy changes over a constant pressure path are always zero for __________ gas.
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For a spontaneous process, free energy
C. Decreases whereas the entropy increases
D. And entropy both decrease
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What is the number of degree of freedom for a system of two miscible non-reacting species in vapor-liquid equilibrium forming an azeotrope?
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Sound waves propagation in air exemplifies an __________ process.
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At equilibrium condition, the chemical potential of a material in different phases in contact with each other is equal. The chemical potential for a real gas (μ) is given by (where, μ = standard chemical potential at unit fugacity (f° = 1 atm.) and the gas behaves ideally.)
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Which of the following is not an intensive property?
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Normal temperature and pressure (N.T.P.) corresponds to
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It is desired to bring about a certain change in the state of a system by performing work on the system under adiabatic conditions.
A. The amount of work needed is path dependent
B. Work alone cannot bring out such a change of state
C. The amount of work needed is independent of path
D. More information is needed to conclude anything about the path dependence or otherwise of the work needed
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On a P-V diagram of an ideal gas, suppose a reversible adiabatic line intersects a reversible isothermal line at point A. Then at a point A, the slope of the reversible adiabatic line (∂P/∂V)s and the slope of the reversible isothermal line (∂P/ ∂V)T are related as (where, y = Cp/Cv)
B. (∂P/∂V)S = [(∂P/∂V)T]Y
D. (∂P/∂V)S = 1/y(∂P/∂V)T
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Joule-Thomson experiment is
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If we increase the pressure on a substance (which is at its triple point), then the triple point
D. May increase or decrease; depends on the substance
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A thermodynamic system is taken from state A to B along ACB and is brought back to A along BDA as shown below in the P-V diagram. The net work done during the complete cycle is given by the area covered by
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4
The main feature of Carnot refrigeration cycle is that, it
A. Does not need the addition of external work for its functioning
B. Transfers heat from high temperature to low temperature
C. Accomplishes the reverse effect of the heat engine
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4
Claude gas liquefaction process employs cooling
C. By expansion in an engine
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The compressibility factor of a gas is given by (where, V1 = actual volume of the gas V2 = gas volume predicted by ideal gas law)
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Refrigeration capacity of a household refrigerator may be round about __________ tons.
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The standard Gibbs free energy change of a reaction depends on the equilibrium
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Compressibility factor for almost all the gases are approximately same at the same
A. Pressure and temperature
B. Reduced pressure and reduced temperature
C. Critical pressure and critical temperature
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An isolated system can exchange __________ with its surroundings.
C. Neither matter nor energy
D. Both matter and energy
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Which of the following decreases with increase in pressure?
C. Boiling point of liquids
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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