Increases, for an exothermic reaction
Decreases, for an exothermic reaction
Increases, for an endothermic reaction
None of these
A. Increases, for an exothermic reaction
Cp/Cv
Cp/(CP-R)
1 + (R/CV)
All (A), (B) and (C)
Activity co-efficient is dimensionless.
In case of an ideal gas, the fugacity is equal to its pressure.
In a mixture of ideal gases, the fugacity of a component is equal to the partial pressure of the component.
The fugacity co-efficient is zero for an ideal gas
Low pressure and high temperature
Low pressure and low temperature
High pressure and low temperature
High pressure and high temperature
Less
More
Same
Dependent on climatic conditions
J/s
J.S
J/kmol
kmol/J
Fugacity
Activity co-efficient
Free energy
None of these
Pressure
Temperature
Both (A) & (B)
Neither (A) nor (B)
Directly proportional
Inversely proportional
Equal
None of these
An ideal liquid or solid solution is defined as one in which each component obeys Raoult's law
If Raoult's law is applied to one component of a binary mixture; Henry's law or Raoult's law is applied to the other component also
Henry's law is rigorously correct in the limit of infinite dilution
None of these
Heat
Momentum
Energy
Work
Pressure
Temperature
Both (A) & (B)
Neither (A) nor (B)
Process must be isobaric
Temperature must decrease
Process must be adiabatic
Both (B) and (C)
Negative
Zero
Infinity
None of these
λb/Tb
Tb/λb
√(λb/Tb)
√(Tb/λb)
Less than
More than
Same as
Not related to
Ideal compression of air
Free expansion of an ideal gas
Adiabatic expansion of steam in a turbine
Adiabatic compression of a perfect gas
Surface tension
Free energy
Specific heat
Refractive index
Molar concentration
Temperature
Internal energy
None of these
Initial concentration of the reactant
Pressure
Temperature
None of these
ds = 0
ds < 0
ds > 0
ds = Constant
Heat capacity of a crystalline solid is zero at absolute zero temperature
Heat transfer from low temperature to high temperature source is not possible without external work
Gases having same reduced properties behaves similarly
None of these
Zero
Positive
Negative
None of these
Turbine
Heat engine
Reversed heat engine
None of these
Cv.dT
Cp.dT
∫ Cp.dT
∫ Cv.dT
Third law of thermodynamics
Second law of thermodynamics
Nernst heat theorem
Maxwell's relations
300 × (32/7)
300 × (33/5)
300 × (333/7)
300 × (35/7)
Concentration of the constituents only
Quantities of the constituents only
Temperature only
All (A), (B) and (C)
Heating occurs
Cooling occurs
Pressure is constant
Temperature is constant
Isothermal
Adiabatic
Isentropic
Polytropic
Decrease in temperature
Increase in temperature
No change in temperature
Change in temperature which is a function of composition