System and surroundings pressure be equal
Friction in the system should be absent
System and surroundings temperature be equal
None of these
B. Friction in the system should be absent
Isobaric
Isothermal
Isentropic
Isometric
n = y = 1.4
n = 0
n = 1
n = 1.66
(∂P/∂V)T
(∂V/∂T)P
(∂P/∂V)V
All (A), (B) & (C)
Increases
Decreases
Remain constant
Increases linearly
2
0
1
3
More
Less
Same
More or less; depending on the system
3
4
5
6
Low pressure & high temperature
High pressure & low temperature
Low pressure & low temperature
None of these
Decrease on addition of Cl2
Increase on addition of an inert gas at constant pressure
Decrease on increasing the pressure of the system
None of these
Enthalpy does not remain constant
Entire apparatus is exposed to surroundings
Temperature remains constant
None of these
-94 kcal
> -94 kcal
< - 94 kcal
Zero
Entropy
Gibbs free energy
Internal energy
All (A), (B) & (C)
Fugacity
Partial pressure
Activity co-efficient
All (A), (B), and (C)
Ice at the base contains impurities which lowers its melting point
Due to the high pressure at the base, its melting point reduces
The iceberg remains in a warmer condition at the base
All (A), (B) and (C)
Vapor compression cycle using expansion valve
Air refrigeration cycle
Vapor compression cycle using expansion engine
Carnot refrigeration cycle
Cp/Cv
Cp/(CP-R)
1 + (R/CV)
All (A), (B) and (C)
Momentum
Mass
Energy
None of these
Constant volume
Polytropic
Adiabatic
Constant pressure
0
< 0
> 0
A function of pressure
System (of partially miscible liquid pairs), in which the mutual solubility increases with rise in temperature, are said to possess an upper consolute temperature
Systems, in which the mutual solubility increases with decrease in temperature, are said to possess lower consolute temperature
Nicotine-water system shows both an upper as well as a lower consolute temperature, implying that they are partially miscible between these two limiting temperatures
None of these
Specific volume
Temperature
Mass
Pressure
Air cycle
Carnot cycle
Ordinary vapour compression cycle
Vapour compression with a reversible expansion engine
Triple point
Boiling point
Below triple point
Always
Molecular size
Volume
Pressure
Temperature
Work done under adiabatic condition
Co-efficient of thermal expansion
Compressibility
None of these
Not changed
Decreasing
Increasing
Data sufficient, can't be predicted
(T2 - T1)/T2
(T2 - T1)/T1
(T1 - T2)/T2
(T1 - T2)/T1
Isothermal
Adiabatic
Isentropic
Polytropic
Endothermic
Exothermic
Isothermal
Adiabatic
Zero
Unity
Infinity
An indeterminate value