Hour
Day
Minute
Second
B. Day
Increases
Decreases
Remains unchanged
May increase or decrease; depends on the substance
Heating takes place
Cooling takes place
Pressure is constant
Temperature is constant
With pressure changes at constant temperature
Under reversible isothermal volume change
During heating of an ideal gas
During cooling of an ideal gas
Enthalpy
Internal energy
Either (A) or (B)
Neither (A) nor (B)
A homogeneous solution (say of phenol water) is formed
Mutual solubility of the two liquids shows a decreasing trend
Two liquids are completely separated into two layers
None of these
6738.9
6753.5
7058.3
9000
Cold reservoir approaches zero
Hot reservoir approaches infinity
Either (A) or (B)
Neither (A) nor (B)
Triple point
Boiling point
Below triple point
Always
Mass
Energy
Momentum
None of these
100,000 kW
160,000 kW
200,000 kW
320,000 kW
More than
Less than
Equal to
Data insufficient, can't be predicted
Zero
One
Infinity
Negative
Does not depend upon temperature
Is independent of pressure only
Is independent of volume only
Is independent of both pressure and volume
0
1
2
3
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
(R/ΔH) (1/T1 - 1/T2)
(ΔH/R) (1/T1 - 1/T2)
(ΔH/R) (1/T2 - 1/T1)
(1/R) (1/T1 - 1/T2)
Adiabatic process
Endothermic reaction
Exothermic reaction
Process involving a chemical reaction
0
1
2
3
Increases
Decreases
Remains unchanged
Decreases linearly
Same in both the phases
Zero in both the phases
More in vapour phase
More in liquid phase
349
651
667
1000
Less
More
Same
Dependent on climatic conditions
Tds = dE - dW = 0
dE - dW - Tds = 0
Tds - dE + dW < 0
Tds - dT + dW < 0
The values of (∂P/∂V)T and (∂2P/∂V2)T are zero for a real gas at its critical point
Heat transferred is equal to the change in the enthalpy of the system, for a constant pressure, non-flow, mechanically reversible process
Thermal efficiency of a Carnot engine depends upon the properties of the working fluid besides the source & sink temperatures
During a reversible adiabatic process, the entropy of a substance remains constant
F = E - TS
F = H - TS
F = H + TS
F = E + TS
V/T = Constant
V ∝ 1/T
V ∝ 1/P
PV/T = Constant
Direction of energy transfer
Reversible processes only
Irreversible processes only
None of these
Is the most efficient of all refrigeration cycles
Has very low efficiency
Requires relatively large quantities of air to achieve a significant amount of refrigeration
Both (B) and (C)
ds = 0
ds < 0
ds > 0
ds = Constant
Freon
Liquid sulphur dioxide
Methyl chloride
Ammonia