$\therefore$ n = W/H
= 5.4 × 108/3.6 × 109 Hence, the percentage efficiency of the engine is 15%. Amount of heat wasted = 3.6 × 109 - 5.4 × 108 = 30.6 × 108 = 3.06 × 109J Therefore, the amount of heat wasted per minute is 3.06 × 109J.50 questions · self-marked practice — reveal the answer and mark yourself.
$\therefore$ n = W/H
= 5.4 × 108/3.6 × 109 Hence, the percentage efficiency of the engine is 15%. Amount of heat wasted = 3.6 × 109 - 5.4 × 108 = 30.6 × 108 = 3.06 × 109J Therefore, the amount of heat wasted per minute is 3.06 × 109J.$\therefore$ U = Q - W
= 100 - 75 = 25J/s = 25W Therefore, the internal energy of the given electric heater increases at a rate of 25W.
For Kr, $\text{C}_\upsilon=0.0357\text{cal/gm}^\circ\text{C}$ and $\text{C}_\text{P}=0.0595\text{cal/gm}^\circ\text{C.}$
$\Delta\text{Q}=\Delta\text{U}+\Delta\text{W}$
At constant volume, $\Delta\text{W}=0$ so $\Delta\text{Q}=\Delta\text{U}$
$=(3\times10^3)0.0357\times100$
$=10710\text{cal}=1071\text{ kcal}$
$=(3\times10^3)0.0595\times10$
$\Delta\text{U}=10.71\text{ kcal}$
Work done $\Delta\text{W}=\Delta\text{Q}-\Delta\text{U}$
$=17.85-10.71=7.14\text{ kcal}$
$=7.14\times4.184\text{kJ}=29.9\text{kJ}$
$=\Big(1-\frac{375}{500}\Big)\times100=25\%$
$\text{W}=\eta\text{ Q}_1;\text{Q}_1=6000\times10^3\text{cal}$
$\text{W}=\frac{25}{100}\times600\times10^3\text{cal}$
$=150\times10^3\text{cal}=150\times10^3\times4.2\text{J}$
$=6.8\times10^5\text{J(approx.)}$
$=600\times10^3-150\times10^3$
$=45\times10^4$
Also, $\text{PV}=\text{nRT}$
$\therefore\text{P}=\frac{\text{nRT}}{\text{V}}$
Replacing P, we have $\frac{\text{nRT}}{\text{RT}}.\text{V}^{\gamma}=$ constant (or) $\text{TV}^{\gamma-1}=$ constant.
Replacing V, we have, $\text{P}\Big(\frac{\text{nRT}}{\text{P}}\Big)^{\gamma}=$ constant.
$\therefore\text{T}^{\gamma}\text{P}^{1-\gamma}=$ constant.
$\frac{\text{dP}}{\text{P}}=\frac{\text{dV}}{\text{V}}$
But for an adiabatic process, since
$\text{PV}^\gamma=\text{constant},\frac{\text{dP}}{\text{P}}=-\gamma\frac{\text{dV}}{\text{V}}$
So P-V graph is steaper for adiabatic process.



$\text{W}_{\text{NM}}=\text{P}[\text{V}_\text{M}-\text{V}_\text{M}]=10[6-2]=40\text{J}$
$\text{W}_\text{LMN}=\text{W}_{\text{NM}}=0+40=40\text{J}$
Along LM WLM = Area under the curve LM
= Area of $\Delta\text{LMQ}+$ Area of rectangle LQZP.
$=\frac12\times\text{LQ}\times\text{MQ}+\text{LP}\times\text{PZ}$
$=\frac12\times4\times5+5\times4$
$=10+20=30\text{J}$
So work done is less along LM.
$\Delta\text{Q}=400\text{J}$
$\text{dQ}=\text{dU}+\text{dW}$
$=(\text{U}_\text{M}-\text{U}_\text{L})+\Delta\text{W}_{\text{LM}}$
$\text{U}_\text{M}=\text{dQ}+\text{U}_\text{L}-\Delta\text{W}_\text{LM}$
$=400+20-30$
$=390\text{J}$


Change in volume dV = 600 - 300 = 300 cc = 300 × 10-6 m3
Work done by the gas from D to E to F
= Area of $\Delta\text{DEF}$
$=\frac{1}{2}\times\text{dP}\times\text{dV}$
$=\frac12\times3.0\times10^5\times300\times10^{-6}\text{m}^3$
$=45\times10^6\times10^{-6}=45\text{J}$

Limitations:
First law do not tell us,
$\text{W}_\text{A}=\text{W}_\text{B}$
$\Big(1-\frac{\text{T}}{800}\Big)\text{Q}_1=\Big(1-\frac{300}{\text{T}}\Big)\text{Q}_2$
$\Big(1-\frac{\text{T}}{800}\Big)=\Big(1-\frac{300}{\text{T}}\Big)\frac{\text{Q}_2}{\text{Q}_1}=\Big(1-\frac{300}{\text{T}}\Big)\frac{\text{T}}{800}$
On solving, we get T = 550K
$1-\frac{\text{T}}{800}=1-\frac{300}{\text{T}}$
$\text{T}^2=24\times10^4$
$\therefore\text{T}=489.9\text{K}$


$\therefore$ Using the relation,
$\eta=1-\frac{\text{T}_2}{\text{T}_1},$ we get
$\eta=\frac{\text{T}_1-\text{T}_2}{\text{T}_1}$
$=\frac{500-375}{500}$
$=\frac{125}{500}=0.25$
$\eta\%=0.25\times100$
$=25\%$
$\therefore$ Using the relation
$\eta=\frac{\text{W}}{\text{Q}_1},$ we get
$\text{W}=\eta\text{Q}_1=0.25\times600\text{ kcal}=150\text{ kcal}$
$=150\times10^3\times4.2\text{J}$
$=6.3\times10^5\text{J}$
$\therefore$ Using the relation
$\text{W}=\text{Q}_1-\text{Q}_2,$ we get
$\text{Q}_2=\text{Q}_1-\text{W}$
$=600-150=450\text{ kcal}$