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Heat and Thermodynamics question

2025 · Shift 2 · Q43
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Heat and Thermodynamics question

2025 · Shift 2 · Q43

JEE AdvancedPhysicsHeat and ThermodynamicsNumerical+4 / −1
An ideal monatomic gas of nnn moles is taken through a cycle WXYZWW X Y Z WWXYZW consisting of consecutive adiabatic and isobaric quasi-static processes, as shown in the schematic V−TV-TV−T diagram. The volume of the gas at W,XW, XW,X and YYY points are, 64 cm3,125 cm364 \mathrm{~cm}^3, 125 \mathrm{~cm}^364 cm3,125 cm3 and 250 cm3250 \mathrm{~cm}^3250 cm3, respectively. If the absolute temperature of the gas TWT_WTW​ at the point WWW is such that nRTW=1 Jn R T_W=1 \mathrm{~J}nRTW​=1 J(RRR is the universal gas constant), then the amount of heat absorbed (in J ) by the gas along the path XYX YXY is ‾\underline{\hspace{2cm}}​. JEE Advanced 2025 Paper 2 Online Physics - Heat and Thermodynamics Question 3 English
Numerical answer
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Correct answer: 1.6

  1. Identify the processes from the VVV-TTT diagram

    The cycle consists of alternating adiabatic and isobaric processes:

    • W→XW \to XW→X : adiabatic
    • X→YX \to YX→Y : isobaric
    • Y→ZY \to ZY→Z : adiabatic
    • Z→WZ \to WZ→W : isobaric

    We need the heat absorbed along the path X→YX \to YX→Y.

  2. Use adiabatic relation in VVV-TTT form

    For an ideal gas in a quasi-static adiabatic process, TVγ−1=constantT V^{\gamma-1} = \text{constant}TVγ−1=constant For a monatomic gas, γ=53⇒γ−1=23\gamma = \frac{5}{3} \quad \Rightarrow \quad \gamma-1 = \frac{2}{3}γ=35​⇒γ−1=32​

    Hence for W→XW \to XW→X, TWVW2/3=TXVX2/3T_W V_W^{2/3} = T_X V_X^{2/3}TW​VW2/3​=TX​VX2/3​ so TX=TW(VWVX)2/3T_X = T_W \left(\frac{V_W}{V_X}\right)^{2/3}TX​=TW​(VX​VW​​)2/3

    Given: VW=64 cm3,VX=125 cm3V_W = 64\ \text{cm}^3, \quad V_X = 125\ \text{cm}^3VW​=64 cm3,VX​=125 cm3

    Therefore, TX=TW(64125)2/3T_X = T_W \left(\frac{64}{125}\right)^{2/3}TX​=TW​(12564​)2/3

    Now, (64125)1/3=45\left(\frac{64}{125}\right)^{1/3} = \frac{4}{5}(12564​)1/3=54​ so (64125)2/3=(45)2=1625\left(\frac{64}{125}\right)^{2/3} = \left(\frac{4}{5}\right)^2 = \frac{16}{25}(12564​)2/3=(54​)2=2516​

    Hence, TX=1625TWT_X = \frac{16}{25} T_WTX​=2516​TW​

  3. Use isobaric relation for X→YX \to YX→Y

    For an isobaric process of an ideal gas, VT=constant⇒T∝V\frac{V}{T} = \text{constant} \Rightarrow T \propto VTV​=constant⇒T∝V

    So, TYTX=VYVX\frac{T_Y}{T_X} = \frac{V_Y}{V_X}TX​TY​​=VX​VY​​

    Given: VY=250 cm3,VX=125 cm3V_Y = 250\ \text{cm}^3, \quad V_X = 125\ \text{cm}^3VY​=250 cm3,VX​=125 cm3 Thus, TYTX=250125=2\frac{T_Y}{T_X} = \frac{250}{125} = 2TX​TY​​=125250​=2 TY=2TXT_Y = 2T_XTY​=2TX​

    Therefore, ΔTXY=TY−TX=TX\Delta T_{XY} = T_Y - T_X = T_XΔTXY​=TY​−TX​=TX​

    Using TX=1625TWT_X = \frac{16}{25}T_WTX​=2516​TW​, ΔTXY=1625TW\Delta T_{XY} = \frac{16}{25}T_WΔTXY​=2516​TW​

  4. Heat absorbed in an isobaric process

    For a monatomic ideal gas, CP=5R2C_P = \frac{5R}{2}CP​=25R​

    Hence heat absorbed along X→YX \to YX→Y is QXY=nCP(TY−TX)Q_{XY} = n C_P (T_Y - T_X)QXY​=nCP​(TY​−TX​) QXY=n⋅5R2⋅1625TWQ_{XY} = n \cdot \frac{5R}{2} \cdot \frac{16}{25}T_WQXY​=n⋅25R​⋅2516​TW​

    Rearranging, QXY=52⋅1625⋅nRTWQ_{XY} = \frac{5}{2} \cdot \frac{16}{25} \cdot nRT_WQXY​=25​⋅2516​⋅nRTW​ QXY=85 nRTWQ_{XY} = \frac{8}{5} \, nRT_WQXY​=58​nRTW​

    Given, nRTW=1 JnRT_W = 1\ \text{J}nRTW​=1 J

    Therefore, QXY=85=1.6 JQ_{XY} = \frac{8}{5} = 1.6\ \text{J}QXY​=58​=1.6 J

  5. Final answer

    The amount of heat absorbed along X→YX \to YX→Y is 1.6 J\boxed{1.6\ \text{J}}1.6 J​

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