Physics by Lamhi: Not Your Boring Physics

CLASS 11 · CHAPTER 11 · HEAT

DETAILED NOTES

Thermodynamics

The complete chapter, section by section: thermal equilibrium and the zeroth law, the first law of thermodynamics, isothermal and adiabatic processes, specific heats, and the Carnot limit on any heat engine, explained in plain language with original worked examples. For the interactive isothermal vs. adiabatic P-V simulation, see the concept page.

11.1 Thermal Equilibrium and the Zeroth Law of Thermodynamics

Put a cup of hot tea on a table and leave it. Its temperature falls, the room’s rises by an imperceptible amount, and after a while nothing changes any further. Two systems in contact reach a common state called thermal equilibrium, in which no net heat flows between them even though they remain in contact. This is the state that lets you assign a single number, temperature, to describe “hotness” at all.

The trouble is that checking whether two systems are in equilibrium by placing them in direct contact is often inconvenient, you want to know if a patient and a healthy person are at the same temperature without pressing them together. The zeroth law rescues this:

If two systems A and B are separately in thermal equilibrium with a third system C, then A and B are in thermal equilibrium with each other.

Let C be a thermometer. The zeroth law says you never need to touch the patient and the healthy person together, touching each in turn to the same thermometer and reading the same value is enough to guarantee they’d be in equilibrium if they were in contact. This is precisely what makes a thermometer, and a temperature scale, a logically sound idea rather than a convenient fiction. It sounds obvious once stated, which is exactly why it went unnoticed and unnamed until after the first and second laws were already established, hence “zeroth”.

11.2 Heat, Internal Energy, Work, and the First Law of Thermodynamics

Internal energy UU is the sum of all the microscopic kinetic and potential energy inside a system, the random translational, rotational and vibrational motion of its molecules, and the energy stored in the forces between them. The one property that matters most about UU is that it is a state variable: its value is fixed entirely by the current state of the system (for an ideal gas, by its temperature alone), with no memory of how that state was reached.

Heat QQ and work WW are different in kind. Neither is something a system has, both are modes of energy in transit, across the boundary of the system, and both can depend on the exact path taken between two states even when the start and end states are identical. Saying “this gas contains so much heat” is not loose language, it is simply false; the gas contains internal energy, and heat is one of the two ways that energy gets transferred in or out.

The first law of thermodynamics is nothing more than energy conservation, written so as to keep heat and work separately visible:

First law of thermodynamics
ΔU=Q−W\textcolor{#e08a1e}{\Delta U} = Q - W

with the sign convention used throughout this chapter: QQ is positive when heat is absorbed by the system, and WW is positive when work is done by the system on its surroundings (such as a gas pushing a piston outward). Get either sign backwards and every later result in this chapter, isothermal work, adiabatic cooling, engine efficiency, comes out wrong, so it is worth fixing firmly: heat in is positive, work out is positive, and both appear on the side of the equation that increases ΔU\Delta U.

For a gas doing work only by changing its volume against a pressure PP, the work done by the gas as it expands from V1V_1 to V2V_2 is the area under its P-V curve:

W=∫V1V2P dVW = \int_{V_1}^{V_2} P\,dV

which depends on the exact shape of that curve, the path, not just its endpoints. ΔU\Delta U depends only on the endpoints.QQ then has to absorb whatever path-dependence is left over, which is exactly why heat, like work, cannot be a state variable.

11.3 Thermodynamic Processes: Isothermal and Adiabatic

A thermodynamic process is any change from one equilibrium state of a gas to another. Two idealized processes matter more than any others in this chapter, because they sit at opposite extremes of how a gas exchanges heat with its surroundings while its volume changes.

11.3.1 Isothermal processes

An isothermal process holds temperature fixed throughout, which requires the gas to be in contact with a large heat reservoir and for the change to happen slowly enough that heat has time to flow in or out and keep TT constant at every instant. Since an ideal gas’s internal energy depends on temperature alone, TT fixed means ΔU=0\Delta U = 0 for the entire process, no matter how far the volume changes. The first law then collapses to Q=WQ = W: every joule of heat that flows in becomes a joule of work done by the gas, and nothing is left over to change UU.

With TT constant, Boyle’s law PV=nRT=constantPV = nRT = \text{constant} fixes the whole curve, and integrating P dV=nRTVdVP\,dV = \dfrac{nRT}{V}dV from V1V_1 to V2V_2 gives the work done by nn moles of gas in an isothermal process:

Isothermal work
W=nRTln⁡ ⁣(V2V1)\textcolor{#e08a1e}{W} = nRT\ln\!\left(\dfrac{V_2}{V_1}\right)

11.3.2 Adiabatic processes, and the diesel-engine effect

An adiabatic process is the opposite extreme: the system is thermally insulated, so Q=0Q = 0 at every instant, achieved in practice either by genuinely insulating the gas or, just as often, by changing its volume so fast that heat simply has no time to flow before the process is over. With Q=0Q = 0, the first law gives:

ΔU=−W\Delta U = -W

Compress the gas and it does negative work (work is done on it), so ΔU\Delta U is positive and its temperature rises, with no flame, heater, or heat source anywhere nearby. This is exactly the contrast the simulation on the concept page is built around: compress the same gas, from the same starting point, adiabatically and it visibly reddens as it heats; compress it isothermally instead and its colour never moves, a reservoir quietly pulls the same heat back out as fast as compression makes it. It is also precisely why a diesel engine needs no spark plug: the piston compresses air fast enough that the compression is effectively adiabatic, and that alone drives the air’s temperature past the ignition point of injected diesel fuel.

Because TT is no longer fixed, Boyle’s law does not apply; instead an adiabatic process of an ideal gas follows:

Adiabatic condition
PVγ=constant\textcolor{#e08a1e}{PV^{\gamma}} = \text{constant}

where γ=Cp/Cv\gamma = C_p/C_v (next section) is always greater than 1, which is why the adiabatic curve through any point on a P-V diagram is always steeper than the isothermal curve through that same point. Combining PVγ=constPV^{\gamma}=\text{const} with PV=nRTPV=nRT also gives TVγ−1=constantTV^{\gamma-1}=\text{constant}, and integrating P dVP\,dV along this curve gives the work done by the gas between states (P1,V1)(P_1,V_1) and (P2,V2)(P_2,V_2):

W=P1V1−P2V2γ−1W = \dfrac{P_1V_1 - P_2V_2}{\gamma - 1}

Worked example

Adiabatic compression heats a gas with no heater at all

2.0 L of an ideal diatomic gas (γ=1.4\gamma = 1.4) at 100 kPa and 300 K is compressed adiabatically, quickly, to 0.80 L. Find the final temperature and the work done on the gas.

First the final temperature, from TVγ−1=constTV^{\gamma-1}=\text{const}:

T2=T1(V1V2)γ−1=300(2.00.80)0.4≈300×1.4427≈432.8 KT_2 = T_1\left(\dfrac{V_1}{V_2}\right)^{\gamma-1} = 300\left(\dfrac{2.0}{0.80}\right)^{0.4} \approx 300\times1.4427 \approx \textcolor{#e08a1e}{432.8\text{ K}}

which is a jump of nearly 133 K from compression alone. The final pressure, from PVγ=constPV^\gamma=\text{const}:

P2=P1(V1V2)γ=100(2.00.80)1.4≈360.7 kPaP_2 = P_1\left(\dfrac{V_1}{V_2}\right)^{\gamma} = 100\left(\dfrac{2.0}{0.80}\right)^{1.4} \approx \textcolor{#e08a1e}{360.7\text{ kPa}}

and the work done by the gas, then on it (opposite sign); since 1 kPa×1 L=1 J1\text{ kPa}\times1\text{ L} = 1\text{ J}, pressures in kPa and volumes in L can be multiplied directly:

Wby gas=P1V1−P2V2γ−1=(100)(2.0)−(360.7)(0.80)0.4W_{by\,gas} = \dfrac{P_1V_1 - P_2V_2}{\gamma-1} = \dfrac{(100)(2.0) - (360.7)(0.80)}{0.4}=200−288.60.4≈−221.3 J  ⇒  Won gas≈+221.3 J= \dfrac{200 - 288.6}{0.4} \approx -221.3\text{ J} \;\Rightarrow\; W_{on\,gas}\approx \textcolor{#e08a1e}{+221.3\text{ J}}

which checks out against the first law directly: with Q=0Q=0, every one of those 221.3 J done on the gas becomes ΔU\Delta U, raising its temperature.

11.4 Specific Heats Cp and Cv, and Why Cp Exceeds Cv

How much heat raises a gas’s temperature by a fixed amount depends on how it is heated, specifically, whether its volume or its pressure is held fixed while heating. This gives two distinct molar specific heats: CvC_v, the heat needed per mole per kelvin at constant volume, and CpC_p, the same thing at constant pressure.

At constant volume, the gas cannot expand, so it can do no work at all (W=0W=0), and the first law says every joule of heat supplied goes directly into ΔU\Delta U:

Q=nCvΔT=ΔUQ = nC_v\Delta T = \Delta U

At constant pressure, raising the temperature by the same ΔT\Delta T still requires that same ΔU\Delta U (internal energy of an ideal gas depends on TT alone, regardless of path), but now the gas also expands and does positive work PΔVP\Delta V on its surroundings, and that work has to be paid for with additional heat on top of what raised ΔU\Delta U:

Q=nCpΔT=ΔU+PΔVQ = nC_p\Delta T = \Delta U + P\Delta V

so CpC_p must exceed CvC_v, for exactly the same ΔT\Delta T, heating at constant pressure costs strictly more heat because some of it leaks out as expansion work rather than staying behind as internal energy. Substituting PΔV=nRΔTP\Delta V = nR\Delta T (from the ideal gas law at constant PP) gives the exact gap between them:

Specific heats of an ideal gas
Cp−Cv=R\textcolor{#e08a1e}{C_p - C_v} = R

independent of the gas, a genuinely universal relation for any ideal gas, monatomic or diatomic.

11.5 Heat Engines and the Second Law of Thermodynamics

A heat engine is any device that absorbs heat Q1Q_1 from a hot reservoir, converts part of it into work WW, rejects the rest, Q2Q_2, to a cold reservoir, and returns to its starting state so it can repeat the cycle indefinitely. Returning to the starting state matters, it means ΔU=0\Delta U = 0 over one full cycle, so the first law forces:

W=Q1−Q2W = Q_1 - Q_2

Its efficiency is the fraction of the absorbed heat that actually becomes useful work:

Heat engine efficiency
η=WQ1=1−Q2Q1\textcolor{#e08a1e}{\eta} = \dfrac{W}{Q_1} = 1 - \dfrac{Q_2}{Q_1}

It is tempting to imagine a sufficiently clever engine with Q2=0Q_2=0, converting every joule of absorbed heat straight into work, η=1\eta = 1. The second law of thermodynamics forbids this absolutely, not as an engineering shortfall but as a structural limit on what any cyclic process can do:

No process is possible whose sole result is the absorption of heat from a reservoir and its complete conversion into work. (Kelvin-Planck statement)

Every real heat engine must reject some heat to a cold sink; a refrigerator or heat pump is the mirror image, using external work to force heat to flow from cold to hot, which is the direction it never flows on its own, the companion Clausius statement of the same law. Both are experimentally equivalent statements of the same underlying fact: heat engines have a hard ceiling on efficiency, well short of 100%.

11.6 The Carnot Engine

If every real engine falls short of η=1\eta=1, the natural next question is: what is the best possible efficiency between two given temperatures? Sadi Carnot answered this with an idealized engine built from four reversible steps, working between a hot reservoir at T1T_1 and a cold one at T2T_2:

  1. Isothermal expansion at T1T_1, absorbing heat Q1Q_1 from the hot reservoir.
  2. Adiabatic expansion, cooling the gas from T1T_1 down to T2T_2 with no heat exchange.
  3. Isothermal compression at T2T_2, rejecting heat Q2Q_2 to the cold reservoir.
  4. Adiabatic compression, returning the gas from T2T_2 back up to T1T_1, closing the cycle.

Every one of these four steps is a process already derived in §11.3, the Carnot cycle adds nothing new physically, it simply chains two isothermal and two adiabatic steps together in the most efficient possible sequence. Working through the heat exchanged in the two isothermal legs gives Q2/Q1=T2/T1Q_2/Q_1 = T_2/T_1, so the efficiency depends on nothing but the two reservoir temperatures:

Carnot efficiency
ηCarnot=1−T2T1\textcolor{#e08a1e}{\eta_{Carnot}} = 1 - \dfrac{T_2}{T_1}

This is the theoretical ceiling: no engine, however cleverly designed, can exceed ηCarnot\eta_{Carnot} while operating between the same two temperatures, and a Carnot engine is the only kind that actually reaches it, because every one of its four steps is reversible. Real engines fall short of even this ceiling because real processes involve friction and irreversible heat loss that the idealized Carnot cycle has no room for. Notice, too, that ηCarnot\eta_{Carnot} reaches 1 only if T2=0 KT_2 = 0\text{ K}, absolute zero, which is itself unreachable, a different, related limit this chapter does not derive but is worth knowing by name (the third law of thermodynamics).

Worked example

How much hotter must the source be to gain 10 percentage points of efficiency?

A Carnot engine rejects heat to a sink at 290 K and currently runs at 35% efficiency. Find its source temperature, then find the new source temperature needed to raise the efficiency to 45%, keeping the same sink.

From η=1−T2/T1\eta = 1-T_2/T_1, solving for T1T_1:

T1=T21−η=2901−0.35=2900.65≈446.2 KT_1 = \dfrac{T_2}{1-\eta} = \dfrac{290}{1-0.35} = \dfrac{290}{0.65} \approx \textcolor{#e08a1e}{446.2\text{ K}}

and at 45% efficiency, with the same sink:

T1′=2901−0.45=2900.55≈527.3 KT_1' = \dfrac{290}{1-0.45} = \dfrac{290}{0.55} \approx \textcolor{#e08a1e}{527.3\text{ K}}

Gaining ten more percentage points of efficiency needed the source to climb by over 80 K, efficiency gains get steadily more expensive in temperature as η\eta approaches 1, since T1T_1 would need to diverge to reach η=1\eta=1 exactly.

— From the NCERT exercises

A couple of the chapter’s own classic exercise questions, with original worked solutions.

NCERT Exercise 11.9

A steam engine delivers 5.4×10⁸ J of work per minute and services a boiler at a temperature of 727°C with the sink at a temperature of 27°C. What is the efficiency of the engine? How much heat is wasted per minute, assuming it is an ideal engine?

Solution

Converting both reservoir temperatures to kelvin, T1=727+273=1000 KT_1 = 727+273 = 1000\text{ K} and T2=27+273=300 KT_2 = 27+273=300\text{ K}, and treating it as an ideal (Carnot) engine:

η=1−T2T1=1−3001000=0.70 (70%)\eta = 1-\dfrac{T_2}{T_1} = 1-\dfrac{300}{1000} = \textcolor{#e08a1e}{0.70\ (70\%)}

With W=5.4×108 J/minW = 5.4\times10^8\text{ J/min}, the heat absorbed per minute follows from η=W/Q1\eta = W/Q_1:

Q1=Wη=5.4×1080.70≈7.714×108 J/minQ_1 = \dfrac{W}{\eta} = \dfrac{5.4\times10^8}{0.70} \approx 7.714\times10^8\text{ J/min}

and the heat wasted (rejected to the sink) per minute is:

Q2=Q1−W≈7.714×108−5.4×108≈2.31×108 J/minQ_2 = Q_1 - W \approx 7.714\times10^8 - 5.4\times10^8 \approx \textcolor{#e08a1e}{2.31\times10^8\text{ J/min}}

NCERT Exercise 11.10

A Carnot engine takes 3×10⁶ cal of heat from a reservoir at 627°C and gives it to a sink at 27°C. What is the work done by the engine?

Solution

Converting temperatures, T1=627+273=900 KT_1 = 627+273=900\text{ K} and T2=27+273=300 KT_2 = 27+273=300\text{ K}, the Carnot efficiency is:

η=1−T2T1=1−300900=23\eta = 1-\dfrac{T_2}{T_1} = 1-\dfrac{300}{900} = \dfrac{2}{3}

Converting the absorbed heat to joules first (1 cal = 4.186 J):

Q1=3×106×4.186≈1.256×107 JQ_1 = 3\times10^6\times4.186 \approx 1.256\times10^7\text{ J}

and the work done is this fraction of the absorbed heat:

W=ηQ1=23×1.256×107≈8.37×106 JW = \eta Q_1 = \dfrac{2}{3}\times1.256\times10^7 \approx \textcolor{#e08a1e}{8.37\times10^6\text{ J}}