GATE GUIDE

GATE ME Thermodynamics Formula Sheet 2027: Cycles to Pumps

By MD ANISH AHAMADUpdated 4 Oct 202610 min read
GATE ME Thermodynamics Formula Sheet 2027: Cycles to Pumps

Which thermodynamics formulas does a GATE ME candidate actually need? The ones that turn a property table or a cycle diagram into a number: energy balances, entropy, cycle efficiencies, COP, specific humidity and the turbomachinery relations. This sheet gives the most-used of them across Thermodynamics and Applications, each topic with a worked example and its trap.

In this guide
  1. Key takeaways
  2. The terms and notation this sheet uses
  3. Work, heat and the first law
  4. Entropy, the second law and exergy
  5. Power cycles: Rankine and Brayton
  6. Air-standard engine cycles
  7. Combustion: air-fuel ratio and equivalence ratio (New in 2027)
  8. Refrigeration and psychrometry
  9. Turbomachinery, compressors and pumps
  10. The mistakes that cost marks under time pressure
  11. Quick revision

Key takeaways

The terms and notation this sheet uses

A closed system lets no mass cross its boundary; an open system (a control volume) lets mass flow in and out; an isolated system exchanges neither mass nor energy. Properties such as pressure and temperature are point functions; heat and work are path functions.

Notation: QQ is heat added to the system and WW is work done by it. Lower case (qq, ww, uu, hh, ss, vv) means per kilogram. A dot means a rate, so m˙\dot{m} is mass flow in kg/s. Subscript 1 is the inlet or initial state, 2 the exit or final state, and 0 the surroundings (the dead state). The quality xx is the dryness fraction of a wet mixture. For air, take R=0.287R = 0.287, cp=1.005c_p = 1.005 and cv=0.718c_v = 0.718 kJ/kg K, with γ=1.4\gamma = 1.4, unless the question gives its own values.

Work, heat and the first law

Work is the area under the path on a pp-VV diagram. The first law books the energy: heat in minus work out equals the rise in stored energy.

Formula Watch out for
W=p(V2−V1)W = p(V_2 - V_1) at constant pp; W=p1V1ln⁡(V2/V1)W = p_1 V_1 \ln(V_2/V_1) isothermal; W=p1V1−p2V2n−1\displaystyle W = \dfrac{p_1 V_1 - p_2 V_2}{n - 1} for pVn=CpV^n = C Constant volume gives zero; with stops, split into a constant-pressure leg and a constant-volume leg
Closed: Q−W=ΔUQ - W = \Delta U; polytropic ideal gas Q=W γ−nγ−1\displaystyle Q = W\,\dfrac{\gamma - n}{\gamma - 1} New in 2027 wording: closed-system analysis is named
Steady flow: Q˙−W˙=m˙[(h2−h1)+V22−V122+g(z2−z1)]\displaystyle \dot{Q} - \dot{W} = \dot{m}\left[(h_2 - h_1) + \dfrac{V_2^2 - V_1^2}{2} + g(z_2 - z_1)\right] New in 2027 wording: open-system analysis is named; kinetic terms in J/kg, enthalpy in kJ/kg
Throttle h2=h1h_2 = h_1; nozzle from rest V2=44.72ΔhV_2 = 44.72\sqrt{\Delta h} (Δh\Delta h in kJ/kg) The 44.72 is 2000\sqrt{2000} and already converts kJ to J
Evacuated insulated tank filled from a line: u2=hlineu_2 = h_{\text{line}}, so T2=γTlineT_2 = \gamma T_{\text{line}} Flow enthalpy hh enters, not uu
pv=RTpv = RT, R=Rˉ/MR = \bar{R}/M, Rˉ=8.314\bar{R} = 8.314 kJ/kmol K; cp−cv=Rc_p - c_v = R; Δu=cvΔT\Delta u = c_v \Delta T, Δh=cpΔT\Delta h = c_p \Delta T Absolute pressure and kelvin in pv=RTpv = RT
Wet steam: v=vf+xvfgv = v_f + x v_{fg}, and the same for hh, ss, uu A rigid vessel keeps vv fixed

Worked example. Air at 100 kPa and 0.1 m³ is compressed to 0.05 m³ along pV1.3=CpV^{1.3} = C. Then p2=100×21.3=246.2p_2 = 100 \times 2^{1.3} = 246.2 kPa, and

W=(100)(0.1)−(246.2)(0.05)1.3−1=10−12.310.3=−7.70 kJW = \frac{(100)(0.1) - (246.2)(0.05)}{1.3 - 1} = \frac{10 - 12.31}{0.3} = -7.70 \text{ kJ}

The sign says work is done on the gas. For a nozzle with a 200 kJ/kg enthalpy drop from rest, V2=44.72200=632V_2 = 44.72\sqrt{200} = 632 m/s.

Trap: In a nozzle or a turbine, enthalpy comes from tables in kJ/kg while V2/2V^2/2 comes out in J/kg. Convert one of them before you add, or the kinetic term is out by a factor of 1000.

Entropy, the second law and exergy

The second law says entropy generated is never negative; exergy measures how much of an energy flow could still become work.

Formula Watch out for
ηCarnot=1−TLTH\displaystyle \eta_{\text{Carnot}} = 1 - \dfrac{T_L}{T_H}; COPR=TLTH−TL\displaystyle \text{COP}_R = \dfrac{T_L}{T_H - T_L}; COPHP=THTH−TL=COPR+1\displaystyle \text{COP}_{HP} = \dfrac{T_H}{T_H - T_L} = \text{COP}_R + 1 Kelvin only
Ideal gas: Δs=cpln⁡T2T1−Rln⁡p2p1=cvln⁡T2T1+Rln⁡v2v1\displaystyle \Delta s = c_p \ln\dfrac{T_2}{T_1} - R \ln\dfrac{p_2}{p_1} = c_v \ln\dfrac{T_2}{T_1} + R \ln\dfrac{v_2}{v_1} New in 2027 wording: entropy changes are named
Isentropic: T2T1=(p2p1)(γ−1)/γ=(v1v2)γ−1\displaystyle \dfrac{T_2}{T_1} = \left(\dfrac{p_2}{p_1}\right)^{(\gamma - 1)/\gamma} = \left(\dfrac{v_1}{v_2}\right)^{\gamma - 1} Absolute pressures
Solid or liquid Δs=cln⁡(T2/T1)\Delta s = c \ln(T_2/T_1); reservoir ΔS=Q/T\Delta S = Q/T; Sgen=ΔSsys+ΔSsurr≥0S_{\text{gen}} = \Delta S_{\text{sys}} + \Delta S_{\text{surr}} \ge 0 A reservoir's temperature does not change
Exergy of heat Q(1−T0/T)Q(1 - T_0/T); flow exergy ψ=(h−h0)−T0(s−s0)\psi = (h - h_0) - T_0(s - s_0); I=T0SgenI = T_0 S_{\text{gen}} T0T_0 is the surroundings, not the cold end of a cycle
T ds=du+p dv=dh−v dpT\,ds = du + p\,dv = dh - v\,dp; Clapeyron dpdT=hfgTvfg\displaystyle \dfrac{dp}{dT} = \dfrac{h_{fg}}{T v_{fg}} Joule-Thomson coefficient is zero for an ideal gas

Worked example. Air heated at constant pressure from 300 K to 600 K gains Δs=1.005ln⁡2=0.697\Delta s = 1.005 \ln 2 = 0.697 kJ/kg K. And 100 kJ of heat at 600 K with the surroundings at 300 K carries exergy 100(1−300/600)=50100(1 - 300/600) = 50 kJ.

Remember: If a temperature sits inside a ratio, a power or a logarithm, it must be in kelvin. Celsius survives only in a difference such as cpΔTc_p \Delta T.

Power cycles: Rankine and Brayton

Number the Rankine states as 1 turbine inlet, 2 turbine exit, 3 pump inlet (saturated liquid) and 4 pump exit. Efficiency is net work over heat added in the boiler.

Formula Watch out for
Rankine η=(h1−h2)−(h4−h3)h1−h4\displaystyle \eta = \dfrac{(h_1 - h_2) - (h_4 - h_3)}{h_1 - h_4}; pump work vf(p4−p3)v_f(p_4 - p_3) Heat added starts at h4h_4, not h3h_3
Specific steam consumption =3600/wnet= 3600/w_{\text{net}} kg/kWh, wnetw_{\text{net}} in kJ/kg Reheat chiefly raises exhaust dryness and work per kilogram
Open feedwater heater: m hbleed+(1−m)hin=houtm\,h_{\text{bleed}} + (1 - m)h_{\text{in}} = h_{\text{out}} Saturated liquid leaves at the bleed pressure
Brayton η=1−1rp(γ−1)/γ\displaystyle \eta = 1 - \dfrac{1}{r_p^{(\gamma - 1)/\gamma}}; maximum work at rp=(Tmax⁡/Tmin⁡)γ/(2(γ−1))r_p = (T_{\max}/T_{\min})^{\gamma/(2(\gamma - 1))} A regenerator cuts heat added, not the net work
Turbine ηs=actual Δhisentropic Δh\displaystyle \eta_s = \dfrac{\text{actual } \Delta h}{\text{isentropic } \Delta h}; compressor and pump ηs=isentropic Δhactual Δh\displaystyle \eta_s = \dfrac{\text{isentropic } \Delta h}{\text{actual } \Delta h} The two are inverses of each other

Worked example. Take h1=3200h_1 = 3200, h2=2200h_2 = 2200 and h3=190h_3 = 190 kJ/kg, with vf=0.001v_f = 0.001 m³/kg pumping from 10 kPa to 8 MPa. Pump work is 0.001×7990=7.990.001 \times 7990 = 7.99 kJ/kg, so h4=198.0h_4 = 198.0 kJ/kg.

η=1000−7.993200−198.0=992.03002=0.330,SSC=3600992.0=3.63 kg/kWh\eta = \frac{1000 - 7.99}{3200 - 198.0} = \frac{992.0}{3002} = 0.330, \qquad \text{SSC} = \frac{3600}{992.0} = 3.63 \text{ kg/kWh}

A Brayton cycle with rp=8r_p = 8 and γ=1.4\gamma = 1.4 gives η=1−1/80.2857=1−1/1.811=0.448\eta = 1 - 1/8^{0.2857} = 1 - 1/1.811 = 0.448.

Air-standard engine cycles

The compression ratio is r=(Vc+Vs)/Vcr = (V_c + V_s)/V_c, clearance plus swept volume over clearance volume. The cut-off ratio ρ\rho is the volume ratio across the constant-pressure heat addition.

Formula Watch out for
Otto η=1−1rγ−1\displaystyle \eta = 1 - \dfrac{1}{r^{\gamma - 1}} rr is a volume ratio, not a pressure ratio
Diesel η=1−1rγ−1⋅ργ−1γ(ρ−1)\displaystyle \eta = 1 - \dfrac{1}{r^{\gamma - 1}} \cdot \dfrac{\rho^\gamma - 1}{\gamma(\rho - 1)} The bracket exceeds 1, so Diesel is below Otto at equal rr
Dual η=1−1rγ−1⋅αργ−1(α−1)+γα(ρ−1)\displaystyle \eta = 1 - \dfrac{1}{r^{\gamma - 1}} \cdot \dfrac{\alpha \rho^\gamma - 1}{(\alpha - 1) + \gamma \alpha (\rho - 1)} α\alpha is the constant-volume pressure ratio
Same rr and heat input: Otto >> dual >> Diesel; same peak pressure and temperature: Diesel >> dual >> Otto The order reverses with the basis
Mean effective pressure == net work // swept volume; indicated power pmLAN′k/60p_m L A N' k/60, N′=N/2N' = N/2 for four-stroke Mechanical efficiency =BP/IP= \text{BP}/\text{IP}

Worked example. Otto with r=10r = 10: η=1−1/100.4=1−1/2.512=0.602\eta = 1 - 1/10^{0.4} = 1 - 1/2.512 = 0.602. Diesel with r=16r = 16 and ρ=2\rho = 2: 21.4=2.6392^{1.4} = 2.639, so the bracket is 1.639/1.4=1.1711.639/1.4 = 1.171, and η=1−1.171/3.031=0.614\eta = 1 - 1.171/3.031 = 0.614. Work such powers on the GATE virtual calculator with its xyx^y key.

The last-minute formula sheet in the GATE ME 2027 book covers all ten technical sections with each formula's conditions, alongside 942 questions with worked solutions and 10 full mock tests.

Combustion: air-fuel ratio and equivalence ratio (New in 2027)

Air is 21 per cent oxygen by volume (3.76 mol nitrogen per mol oxygen) and about 23.2 per cent oxygen by mass.

Formula Watch out for
CxHy+(x+y4)(O2+3.76 N2)→x CO2+y2 H2O+3.76(x+y4)N2\displaystyle \text{C}_x\text{H}_y + \left(x + \tfrac{y}{4}\right)(\text{O}_2 + 3.76\,\text{N}_2) \to x\,\text{CO}_2 + \tfrac{y}{2}\,\text{H}_2\text{O} + 3.76\left(x + \tfrac{y}{4}\right)\text{N}_2 New in 2027
A/F=mass of airmass of fuel\displaystyle A/F = \dfrac{\text{mass of air}}{\text{mass of fuel}}; stoichiometric about 17.2 for methane, 15.1 for octane New in 2027; by mass, not by moles
ϕ=(F/A)actual(F/A)stoich=(A/F)stoich(A/F)actual\displaystyle \phi = \dfrac{(F/A)_{\text{actual}}}{(F/A)_{\text{stoich}}} = \dfrac{(A/F)_{\text{stoich}}}{(A/F)_{\text{actual}}}; λ=1/ϕ\lambda = 1/\phi New in 2027; ϕ<1\phi < 1 lean, ϕ>1\phi > 1 rich
Excess air =(1/ϕ−1)×100%= (1/\phi - 1) \times 100\%; HHV−LHV=mwater hfg\text{HHV} - \text{LHV} = m_{\text{water}}\,h_{fg} HHV has the water condensed

Worked example. Methane has x=1x = 1, y=4y = 4, so it needs 2 mol of oxygen, or 64 kg per 16 kg of fuel. The air is 64/0.232=275.964/0.232 = 275.9 kg, and A/F=275.9/16=17.2A/F = 275.9/16 = 17.2. Burned at A/F=21.5A/F = 21.5, it has ϕ=17.2/21.5=0.8\phi = 17.2/21.5 = 0.8, a lean mixture with (1/0.8−1)×100=25(1/0.8 - 1) \times 100 = 25 per cent excess air.

In one line: The equivalence ratio compares fuel to fuel, actual over stoichiometric, so a mixture with more air than it needs has ϕ\phi below 1.

Refrigeration and psychrometry

Number the vapour-compression states as 1 evaporator exit, 2 compressor exit, 3 condenser exit and 4 after the throttle.

Formula Watch out for
COP=h1−h4h2−h1\displaystyle \text{COP} = \dfrac{h_1 - h_4}{h_2 - h_1}, with h4=h3h_4 = h_3 Subcooling raises the refrigerating effect
COPHP=COPR+1\text{COP}_{HP} = \text{COP}_R + 1 on the same cycle; 1 TR =3.517= 3.517 kW =211= 211 kJ/min Tonnes of refrigeration are a rate
Bell-Coleman COP=1rp(γ−1)/γ−1\displaystyle \text{COP} = \dfrac{1}{r_p^{(\gamma - 1)/\gamma} - 1} Reversed Brayton cycle
ω=0.622 pvp−pv\displaystyle \omega = 0.622\,\dfrac{p_v}{p - p_v}; relative humidity =pv/psat(T)= p_v/p_{\text{sat}}(T) pp is the total pressure
h=1.005t+ω(2501+1.88t)h = 1.005t + \omega(2501 + 1.88t) kJ/kg dry air, tt in ∘^\circC Per kilogram of dry air
Bypass factor =tout−tcoiltin−tcoil\displaystyle = \dfrac{t_{\text{out}} - t_{\text{coil}}}{t_{\text{in}} - t_{\text{coil}}}; sensible heat factor =sensiblesensible+latent\displaystyle = \dfrac{\text{sensible}}{\text{sensible} + \text{latent}} Sensible heating keeps ω\omega constant

Worked example. With h1=400h_1 = 400, h2=430h_2 = 430 and h3=h4=250h_3 = h_4 = 250 kJ/kg, the refrigerating effect is 150 kJ/kg and the work 30 kJ/kg, so COP=5\text{COP} = 5 and COPHP=6\text{COP}_{HP} = 6. Moist air at 30 ∘^\circC with pv=3p_v = 3 kPa at 101.325 kPa has ω=0.622×3/98.325=0.0190\omega = 0.622 \times 3/98.325 = 0.0190 kg/kg and h=30.15+0.0190×2557.4=78.7h = 30.15 + 0.0190 \times 2557.4 = 78.7 kJ/kg dry air.

Trap: The throttle keeps enthalpy constant, not entropy. Put h4=h3h_4 = h_3, and never draw the expansion as a vertical line on the TT-ss diagram.

Turbomachinery, compressors and pumps

Every rotor obeys Euler's equation: the work per kilogram is the change in blade speed times whirl velocity.

Formula Watch out for
Euler: w=U1Vw1−U2Vw2w = U_1 V_{w1} - U_2 V_{w2} (turbine; reversed for a pump) Signs come from the velocity diagrams
Pelton: jet V=Cv2gHV = C_v\sqrt{2gH}; best bucket speed U=V/2U = V/2 Blade speed U=πDN/60U = \pi D N/60
Turbine Ns=NPH5/4\displaystyle N_s = \dfrac{N\sqrt{P}}{H^{5/4}}; pump Ns=NQH3/4\displaystyle N_s = \dfrac{N\sqrt{Q}}{H^{3/4}} Pelton low, Kaplan high specific speed
Two-stage compressor, perfect intercooling: p2=p1p3p_2 = \sqrt{p_1 p_3}; volumetric efficiency 1+C−C(p2/p1)1/n1 + C - C(p_2/p_1)^{1/n} Isothermal work is the least
Affinity laws: Q∝ND3Q \propto ND^3, H∝N2D2H \propto N^2 D^2, P∝N3D5P \propto N^3 D^5 New in 2027: pumps
Operating point: pump curve meets H=Hstatic+kQ2H = H_{\text{static}} + kQ^2; series adds heads, parallel adds flows New in 2027: pump characteristics
NPSHa=patm−pvρg−suction lift−losses\displaystyle \text{NPSH}_a = \dfrac{p_{\text{atm}} - p_v}{\rho g} - \text{suction lift} - \text{losses} Cavitation when it falls below the required NPSH

Worked example. A pump speeded up from 1440 to 1800 rpm has N2/N1=1.25N_2/N_1 = 1.25, so flow rises by 1.25, head by 1.252=1.56251.25^2 = 1.5625 and power by 1.253=1.9531.25^3 = 1.953. If a pump curve H=30−300Q2H = 30 - 300Q^2 meets a system curve H=10+200Q2H = 10 + 200Q^2, then 500Q2=20500Q^2 = 20, Q=0.2Q = 0.2 m³/s and H=18H = 18 m. A two-stage compressor from 1 bar to 16 bar intercools best at 1×16=4\sqrt{1 \times 16} = 4 bar.

Remember: Pumps in series add heads at one flow; pumps in parallel add flows at one head.

The mistakes that cost marks under time pressure

Check these four before you type an answer.

  1. Units: kJ/kg times kg/s is kW; rpm becomes rad/s through ω=2πN/60\omega = 2\pi N/60.
  2. Temperature: kelvin in every ratio, power or exponential.
  3. Pressure: gauge or absolute; the ideal-gas law and isentropic ratios need absolute.
  4. Efficiency: turbine actual over ideal; compressor and pump ideal over actual.

Numerical-answer questions carry no negative marking, while a wrong MCQ does; the marking scheme, which is common to every GATE paper, sets out both. You cannot carry this sheet into the hall, so read the admit card and exam-day rules and keep the formulas in memory.

More formula sheets: all of GATE ME · Fluid Mechanics · Heat Transfer · Strength of Materials

Quick revision

  1. Closed system Q−W=ΔUQ - W = \Delta U; steady flow adds enthalpy, kinetic and potential terms per kilogram.
  2. Polytropic work is (p1V1−p2V2)/(n−1)(p_1V_1 - p_2V_2)/(n - 1); isothermal work uses a logarithm of the volume ratio.
  3. Carnot, COP and isentropic relations all take kelvin and absolute pressure.
  4. Rankine heat added runs from h4h_4, after the pump; specific steam consumption is 3600/wnet3600/w_{\text{net}}.
  5. At equal compression ratio, Otto beats dual beats Diesel; at equal peak pressure the order reverses.
  6. The equivalence ratio is (A/F)stoich/(A/F)actual(A/F)_{\text{stoich}}/(A/F)_{\text{actual}}; below 1 means lean.
  7. In refrigeration h4=h3h_4 = h_3 across the throttle, and COPHP=COPR+1\text{COP}_{HP} = \text{COP}_R + 1.
  8. Pump affinity laws scale flow with NN, head with N2N^2 and power with N3N^3 at a fixed diameter.

Frequently asked questions

Which thermodynamics topics are new in the GATE ME 2027 syllabus?

The Applications paragraph adds Basics of Combustion (air-fuel ratio and equivalence ratio) and ends the turbomachinery line with pumps and pump characteristics. The Thermodynamics paragraph now names energy changes, entropy changes and the analysis of closed and open systems. Nothing was removed. Confirm the official syllabus at gate2027.iitm.ac.in before you plan.

What is the equivalence ratio in combustion?

The equivalence ratio is the actual fuel-air ratio divided by the stoichiometric one, ϕ=(A/F)stoich/(A/F)actual\phi = (A/F)_{\text{stoich}} / (A/F)_{\text{actual}}. A value below 1 is a lean mixture and above 1 a rich one. Excess air is (1/ϕ−1)×100(1/\phi - 1) \times 100 per cent, so ϕ=0.8\phi = 0.8 means 25 per cent excess air.

Why must temperatures be in kelvin in thermodynamics formulas?

Any ratio, power or exponential of temperature needs absolute temperature: the Carnot efficiency, the coefficients of performance, the isentropic relations and the ideal-gas law. Degrees Celsius are safe only inside a difference, such as the change in enthalpy of an ideal gas. Using Celsius in a ratio gives a confident but wrong answer.

How do I find the operating point of a pump?

The operating point is where the pump curve meets the system curve H=Hstatic+kQ2H = H_{\text{static}} + kQ^2. Set the two heads equal and solve for the flow. Pumps in series add heads at one flow, and pumps in parallel add flows at one head. Efficiency is highest at the best-efficiency point.

Is the isentropic efficiency of a compressor actual over ideal work?

No. For a turbine, isentropic efficiency is actual work over isentropic work, because the real machine gives out less. For a compressor or a pump it is isentropic work over actual work, because the real machine needs more. Inverting either one still gives a plausible-looking number, which is why it is a common way to lose marks.

Sources

Dates, fees and the syllabus are set by the GATE 2027 organising institute and can change. Always confirm at gate2027.iitm.ac.in.

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