Thermodynamics Exam Cheat Sheet: Problem Solving Recipes
Thermodynamics Exam Cheat Sheet: Problem-Solving Recipes
🔹 Problem 1: Property Changes & T-s Sketch
(HW 9 Q1–Q3)
1a. Ideal-Gas Entropy Change
Statement: Air (ideal gas) in a piston-cylinder goes from State 1: T₁ = 350 K, p₁ = 100 kPa to State 2: T₂ = 550 K, p₂ = 700 kPa. Find Δs (kJ/kg·K) (a) reversible, (b) with irreversibilities.
1b. Isothermal Water Compression
Statement: 1 kg water in a piston-cylinder, initially saturated vapor at T = 160 °C, p = 150 kPa, isothermally compressed to saturated liquid. Work on water W = -471.5 kJ. Find (a) Q (kJ), (b) ΔS (kJ/K). Sketch T-s.
Steps for 1a (Ideal Gas)
Formula:
Compute
Evaluate
Irreversible:
Steps for 1b (Water Compression)
1st Law:
Table Lookup at 160 °C (saturated):
Compute ΔU:
Compute Q:
Compute ΔS:
Sketch T-s:
🔹 Problem 2: Single-Component Device Check
(HW 10 Q1–Q4 & HW 9 Q5–Q10)
Statement: Steady-flow device (turbine or compressor) with inlet (p₁,T₁) and outlet (p₂,T₂_meas). (a) Check feasibility via entropy generation (2nd Law). (b) Use energy balance (1st Law) to find W or Q. (c) Compute isentropic efficiency if asked.
Steps
Sketch control volume with inlet 1 and outlet 2.
2nd Law Check:
Isentropic Efficiency:
1st Law Steady-Flow:
Entropy Balance:
🔹 Problem 3: Carnot Cycle Analysis
(HW 8 – All Q’s)
Statement: Analyze a Carnot cycle (power, refrigerator, or heat pump) between temperatures T_H and T_C:
- Two isothermals (T_H, T_C)
- Two isentropics
Steps
Draw p-v and T-s (or T-v) loops, label states 1→4.
List Processes:
- Isothermal @ T_H (q_in or q_out)
- Adiabatic (isentropic)
- Isothermal @ T_C (q_out or q_in)
- Adiabatic (isentropic)
Compute Each Leg:
- Isothermal: q=TΔs=h_end-h_start
- Adiabatic: w=h_start-h_end with s constant.
Net Work/Heat: w_net=q_in-q_out.
Efficiency/COP:
η=1-(T_C/T_H), COP_ref=T_C/(T_H-T_C), COP_hp=T_H/(T_H-T_C).
🔹 Problem 4: Integrated Multi-Component Cycle
(HW 10 Q5–Q9 & HW 7 Q4–Q5)
Statement: Full Rankine or combined-cycle plant: boiler → turbine(s) → condenser → pump(s) → reheater/heat exchanger. Find net power, η_th, component η’s, cooling-water flow, entropy generation.
Steps
Sketch full plant, label all states.
State Table: p, T, h, s, x.
Turbine/Nozzle:
w_t=h_in-h_out,act, η_t=(h_in-h_out,act)/(h_in-h_out,s)Pump/Compressor:
w_p=h_out,act-h_in, η_p=(h_out,s-h_in)/(h_out,act-h_in)
with w_p,s ≈ v(P_out-P_in).Heat Duties:
q_in=h_boiler,out-h_boiler,in, q_out=h_cond,in-h_cond,outNet Work & Efficiency:
w_net=∑w_t-∑w_p, η_th=w_net/q_inCooling-Water Flow:
ṁ_w=Q_out/(c_p,w(T_w,out-T_w,in))Entropy-Generation:
Ṡ_gen=∑ṁ(s_out-s_in)+∑(Q/T_b)≥0
Use this sheet verbatim. Each problem includes its statement, source, and a numbered recipe—only algebra and table lookups remain. Good luck!
English with a size of 115.47 KB