NivaarExam PrepOfficial exam papers ↗

22-Mec-A1 Applied Thermodynamics and Heat Transfer · Undated paper

Question 1 of 8: Work and internal-energy change of a gas with a P–V equation of state

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Paper format: National Examination 16-Mec-A1 Applied Thermodynamics and Heat Transfer — 3 hours, open book. Two parts: Part A (Thermodynamics, Q1–Q4) and Part B (Heat Transfer, Q5–Q8). The rubric asks for five questions (three from one part, two from the other), each of equal value; all eight are solved.

Reference texts: Çengel & Boles, Thermodynamics: An Engineering Approach (9th ed.); Çengel & Ghajar, Heat and Mass Transfer (6th ed.); Incropera & DeWitt, Fundamentals of Heat and Mass Transfer (8th ed.); Moran & Shapiro, Fundamentals of Engineering Thermodynamics. Property data: saturated ammonia and R-134a tables printed with the paper.

Question 1 — Work and internal-energy change of a gas with a P–V equation of state (Part A, equal value)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given.

QuantitySymbolValue
Equation of state$P(v)$$300v-200v^{2}$ kPa
Internal-energy relation$u$$0.3\,Pv+20$ kJ/kg
Initial specific volume$v_1$0.1 m³/kg
Final specific volume$v_2$0.4 m³/kg

Find. (a) boundary work $w$; (b) internal-energy change $\Delta u$; (c) heat transfer $q$ (per kg).

P–v process (work = area under curve) vP 1 (28 kPa) 2 (88 kPa) v₁=0.1v₂=0.4 w = ∫P dv
Boundary work is the area under the reconstructed $P$–$v$ curve between $v_1$ and $v_2$.

Approach. Integrate the given $P(v)$ for the closed-system boundary work, differentiate the $u$-relation across the end states for $\Delta u$, then close with the first law $q=\Delta u+w$.

  1. Boundary work by integration. For a quasi-static process $w=\int_{v_1}^{v_2}P\,dv$ with $P=300v-200v^2$: $$w=\Big[150\,v^{2}-\tfrac{200}{3}v^{3}\Big]_{0.1}^{0.4}=\big(150(0.16)-66.7(0.064)\big)-\big(150(0.01)-66.7(0.001)\big)$$ $$w=(24.0-4.27)-(1.50-0.067)=\boxed{18.30\ \text{kJ/kg}}$$ The gas expands, so the work is done by the gas (positive).
  2. Internal-energy change from the state relation. With $u=0.3Pv+20$, only the $Pv$ term changes, so $\Delta u=0.3\,(P_2v_2-P_1v_1)$. Evaluate the endpoints from $P(v)$: $P_1=300(0.1)-200(0.1)^2=28$ kPa and $P_2=300(0.4)-200(0.4)^2=88$ kPa. Hence $$\Delta u=0.3\big[(88)(0.4)-(28)(0.1)\big]=0.3\,(35.2-2.8)=\boxed{9.72\ \text{kJ/kg}}$$
  3. Heat transfer (first law, closed system). $$q=\Delta u+w=9.72+18.30=\boxed{28.02\ \text{kJ/kg}}$$ Both energy stores increase, so heat is added to the gas.
QuantityResult
Boundary work $w$18.30 kJ/kg (by the gas)
Internal-energy change $\Delta u$+9.72 kJ/kg
Heat transfer $q$+28.02 kJ/kg (added)
Check — reconstructed coefficients.
The state-equation coefficients are given inconsistently ("0.3", "0.317", "0.2") and the question can be read either as a curve process or as a "constant 100 kPa" process. The self-consistent reconstruction used here, $P=300v-200v^2$ (kPa), reproduces exam-scale numbers ($w\sim18$ kJ/kg, $\Delta u\sim10$ kJ/kg); the method — integrate $P(v)$ for work, differentiate $u(Pv)$ for $\Delta u$, close with the first law — is what the question tests and is unaffected by the exact coefficients.
← Paper overview