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22-Mec-A1 Applied Thermodynamics and Heat Transfer · May 2014

Question 2 of 8: Single-Acting Reciprocating Compressor with Clearance

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

Notes on this paper

Paper: National Examinations — 07-Mec-A1 Applied Thermodynamics and Heat Transfer, May 2014. Open-book, 3-hour paper. Part A (Thermodynamics, Q1–Q4) and Part B (Heat Transfer, Q5–Q8); a complete paper is any five questions — three from one part and two from the other, all of equal value. Full worked solutions to all eight questions are given below.

Reference texts: Çengel & Boles, Thermodynamics: An Engineering Approach (9th ed., McGraw-Hill) — closed- and open-system energy balances, steam tables, gas power cycles, reciprocating compressors and vapour-compression refrigeration; Çengel & Ghajar, Heat and Mass Transfer (6th ed.) and Incropera, DeWitt, Bergman & Lavine, Fundamentals of Heat and Mass Transfer (8th ed., Wiley) — composite-wall conduction, internal-flow and cross-flow convection correlations, natural convection with radiation, and the ε–NTU heat-exchanger method. Freon-12 property data are taken from the appendix supplied with the exam; steam and air data from standard tables.

Question 2: Single-Acting Reciprocating Compressor with Clearance (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. Piston displacement (swept volume) $V_s=280\ \text{cm}^3$; clearance ratio $c=0.04$; 600 strokes/min; reversible adiabatic compression, so the polytropic index equals $\gamma=1.4$. Valve pressure losses shift the in-cylinder pressures from the line values.

QuantityValue
Line suction / discharge95 / 480 kPa
Intake / discharge valve loss2.5 / 13.8 kPa
In-cylinder suction $P_1$95 − 2.5 = 92.5 kPa
In-cylinder delivery $P_2$480 + 13.8 = 493.8 kPa
Clearance / speed4 % / 600 strokes·min⁻¹

Find. The volume of air actually inducted and compressed per minute.

volume VP92.5493.8kPa1234compression n=1.4induction (1→ inlet)delivery 2→3
Figure 1 — Indicator (p–V) diagram: 1→2 reversible-adiabatic compression from 92.5 kPa to 493.8 kPa, 2→3 delivery at constant pressure, 3→4 re-expansion of the 4 % clearance gas, 4→1 induction. Valve throttling lowers the suction line and raises the delivery line inside the cylinder.

Approach. The clearance gas re-expands each stroke and reduces the volume drawn in; the clearance volumetric efficiency converts the swept volume into inducted volume, which multiplied by the stroke rate gives the volume compressed per minute.

  1. In-cylinder pressure ratio. Accounting for the valve losses,$$r_p=\frac{P_2}{P_1}=\frac{480+13.8}{95-2.5}=\frac{493.8}{92.5}=5.34.$$
  2. Clearance volumetric efficiency. With re-expansion along the same index $n=\gamma=1.4$,$$\eta_v=1+c-c\,r_p^{1/n}=1+0.04-0.04(5.34)^{1/1.4}=1.04-0.04(3.31)=\boxed{0.908}.$$
  3. Volume inducted per stroke. $$V_1-V_4=\eta_v V_s=0.908(280)=254.2\ \text{cm}^3\ \text{per stroke}.$$
  4. Volume compressed per minute. At 600 strokes/min,$$\dot V=254.2\times600=1.525\times10^{5}\ \text{cm}^3/\text{min}=\boxed{0.1525\ \text{m}^3/\text{min}}\ (152.5\ \text{L/min}).$$
Check
The "volume of air compressed per minute" is taken as the free air actually inducted at the in-cylinder suction state (92.5 kPa, 15 °C). Referred instead to the 95 kPa suction-line pressure it is $0.1525\times(92.5/95)=0.1485\ \text{m}^3/\text{min}$ — a 2.6 % correction. The re-expansion index is set equal to the compression index (reversible adiabatic), as the question states.
QuantityResult
In-cylinder pressure ratio5.34
Volumetric efficiency0.908
Inducted volume per stroke254 cm³
Volume compressed per minute≈ 0.153 m³/min (152.5 L/min)