Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format: National Examination 07-Mec-A6-1 Fluid Machinery, December 2014 — closed book, three hours, 60 marks. Section A is calculative (Q1–Q5) and Section B is descriptive (Q6–Q8); the rubric asks for four questions of Section A plus two of Section B (six questions, each of equal value, 10 marks). All eight questions are solved in full as a study resource. General constants supplied with the paper: g = 9.81 m/s², patm = 100 kPa, pvapour = 2.34 kPa (20 °C), ρwater = 1000 kg/m³, ρair = 1.21 kg/m³ (15 °C), cp,air = 1.005, cv,air = 0.718 kJ/kg·K.
Reference texts. S. L. Dixon & C. A. Hall, Fluid Mechanics and Thermodynamics of Turbomachinery (7th ed.); R. A. Sabersky, A. J. Acosta, E. G. Hauptmann & E. M. Gates, Fluid Flow: A First Course in Fluid Mechanics (4th ed.) — source of the pump-selection charts Figs 15.11/15.12; H. Cohen, G. F. C. Rogers & H. I. H. Saravanamuttoo, Gas Turbine Theory; R. W. Fox, A. T. McDonald & P. J. Pritchard, Introduction to Fluid Mechanics.
Check: Questions 3 rely on chart reads from the examination attachments (Figs 15.11 & 15.12). Values read from those charts (φe, σc, η) are quoted to the precision the graphs allow and are flagged where used; a candidate would read the same values off the supplied plots. The induction-motor pole count is not stated in Q3, so a standard 4-pole (1800 rev/min synchronous) machine is assumed — the governing method is unaffected.
Approach. Use the isentropic temperature ratio $r_p^{(k-1)/k}$ with the component efficiencies to get the actual compressor-exit and turbine-exit temperatures, then form the net work per unit mass of gas (turbine work degraded by mechanical efficiency, less compressor work) and divide the fuel flow by the net work for the specific fuel consumption.
Compressor exit (points 1→2). The isentropic ratio is $r_p^{(k-1)/k}=12^{0.2857}=2.034$, so $T_{2s}=T_1\,r_p^{(k-1)/k}=288(2.034)=585.8\ \text{K}$. The compressor efficiency gives the actual exit temperature,$$T_2=T_1+\frac{T_{2s}-T_1}{\eta_c}=288+\frac{585.8-288}{0.86}=634\ \text{K}.$$
Turbine exit (points 3→4). The isentropic exhaust temperature is $T_{4s}=T_3/r_p^{(k-1)/k}=1350/2.034=663.7\ \text{K}$, and the turbine efficiency gives$$T_4=T_3-\eta_t(T_3-T_{4s})=1350-0.89(1350-663.7)=739\ \text{K}.$$$$\boxed{T_1=288,\;T_2=634,\;T_3=1350,\;T_4=739\ \text{K}}$$
Specific work per kg of gas. Take a basis of 1 kg of gas leaving the turbine. With an air/fuel ratio of 50 the gas is 50/51 kg air + 1/51 kg fuel, so the compressor (which handles only air) does $w_c=\tfrac{50}{51}c_p(T_2-T_1)=0.9804(1.005)(634-288)=341\ \text{kJ}$, while the turbine expands the full gas stream, $w_t=c_p(T_3-T_4)=1.005(1350-739)=614\ \text{kJ}$. The net work at the coupling (mechanical losses on the turbine output) is$$w_{net}=\eta_m w_t-w_c=0.98(614)-341=260\ \text{kJ per kg gas}.$$$$\boxed{w_{net}=260\ \text{kW}\!\cdot\!\text{s/kg}}$$
Specific fuel consumption. Per kg of gas the fuel burned is 1/51 = 0.01961 kg. Converting the net work to a kWh basis ($1\ \text{kWh}=3600\ \text{kJ}$),$$\text{SFC}=\frac{m_{fuel}}{w_{net}}\times3600=\frac{0.01961}{260}\times3600=0.271\ \text{kg/kWh}.$$$$\boxed{\text{SFC}=0.271\ \text{kg/kWh}}$$
Check: Only air property data (cp = 1.005 kJ/kg·K, k = 1.4) are supplied, so a cold-air-standard analysis is used throughout with the fuel mass accounted for via the air/fuel ratio. Using hotter combustion-gas properties (cp ≈ 1.15) would raise the turbine work modestly; the method is unchanged.