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thermodynamics question papers
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VAAL UNIVERSITY OF TECHNOLOGY EMTGA3 2008 NOVEMBER (MAIN)
1 kg of air at 100 kPa and 600 K expands according to the law PV^16 = C. The final volume is three times larger than the initial volume.
Draw a P-V and T-S diagram and calculate the work, heat flow and entropy change. [13]
In a Joule cycle the pressure ratio is 10 and the upper and lower temperature limits are 773 K and 283 K respectively.
A single stage compressor has a F.A.D of 5m^3 /min at 15°C and 101.3 kPa. The inlet conditions are 95 kPa and 20°C. The delivery pressure is 500 kPa. The compression index is 1.25 and the clearance volume is 2% of the swept volume. The compressor runs at 1450 rev/min and the stroke is twice the piston diameter.
Calculate: 1 The mass flow of air. (1) 2 The volumetric efficiency. (5) 3 The piston diameter. (5) 4 The power requirement of the compressor. (2) 5 The heat rejected from the cylinder. (2) 6 The isothermal efficiency. (2) 7 Draw a correctly labeled P-V diagram. (2) [19]
An eight cylinder 4-stroke engine has a bore of 229 mm and a stroke of 304 mm. The compression ratio is 14/1. The engine develops 500 kW at 750 rev/min. The mechanical efficiency is 90% and the volumetric efficiency is 78%. Fuel with a C.V. of 42 MJ/kg is supplied at an air/fuel ratio of 16/1. The ambient conditions are 100 kPa and 288 K. The IMEP for the pumping loop is 34.5 kPa. The exhaust gas temperature is 450°C and cp for exhaust gasses is 1.135 kJ/kg.K.
Calculate: 1 The brake thermal efficiency. (9) 2 The heat rejected from the engine. (4) 3 The IMEP for the power loop. (4) 4 The efficiency ratio if the cycle is based on the Otto cycle. (2) 5 Draw the P-V diagram for the Otto cycle. (1) [20]
A refrigeration plant is required to cool a cold room at -10°C with a cooling load of lOOMJ/h. The refrigerant to be used is Freon 12 (R 12). The refrigerant enters the compressor dry saturated. The temperature of the condensate is 5°C and it is 5°C undercooled. The heat rejected by the condenser is absorbed by water. The temperature rise of the water is 10°C. Assume isentropic compression
THERMODYNAMICS
General formulae
m [ Z,g + Vt C,^2 + h, ] +Q + W = m [ Zjg + 14 C 22 + h 2 ] h = u + pv m = CA/v
U = Uf+X-Ufg S = Sf+Z.Sfg Sfg = Sg - Sf V = Vf + (^) XVfg
Y = Cv=R/(A.-l) R = cp - cv R = Ro/mo pV = mRT m = n.nio
= 8.3145 kJ.kmol'.K -1^ _v-_
Expansion law V=C PV=C PVn=C P=C
pi/r,=p2^r 2 P.V,=p 2 V 2 P,/p2=[V 2 /V,]n
T,A' 2 =[V 2 A^l]n-^1 T,/r 2 =Pl/jp 2 *^1
Process Isochoric Isobaric
Isothermal
Isentropic Polytropic
Law V=C p=C pV=C pVY=C pVn=C
w —
cv.ln (T 2 /T,) cp.ln (T 2 /T,) Q/T = R.ln(V 2 /Vi) 0 R.ln (V 2 A^,)+ c.ln (T 2 /T,)
-Glnfa/pj) -CrVj^-V^/Cy-l) (P2VrPiV,)/(n-l)
W[(n-y)/(y-l)l
Process Isochoric Isobaric
Isothermal Isentropic
Polytropic
Other
Law V=C p=C T=C AS=Q= pVn=C pV=C None
Tables Tables Tables Tables Tables
Tables
Tables Tables Q/T 0 Tables
Tables
(P2V 2 - PlV,)/(n-l) -pV.ln(p,/p 2 ) AU-Q
"Boiler = msxAh / mfxC.V. ^lpiant = msxAh^rt, / mfxC.V.
E.E. = ms/mf
C. O. P R E F - T , / ( T 2 - T , )