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PROBLEM 3.130

PROBLEM 3.117

3 o 2 As shown in Fig. P3.117, 20 ft of air at T1 = 600 R, 100 lbf/in. undergoes a polytropic expansion to a final of 51.4 lbf/in.2 The process follows pV1.2 = constant. The is W = 194.34 Btu. Assuming behavior for the air, and neglecting kinetic and potential effects, determine (a) the mass of air, in lb, and the final , in oR. (b) the transfer, in Btu.

KNOWN: Air undergoes a polytropic process in a piston-cylinder assembly. The work is known.

FIND: Determine the mass of air, the final temperature, and the heat transfer.

SCHEMATIC AND GIVEN DATA:

o T1 = 600 R Q 2 p1 = 100 lbf/in. 3 V1 = 20 ft Air 2 P2 = 51.4 lbf/in. W = 194.34 Btu 1.2 pV = constant pv1.2 = constant p 1 100 . T1 ENGINEERING MODEL: 1. The air is a closed system. 2. change is the only work mode. 3. The process is 1.2 2 polytropic, with pV = constant and W = 194.34 Btu. 51.4 . T2 4. Kinetic and effects can be neglected.

ANALYSIS: (a) The mass is determined using the ideal gas . v

m = = = 9.00 lb

1.2 To get the final temperature, we use the polytropic process, pV = constant, to evaluate V2 as follows.

3 3 V2 = = (20 ft ) = 34.83 ft

Now

PROBLEM 3.117 (CONTINUED)

o T2 = = = 537 R

Alternative solution for T2

The work for the polytropic process can be evaluated using W = . For the process pV1.2 = constant, and incorporating the ideal gas equation of state, we get

W = =

Solving for T2 and inserting values

o o T2 = + T1 = + (600 R) = 537 R

(b) Applying the energy balance; ΔKE + ΔPE + ΔU = Q – W. With ΔU = m(u2 – u1), we get

Q = m(u2 – u1) + W

From Table A-22E: u(600oR) = 102.34 Btu/lb and u(537oR) = 91.53 Btu/lb. Thus,

Q = (9.00 lb)(91.53 – 102.34)Btu/lb + (194.34 Btu) = 97.05 Btu (in)

PROBLEM 3.33

Two kg of Refrigerant 134A undergoes a polytropic process in a piston-cylinder assembly from an initial state of saturated vapor at 2 bar to a final state of 12 bar, 80oC. Determine the work for the process, in kJ.

KNOWN: Refrigerant 134A undergoes a polytropic process in a piston-cylinder assembly.

FIND: Determine the work.

SCHEMATIC AND GIVEN DATA:

p

R-134A 2 m = 2 kg . 12 bar 80oC pvn = constant

. 2 bar ENGINEERING MODEL: 1. The refrigerant is a 1 closed system. 2. The process is polytropic: pvn = constant. v

ANALYSIS: The work for the polytropic process is determined using Eq. 2.17, with pvn = constant. Following the procedure of part (a) of Ex. 2.1

W = (*)

In order to evaluate this expression, we need to determine the specific and the polytropic exponent, n.

3 State 1: From Table A-11; v1 = vg1 = 0.0993 m /kg o 3 State 2: From Table A-12, at 12 bar, 80 C; v2 = 0.02051 m /kg

The polytropic exponent is found from pvn = constant as follows.

→ → n = ln(p1/p2) / ln(v2/v1)

n = ln(2/12) / ln(0.02051/0.0993) = 1.136

Inserting values in Eq. (*) and converting units, we get

PROBLEM 3.33 (CONTINUED)

W = = -69.88 kJ (in)