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HW12s Michigan State University ME 201
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  • Title: HW12s
  • Type: Notes
  • School: Michigan State University
  • Course: ME 201
  • Term: Spring

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2006 Spring Thermodynamics Homework #12 Solution 1. A 2 ft3 scuba diver's air tank is to be filled with air from a compressed air line at 120 psia, 100 F. Initially, the air in the tanks is at 20 psia and 70 F. Assuming that the tank is well insulated, determine the temperature and mass in the tanks when it is filled to 120 psia. Solution: System Type: Transient Working Fluid: Air (ideal gas) Process: Constant total volume, adiabatic State 2 (final) State 3 (inlet) State 1 (initial) T2 = 724 R T1 = 70 F = 530 R T3 = 100 F = 560 R P1 = 20 psia P2 = 120 psia P3 = 120 psia u1 = 90.33 Btu/lbm u2 = 123.95 Btu/lbm h3 = 133.86 Btu/lbm m1 = 0.20377 lbm m2 = 0.895 lbm m3 = 0.689 lbm Italicized values are from air table. Bold values are calculated. Initial State: Fixed Inlet State: Fixed Final State: UNKNOWN Q =0 Wsh = 0 Wbnd = 0 KE and PE are negligible 1st Law: m2u2 - m1u1 = m3h3 mass: m2 - m1 = m3 Approach: To fix the final state we will have to simultaneously solve the 1st law, conservation mass and ideal gas law. First we go to the air tables and find u1 = 90.33 Btu/lbm and h3 = 133.86 Btu/lbm Next we use the ideal gas law to calculate the initial mass or PV (20)(2) m1 = 1 1 = = 0.2038 lb m RT1 (10.73 / 28.97)(530) ME 201 1 ME 201 Thermodynamics Spring 2006 We begin by taking the 1st law and eliminating m3 with the use of the conservation of mass equation or m2 u 2 - m1u1 = (m 2 - m1 )h 3 Rearranging m u + (m 2 - m1 )h 3 u2 = 1 1 m2 Next we use our ideal gas law to eliminate m2 P V m2 = 2 2 RT2 Through the air tables we have a relationship between T2 and u2, but we don't have an equation to substitute with. Hence, we will have to solve this problem by iteration (also known as trial and error). The way an iterative solution works is that an initial guess is made for one of the unknowns. The other unknown is determined based on this guess and then the original unknown is calculated. This calculated value is compared with the guess and if the comparison is poor the process is repeated. For a well posed problem the unknowns will eventually not change. Specifically for our problem we will follow the following steps 1. Guess T2 P2 V2 RT2 m u + (m 2 - m1 )h 3 3. Calculate u2 with u 2 = 1 1 m2 4. Obtain T2 using the air tables and u2 5. Compare the just calculated T2 with the one used to evaluate m2. If the difference is greater than 1 R, re-guess T2 return to step 2 and repeat steps 2-4. 2. Calculate m2 with m2 = Now carrying out our calculations: Loop 1 Guess T2 = 100 F = 560 R PV (120)(2) Calculating m 2 = 2 2 = = 1.157 lb m RT2 (10.73/28.97)(560) m u + (m 2 - m1 )h 3 (0.2038)(90.33) + (1.157 - 0.2038)(133.86) u2 = 1 1 = m2 1.157 Calculating = 126.19 Btu/lbm Going to the air tables, T2 = 738 R Since the difference between the two T2's is greater than 1 R we need to re-guess T2. 2 ME 201 Thermodynamics Spring 2006 Loop 2 Guess T2 = 738 R Calculating m2 = 0.878 lbm Calculating u2 = 123.76 Btu/lbm Going to the air tables, T2 = 724 R Since the difference between the two T2's is greater than 1 R we need to re-guess T2. Loop 3 Guess T2 = 724 R Calculating m2 = 0.895 lbm Calculating u2 = 123.95 Btu/lbm Going to the air tables, = T2 725 R Since the difference between the two T2's is less than 1 R we are finished 2. Consider a rigid tank of volume 2 m3 containing saturated liquid refrigerant-134a at 20 C. The tank is connected to an ideal turbine and as the refrigerant leaves the tanks it flashes to saturated vapor. If the tank is maintained at 20 C and the turbine exit pressure is 100 kPa, how much work will be produced when two thirds of the initial mass has been used? Solution: We first recognize that we will have four states to worry about in this problem: State 1: Initial State of Tank State 2: Outlet State of Tank and Inlet to Turbine State 3: Outlet State of Turbine State 4: Final State of Tank System Type: Transient Working Fluid: R-134a (compressible) Process: Constant total volume, turbine is isentropic State 2 P2 = 572.07 kPa T2 = 20 C s2 = 0.9223 kJ/(kgK) h2 = 261.49 kJ/kg m2 = 1634 kg phase: sat.vap. State 3 P3 = 100 kPa T3 = -26.37 C s3 = 0.9223 kJ/(kgK) h3 = 227.16 kJ/kg m3 = 1634 kg phase: two phase with x3 = 0.966 State 1 P1 = 572.07 kPa T1 = 20 C V1 = 2 m3 u1 = 76.86 kJ/kg m1 = 2451 kg phase: sat.liq. Italicized values are obtained from R-134a tables. Bold values are calculated. State 4 P4 = 572.07 kPa T4 = 20 C V4 = 2 m3 u4 = 86.39 kJ/kg m4 = 817 kg phase: two phase with x4 = 0.0464 3 ME 201 Thermodynamics Spring 2006 State 1: Fixed State 2: Fixed State 3: UNKNOWN State 4: UNKNOWN Q = UNKNOWN Wbnd = 0 KE and PE are negligible 1st Law (tank): m4u4 - m1u1 = -m2h2 + Q mass (tank): m4 - m1 = m2 1st Law (turbine): Wsh = m2(h2-h3) At state 1 the state is fixed. Going to the R-134a tables we have u1 = 78.86 kJ/kg and v1 = 0.0008161 m3/kg and P1 = 572.07 kPa We can then calculate the mass with V 2 m1 = 1 = = 2451 kg v1 0.0008161 At state 2 we have a fixed state so that going to the R-134a tables we have h2 = 261.59 kJ/kg and s2 = 0.92234 kJ/(kgK) and P2 = 572.07 kPa and we are told that the process continues until 2/3 of the mass has been removed, then m2 = (2/3)m1 = (2/3)(2451) = 1634 kg At state 3 we know the pressure and since the turbine is isentropic s3 = s2 = 0.92234 kJ/(kgK) Going to the saturation pressure table at 100 kPa we have sf = 0.07188 kJ/(kgK) and sg = 0.95183 kJ/(kgK) Since s3 lies between these two values, we have a two phase mixture with quality s -s 0.92234 - 0.07188 x3 = 3 f = = 0.966 s g - s f 0.95183 - 0.07188 The enthalpy is then h3 = hf + x3hfg = 17.28 + (0.966)(217.16) = 227.16 kJ/kg with a temperature of -26.37 C. By conservation of mass we have m3 = m2 = 1635 kg Then the work output of the turbine is given by Wsh = m2(h2-h3) = (1635)(261.59-227.16) = 56,293 kJ To fix state 4, we note that using the conservation of mass m4 = m1-m2 = 2451-1634 = 817 kg Then V2 2 v2 = = = 0.002448 m 3 / kg m2 817 4 ME 201 Thermodynamics Spring 2006 which fixes our state 4. We see that we have a two phase mixture with quality v -v 0.002448 - 0.0008161 x4 = 4 f = = 0.0464 v g - v f 0.035969 - 0.0008161 The internal energy is then u4 = uf + x4ufg = 78.86 + (0.0464)(162.16) = 86.39 kJ/kg The heat transfer to the tank is then Q = m4u4 - m1u1 + m2h2 = (817)(86.39)-(2451)(76.86) + (1634)(261.59) = 309,635 kJ 5

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Path: Michigan State University >> ME >> 201 Spring, 2006

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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
Description: Spring 2006 Thermodynamics Homework #12 Due Wednesday, 3/15/06 1. A 2 ft3 scuba diver\'s air tank is to be filled with air from a compressed air line at 120 psia, 100F. Initially, the air in the tanks is at 20 psia and 70F. Assuming that the tank is ...
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> ME >> 201 Spring, 2006
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Path: Michigan State University >> CSE >> 860 Spring, 2004
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Path: Michigan State University >> PHY >> 410 Spring, 2007
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Path: Michigan State University >> PHY >> 102 Spring, 2006
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Path: Michigan State University >> PHY >> 102 Spring, 2006
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Path: Michigan State University >> PHY >> 410 Spring, 2007
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Path: Michigan State University >> PHY >> 410 Spring, 2007
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Path: Michigan State University >> PHY >> 410 Spring, 2007
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Path: Michigan State University >> PHY >> 410 Spring, 2007
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Path: Michigan State University >> PHY >> 410 Spring, 2007
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Path: Michigan State University >> PHY >> 410 Spring, 2007
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Path: Michigan State University >> PHY >> 321 Spring, 2006
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Path: Michigan State University >> PHY >> 321 Spring, 2006
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Path: Michigan State University >> PHY >> 321 Spring, 2006
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Path: Michigan State University >> PHY >> 321 Spring, 2006
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Path: Michigan State University >> PHY >> 410 Spring, 2007
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Physics 410 Homework 12
Path: Michigan State University >> PHY >> 410 Spring, 2007
Description: Physics 410 Homework 12: 1. 2. 3. 4. 5. (6 pts) (6 pts) (12 pts) (7 pts) (14 pts) Problem 7.2 Problem 7.6 Problem 7.8 Problem 7.16 Problem 7.23 from Schroeder. from Schroeder. from Schroeder. from Schroeder. from Schroeder. ...
Physics 410 Homework 2
Path: Michigan State University >> PHY >> 410 Spring, 2007
Description: Physics 410 Homework 2: 1. 2. 3. 4. 5. 6. 7. Problem 1.36 from Schroeder. Problem 1.40 from Schroeder. Problem 1.41 from Schroeder. Problem 1.44 from Schroeder. Problem 1.50from Schroeder. Problem 1.60 from Schroeder. Problem 1.63 from Schroeder. ...
Physics 410 Homework 4
Path: Michigan State University >> PHY >> 410 Spring, 2007
Description: Physics 410 Homework 4: 1. 2. 3. 4. 5. 6. (7 pts) Problem 2.30 from Schroeder. (4 pts) Problem 2.31 from Schroeder. (4 pts) Problem 2.32 from Schroeder. (4 pts) Problem 2.34 from Schroeder. (4 pts) Problem 2.37 from Schroeder. (6 pts) Problem 2.39 fr...
Physics 410 Homework 1
Path: Michigan State University >> PHY >> 410 Spring, 2007
Description: Physics 410 Homework 1: 1. 2. 3. 4. 5. 6. 7. Problem 1.8 from Schroeder. Problem 1.16 from Schroeder. Problem 1.21 from Schroeder. Problem 1.22 from Schroeder. Problem 1.25 from Schroeder. Problem 1.26 from Schroeder. Problem 1.33 from Schroeder. ...
Physics 410 Homework 3
Path: Michigan State University >> PHY >> 410 Spring, 2007
Description: Physics 410 Homework 3: 1. 2. 3. 4. 5. 6. 7. Problem 2.2 from Schroeder. Problem 2.6 from Schroeder. Problem 2.13 from Schroeder. Problem 2.17 from Schroeder. Problem 2.19 from Schroeder. Problem 2.23 from Schroeder. Problem 2.27 from Schroeder. ...
worksheet02
Path: Michigan State University >> PHY >> 102 Spring, 2006
Description: Worksheet #2 - PHY102 (Spr. 2006) Formats and List operations (Vectors) Formating From the toolbar do the following: \"format\" followed by \"style\", the dropdown menu offers you lots of options. \"input\" is the default, and is the \"format\" in which you ...

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