answer The thermodynamic systems shown below operate at steady state. For the specified controlvolume, write the energy balance and mass balance, assuming negligible kinetic andpotential energy effects. The equations must reflect the state points shown in theaccompanying diagram. No partial points will be given to wrong answers, and answers withnotations/subscripts that are not consistent with the state points in the accompanying diagram.Schematic diagramAirP₁ = 1 barT₁ = 300 Km₁=0.6 kg/sCompressor AP₂=3 barI T₂=600 KWCVAT6=30°CP6 PswwwwwwwwwwwSaturated liquid R-134aT3 = 115°Fm₂ = 1.5 lb/sThrottlingvalve4P₁ = 60 lbf/in.²P4= 9 bar--T880-K4Compressor BHeat exchangerT₂=328 RP3= P₂T₂=450 KWaterT₁= 20°CPs= 1 barAirT₁=535°RCp=0.240 Btu/lb-ºRFanwwwwWVBWey=-0.2 hpSaturated vaporPs= P4Heat exchangerControl Volume1. Air line only (from state 1 tostate 4- enclosed in red box)2. The whole heat exchanger(enclosed in green box)3. The whole heat exchanger4. The refrigerant line (R-134a)from state 3 to state 5. Notethat no mixing occurs in theheat exchanger5. Fan and whole heat exchanger(enclosed in red box)

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The thermodynamic systems shown below operate at steady state. For the specified contro volume, write the energy balance and mass balance, assuming negligible kinetic an potential energy effects. The equations must reflect the state points shown in the accompanying diagram. No partial points will be given to wrong answers, and answers with notations/subscripts that are not consistent with the state points in the accompanying diagram. Schematic diagram Air P₁ = 1 bar T₁ = 300 K m₁=0.6 kg/s Compressor A P₂=3 bar T₂=600 K T6=30°C P6 Ps wwwwww wwwww Saturated liquid R-134a T3 = 115°F m3 = 1.5 lb/s Throttling valve 4 P₁ = 60 lbf/in.² P4= 9 bar --7--800-K Compressor B Heat exchanger 7₂=328 K P3 P₂ T₁=450 K Water T₁= 20°C Ps= 1 bar Air T₁=535°R Cp=0 0.240 Btu/lb. R Fan wwwwwww WVB Wey=-0.2 hp Saturated vapor Ps= P4 Heat exchanger Control Volume 1. Air line only (from state 1 to state 4- enclosed in red box) 2. The whole heat exchanger (enclosed in green box) 3. The whole heat exchanger 4. The refrigerant line (R-134a) from state 3 to state 5. Note that no mixing occurs in the heat exchanger 5. Fan and whole heat exchanger (enclosed in red box)

The thermodynamic systems shown below operate at steady state. For the specified contro volume, write the energy balance and mass balance, assuming negligible kinetic an potential energy effects. The equations must reflect the state points shown in the accompanying diagram. No partial points will be given to wrong answers, and answers with notations/subscripts that are not consistent with the state points in the accompanying diagram. Schematic diagram Air P₁ = 1 bar T₁ = 300 K m₁=0.6 kg/s Compressor A P₂=3 bar T₂=600 K T6=30°C P6 Ps wwwwww wwwww Saturated liquid R-134a T3 = 115°F m3 = 1.5 lb/s Throttling valve 4 P₁ = 60 lbf/in.² P4= 9 bar --7--800-K Compressor B Heat exchanger 7₂=328 K P3 P₂ T₁=450 K Water T₁= 20°C Ps= 1 bar Air T₁=535°R Cp=0 0.240 Btu/lb. R Fan wwwwwww WVB Wey=-0.2 hp Saturated vapor Ps= P4 Heat exchanger Control Volume 1. Air line only (from state 1 to state 4- enclosed in red box) 2. The whole heat exchanger (enclosed in green box) 3. The whole heat exchanger 4. The refrigerant line (R-134a) from state 3 to state 5. Note that no mixing occurs in the heat exchanger 5. Fan and whole heat exchanger (enclosed in red box)

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

Problem 1.1MA

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