Refrigerant-134a at 1 MPa and 90°C is to be cooled to 1 MPa and 30°C in a condenser by air. The air enters at 100 kPa and 27°C with a volum flow rate of 600 mmin and leaves at 95 kPa and 60°C. Determine the mass flow rate of the refrigerant.
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Q: Refrigerant-134a at 1 MPa and 90 degrees * C is to be cooled to 1 MPa and 30 degrees * C in a…
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Q: Air at 200 kPa and 950 K enters an adiabatic nozzle at low velocity and is discharged at a pressure…
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- Condensers in these refrigerators are all_______cooled.The condensing pressure is 260 psig and the condenser outlet temperature is 108F for R-22. By how many degrees is the liquid subcooled in the condenser? A. 12F B. 42F C. 7F D. 14FWhy is two-stage compression popular for extra-low-temperature refrigeration systems?
- A 1200 kW water-cooled chiller has a centrifugal compressor with refrigerant R134a as the working fluid. The compressor runs at 9600 rev/min and has a slip factor of 0.95 and an overall isentropic efficiency of 90%. The impeller tip speed is not to exceed 160m/s. The evaporating and condensing temperatures are 2°C and 40°C respectively. Assuming that there is no superheating and sub-cooling, a) sketch the refrigration cycle on a P-h diagram (please indicate the pressures and specific enthalpies of all points in the cycle); b) determine the mass flow rate of the refrigerant R134a; c) determine the coefficient of performance of the chilled water plant; and discuss the possible measures to uplift the plant COP d) determine the number of stages and the impeller tip diameters, assuming that all stages would share same work input and each stage compression would have the same impeller tip diameter. e) Please also comment how the slip factor can affect the energy performance of the…An R134a compressor with a bore of 10 cm and stroke of 10 cm runs at 750 rpm . The clearance volume ratio is 0.04 . It runs between the evaporator and condenser temperatures of -6 ° C and 40 ° C respectively . The isentropic index of compression is 1.35 . ( a ) Determine the mass flow rate , refrigeration capacity , and work requirement . Compare the results of the isentropic work with that determined via superheat table .An ideal double-reheat Steam turbine receives 300,000 kg/hr of steam at 10 Mpa and 400°C. After expansion from high pressure turbine shell, it is reheated twice from saturated vapor condition back to its initial temperature. The steam entering the condenser is 97% dry. Determine: a.) Engine work b.) Engine thermal efficiency c.) Steam rate
- An engine with incomplete-expansion is supplied with steam at 2.75 MPa and 260C.Release occurs at 0.35 MPa and the condenser temperature is 42C. (a) If the brake efficiency is 60% and if 1225 kg/h of steam are used, what is the brake power in kW? (b) If the mechanical efficiency is 87%, what is the indicated steam rate? (c) If the engine drives a generator whose efficiency is 92%, what are the combined thermal efficiency and the combined steam rate?a 140x140-mm, twin-cylinder, single acting refrigerant-12 compressor running at 600 rpm carries a refrigeration capacity of 40kW while operating at 350 kPa suction and 1300 kPa discharge pressures, assuming the same load to be carried with the same volumetric efficiency and if the discharge pressure shall be raised to 1400 kPa, a) what is the percent increase in mass of R-12 b.) what will be the new volumetric displacement of the compressor in m3/sec c.) at what speed should the compressor be run?A flashed steam geothermal power plant is located where underground hot water is available as a saturated liquid at 700 kPa. The well-head pressure is 600 kPa. The flashed steam enters the steam turbine at 500 kPa and expands to 15 kPa when it is condensed. The flow rate from the well is 29.6 kg/s. Determine the cycle thermal efficiency of the plant in %. FINAL ANSWER MUST BE IN 3 DECIMAL POINTS
- Steam turbine receives steam at 9.5 MPa, 540°C and the condenser at 0.01 MPa. Steam are extracted at 3 MPa, 1.8 MPa, and 0.6 MPa. Determine the following: Degree superheat at point 2 Quality of steam at point 4 Mass extracted in kg/hr for each feedwater open heater and the remaining mass that enters the condenser assuming 20,000 kg/hr of throttle flow Work net in kW Cycle thermal efficiencySteam enters the turbine of a cogeneration plant at 6 MPa and 550°C. One-third of the steam is extractedfrom the turbine at 1400 kPa pressure for process heating. The remaining steam continues to expand to20 kPa. The extracted steam is then condensed and mixed with feedwater at constant pressure and themixture is pumped to the boiler pressure of 6 MPa. The mass flow rate of steam through the boiler is 30kg/s. Disregarding any pressure drops and heat losses in the piping, and assuming the turbine and thepump to be isentropic, determine (a) the net power produced, (b) the utilization factor of the plant, (c)the exergy destruction associated with the process heating, and (d) the entropy generation associatedwith the process in the boiler.Assuming a source temperature of 1000 K and a sink temperature of 298 K.Problem 1: The boiler of a power steam cycle operates at 6000 kPa and the condenser at 50 kPa. At the entrance to the turbine, the temperature is 500°C. The isentropic efficiency of the turbine is 90 percent, pressure and pump losses are negligible, and the water leaving the condenser is subcooled by 6.3°C. The boiler is sized for a mass flow rate of 18 kg/s. You are asked to: a. Represent the cycle on P-v and T-s diagrams. b. Compute the rate at which heat is added in the boiler. c. Compute the power required to operate the pumps. d. Determine the net power produced by the cycle. e. Compute the thermal efficiency.