B MWR 150 p AIR DRYER E H 10 SOLENOIDS MWP100 AIR DRYER -FIGURE 60- D
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- I posted this question and was told it was too complex to answer. I would like to know why. I would figure that a question meant for a college student could be answered by experts with "Masters and PhDs." Is there a table or chart I need to provide for the refrigerant, R-134A? I just need some help, hahaTopic: HEAT ENGINES, HEAT PUMPS & THERMAL EFFICIENCY The energy transferred by heat from an engine during one cycle is 500 J. Howmuch energy must be added to the engine so that it can operate at 30%efficiency?I need answers to parts 10, 11, and 12, pertaining to the print provided.
- Please find the highest thermal efficiency possible, while remaining within the boundaries. What is required: -Power produced must be at least 60 Mega Watts -Thermal efficiency must be greater than 36% -Back-work ratio must be smaller than 48% Assume: -air is the working fluid -specific heats vary with temperature (use table A-17) -Compressor inlet is at 1atm and 300k -the combustion process is isobaric and is modeled as a heat exchanger -Turbine exhaust is the same pressure as compressor inlet Compressor specifics: -Max volume flow rate (m^3/h) = 600,000 -Max outlet pressure (atm) = 12 -Isentropic efficiency = 90% Combustion chamber and gas tubine specifics (Note these come as a set) -Max pressure = 16.7 atm -Max temp = 1500 (celcius) -Turbine isentropic efficiency = 92% -Max heat rate = 230MWSTEAM ENGINE PROBLEM. Please solve carefully/ellaborately and include the untis in every step, show diagram and write your solutions clearly and must be readable if your solution is in written form. Your work will be appreaciated much. Thank You.16-4 A refrigerant 22 system has a capacity of 180 kW at an evaporating temperature of -30°°C when the condensing pressure is 1500 kPa. (a) Compute the power requirement for a system with a single compressor. (b)Compute the total power required by the two compressors in the system shown in Fig. 16-17 where there is no intercooling but there is flash-gas removal at600 kPa. Ans. 60.7 kW Condenser 1500 kPa 5 600 kPa 3 Flash-gas compressor Evaporator 180 kW -30°C Figure 16-17 Flash-gas removal system in Prob. 16-4. 2 Evaporator compressor
- An industrial plant has available a 4 cylinder, 76-mm bore by 102-mm stroke, 800 rpm, single-acting compressor for use with Refrigerant 12. Proposed operating conditions for the compressor are 38 degrees * C condensing temperature and 5 degrees * C evaporating temperature. It is estimated that the refrigerant will enter the expansion valve as a saturated liquid, that the vapor will leave the evaporator at a temperature of 7 degrees * C and will enter the compressor at a temperature of 13 degrees * C . Assume a compressor volumetric efficiency of 70%. Assume frictionless flow. Calculate the refrigerating capacity in kW for a system equipped with this compressor.Problem 9-d12.The question is in the images, i am having difficulties getting the correct answer, if you could show each stage of the questions . Thanks
- please anwser task 2Do not give answer in image formet and hand writingPlease answer questions g, h, and i. g.Calculate the heat transferred in the condenser. h.Calculate the diameter of the pipe connecting the turbine to the condenser. Design data for the plant shows the following pipe diameters. i. Calculatecooling water flow rate in GPM (‘gallons per minute’)through the condenser if the temperature of the cooling water increases from 13 C to 24 C in the condenser.