Complete the Table shown below to include R134a. Based on the data in what refrigerant can R134a be a substitute? Explain your answer.
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Complete the Table shown below to include R134a. Based on the data in what
refrigerant can R134a be a substitute? Explain your answer.
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- Steam is to be condensed by direct injection of cold water. The steam enters the condenser at the rate of (450 kg/hr) with dryness fraction of (0.9) and pressure (1 bar). The estimated heat losses from the condenser to the surroundings is (8500 kJ/hr). If cold water enters at (15"C) and the mixture of condensate and cooling water is to leave at (95"C). Determine the required flow of cooling water.Steam with an enthalpy of 2168 kJ/kg enters a condenser at a rate of 10,000 kg/h. If the steam leaves the condenser with an enthalpy of 251 kJ/kg, determine the heat rejection rate. Provide complete solution, with diagramAn Ammonia vapor compression refrigerator has aneffective swept volume of 0.308 m3/min. The condensationand evaporation takes place at 28.9°C and -12.2°C,respectively. There is no undercooling and the gastemperature after compression is 48.9°C. Determine thefollowing.(a) Dryness fraction of vapor entering the compressor(b) Rate of circulation of ammonia in kg/min(c) Rate of extraction of heat in kJ/min(d) Heat rejected in condenser per minute(e) Actual and Theoretical COP
- A single-effect evaporator is being used to concentrate10,000 kg/h of tomato juice from 5% total solids to 30% totalsolids. The juice enters the evaporator at 15°C. The evaporatoris operated with steam (80% quality) at 143.27 kPa. Thevacuum inside the evaporator allows the juice to boil at 75°C.Calculate (a) the steam requirements and (b) steam economyfor the process. Assume the condensate is discharged at 75°C.The specifi c heat of the liquid feed is 4.1 kJ/(kg°C) and theconcentrated product is 3.1 kJ/(kg°C). Make it in the form of an example solution spreadsheet .....A water tube boiler produces 250,000 pounds of steam per hour at 1200 psia and1000OF from feed water entering the boiler at 1500 psia and 360oF. Fuel oil havinga higher heating value of 18,200 Btu/lb is supplied to the burners at the rate of20,700 lb/hr. Furnace volume is 1500 cubic feet. Calculate the equivalentevaporation, lb/hrA. 300,117 B. 300,317 C. 300,517 D. 300,717What are the economical & opetational advantages of different types(water tube boiler & fire tube) of boiler??which one is preferable for a supramax vessel based on economical & operational advantage????
- Design a hydrocooling unit that can cool fruits and vegetables from 30°C to 5°C at a rate of 20,000 kg/h under the following conditions: The unit will be of flood type that will cool the products as they are conveyed into the channel filled with water. The products will be dropped into the channel filled with water at one end and picked up at the other end. The channel can be as wide as 3 m and as high as 90 cm. The water is to be circulated and cooled by the evaporator section of a refrigeration system. The refrigerant temperature inside the coils is to be -2°C, and the water temperature is not to drop below 1°C and not to exceed 6°C. Assuming reasonable values for the average product density, specific heat, and porosity (the fraction of air volume in a box), recommend reasonable values for the quantities related to the thermal aspects of the hydrocooler, including (a) how long the fruits and vegetables need to remain in the channel, (b) the length of the channel, (c) the water…What are the design parameters for the various equipment and components (includes the table of specification) used in the refrigeration and cryogenic plant for liquid oxygen production? What are the considerations? What are the design assumptions?A two-stage ammonia food-freezing plant – with a desired capacity of 528,000 kJ/h at -40℃ evaporating temperature and 35C condensing temperature – has a flash intercooling system with a liquid sub cooler. The vapour leaving the evaporator is at -30℃ and entering the first stage compressor is at -15℃. The vapour leaving the flash chamber is superheated by 10℃ in the suction line to the second stage compressor. Water intercooling is done to cool the vapour to 45℃. Adiabatic efficiencies of both compressors are 0.65 and 0.77 respectively. Find the piston displacements, discharge temperatures and power requirements of the two compressors.
- How does the latent heat of water vary with the working pressure? ExplainHow to do a heat/energy balance on a anode fuel cell and a condenser given that the fuel cell is isothermal and the outlet of the condenser is 25 degrees?5. Air at 30 ° C and 50% RH is heated using a heat exchanger to reach 80 ° C. Using a psychrometric chart, determine a. The amount of heat added per 1 m³ of initial air = Answer (kJ). b. Condensation temperature = Answer (° C)