Outdoor air is mixed with room return air to reduce the refrigeration load on a cooling coil. (a) For a space condition of 77 F (25 C) db and 68 F (20 C) wb, describe the maximum wet bulb and dry bulb temperatures that will reduce the coil load. (b) Suppose a system is designed to supply 10,300 cfm (5 m3/s) at 64 F (18 C) db and 63 F (17 C) wb to a space maintained at the conditions given in part (a) above. What amount of outdoor air at 68 F (20 C) db and 90 percent relative humidity can be mixed with the return air if the coil SHF is 0.6? (c) What is the apparatus dew point in part (b) above? (d) Compare the coil refrigeration load in part (b) above with the outdoor air to that without outdoor air. Assume sea-level pressure.
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Heating Ventilating and Air Conditioning: Analysis and Design
- An ammonia refrigeration plant operates between a condensing temperature of 40°C and an evaporating temperature of –10°C. The vapour is dry at the end of compression. Only the following property values are given: 8. °C kJ/kg kJ/kg kJ/kg.K 40°C 371.5 1473 1.36 |-10°C 135.4 1433 0.544 The specific heat of NH3 vapour is 2.1897 kJ/kg.K. Calculate the theoretical coefficient of performance of the cycle.arrow_forwardAn engineer has been given the following data on a conditioned room: Sensible heat gain 30 kW Latent heat gain 15 kW Supply air 18°C Outdoor air 35°C DB and 24°C WB Desired room condition 27°C DB and 50% RH For ventilation, 15% is outdoor air, the balance of air requirement being recirculated from room conditioned with some portion being by-passed around the cooling coil. There is no reheater, the desired room state is attained by the by-passing of air. It is found that the apparatus DP temperature of coil is 10°C. Find the: a. tons of refrigeration; and b. mass flow rate of the time by-passed air.arrow_forward20 kg/s of steam enters a condenser at a pressure of 0.08 bar and quality of 0.68 and exits as saturated liquid at the same pressure. What is the mas flow rate of cooling water if the temperature rise of cooling water is 10 oC and its specific heat equals 4.2 kJ/kg.k?arrow_forward
- Problem 5.7 For air-conditioning system operation in cold weather, it is possible to introduce enough outdoor air to eliminate cooling by the air conditioner. This is called an economizer, and the control strategy is to vary the amount of outdoor air entering a plenum so that the outlet state is at the set point. For zone conditions of 75 F and 50 % and a constant circulating air flow rate of 25,000 cfm, determine the outdoor and return air flow rates necessary to maintain a 55 F supply air leaving the plenum. The outdoor air temperature varies between 10 F and 50 F and the relative humidity is always 30 %. Draw some conclusions from your results.arrow_forwardA 72 tons refrigeration system is used to produce chilled water from 20 ° C to 4 ° c. determine the volume flow of waterarrow_forwardThe sensible and latent heat gains to a room are 10 kW and 1 kW, respectively. The occupancy of the room is 12 people and the minimum fresh air allowance is 12 Li/s for each person. The outside summer design state is: 28ᵒC dry-bulb, 19.5 ᵒC wet bulb, 10.65 g/kg dry air. The room state is: 22 ᵒC dry-bulb, 50 percent saturation, 8.366 g/kg dry air, 43.39 kJ/kg dry air. Select a suitable air state, specify the states on and off the cooler coil and calculate the design cooling load. Analyse and check the cooling load. The temperature rise through the extract system is estimated as 0.5 ᵒC. A low velocity supply system is to be adopted and the temperature rise for supply fan power and duct heat gain is estimated 2ᵒ. Minimum fresh air requirement Plot the process on the psychrometric chart Determine the SHR. Contact Factor & Bypass Factor Total Cooling load.arrow_forward
- The sensible and latent heat gains to a room are 10 kW and 1 kW, respectively. The occupancy of the room is 12 people and the minimum fresh air allowance is 12 Li/s for each person. The outside summer design state is: 28ᵒC dry-bulb, 19.5 ᵒC wet bulb, 10.65 g/kg dry air. The room state is: 22 ᵒC dry-bulb, 50 percent saturation, 8.366 g/kg dry air, 43.39 kJ/kg dry air. Select a suitable air state, specify the states on and off the cooler coil and calculate the design cooling load. Analyse and check the cooling load. The temperature rise through the extract system is estimated as 0.5 ᵒC. A low velocity supply system is to be adopted and the temperature rise for supply fan power and duct heat gain is estimated 2ᵒ. Solve for the following: 1. Minimum fresh air requirement2. Plot the process on the psychrometric chart3. Determine the SHR.4. Contact Factor & Bypass Factor5. Total Cooling load.arrow_forwardQ2// A parallel - feed double - effect evaporator with equal vaporized for both, are fed with 5 Kg/s liquor with 10 percent for each effect. The overall heat transfer coefficients are 1.25 and 1.7 KW / m². K respectively. Steam is feed at 1.8630 bar and the second effect operates at 0.2856 bar. If the mass fraction from the 1st effect was 40 percent, What will be the total concentrated liquid from both? And compute the Temperature distribution for the system. Cp=4.18kJ/kg.karrow_forwardFind the mass of water, in kg, that can be cooled from 24 0C to -80C from a 10 tons refrigeration system for 15 hrs. ANSWER: 4197.930 kg A refrigeration system is used to cool water in the evaporator at 3 kg/s of water from 22 oC to ice. Find the tons of refrigeration required. ANSWER: 364.48805 TR A two stage cascade refrigeration system uses R-11 as the working substance. The evaporator is at -30 0C and the high pressure condenser is at 300C. The cascade condenser is a direct contact type. The refrigeration load is 24 tons. Given that, h2 = 393 kJ/kg; h6 = 408 kJ/kg. Find the mass flow rate in the low pressure loop. ANSWER: 0.4771 kg/sarrow_forward
- Q1: An engineer claimed that his device produces two streams of 1 am air (outlet 1) and 1.5 atm (outlet 2) at temperatures of 460 °R and 635 °R, respectively, if he enters 530 °R of the air at 5.1 atm. If the ratio of outlet 2 to outlet 1 is 0.6, justify the engineer's claim. Assume ideal gas process with a constant heat capacity of 0.24 Btu/lb.°R.arrow_forwardT, = 38°C rit = 2 kg/s T,= 10°C P= 140 kPa Saturated liquid P= 140 kPi mz = 0.42 kg/s T = 120°C P:= 140 kPa Above figure provides steady-state operating data for a mixing chamber in which entering liquid and vapor streams of water mix to form an exiting saturated liquid stream. Heat transfer from the mixing chamber to its surroundings occurs at an average surface temperature of 38°C. The effects of motion and gravity are negligible. Let To = 20°C, po = 1 bar. For the mixing chamber, determine, each in kl/s, (a) enthalpy of the stream 1, 2, and 3, (b) entropy of the stream 1, 2, and 3, (c) the rate of heat transfer between the chamber and environment, (d) the accompanying rate of exergy transfer due to the rate of heat transfer in (a). (e) the rate of exergy destruction.arrow_forwardAn ideal gas at 15 lbf/in2, 77°F flows horizontally at 516 ft/s into an adiabatic diffuser. It exits at 28 ft/s. Assume the heat capacity of the gas is constant.a. Determine the change in specific enthalpy (in Btu/lbm) and the outlet temperature if the gas is He.b. Repeat for R-125.c. Repeat for ozone (O3), which has a Molecular Mass of 47.9982 and a Cv0 of 0.1538 Btu/(lbm∙°R).arrow_forward
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