Document oeq8e4DkJ2p9wmpz82zNZzK97

'924 CHAPTER 36 1957 Guide face; cooling it to approximately the wet-bulb temperature of the surrounding atmosphere. The end view of a typical evaporative condenser is shown in Fig. 13. The fan draws the air over the condenser surface which is kept wet by a water spray. The discharge refrigerant gas from the compressor enters the top of the condenser coil; arid the liquid refrigerant is drained from the bottom of the coil into a liquid receiver; and. then circulates through the remaining portion of the system in the usual way. The water is circulated through the spray nozzles, and the level is maintained in the sump by means of a float valve. The eliminator plates are placed in the path of the water-air mixture so as to remove the entrained water. The air leaving the Fio. 13. Schematic View op an Evaporative Condenser unit is almost completely saturated, so that care must be taken in locating discharge ducts to prevent condensation. Evaporative condensers are available in sizes up to 300 tons or more. These units use only a small portion of the water required for a waste water cooled con denser. The water is vaporized by the heat of the refrigerant so that each pound oi water used extracts approximately 1000 Btu from the refrigerant, whereas under standard rating conditions where the water temperature rise is 20 F, each pound oi water extracts only 20 Btu from the refrigerant. The water used, including the loss by entrainment in the discharge air, by blow down and the stand-by. evaporation, amounts to about 3 to 5 percent of that which would be required for a water cooled condenser. The evaporative condenser requires more maintenance, occupies greater space (must be located where air is available), and has a higher first cost than the wate cooled condenser, but where the use of water is restricted or expensive, the evapora tive condenser has become widely accepted. Compared with a water cooled con denser and cooling tower, which combination uses about the same quantity of water, the evaporative condenser has the advantage of lower cost and smaller space re quirements. Refrigeration 925 Evaporators and Coolers Refrigeration evaporators must be designed for efficient removal of heat from the medium being cooled, as well as effective boiling of the refrigerant and a minimum drop of pressure through the coil. There are two general types of evaporators, dry and flooded. In the dry evaporator the re frigerant enters in the liquid state, and the design provides for complete evaporation with the vapors leaving slightly superheated. In flooded evaporators not all of the refrigerant is evaporated, the liquid-vapor mix- ture leaving the evaporator flows into a surge drum from which the vapors are drawn into the compressor suction line, and the liquid is recirculated through the evaporator. The types of coolers used in connection with air conditioning work fall into three general groups: (1) direct water coolers, (2) direct air coolers, and (3) brine coolers for circulation of the brine in a closed system, and thus cooling indirectly either water or air. 1. Water coolers. One method of the direct cooling of water is to install direct expansion coils in the spray chamber so that the water sprayed into the air comes in direct contact with the cooling coils. Another common and efficient method of cooling spray water is to use a Baudelot type of heat absorber where the water flows over direct expansion coils at a rate sufficiently high to give efficient heat transfer from water to refrigerant. Another type of spray water cooler is the shell and tube heat exchanger in which the refrigerant is expanded into a shell enclosing the tubes through which the water flows. The velocity of the water in the tubes affects the rate of heat transfer, and as the refrigerant is in the shell completely surrounding the tubes at all times, good contact and a high rate of heat transfer are insured. The disadvantage of such a Bystem is that with the falling off of load on the compressor, the suction tempera ture or the temperature in the evaporator drops, and there is a possibility of freezing the water in the tubes, which, of course, might split the tubes and allow the re frigerant to escape into the water passage. This danger can be eliminated by auto matic Bafety devices. Another system of cooling spray water is to submerge coils in the spray collecting tank, or in a separate tank used for storage. The heat transmission through the walls of the coils, however, is low and a great deal more surface is required than for any other type of cooler. However, with large storage tanks this type of cooling can be utilized to advantage. 2. Air coolers. When direct cooling of air is employed, the refrigerant is inside the coil and the air passes over it. Cooling depends upon convection and con duction for removing the heat from the air. The type of coil used can be either smooth or finned, the finned coil being more economical in space requirement than the smooth coil. The fins, however, must be far enough apart so as not to retain the moisture which condenses out of the air. When refrigeration evaporators are used for cooling air or other gases by forced convection, they are usually termed blast coils or unit coolers. A blast coil may be placed in a duct or in an assembled unit, and the air forced across the coil and dis charged through distributing ducts or directly into the space to be conditioned, umt coolers, designed much like unit heaters, consist of a finned coil, propeller fan, and controls suspended directly in the space to be cooled. 3. Indirect brine coolers. The indirect cooler, where brine is cooled by the rengerant and the resulting cold brine is used to cool either air or water, introduces everal other considerations. It is not the most economical from a power consump- aiKiPin.k' as it is necessary to cool the brine to a temperature sufficiently low and "ere *s an appreciable difference between the average brine temperature a. that of the substance being cooled. This requires that the temperature of the ingcraiit must be still lower, and consequently the amount of power required to rat*'ce a given amount of refrigeration increases due to the higher compression firsd There are other considerations which make such a system desirable. In the or t?Iace, where a toxic refrigerant is undesirable or cannot be used because of fire isnl i r'8*cs' especially in densely populated areas, the brine can be cooled in an elated room or building and can then be circulated through the air conditioning