Document mqBG7LdjyLjgXOZODeBLRo87Q

764 . CHAPTER 34 1952 Guide The selection.of-a proper water-cooling range-depends upon: (1) type of service--refrigeration, internal-combustion engine, or steam condenser; (2) wet-bulb air temperature at which the equipment must operate; and (3) type of condenser or heat exchanger employed: , ' , Because the design of an entire plaint ;is usually affected by the quantity hnd temperature of the cooling water supply, plants should be designed for cooling water conditions which can be most efficiently attained. The first consideration is usually the limiting temperature of the plant. For example, if an ammonia compressor refrigerating plant is to be designed for 185 prig head pressure as a normal maximum, the limiting temperature of the ammonia in the condenser is 96 F.1 Should the ammonia tempera ture go above this figure, the head pressure will exceed, 185 psig and the power consumption increase. ; To obtain this'head, pressure, the tempera-: ture of the circulating water leaving ,the condenser' must' always be less Table 6. Condenser Design Data GA8 Desired Pressure in . ' Condenser Leaving Hot-Water v ' Temperature, Gas Temperature Fahrenheit in Condenser, '-Fahrenheit Best Average Condenser -Condenser Design' Design Steam..:.. ............ ... - 28 in. vacuum:: 101.2 1 97 93 '' Steam........................................ 27 in. vacuum ; 115.1 110 105' Steam.................................;................. . - 26 in. vacuum . 125.4 .; 120 114 .7 Ammonia............................................ 185 psi* 96.0 .. 92 88... Carbon dioxide............................ i030 psig* 86.0 83 80 Methyl chloride.......................... 102 psig* . 100.0 ... : 96 : - . ' 92 Freon, F-12.................................... 117 psig* . 100.0 .... 96., 93 . Freon, F-12........ ............ i26 psig* 105.0 1 100 97 Freon, F-12.................... 136 psig* 110.0 ' 104 101 : Head pressure. than 96 F by an. amount depending upon the size, and design .of the con denser, the quantity of water being circulated, and the refrigerating tonnage being produced. A condenser having a large surface per ton of refrigera tion may be designed to operate satisfactorily with the leaving, hot-water temperature within 3 or 4 deg of the ammonia, temperature corresponding to the head pressure, while a small condenser, may require a 10 deg dif ference. .; ... Table 6 lists several gases,with data, for the temperatures and pressures for which commercial condensers are designed. Careful evaluation of costs of water and electrical power should be made before deciding to use city water for jacket water and condensers. Economy of. operation gen erally indicates the use of either a water-cooling tower or an evaporative condenser for most refrigeration installations of five tons or more capacity. Refer to Chapter 36, for information on Evaporative Condensers. In ternal-combustion engines have limiting hot water temperatures of 140 to 180 F for closed systems, and 110 to 130 F for open systems, depending upon the quality of the cooling water. The cooling of such fluids, as milk or wort has variable requirements, and.is usually accomplished in counter- flow. heat-exchangers in which the leaving circulating water is at a much higher temperature than.is the leaving fluid. -. Spray Apparatus 765 - OPERATION AND MAINTENANCE Water Treatment. , The amount of make-up water required by a cooling, tower depends upon evaporation loss, drift loss, and blow-down. Evapora tion losses average: 0.80 percent of the waiter circulated foreach 10 F deg range.'. Drift loss is the water carried out ;of the tower by the air currents in the form of droplets or mist. In properly''designed induced; draft towers this loss normally approximates one-tenth of one percent, and most cooling tower manufacturers;will guarantee a drift loss not to exceed twotenths of-one percent. The'amount of blow-down water wasted depends upon the hardness of the'-circulating water, type of water softening used and the amount of drift loss. ' Blow-down is normally controlled, to main tain the concentration of soluble and scaledorming'solids below the point Where the formation of scale would occur or would be caused by corrosion. Algae formations will plug nozzles and prevent proper distribution of; the water over the. tower filling. This growth may also collect on equip-, ment served by the cooling tower, and thereby reduce the heat transfer. rate. Algae should be held at a minimum or eliminated by use of bromine, chlorine, chlorinated lime, copper sulfate, or -various blends of chloro- phenates (see Chapter 42). ... ... . Although some scale-forming materials are found in practically all water, those which cause trouble in water-cooling systems are normally'calcium; and magnesium carbonates. Scale formation in equipment served also' induces heat-transfer rates. Scale .can be reduced materially, or prevented by softening the make-up. water with lime and soda ash, zeolite, orsulfuric acid, or by use of small amounts of sodium hexametaphosphate. Water, softening or treatment requires close regulation and control by a competent chemist. Too high a concentration of soluble solids in cooling tower water- may raise the temperature, of the water leaving the tower, and may cause> sludge deposits or corrosion in the system. Concentration of solids is normally controlled by either blowing down or by a continuous overflow . to the sewer. Refer also to Chapter 42. .?. r Delignification. The presence of. sodium .carbonate in the circulating water results in delignification of any wood with which water comes in contact. This chemical dissolves lignin which binds the wood fibers, to-1 gether and leaves the wood surface in a white fibrous condition.': Prolonged, exposure reduces the structural strength of-the, wood. Delignification first appears on parts of the tower that are alternately wet and dry, since, evaporation at such points rapidly increases the concentration, of dissolved solids. The presence of sodium carbonate in harmful amounts is generally- indicated by a high pH of 9 to li. The effect of the sodium carbonate may be neutralized by the use of sulfuric acid. It is desirable to have the pH value of the water at 7 to 7.5 (7.2 pH value is neutral for redwood). ; Two-epeed Motors. For readily adapting tower performance to tempor rary or seasonal decreases in heat load, and especially for winter operation, the use of two-speed motors (for fan drives) is recommended: The chief advantage is that when operated at half-speed, fans require only about 15 percent of the power used at full speed. Particularly in multi-fan towers, the ready flexibility provided by two-speed motors results in considerable savings, even though load reductions may sometimes call for only one or a few fans to be operated at half speed. Cold-weather- Operation. Extremely cold water normally does not in-