ASHRAE REFRIGERATION SI CH 14-2010 FORCED-CIRCULATION AIR COOLERS《强制循环空气冷却器》.pdf

1、14.1CHAPTER 14FORCED-CIRCULATION AIR COOLERSTypes of Forced-Circulation Air Coolers . 14.1Components. 14.2Air Movement and Distribution 14.3Unit Ratings 14.4Installation and Operation 14.6More Information 14.6ORCED-CIRCULATION unit coolers and product coolers areFdesigned to operate continuously in

2、refrigerated enclosures; acooling coil and motor-driven fan are their basic components, andprovide cooling or freezing temperatures and proper airflow to theroom. Coil defrost equipment is added for low-temperature opera-tions when coil frosting might impede performance.Any unit (e.g., blower coil,

3、unit cooler, product cooler, cold dif-fuser unit, air-conditioning air handler) is considered a forced-aircooler when operated under refrigeration conditions. Many designand construction choices are available, including (1) various coiltypes and fin spacing; (2) electric, gas, air, water, or hot-bri

4、ne de-frosting; (3) discharge air velocity and direction; (4) centrifugal orpropeller fans, either belt- or direct-driven; (5) ducted or nonducted;and/or (6) freestanding or ceiling-suspended, or penthouse (roof-mounted).Fans in these units direct air over a refrigerated coil contained inan enclosur

5、e. For nearly all applications of these units, the coil low-ers airflow temperature below its dew point, which causes conden-sate or frost to form on the coil surface. However, the normalrefrigeration load is a sensible heat load; therefore, the coil surfaceis considered dry. Rapid and frequent defr

6、osting on a timed cyclecan maintain this dry-surface condition, or the coil and airflow canbe designed to reduce frost accumulation and its effect on refriger-ation capacity.TYPES OF FORCED-CIRCULATION AIR COOLERSFigures 1 to 4 illustrate features of some types of air coolers.Sloped-front unit coole

7、rs, often called reach-in unit coolers,range from 125 to 250 mm high (Figure 1). Their distinctive slopedfronts are designed for horizontal top mounting as a single unit, orfor installation as a group of parallel connected units. Direct-drivefans are sloped to fit in the restricted return airstream,

8、 which risespast the access doors and across the ceiling of the enclosure. Air-flows are usually less than 70 L/s per fan. Commonly, these unitsare installed in back-bar and under-the-counter fixtures, as well asin vertical, self-serve, glass door reach-in enclosures.Low-air-velocity units feature a

9、 long, narrow profile (Figure 2).They have a dual-coil arrangement, and usually two or more fans.These units are used in above-freezing meat-cutting rooms and incarcass and floral walk-in enclosures, as well as 2C meat carcassholding rooms. They are designed to maintain as high a humidity aspossible

10、 in the enclosure. The units airflow velocity is low and finson the coil are amply spaced, which reduces the coils wetted surfacearea and thus the amount of dew-point contact area for the air stream.Discharge air velocities at the coil face range from 0.4 to 1.0 m/s.Medium-air-velocity unit coolers

11、originally had a half-roundappearance, although the more common version (often called low-profile units) features a long, narrow, dual-coil unit design (Figure 3).Both types of units are equipped with higher-volume fans. They areused in vegetable preparation rooms, walk-in rooms for wrappedfresh mea

12、t, and dairy coolers. These units normally extract moremoisture from ambient air than low-velocity units do. Discharge airvelocities at the coil face range from 1 to 2 m/s.Low-silhouette units are 300 to 380 mm high. Medium- ormid-height units are 450 to 900 mm high. Those over 900 mm highThe prepar

13、ation of this chapter is assigned to TC 8.4, Air-to-RefrigerantHeat Transfer Equipment.Fig. 1 Sloped-Front Unit Cooler for Reach-In CabinetsFig. 1 Sloped-Front Unit Cooler for Reach-In CabinetsFig. 2 Low-Air-Velocity UnitFig. 2 Low-Air-Velocity Unit14.2 2010 ASHRAE HandbookRefrigeration (SI)are clas

14、sified as high-silhouette unit coolers, which are used inwarehouse-sized coolers and freezers. Air velocity at the coil facecan be over 3 m/s. Outlet air velocities range from 5 to 10 m/s whenthe unit is equipped with cone-shaped fan discharge venturis forextended air throw.Spray coils feature a sat

15、urated coil surface that can cool pro-cessed air closer to the coil surface temperature than can a regular(nonsprayed) coil. In addition, the spray continuously defrosts thelow-temperature coil. Unlike unit coolers, spray coolers are usuallyfloor-mounted and discharge air vertically. Unit sections i

16、nclude adrain pan/sump, coil with spray section, moisture eliminators, andfan with drive. The eliminators prevent airborne spray droplets fromdischarging into the refrigerated area. Typically, belt-driven centrif-ugal fans draw air through the coil at 3 m/s or less.Water can be used as the spray med

17、ium for coil surfaces with tem-peratures above freezing. For coil surfaces with temperatures belowfreezing, a suitable chemical must be added to the water to lower thefreezing point to 11C, or below the coil surface temperature. Somesuitable recirculating solutions include the following:Sodium chlor

18、ide solution is limited to a room temperature of12C or higher. Its minimum freezing point is 21C.Calcium chloride solution can be used for enclosure tempera-tures down to about 23C, but its use may be prohibited in enclo-sures containing food products.Aqueous glycol solutions are commonly used in wa

19、ter and/orsprayed-coil coolers operating below freezing. Food-grade pro-pylene glycol solutions are commonly used because of their loworal toxicity, but they generally become too viscous to pump attemperatures below 25C. Ethylene glycol solutions may bepumped at temperatures as low as 40C. Because o

20、f its toxicity,sprayed ethylene glycol in other than sealed tunnels or freezers(no human access allowed during process) is usually prohibitedby most jurisdictions. When a glycol mix is sprayed in food stor-age rooms, any spray carryover must be maintained within thelimits prescribed by all applicabl

21、e regulations.All brines are hygroscopic; that is, they absorb condensate andbecome progressively weaker. This dilution can be corrected by con-tinually adding salt to the solution to maintain a sufficient below-freezing temperature. Salt is extremely corrosive, and must becontained in the sprayed-c

22、oil unit with suitable corrosive-resistantmaterials or coatings, which must be periodically inspected andmaintained. All untreated brines are corrosive: neutralizing thespray solution relative to its contact material is required.Sprayed-coil units are usually installed in refrigerated enclosuresrequ

23、iring high humidity (e.g., chill coolers). Paradoxically, the samesprayed-coil units can be used in special applications requiring lowrelative humidity. For these applications, both a high brine concen-trate (near its eutectic point) and a large difference between the pro-cess air and the refrigeran

24、t temperature are maintained. Process airis reheated downstream from the sprayed coil to correct the dry-bulbtemperature.COMPONENTSDraw-Through and Blow-Through AirflowUnit fans may draw air through the cooling coil and discharge itthrough the fan outlet into the enclosure, or they may blow airthrou

25、gh the cooling coil and discharge it from the coil face into theenclosure. Blow-through units have a slightly higher thermal effi-ciency because heat from the fan is removed from the forced air-stream by the coil, but their air distribution pattern is less effectivethan the draw-through design. Draw

26、-through fan energy adds to theheat load of the refrigerated enclosure, but heat gain from small (lessthan 1 kW) or small three-phase integral fan motors is not signifi-cant. Selection of draw-through or blow-through depends more on amanufacturers design features for the unit size required, air thro

27、wrequired for the particular enclosure, and accessibility of the coil forperiodic surface cleaning.The blow-through design has a lower discharge air velocity be-cause the entire coil face area is usually the discharge opening(grilles and diffusers not considered). Throw of 10 m or less is com-mon fo

28、r the average standard air velocity from a blow-through unit.Greater throw, in excess of 30 m, is normal for draw-through cen-trifugal units. The propeller fan in the high-silhouette draw-throughunit cooler is popular for intermediate ranges of air throw.Fan AssembliesDirect-drive propeller fans (mo

29、tor plus blade) are popularbecause they are simple, economical, and can be installed in multi-ple assemblies in a unit cooler housing. Additionally, they requireless motor power for a given airflow capacity.The centrifugal fan assembly usually includes belts, bearings,sheaves, and coupler drives, ea

30、ch with inherent maintenance prob-lems. This design is necessary, however, for applications with highair distribution static pressure losses (e.g., enclosures with ductworkruns, tunnel conveyors, and densely stacked products). Centrifugal-fan-equipped units are also used in produce-ripening rooms, w

31、hereFig. 3 Low-Profile CoolerFig. 3 Low-Profile CoolerFig. 4 Liquid Overfeed Type Unit CoolerFig. 4 Liquid Overfeed Unit CoolerForced-Circulation Air Coolers 14.3a large air blast and 125 to 185 Pa discharge air static is needed forproper air circulation around all the product in the enclosure, toen

32、sure uniform batch ripening.CasingCasing materials are selected for compatibility with the enclo-sure environment. Aluminum (coated or uncoated) or steel (galva-nized or suitably coated) are typical casing materials. Stainless steelis also used in food storage or preparation enclosures where sanita-

33、tion must be maintained. On larger cooler units, internal framing isfabricated of sufficiently substantial material, such as galvanizedsteel, and casings are usually made with similar material. Someplastic casings are used in small unit coolers, whereas some large,ceiling-suspended units may have al

34、l-aluminum construction toreduce weight.Coil ConstructionCoil construction varies from uncoated (all) aluminum tube andfin to hot-dipped galvanized (all) steel tube and fin, depending on thetype of refrigerant used and the environmental exposure of the coil.The most popular unit coolers have coils w

35、ith copper tubes and alu-minum fins. Ammonia refrigerant evaporators never use coppertubes because ammonia corrodes copper. Also, sprayed coils are notconstructed with aluminum fins unless they are completely protectedwith a baked-on phenolic dip coating or similar protection appliedafter fabricatio

36、n. Coils constructed with stainless steel tubes and finsare preferred in corrosive environments, and all-stainless construc-tion, or with aluminum fins, is preferred in environments where highstandards of sanitation are maintained.Fin spacings vary from 3 to 4 mm between fins for coils with sur-face

37、s above 0C when latent loads are insignificant. Otherwise, 4 to8 mm between fins is the accepted spacing for coil surfaces below0C, with a 6 mm fin spacing when latent loads exceed 15% of thetotal load. Fin spacings of 25 and 12 mm are used when defrostingis set for once a day, such as in low-temper

38、ature supermarket displaycases. Staged fins in a row of coils, such as a 24-12-6 mm fin spac-ing combination, greatly reduce fin blockage by frost accumulation(Ogawa et al. 1993).Even distribution of the refrigerant flow to each circuit of the coilis vital for maximizing cooler coil performance. Dis

39、tributor assem-blies are used for direct-expansion halocarbon refrigerants and occa-sionally for large, medium-temperature ammonia units. Applicationrequires that they be precisely sized. Distributor design and construc-tion material may vary by refrigerant type and application. Applica-tion informa

40、tion from the distributor manufacturer should be closelyfollowed, particularly regarding orifice sizing and assembly mount-ing orientation on the coil.For liquid pumped recirculating systems, orifice disks are usu-ally used in lieu of a distributor assembly. These disks are sized andinstalled by the

41、 coil manufacturer. They fit in the inlet (supply)header, at the connection spuds of each coil circuit. The specifyingengineer may require a down-feed distributor assembly, less any ori-fice, if significant flash gas is anticipated.Headers and their piping connections are part of the coil assem-bly.

42、 Usually, header lengths equal the coil height dimension; there-fore each header is sized to the coil capacity for the application,based on refrigerant flow velocities and not on the temperatureequivalent of the saturated suction temperature drop. Velocities ofapproximately 7.5 m/s are used to compu

43、te the size of the return gasheader and its connection size. In the field, connection size is oftenmistaken to be the recommended return line size, but the size oflines installed in the field should be based on the suction drop cal-culation method (see Chapters 1 to 4).Frost ControlCoils must be def

44、rosted when frost accumulates on their sur-faces. The frost (or ice) is usually greatest at the coils air entryside; therefore, the required defrost cycle is determined by the inletsurface condition. In contrast, a reduced secondary-surface-to-primary-surface ratio produces greater frost accumulatio

45、ns at thecoil outlet face. A long-held theory is that accumulation of rela-tively more frost at the coil entry air surface somewhat improvesthe heat transfer capacity of the coil. However, overall accumu-lated coil frost usually has two negative effects: it (1) impedes heattransfer because of its in

46、sulating effect, and (2) reduces airflow be-cause it restricts the free airflow area within the coil. Both effects,to different degrees, result from combinations of airflow, fin spac-ing, frost density, and ambient air conditions.Depending on the defrost method, as much as 80% of the de-frost head l

47、oad of the unit could be transferred into the enclosure.This heat load is not normally included as part of the enclosureheat gain calculation. The units refrigeration capacity rating is av-eraged over a 24 h period, by a factor that estimates the typicalhours per day of refrigeration running time, i

48、ncluding the defrostcycles.As previously mentioned, time between defrost cycles can beincreased by using more coil tube rows and wider fin spacing. Iceaccumulation, which interferes with airflow, should be avoided toreduce both the frequency and duration of the defrost cycles. Forexample, in low-tem

49、perature applications having high latent loads,unit coolers should not be located above freezer entry or exit doors.Operational ControlsIn the simplest form, electromechanical controls cycle the refrig-eration system components to maintain the desired enclosure tem-perature and defrost cycle. Pressure-responsive modulating controlvalves, such as evaporator-pressure regulators and head-pressurecontrols, are also used. A temperature control could be a thermostatmounted in the enclosure, used to cycle the compressor on and off,or a liquid-line solenoid valve that allows li