NAVY A-A-50573-1997 WATER SOFTENER UNIT LIME-SODA TYPE [Superseded NAVY MIL-W-17122 D CANC NOTICE 1 NAVY MIL-W-17122 D NAVY MIL-W-17122 C NAVY MIL-W-17122 B NAVY MIL-W-17122 A]《石灰纯.pdf
《NAVY A-A-50573-1997 WATER SOFTENER UNIT LIME-SODA TYPE [Superseded NAVY MIL-W-17122 D CANC NOTICE 1 NAVY MIL-W-17122 D NAVY MIL-W-17122 C NAVY MIL-W-17122 B NAVY MIL-W-17122 A]《石灰纯.pdf》由会员分享,可在线阅读,更多相关《NAVY A-A-50573-1997 WATER SOFTENER UNIT LIME-SODA TYPE [Superseded NAVY MIL-W-17122 D CANC NOTICE 1 NAVY MIL-W-17122 D NAVY MIL-W-17122 C NAVY MIL-W-17122 B NAVY MIL-W-17122 A]《石灰纯.pdf(8页珍藏版)》请在麦多课文档分享上搜索。
1、- A-A-50573 74 0374544 77T INCH-POUND A-A-50573 Aril21. 1997 SUPERSEDING 30August 1991 MIL-W- 17 122D COMMERCIAL ITEM DESCRIPTION WATER SOFTENER UNIT, LIME-SODA TYPE The General Services Administration has authorized the use of this commercial item description for ail Federal agencies. 1. SCOPE. Thi
2、s commercial item description (CID) covers water softening equipment for process and boiler feed water treatment using lime or soda ash. Both hot process and cold process equipment are covered. 2. CLASSIFICATION. Water softeners are of the following types, as specified (see 7.1 and 7.3). 2.1 Type: T
3、ype I Type II - Hot process, lime-soda - Cold process, lime-soda 2.2 Capacity: Class 1 Class 2 Class 3 - Under 5,000 galions per hour (ah) (Under 5 250 cubic centimetre per second (cm3/s) - 5,000 to 7,000 gph (5 250 to 7 350 cm3/s) - 7,000 to 10,000 gph (7 350 to 10 500 cm3/s) Beneficial comments, r
4、ecommendations, additions, deletions, clarifications, etc. and any data which may improve this document should be sent to: Commanding Officer (Code 15E2), Naval Construction Battalion Center, 1000 23rd Avenue, Port Hueneme, CA 93043-4301, by using the Standardization Document Improvement. Proposal (
5、DD Form 1426) appearing at the end of this document or by letter. AMSC NIA FSC 4610 Licensed by Information Handling ServicesA-8-50573 H 9999974 0374545 bob = A-A-50573 3. SALfrn CHARACTERISTICS. 3.1 Description Water softeners covered by this CID shall be designed to treat boiler feed water or proc
6、ess water in self-contained units. The softening process shall include the use of lime and soda ash. Provisions shd be made for the addition of a chemical feeder for coagulant, phosphates, and sulfuric acid. Supplementary treatment with phosphates and sulfuric acid, if necessary in order to meet eff
7、luent requirements, shd be included. The equipment shall be complete and ready for service with all interconnection piping, fittings, valves, and control lines. The equipment shall include principally the softener tank with or without heating chamber, settling tank and, ifrequired, a deaerator (see
8、3.6 and 7.3), and ali connections, the control systems, the chemical feeders and the filters. 3.2 Standard commercial product. The water softening equipment shall, as a minimum, be in accordance with the requirements of this CID and shall be the manufacturers standard commercial product. Additional
9、or better features which are not specifically prohibited by this CID but which are a part of the manufacturers standard commercial product, shall be included in the water softening equipment being furnished. A standard commercial product is a product which has been sold or is being currently offered
10、 for sale on the commercial market through advertisement or manufacturers catalogs or brochures, and represents the latest production model. 3.3 Performance. The water softener equipment shall be capable of meeting the capacities specified.(see 2.) The tank interiors shall be provided with aii ofthe
11、 necessary baffles, cylinders, partitions or tubes required for the satisfactory performance of the equipment. Unless otherwise specified (see 7.3), the treated water shall have hardness of less than 1.50 grains per gallon (25.68 milligrams per litre (mg/L) in terms of calcium carbonate (CaCO3) for
12、type I, and less than 3 grains per gallon (5 1.36 mgL) for type II, with an excess soda ash content of less than 2.00 grains per gallon (34.24 ma). 3.4 Components for tpe I. 3.4.1 Softener tanks. The softener tank shall conform to MME Boiler and Pressure Vessel Code, Section VIII, Division 1. The ta
13、nk shall be of the sludge blanket or solids contact type as specified (see 7.3) and meet the design pressure specified (see 7.3). Softeners equipped for deaerating and heating returned condensate shall be so designed that oniy raw or makeup water shall pass through the softening section and the filt
14、ers. 3.4.2 Settling tanks. The settling tanks shall be huge enough to provide one-hour retention when the units are working at rated capacity. The rise rate based on the outlet service flow shall be not greater than 2.3 gallons per minute (gpm) per square foot (fi2) (O. 15 litre per second &/s) per
15、square metre (m). The flow rate through the softener shall be low enough so that a filter can be backwashed at the specified rate continuously for 10 minutes without any carryover of the slurry fiom the softener to the filter. The conical bottom shal have SuniCient slope as to ailow for sludge remov
16、al. 2 Licensed by Information Handling ServicesA-A-50573 = 9999974 0374546 542 A-A-50573 3.4.3 Tank connections. The tank shall have ail the connections necessary for the satisfactory operation of the equipment including the following: a. b. d. e. f. g. h. C. I. i k. 1. m. n. O. Internal direct cont
17、act vent condenser Makeup inlet Vacuum breaker Chemical inlet Recirculation inlet Sludge drain Treated water outlet Overflow Clean backwash fiil Dirty backwash return Sample connections Pressure and temperature connections Vent and access manways for access to upper chemical reaction zone Lower sett
18、ling zone Backwash compartments 3.4.4 Spray valves. Heating the makeup water shall be accomplished by use of self-regulating, nonfouling spray valves. The spray valves shaii be accessible fiom outside of the pressure vessel through removable cover plates. The spray valves shaii provide a constant an
19、gle of thin fiim spray with uniform water film at rates from 3 percent to 120 percent of rated system design capacity. The pressure drop required for the spray valves shail be kept to a minimum to effect complete and uniform spraying at fli flow when the water is heated to within 2 degrees Fahrenhei
20、t (OF) (I. 1 degrees Celsius (OC) of saturation temperature maintained by heating steam in process vessel. 3.4.5 Vent condensers. Provisions shaii be made for complete venting of ail released noncondensable gases, including oxygen, carbon dioxide, and nitrogen using supply vent condensers of the dir
21、ect contact internal type, using makeup water as the cooling fluid, with a minimum of steam loss. 3.4.6 Vacuum breakers. Tanks shall be equipped with vacuum breakers of adequate size. Sheils less than 10 feet (3 metre (m) in diameter may have oniy a singie port, not smaller than the siie given below
22、. The vacuum breakers shali seal tight against steam pressure and open to relieve vacuum before the tanks are in danger of collapsing. Type I softeners Breaker nominal pipe size Class 1 Class 2 Class 3 One 6-inch (150 mm) breaker One 10-inch (250 mm) breaker One 16-inch (410 mm) breaker 3 Licensed b
23、y Information Handling ServicesA-A-50573 H 9999974 0374547 489 H A-A-50573 3.5 Components for type II. 3.5.1 Softener tanks. Tanks shall be designed for field assembly and be of the solids-contact, sludge recirculation type units. Tanks shall be large enough to provide one-hour retention of water be
24、ing treated when operating at rated capacity. The takeoff rate shall be not greater than 1.5 gpm per fi2 (0.09 Ws per m2) of surface area. 3.5.2 Tank connections. Connections shall be provided for the water inlet, the outlet, sludge removal, sampling pipes, and bottom drain. Ail necessary pipe and f
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