ARMY UFGS-22 13 29-2011 SANITARY SEWERAGE PUMPS.pdf
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1、*USACE / NAVFAC / AFCESA / NASA UFGS-22 13 29 (February 2011)-Preparing Activity: USACE SupersedingUFGS-44 46 00 (April 2006)UNIFIED FACILITIES GUIDE SPECIFICATIONSReferences are in agreement with UMRL dated January 2011*SECTION TABLE OF CONTENTSDIVISION 22 - PLUMBINGSECTION 22 13 29SANITARY SEWERAG
2、E PUMPS02/11PART 1 GENERAL1.1 REFERENCES1.2 SUBMITTALS1.3 DELIVERY, STORAGE, AND HANDLING1.4 EXTRA MATERIALSPART 2 PRODUCTS2.1 MATERIALS AND EQUIPMENT2.1.1 Nameplates2.1.2 Equipment Guards2.1.3 Special Tools2.1.4 Electric Motors2.1.5 Motor Controls2.1.6 Bolts, Nuts, Anchors, and Washers2.1.7 Pressur
3、e Gauges2.1.8 Seal Water Systems2.1.8.1 Float Valve2.1.8.2 Auxiliary Equipment2.1.8.3 Controls2.1.8.4 System Characteristics2.2 CENTRIFUGAL SOLIDS HANDLING PUMPS2.2.1 Pump Characteristics2.2.2 Pump Casing2.2.3 Impeller2.2.4 Wearing Rings2.2.5 Pump Shaft2.2.6 Pump Shaft Sleeve2.2.7 Stuffing Box2.2.8
4、Mechanical Seals2.2.9 Bearings2.2.10 Lubrication2.2.11 Pump Support2.2.12 Coupling2.3 SUBMERSIBLE CENTRIFUGAL PUMPSSECTION 22 13 29 Page 1Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-2.3.1 Pump Characteristics2.3.2 Pump Casing2.3.3 Mating Surfaces
5、2.3.4 Coatings2.3.5 Impeller2.3.6 Wearing Rings2.3.7 Pump Shaft2.3.8 Seals2.3.9 Bearings2.3.10 Motor2.3.11 Power Cable2.3.12 Installation Systems2.3.12.1 Rail Mounted Systems2.3.12.2 Bolt Down Systems2.3.12.3 Lifting Chain2.4 SELF-PRIMING CENTRIFUGAL PUMPS2.4.1 Pump Characteristics2.4.2 Pump Casing2
6、.4.3 Impeller2.4.4 Wear Plate2.4.5 Pump Shaft2.4.6 Pump Shaft Sleeve2.4.7 Seals2.4.8 Bearings2.4.9 Lubrication2.4.10 Suction Check Valve2.4.11 Pump Support2.4.12 Coupling2.5 SCREW PUMPS2.5.1 Pump Characteristics2.5.2 Lower Bearing Assembly2.5.2.1 Seals2.5.2.2 Bearing Shield2.5.3 Spiral Screw2.5.3.1
7、Torque Tube2.5.3.2 Shafts2.5.4 Flow Defector Plates2.5.5 Upper Bearing Assembly2.5.5.1 Housing2.5.5.2 Bearing2.5.5.3 Seals2.5.5.4 Mounting Plate2.5.5.5 Cover2.5.6 Drive Assembly2.5.6.1 Gear Reducer2.5.6.2 Backstop2.5.6.3 Drive2.5.7 Lubrication System2.5.8 Radius Screed2.6 PLUNGER PUMPS2.6.1 Pump Cha
8、racteristics2.6.2 Pump Base2.6.3 Pump Body2.6.4 Valves2.6.5 Connecting Rod, Eccentric, Eccentric Bearings, and Shaft2.6.6 Plungers2.6.7 Cylinders2.6.8 Stuffing Box2.6.9 Air ChambersSECTION 22 13 29 Page 2Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-
9、,-2.6.10 Sampling Valve2.6.11 Pressure Relief Valve2.6.12 Lubrication2.6.13 Chain Drive2.6.14 V-Belt and Integral Gear Drive2.6.15 Gear Reducer Drive2.7 PROGRESSIVE CAVITY PUMPS2.7.1 Pump Characteristics2.7.2 Casing2.7.3 Rotor2.7.4 Stator2.7.5 Drive Shaft and Connecting Rod2.7.6 Flexible Drive Shaft
10、2.7.7 Seals2.7.8 Bearings2.8 DIAPHRAGM PUMPS2.8.1 Pump Characteristics2.8.2 Casing2.8.3 Suction and Discharge Check Valves2.8.4 Pulsation Dampers2.8.5 Air-Operated Actuators2.8.5.1 Valve2.8.5.2 Timer2.8.5.3 Muffler2.8.5.4 Pressure Regulator2.8.5.5 Strainer2.8.5.6 Assist2.8.6 Mechanical Actuators2.9
11、RECESSED IMPELLER PUMPS2.9.1 Pump Characteristics2.9.2 Pump Casing2.9.3 Impeller2.9.4 Pump Shaft2.9.5 Sleeve2.9.6 Seals2.9.6.1 Packing2.9.6.2 Mechanical Seals2.9.7 Bearings2.10 ROTARY LOBE PUMPS2.10.1 Pump Characteristics2.10.2 Casing2.10.3 Rotors2.10.4 Shafts and Sleeves2.10.5 Packing Glands2.10.6
12、Bearings2.11 ELECTRICAL WORKPART 3 EXECUTION3.1 EXAMINATION3.2 EQUIPMENT INSTALLATION3.2.1 Pump Installation3.2.2 Concrete3.2.3 Grouting Screw Pump Flow Channel3.3 PAINTING3.4 FRAMED INSTRUCTIONS3.5 FIELD TESTING AND ADJUSTING EQUIPMENT3.5.1 Operational Test3.5.2 RetestingSECTION 22 13 29 Page 3Prov
13、ided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-3.6 MANUFACTURERS SERVICES3.7 FIELD TRAINING- End of Section Table of Contents -SECTION 22 13 29 Page 4Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-*USAC
14、E / NAVFAC / AFCESA / NASA UFGS-22 13 29 (February 2011)-Preparing Activity: USACE SupersedingUFGS-44 46 00 (April 2006)UNIFIED FACILITIES GUIDE SPECIFICATIONSReferences are in agreement with UMRL dated January 2011*SECTION 22 13 29SANITARY SEWERAGE PUMPS02/11*NOTE: This guide specification covers t
15、he requirements for sewage and sludge pumps for domestic type waste.Edit this guide specification for project specific requirements by adding, deleting, or revising text. For bracketed items, choose applicable items(s) or insert appropriate information.Remove information and requirements not require
16、d in respective project, whether or not brackets are present.Comments, suggestions and recommended changes for this guide specification are welcome and should be submitted as a Criteria Change Request (CCR).*PART 1 GENERAL*NOTE: This specification guide covers pumps for domestic sewage and sludge. I
17、ndustrial wastewater and sludge may require special consideration and design. Refer to UFC 3-240-08FA and consult the published data of representative manufacturers and the Hydraulics Institute. Pneumatic ejectors are specified in Section 22 13 36 PNEUMATIC SEWAGE EJECTORS. The following are the typ
18、es of pumps included and the general uses:a. Centrifugal solids handling pumps have high head (up to 69 m (225 feet) and high capacity (up to 2840 L/second (45,000 gpm) capabilities and high efficiency relative to other solids handling pumps. They are ideal for sewage applications.b. Submersible cen
19、trifugal pumps have high head (up to 55 m (180 feet) and high capacity (up to 1390 L/second (22,000 gpm) capabilities but are less SECTION 22 13 29 Page 5Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-efficient than standard centrifugal pumps. They
20、have higher operating costs but lower installation costs than standard centrifugal pumps. They are ideal for sewage and low concentration sludge applications.c. Self-priming centrifugal pumps have moderate head (up to 31 m (100 feet) and moderate capacity (up to 158 L/second (2,500 gpm) capabilities
21、 and are less efficient than standard centrifugal pumps. They have higher operating costs but lower installation costs than standard centrifugal pumps. They are ideal for raw sewage applications where occasional service interruptions are acceptable.d. Screw pumps have low head (up to 9 m (30 feet) a
22、nd high capacity (up to 5050 L/second (80,000 gpm) capabilities and are relatively efficient (70 to 75 percent). They are ideal for raw sewage, storm water, and activated sludge lift stations.e. Plunger pumps have high head 76 to 92 m (250 to 300 feet) and moderate capacity (up to 35 L/second (550 g
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