Asme b73 1m 2001 (american society of mechanical engineers)

ASME B73.1-2001 [Revision of ASME B73.1M-1991(R1999)] SPECIFICATION FOR HORIZONTAL END SUCTION CENTRIFUGAL PUMPS FOR CHEMICAL PROCESS AN AMERICAN NATIONAL STANDARD A N A M E R I C A N N A T I O N A L S T A N D A R D SPECIFICATION FOR HORIZONTAL END SUCTION CENTRIFUGAL PUMPS FOR CHEMICAL PROCESS ASME B73.1-2001 [Revision of ASME B73.1M-1991(R1999)] Date of Issuance: February 25, 2002 The next edition of this Standard is scheduled for publication in 2006 There will be no addenda or written interpretations of the requirements of this Standard issued to this edition ASME is the registered trademark of The American Society of Mechanical Engineers This code or standard was developed under procedures accredited as meeting the criteria for American National Standards The Standards Committee that approved the code or standard was balanced to assure that individuals from competent and concerned interests have had an opportunity to participate The proposed code or standard was made available for public review and comment that provides an opportunity for additional public input from industry, academia, regulatory agencies, and the public-at-large ASME does not “approve,” “rate,” or “endorse” any item, construction, proprietary device, or activity ASME does not take any position with respect to the validity of any patent rights asserted in connection with any items mentioned in this document, and does not undertake to insure anyone utilizing a standard against liability for infringement of any applicable letters patent, nor assume any such liability Users of a code or standard are expressly advised that determination of the validity of any such patent rights, and the risk of infringement of such rights, is entirely their own responsibility Participation by federal agency representative(s) or person(s) affiliated with industry is not to be interpreted as government or industry endorsement of this code or standard ASME accepts responsibility for only those interpretations of this document issued in accordance with the established ASME procedures and policies, which precludes the issuance of interpretations by individuals No part of this document may be reproduced in any form, in an electronic retrieval system or otherwise, without the prior written permission of the publisher The American Society of Mechanical Engineers Three Park Avenue, New York, NY 10016-5990 Copyright © 2002 by THE AMERICAN SOCIETY OF MECHANICAL ENGINEERS All Rights Reserved Printed in U.S.A FOREWORD In 1955, the Standards Committee on Centrifugal Pumps for Chemical Industry Use, B73, undertook the development of centrifugal pump standards to meet the needs of the chemical industry Although the Standards Committee had not completed its assignment, the work of one of its task forces resulted in the development of a de facto standard which was published by the Manufacturing Chemists Association in 1962 as an American Voluntary Standard More than a dozen manufacturers of chemical process pumps have been marketing pumps conforming with the AVS since that time In 1965 the Hydraulic Institute published a tentative standard similar in content to the AVS, but updated certain portions Although the Hydraulic Institute Tentative Standard reflected more nearly the current practice of manufacturers and users, it was believed necessary to publish a new document which would supersede both the original AVS and the tentative standard, and which could incorporate the technical content of both documents, in addition to dimensional criteria and features generally accepted by manufacturers and users The January 1968 revision of the AVS was therefore approved as an American National Standard under the existing standards method and published as ANSI B123.1-1971 ANSI B73.1 superseded ANSI B123.1-1971 and was first published in 1974 The 1974 edition brought to 15 the number of pump sizes covered by the standard Since then, the committee has continued to be active and has added five more sizes for a total of 20, and made a number of revisions in the text of the standard Shortly thereafter, the American National Standards Committee B73 undertook to revise the standard, and as a result, new information on baseplate rigidity, bearing frame adapter, and bearing housing drain was introduced The 1984 edition included, for the first time, information that covered documentation of pump and driver outline drawing of the centrifugal pump, data sheet, mechanical seal drawing, stuffing box piping plans, and cooling/heating piping plans The 1991 revision included larger and self-venting tapered seal chambers, as well as conventional stuffing boxes, revised baseplate dimensions, with a new identification numbering system, and a ductile material requirement for the bearing frame adapter if it clamps the rear cover plate to the casing With the expanding utilization of the ASME B73.1 pumps in the chemical process industry and its growing acceptance in the hydrocarbons processing industry, the B73 committee has continued to improve the B73.1 standard This revision of the Standard incorporates new sizes of pumps, bringing the total number to 27 Many of the new additions were at the request of the user population Although inclusion of “ISO” standard size pumps was entertained, the proposed additions of the “ISO” sizes were rejected by the committee It was thought that the addition of the “ISO” sizes made the standard overly complex and weakened its mechanical fortitude The material of construction section of the standard was expanded to include readily available corrosion resistant alloys Recent publications by the Hydraulic Institute in areas such as baseplate tolerance, acceptable nozzle loads, preferred operating region and NPSH margin have been incorporated into this revision The former Appendix covering documentation has been established as an integral portion of the Standard This is in part in response to the needs of the user community for compliance to U.S Government regulations covering chemical process equipment and pumps specifically OSHA iii Process Safety Management, 29 CFR 1910.119 In total, these revisions to the standard are intended to better serve process industries and expand the use of ASME B73 pumps world wide Suggestions for improvement in this Standard will be welcome and should be sent to the American Society of Mechanical Engineers, Attn: Secretary B73 Committee, Three Park Ave., New York, NY 10016-5990 This revision was approved as an American National Standard on September 7, 2001 iv ASME STANDARDS COMMITTEE B73 Chemical Standard Pumps (The following is the roster of the Committee at the time of approval of this Standard.) OFFICERS R J Hart, Chair G W Sabol, Vice Chair C J Gomez, Secretary COMMITTEE PERSONNEL B M Burkelman, Ingersoll-Dresser Pumps F W Buse, Alternate, Ingersoll-Dresser Pumps G C Clasby, Flowserve Corp., Pump Division J F Dolniak, Eli Lilly & Co R W Estep, Union Carbide Corp C J Gomez, The American Society of Mechanical Engineers R J Hart, E.I DuPont de Nemours & Co M T Henessey, Flowserve Corp W G Klingberg, Sterling Fluid Systems E W Allis, Alternate, Sterling Fluid Systems T Matthews, Dow Chemical Co R A Lewis, Alternate, Dow Chemical Co R H Monroe, Jr., Solutia Inc J C Osborne, AR Wilfley & Sons Inc J D Quill, ITT Industries — Goulds A E Stavale, Alternate, ITT Industries — Goulds J L Ryan, Met-Pro Corp., Dean Pump Division G W Sabol, Union Carbide Corp M D Smith, Syndyne Corp D M Threlkel, NEMA v CONTENTS Foreword Committee Roster iii v Scope Alternative Design Nomenclature and Definitions 3.1 Source 1 Design and Construction Features 4.1 Pressure and Temperature Limits 4.2 Flanges 4.3 Casing 4.4 Impeller 4.5 Shaft 4.6 Shaft Sealing 4.7 Bearings 4.8 Materials of Construction 4.9 Corrosion Allowance 4.10 Direction of Rotation 4.11 Dimensions 4.12 Miscellaneous Design Features 1 1 5 13 13 13 13 14 14 General Information 5.1 Application 5.2 Test 5.3 Nameplates 14 14 16 16 References 17 Documentation 7.1 General 7.2 Requirements 7.3 Information 7.4 Specially Requested Documentation 18 18 18 18 21 Figures Shaft Sleeve Runout Mechanical Seal Piping Plans Cooling and Heating Piping Plans Typical Seal Arrangements Cylindrical Seal Chamber 10 11 vi 10 Self-Venting Tapered Seal Chamber Stuffing Box Seal Chamber Face Runout Seal Chamber Register Concentricity Sample Outline Drawing 11 12 12 12 19 Tables Pump Dimensions Baseplate Dimensions Approximate Performance of Standard Pumps (50 Hz) Approximate Performance of Standard Pumps (60 Hz) Minimum Continuous Flow B73 Standardized Electronic Data Exchange File Specification 15 16 17 22 Nonmandatory Appendix A ASME Centrifugal Pump Data Sheet 31 vii ASME B73.1-2001 SPECIFICATION FOR HORIZONTAL END SUCTION CENTRIFUGAL PUMPS FOR CHEMICAL PROCESS SCOPE to 500°F (260°C) with a reduction in pressure corresponding to the reduction in yield strength of the jacket material This Standard covers centrifugal pumps of horizontal, end suction single stage, centerline discharge design This Standard includes dimensional interchangeability requirements and certain design features to facilitate installation and maintenance It is the intent of this Standard that pumps of the same standard dimension designation from all sources of supply shall be interchangeable with respect to mounting dimensions, size and location of suction and discharge nozzles, input shafts, baseplates, and foundation bolt holes (see Tables and 2) 4.1.1.3 Casing, stuffing box, cover or seal chamber, and jackets shall be designed to withstand a hydrostatic test at 1.5 times the maximum design pressure for the particular component and material of construction used (see para 5.2.1) 4.1.2 Temperature Limits Temperature limitations shall be stated by the pump manufacturer Pumps should be available for temperatures up to 500°F (260°C) Jacketing and other modifications may be required to meet the operating temperature ALTERNATIVE DESIGN 4.2 Flanges Alternate designs will be considered, provided they meet the intent of this Standard and cover construction and performance which are equivalent to and otherwise in accordance with these specifications All deviations from these specifications shall be described in detail DESIGN AND CONSTRUCTION FEATURES Suction and discharge nozzles shall be flanged Flanges shall conform to ASME B16.5 or ASME B16.42 Class 150 standards except that marking requirements are not applicable and the maximum acceptable tolerance on parallelism of the back of the flange shall be deg and bolt holes may be tapped where noted in Table Through bolt holes are preferred When tapped holes are supplied, they shall be noted on the outline drawing As an option, Class 300 flanges in accordance with ASME B16.5 or ASME B16.42 may be offered subject to the manufacturer’s casing pressure-temperature limitations All pumps regardless of flange rating shall conform to the X and Y dimensions shown in Table 4.1 Pressure and Temperature Limits 4.3 Casing 4.1.1 Pressure Limits Pressure limitations shall be stated by the pump manufacturer 4.3.1 Drain Connection Boss(es) Pump casing shall have boss(es) to provide for drain connection(s) in the lowest part of the casing Boss size shall accommodate 1⁄2 in NPT Boss(es) shall be drilled and tapped when specified by customer NOMENCLATURE AND DEFINITIONS 3.1 Source All nomenclature and definitions of pump components shall be in accordance with HI 1.1–1.2 4.1.1.1 The design pressure of the casing, including stuffing box or seal chamber and gland, shall be at least as great as the pressure-temperature rating of ASME B16.5 or ASME B16.42 Class 150 flanges for the material used 4.3.2 Auxiliary Connection Boss(es) The suction and discharge nozzles shall have boss(es) for gage connections Boss size shall accommodate 1⁄4 in NPT min., 1⁄2 in NPT preferred Boss(es) shall be drilled and tapped when specified by customer 4.1.1.2 The design pressure of jackets shall be at least 100 psig (690 kPa gage) at 340°F (170°C) Heating jackets may be required for jacket temperatures SPECIFICATION FOR HORIZONTAL END SUCTION CENTRIFUGAL PUMPS FOR CHEMICAL PROCESS ASME B73.1-2001 TABLE B73 STANDARDIZED ELECTRONIC DATA EXCHANGE FILE SPECIFICATION (CONT’D) No Name Field Type Length Contents/Unit Mechanical Seal or Packing A265 A268 A272 A273 A274 A277 A278 A282 A290 A291 A292 A294 A295 A296 A297 A319 A320 A321 A322 A326 Seal Manufacturer Manufacturer Code Circulating Device Sleeve Material Gland Material Flush Gland Taps Drain Gland Taps Quench Gland Taps Flush Minimum Temperature Flush Maximum Temperature Specific Gravity Flush fluid Name Flush Specific Heat Flush vapor pressure Flush vapor pressure temperature Flush Other Flush Maximum Flowrate Flush Minimum Flowrate Flush Maximum Pressure Flush Minimum Pressure Flush Maximum Temperature Flush Minimum Temperature Barrier Minimum Temperature Barrier Maximum Temperature Barrier SG Barrier Liquid Name Barrier Vapor Pressure Barrier Vapor Pressure Temperature Barrier Maximum Pressure Barrier Minimum Pressure Barrier Temperature Maximum Barrier Temperature Minimum Seal Piping Construction A327 Piping Material PIPE_MAT C A328 A330 A331 Other Material Description Aux Piping Plan Construction Aux Piping Plan Material O_MTL_DESC AUX_PLAN_T AUX_PLAN_M C C C 20 1 A332 A337 A342 A343 A346 Other Aux Material Description Seal Flow Indicator Seal Level Switch Type Sea Level Gauge Mechanical Seal Remarks O_AUX_M_D SEAL_FL SEAL_LS_TY SEAL_LG SEAL_RMK C C C C C 20 15 140 SIGHT_FLOW C 1:yes (true); 0:no (false) MANIFOLD_V C 1:yes(true); 0:no(false) A300 A301 A302 A303 A304 A305 A306 A307 A308 A309 A311 A312 A313 SEAL_MFR SEAL_MFR_C CIRC_DEV SLEEVE_MAT GLAND_MATL F_GLAND_TA D_GLAND_TA Q_GLAND_TA FLUSH_T_MI FLUSH_T_MA FLUSH_SG FLUSH_FLUI FLUSH_SP_H FLUSH_VP FLUSH_VP_T C C C C C C C C N N C C N N N 15 15 10 10 1 13 13 13 20 13 13 13 FLUSH_OTHE FLUSH_MAX FLUSH_MIN FLUSH_P_MX FLUSH_P_MIN FLSH_T_MX FLUSH_T_MIN BARR_TM_MN BARR_TM_MX BARR_SG BARR_FLUID BARR_VP_TM BARR_VP_TM C N N N N N N N N C C N B 15 13 13 13 13 13 13 13 13 13 20 13 13 BARR_PR_MX BARR_PR_MN BARR_T_MAX BARR_T_MIN SEAL_PIPE N N N N C 13 13 13 13 1:yes(true); 0:no(false) 1:yes(true); 1:yes(true); 1:yes(true); 1:yes(true); °C °C 0:no(false) 0:no(false) 0:no(false) 0:no(false) KJ/Kg°C kPa abs °C m3/h m3/h kPa kPa °C °C °C °C kPa abs °C kPa kPa °C °C A:tubing; B:piping; C:other; Z:other A:carbon steel; B:stainless steel; C:other; Z:other A:tubing; B:pipe; Z:other; A:carbon steel; B:stainless steel; C:other; Z:other 1:yes (true; 0:no(false) 1:yes (true; 0:no(false) Cooling Water Piping A356 A357 Cooling Water Sight Flow Indicator Cooling Water Manifold Outlet Valve (continued) 25 SPECIFICATION FOR HORIZONTAL END SUCTION CENTRIFUGAL PUMPS FOR CHEMICAL PROCESS ASME B73.1-2001 TABLE B73 STANDARDIZED ELECTRONIC DATA EXCHANGE FILE SPECIFICATION (CONT’D) No Name Field Type Length Contents/Unit A358 Cooling Water Piping Material CW_PIP_MAT C A367 A369 Total Cooling Water Flow Cooling Water Remark TOTAL_FLOW CW_RMK N C 13 140 Temperature Gauges Instrument Remark TEMP_GAGES INST_RMK C C 140 1:yes (true); 0:no (false) Motor Power Motor Speed Motor Remark MTR_POWER MTR_SPEED MTR_RMK N C C 13 13 140 kW RPM PREP_MFR_S C 1:yes (true); 0:no (false) PREP_OTHER SHP_DEST SHP_EXP_BO C C C 20 1 A:domestic; B:export; Z:other 1:yes (true); 0:no (false) A:galvanized pipe; B:copper tube; C:stainless tubing; Z:other m3/h Instrumentation A381 A388 Motor Drive A395 A396 A423 Surface Preparation and Painting A474 A475 A486 A487 Manufacturer Preparation Standard Prep other Shipment Type Export Boxing Required QA Inspection and Test A525 A527 A528 Shop Inspection Hydrostatic Test Performance Test SHOP_INSP HYD PERF C C C 1 A529 NPSH Test NPSH C A532 Dismantle After Test DISM C A538 A539 Other Test Description Other Test DESC_OTH_1 TEST_OTH_1 C C 20 A546 A547 A548 A549 A550 Material Certificate for Casing Material Certificate for Impeller Material Certificate for Shaft Material Certificate for Other Casting Repair Procedure Approval MAT_CER_CA MAT_CER_IM MAT_CER_SH MAT_CER_OT CAS_REP_PR C C C C C 1 20 GEN_RMK1 GEN_RMK2 GEN_RMK3 GEN_RMK4 GEN_RMK5 GEN_RMK6 C C C C C C 254 254 254 254 254 254 CP_G_N_SP C 1:yes (true); 0:no (false) 1:yes( true); 0:no (false) A:non witnessed; B:witnessed; C:observed; D:none; Z:other A:non witnessed; B:witnessed; C:observed; D:none; Z:other A:non witnessed; B:witnessed; C:observed; D:none; Z:other A:nonwitnessed; B:witnessed; C:observed; D:none; Z:other 1:yes (true); 0:no (false) 1:yes (true); 0:no (false) 1:yes (true); 0:no (false) 1:yes(true); 0:no(false) General Remarks A573 A574 A575 A576 A577 A578 General General General General General General Remark Remark Remark Remark Remark Remark Additional Data Construction 8009 Coupling Guard Non-Spark 1:yes (true); 0:no (false) (continued) 26 SPECIFICATION FOR HORIZONTAL END SUCTION CENTRIFUGAL PUMPS FOR CHEMICAL PROCESS ASME B73.1-2001 TABLE B73 STANDARDIZED ELECTRONIC DATA EXCHANGE FILE SPECIFICATION (CONT’D) No Name Field Type Length Contents/Unit Solid Dia SOLID_DIA N 13 Guard Material MTR_MATL C 20 MAX_CAP MAX_CAP SUCTPR_MIN OPT_RATED N N N N 13 13 13 m3/h kPa hr/yr OPT_MAX N hr/yr OPT_NORM N hr/yr OPT_MIN N hr/yr RATED_NPSH N 13 m MAX_NPSH N 13 m NORM_NPSH N 13 m MIN_NPSH N 13 m P012 Maximum Capacity Minimum Capacity Suction Pressure Minimum Operating Time at Rated Capacity Operating Time at Maximum Capacity Operating Time at Normal Capacity Operating Time at Minimum Capacity NPSH Available at Rated Capacity NPSH Available at Maximum Rated Capacity NPSH Available at Normal Capacity NPSH Available at Minimum Capacity System Design SYS_DESIGN C P013 System Control Method SYS_CONTRL C P014 P015 Pumping Temperature Rated Specific Gravity at Rated Temperature Vapor Pressure at Rated Temperature Vapor Pressure at Maximum Temperature Vapor Pressure at Normal Temperature Vapor Pressure at Minimum Temperature Viscosity at Rated Temperature Viscosity at Maximum Temperature Viscosity at Normal Temperature Viscosity at Minimum Temperature Specific Heat at Rated Temperature Specific Heat at Maximum Temperature Specific Heat at Normal Temperature Specific Heat at Minimum Temperature TEMP_RATED SG_RATED N N 13 13 A:stand alone; B:parallel; C:series A:speed; B:flow; D:temperature; E:pressure; F:pi °C VP_RATED N 13 kPa abs VP_MAX N 13 kPa abs VP_NORM N 13 kPa abs VP_MIN N 13 kPa abs VISC_RATED VISC_MAX N N 13 13 cP cP VISC_NORM N 13 cP VISC_MIN N 13 kJ/kg°C SPHT_RATED N 13 kJ/kg°C SPHT_MAX N 13 kJ/kg°C SPHT_NORM N 13 kJ/kg°C SPHT_MIN N 13 kJ/kg°C Liquid B026 Materials B032 PIP Data P001 P002 P003 P004 P005 P006 P007 P008 P009 P010 P011 P016 P017 P018 P019 P020 P021 P022 P023 P024 P025 P026 P027 (continued) 27 SPECIFICATION FOR HORIZONTAL END SUCTION CENTRIFUGAL PUMPS FOR CHEMICAL PROCESS ASME B73.1-2001 TABLE B73 STANDARDIZED ELECTRONIC DATA EXCHANGE FILE SPECIFICATION (CONT’D) No Name Field BP_TEMP BP_PRESS NPSHR_RATE N N N 13 13 13 °C kPa abs m NPSHR_MAX N 13 m NPSHR_NORM N 13 m NPSHR_MIN N 13 m RATED_HEAD N 13 m BEP N 13 m3/h ELEC_HAZRD C 1:yes(true); 0:no(false) P037 Initial Boiling Point Temperature Initial Boiling Point Pressure NPSH Required at Rated Capacity NPSH Required at Maximum Capacity NPSH Required at Normal Capacity NPSH Required at Minimum Capacity Total Differential Head at Rated Impeller Best Efficiency Point for Rated impeller Non Hazardous Electrical Classification Impeller Type IMPLR_TYPE C A:closed; B:semi-opened; C:opened; D:other P038 P039 P040 P041 P042 Other Impeller Type Bearing Manufacturer Bearing isolators Shaft Stiffness Ratio (L3/D4) Lubrication OTHER_IMP BRG_MANUF BRG_ISOL SS_RATIO LUBE_TYPE C C C N C 15 20 25 13 P043 P044 Housing Vent Required Magnetic Drain Plug In Housing Required Oil Cooler Required Seal Spray Guard Required Drain Required Drain Connection Type HSG_VENT MAG_PLUG C C 1 OIL_COOLER SPRAY_GRD DRAIN DRAIN_CONN C C C C 1 1 Cover Material Casing Gasket Material Impeller Gasket Material Casing Fastener Material Gland Fastener Material Bearing Housing Material Bearing Housing Adapter Material Bearing Housing End Seals Driver Selected For Maximum Specific Gravity Driver Selected fo Maximum Viscosity Coupling Type Coupling Size Couplingh Guard Manufacturer’s Standard Coupling Guard Baseplate Mounted Baseplate Type MATL_COVER ML_CSG_GKT ML_IMP_GKT ML_CSG_FST ML_GLD_FST ML_BRG_HSG ML_BRG_HA C C C C C C C 25 25 25 25 25 25 25 ML_BRG_ESL DR_MAX_SG C N 25 13 DR_MAX_VSC N 13 cP CPLING_TYPE CPLING_SIZE CG_MFG_STD C C C 20 20 1:yes(true) 0:no(false) CG_BP_MNT C 1:yes(true) 0:no(false) BP_TYPE C CTR_P_TO_S N 13 A:grouted; B:freestanding; Z:other mm VPC_SUP_BR C 1:yes (true); 0:no (false) BP_DESIGN C A:PIP standard RESP002; B: manufacturer’s standard; Z:other P028 P029 P030 P031 P032 P033 P034 P035 P036 P045 P046 P047 P048 P049 P050 P051 P052 P053 P054 P055 P056 P057 P058 P059 P060 P061 P062 P063 P064 P065 P066 Centerline of Pump to Stilt Bottom Vertical Pump Case Support Bracket Baseplate Design Type Length Contents/Unit 1/mm A:food; B:grease; C:purge mist; E:sheilded; B:seal 1:yes (true) 0:no (false) 1:yes (true); 0:no (false) 1:yes (true) 0:no (false) 1:yes (true) 0:no (false) 1:yes (true) 0:no (false) A:threaded; B:welded and flanged; Z:other (continued) 28 SPECIFICATION FOR HORIZONTAL END SUCTION CENTRIFUGAL PUMPS FOR CHEMICAL PROCESS ASME B73.1-2001 TABLE B73 STANDARDIZED ELECTRONIC DATA EXCHANGE FILE SPECIFICATION (CONT’D) No Name Field P067 P068 Baseplate Remarks Baseplate Paint BP_REMARKS BP_PAINT C C 50 P069 P070 P071 BP_OTH_PNT MTH_STRO DAYS_FI C N N 20 3 Month Day HYDRO_CRT PERF_CRT C C 1 1:yes (true) 0:no (false) 1:yes (true) 0:no (false) P074 P075 Other Baseplate Paint Number of Months of Storage Days Notification Required Final Shop Inspection Hydrostatic Certificate Required Performance Certificate Required NPSHR Certificate Required Vibration Test NPSH_CRT VIBRATION C C 1 P076 P077 P078 P079 Vibration Certificate Required Other Test Certificate Required Material Certificate for Cover Inspection for Connection Welds VIBE_CRT TST_OT_CRT MAT_CER_CV CONN_INSP C C C C 1 1 P080 Inspections for Castings CAST_INSP C 1:yes (true) 0:no (false) A:non-witnessed; B:witnessed; C:none; Z:other 1:yes (true) 0:no (false) 1:yes (true) 0:no (false) 1:yes (true) 0:no (false) A:manufacturer’s standard; B:visual inspection; C:none; Z:other A:manufacturer’s standard; B:visual inspection; C:none Z:other P081 OTH_CINSP C 25 VNDR_DATA C 15 MD_REMARKS C 00 P084 Other Inspection Required for Castings For Vendor Data Requirements Refer to: Manufacturer Documentation Remarks Mechanical Seal Supplied By MS_SUPP_BY C P085 Mechanical Seal Mounted By MS_MNT_BY C P086 P087 P088 Seal Classification Code Seal Model Cartridge or Component Seal Type Seal Design Type MS_CODE SEAL_MODEL MS_TYPE_CC C C C 25 SEAL_DSGN C SEAL_PRTYP C P091 Seal Pressurized or Unpressurized Type Seal Chamber SEALI_CHAM C P092 P093 P094 P095 P096 P097 P098 P099 Seal Chamber Size Throat Bushing Required Throat Bushing Material Other Taps Required Other Taps Required Description Throttle Bushing Required Throttle Bushing Material Primary Flush Plan Number SEAL_CHSIZ THRO_B THRO_B_MAT OT_TAP OSC_OT_TAP THRT_B THRT_B_MAT PR_PI_PL C C C C C C C C 1 20 20 20 P100 Primary Flush Piping/ Tubing Size PR_FL_SIZE N P101 Primary Flush Piping Assembly PR_FL_ASM C P102 Barrier Flush Plan BR_PI_PL C P103 P104 Barrier Fluid Specific heat MAWP of Secondary Seal System BR_FL_SH BR_MAWP N N 13 13 P072 P073 P082 P083 P089 P090 Type Length Contents/Unit A:Manufacturer’s standard; B:Other A:pump manufacturer; B:purchaser; Z:other A:pump manufacturer; B:purchaser; Z:other A:cartridge; B:component; Z:other A:single; B:dual; C:dry gas; D:liquid dual; Z:other A:pressurized; B:unpressurized A:taper bore; B:cylidrical bore; Z:other A:oversized; B:standard; Z:other 1yes (true) 0:no (false) 1yes (true) 0:no (false) 1yes (true) 0:no (false) A:none; B:ASME Plan 7301; C:ASME Plan 7302; D:ASME Plan 7311 mm A:threded; B:unions; C:flanged; D:tube type fittings; E:s A:none; B:ASME Plan 7351; C:ASME Plan 7352; D:ASME Plan 7353 kJ/kg°C kPa (continued) 29 SPECIFICATION FOR HORIZONTAL END SUCTION CENTRIFUGAL PUMPS FOR CHEMICAL PROCESS ASME B73.1-2001 TABLE B73 STANDARDIZED ELECTRONIC DATA EXCHANGE FILE SPECIFICATION (CONT’D) No Name Field Type Length Contents/Unit P105 P106 Barrier Flush Piping/Tubing Size BR_FL_SIZE Barrier Flush Piping Assembly BR_FL_ASM N C 13 P107 Primary Seal Flow Gauge Required Primary Seal Flow Switch Required Primary Seal Temperature Switch Required Primary Seal Pressure Gauge Required Primary Seal Pressure Switch Required Secondary Seal Flow Switch Required Secondary Seal Pressure Gauge SEAL_PFG C mm A:theaded; B:unions; C:flanged; D:tube fittings; E:socket welded 1:yes (true) 0:no (false) SEAL_PFS C 1:yes (true) 0:no (false) SEAL_PTS C 1:yes (true) 0:no (false) SEAL_PPG C 1:yes (true) 0:no (false) SEAL_PPS C 1:yes (true) 0:no (false) SEAL_PSS C 1:yes (true) 0:no (false) SEAL_SPG C 1:yes (true) 0:no (false) P108 P109 P110 P111 P112 P113 GENERAL NOTE: This table is composed of the applicable fields from Appendix Q, ANSI/API 610, Centrifugal Pumps for Petroleum, Heavy-Duty Chemical and Gas Industry Services, with the addition of data fields from the Process Industry Practices (PIP) specification that completely define necessary data for the electronic exchange of ASME B73 pump data See Appendix Q, API 610 for complete information on the neutral data exchange file format 30 ASME B73.1-2001 NONMANDATORY APPENDIX A ASME CENTRIFUGAL PUMP DATA SHEET This data sheet was provided by the Process Industry Practices Initiative (PIP) Copies of the data sheet may be obtained from PIP through their website at http:// www.pip.org 31 ASME B73.1-2001 NONMANDATORY APPENDIX A FORM A1 ASME CENTRIFUGAL PUMP RESP73 PAGE of November 2000 Data Sheet (US Customary Units) Job Number Item Number Req./Spec Number Note: / Indicates Information Completed by Purchaser For Site No Req Manufacturer Purchase Order Number Date Inquiry Number By by Manufacturer Unit by Purchaser or Manufacturer Service Type Pump Size Serial Number Model GENERAL Number Motor Driven Number Turbine Driven Gearbox Item Number Motor Item Number Turbine Item Number Gearbox Provided By Gearbox Mounted By Motor Provided By Turbine Provided By 10 Motor Mounted By Turbine Mounted By 11 OPERATING CONDITIONS 12 Rated Max PERFORMANCE Normal Min Speed (rpm) Performance Curve No 13 Capacity (gpm) 14 Suction Pressure (psig) Measured at Capacity 15 Discharge Pressure (psig) NPSH Req’d (ft.) 16 Differential Pressure (psi) 17 Differential Head (ft.) 18 Hydraulic Power (hp) 19 At Designated Capacity 20 Operating Time (hr./yr.) Allowable Operating Region 21 NPSH Availabl (ft.) Best Efficiency Point for Rated Impeller 22 System Design @ Minimum S.G 24 Series Operation with Item Number Max Normal Min Min Total Differential Head @ Rated Impeller (ft.) Max Differential Head @ Rated Impeller (ft.) Thermal (gpm) Parallel Operation 25 Suction Pressure Min./Max 26 Service Stable (gpm) Impeller Diameter To Rated (gpm) (gpm) / (psig) (bhp) (%) Efficiency Maximum Power @ Rated Impeller Rotation (Viewed from Coupling End) Continuous (In.) Min Max Pump Rated Power (bhp) CW CCW Intermittent (Starts/Day) System Control Method Case Pressure Rating 29 Speed Flow 30 Pressure Pipe Friction Resistance Only 31 32 Normal Suction Specific Speed Stand Alone Operation 28 Max Minimum Continuous Flow Rated 23 27 Rated Level Temperature Max Allowable Working Pressure (psig) (˚F) @ PUMPED FLUID Hydrostatic Test Pressure (psig) SITE CONDITIONS Pumped Fluid 33 Rated 34 Pumping Temperature (˚F) 35 At Designated Temperature 36 Specific Gravity 37 Vapor Pressure (psia) 38 Viscosity (cp) 39 Specific Heat (BTU/Lb ˚F) 40 Initial Boiling Point 41 Liquid Rated Max Max Normal Normal Min Location Indoor Altitude (ft.) Min Outdoor Range of Ambient Temperatures Min./Max / Electrical Classification CL Non Hazardous Div Gr (˚F) GENERAL REMARKS Hazardous (˚F) @ Flammable (psia) Other 42 43 44 45 Corrosion/Erosion Caused By 46 % Solid 47 48 49 50 51 52 REV DATE Max Particle Size (in.) REASON FOR REVISION 32 BY CHECK APPROVED NONMANDATORY APPENDIX A ASME B73.1-2001 FORM A1 ASME CENTRIFUGAL PUMP RESP73 PAGE of November 2000 Data Sheet (US Customary Units) Job Number Item Number Req./Spec Number 53 54 Purchase Order Number / By MECHANICAL DATA COUPLING BETWEEN PUMP AND DRIVER Impeller Type Manufacturer 55 Closed Open Type 56 Semi-open Other Size 57 Casing Mounting Model 58 Foot Centerline Spacer Length (In.) 59 Vertical Inline Close-coupled Coupling Guard Type 60 61 Date Inquiry Number Bearings Manufacturer's Standard Bearings Manufacturer Baseplate Mounted 62 Radial Bearing Type No 63 Thrust Bearing Type No 64 Bearing Isolators 65 Shaft Stiffness Ratio (L3/D4) Non-Spark Coupling Guard Required Remarks 66 Lubrication 67 Flood Pure Mist Shielded (Grease) 68 Grease Purge Mist Sealed (Grease) 69 Constant Level Oiler Required Centerline of Pump to Stilt Bottom 70 Housing Vent Required Vertical Pump Case Support Bracket 71 Magnetic Drain Plug in Housing Required 72 Oil Cooler Required Seal Spray Guard Required 74 Oil Viscosity ISO Grade 76 79 Size Facing Discharge Drain Required Aux Case Connection Size Threaded PIP Standard RESP002 (Data Sheet Attached) Pump Baseplate Manufacturer's Standard Manufacturer's Standard Other Other Shipment Domestic (In.) Welded and Flanged 82 83 Rating Suction 81 Export Export Boxing Required Number of Months of Storage MATERIALS Total Weight (Lbs.) INSPECTION AND TESTING Material Class Code 84 Casing 85 Impeller Test 86 Cover Hydrostatic 87 Shaft Performance 88 Shaft Sleeve NPSHR 89 Baseplate Vibration 90 Casing Gasket Other Days Notification Required Final Inspection Required Non-Witnessed Witnessed 91 Impeller Gasket Dismantle and Inspect After Test 92 Casing Fasteners Casting Repair Procedure Approval Required 93 Bearing Housing 94 Bearing Housing Adapter Casing 95 Bearing Housing End Seals Other Certificate Material Certification Required 96 Coupling Guard 97 Mechanical Seal Gland 98 Mechanical Seal Gland Fasteners Cover Impeller Shaft Inspection Required for Connection Welds Manufacturer's Standard Manufacturer's Standard Horsepower Rating 102 Drive HP Selected or Max S.G 103 Remarks Visual Inspection Other DRIVER 101 Visual Inspection Inspection Required for Castings 99 100 (In.) PAINT AND SHIPMENT PREPARATION Other 80 Free Standing Remarks Nozzle Connections 77 78 Design Grounded Manufacturer's Standard 73 75 BASEPLATE Remarks (hp) Speed & Max Visc (rpm) (cp) MANUFACTURER DOCUMENTATION REQUIREMENTS For Vendor Data Requirements Refer to: Remarks 104 105 106 33 ASME B73.1-2001 NONMANDATORY APPENDIX A FORM A1 ASME CENTRIFUGAL PUMP RESP73 PAGE of November 2000 Data Sheet (US Customary Units) Job Number Item Number Req./Spec Number / 107 108 Supplied By MECHANICAL SEAL Pump Manufacturer 109 Mounted By Pump Manufacturer 110 Seal Classification Code 111 112 113 Purchase Order Number Date Inquiry Number By BARRIER/BUFFER FLUSH SYSTEM Purchaser Purchaser Barrier Flush Plan Barrier Flush Liquid Temperature Min./Max Manufacturer / Model Specific Heat 114 Manufacturer Code Seal Type Cartridge Component 115 Seal Design Single Dual Pressurized Unpressurized 116 (BTU/Lb ˚F) Vapor Pressure / Pressure Required Min./Max Dry Gas (˚F) (psia) @ (psig) (psig) MAWP of Secondary Seal System / Temperature Required Min./Max 117 Seal Chamber Taper Bore Cylindrical Bore Secondary Seal Flush Piping 118 Seal Chamber Size Oversized Standard Material 119 316SS Tubing Pipe Carbon Steel Other 120 Pumping Ring Required 121 Throat Bushing Required Remarks 122 (˚F) Specific Gravity Piping/Tubing Size Materials Piping Assembly (In.) Threaded Unions Tube Type Fittings 123 Flanged Socket Welded Remarks 124 SEAL GLAND 125 126 Taps Required Quench 127 128 SEAL SYSTEM INSTRUMENTATION Drain Primary Seals Other Throttle Bushing Temperature Secondary Seals External Flush Liquid 132 Supply Temperature Min./Max Specific Gravity 134 Specific Heat Flow / (˚F) Level Vapor Pressure 136 Flow Rate Required Min./Max / (gpm) 137 Pressure Required Min./Max / (psig) Temperature Required Min./Max / (˚F) (psia) @ 139 Primary Seal Flush Piping 140 Tubing Material 141 142 143 144 Name of Fluid Other Carbon Steel Piping/Tubing Size Piping Assembly COOLING OR HEATING PIPING PLANS Piping Plan No Other 145 146 Pipe 316SS Pressure (BTU/Lb ˚F) Remarks (˚F) 135 138 Switches Pressure Primary Flush Plan No 131 133 Gauges Flow Materials SEAL FLUSHING 129 130 Flush Unions Tube Type Fittings (˚F) Outlet Temperature (˚F) Rated Flow (gpm) Flanged Supply Pressure (psig) Socket Welded Max Allowable (In.) Threaded Inlet Temperature (psi) P Remarks 147 Galvanized Pipe 148 Sight Flow Indicator 149 Outlet Shut-Off Valve 150 Remarks 151 34 SS Tubing (˚F) NONMANDATORY APPENDIX A ASME B73.1-2001 FORM A2 ASME CENTRIFUGAL PUMP RESP73 PAGE of November 2000 Data Sheet (SI Units) Job Number Item Number Req./Spec Number Note: / Indicates Information Completed by Purchaser Purchase Order Number Date Inquiry Number By by Manufacturer Unit by Purchaser or Manufacturer For Site No Req Pump Size Type Manufacturer Model Serial Number Service GENERAL Number Motor Driven Number Turbine Driven Gearbox Item Number Motor Item Number Turbine Item Number Gearbox Provided By Gearbox Mounted By Motor Provided By Turbine Provided By 10 Motor Mounted By Turbine Mounted By 11 OPERATING CONDITIONS 12 Rated Max PERFORMANCE Normal Min Speed (rpm) Performance Curve No 13 Capacity (m3/h) 14 Suction Pressure (kPa) Measured at Capacity 15 Discharge Pressure (kPa) NPSH Req’d (m) 16 Differential Pressure (kPa) 17 Differential Head (m) 18 Hydraulic Power (kW) 19 At Designated Capacity 20 Operating Time (hr./yr.) Allowable Operating Region 21 NPSH Availabl (m) Best Efficiency Point for Rated Impeller 22 System Design @ Minimum S.G 24 Series Operation with Item Number Max Normal Min Total Differential Head @ Rated Impeller (m) Max Differential Head @ Rated Impeller (m) Thermal (m3/h) Min Parallel Operation 25 Suction Pressure Min./Max 26 Service Stable (m3/h) Impeller Diameter (m3/h) To Rated (m3/h) / (kPa) (bhp) (%) Efficiency Maximum Power @ Rated Impeller Rotation (Viewed from Coupling End) Continuous (mm) Min Max Pump Rated Power (kW) CW CCW Intermittent (Starts/Day) System Control Method Case Pressure Rating 29 Speed Flow 30 Pressure Pipe Friction Resistance Only 31 32 Normal Suction Specific Speed Stand Alone Operation 28 Max Minimum Continuous Flow Rated 23 27 Rated Level Temperature (kPa) Max Allowable Working Pressure (˚C) @ PUMPED FLUID (kPa) Hydrostatic Test Pressure SITE CONDITIONS Pumped Fluid 33 Rated 34 Pumping Temperature (˚C) 35 At Designated Temperature 36 Specific Gravity 37 Vapor Pressure (kPa abs) 38 Viscosity (cp) 39 Specific Heat (kJ/kg ˚C) 40 Initial Boiling Point 41 Liquid Rated Max Max Normal Normal Min Location Indoor Altitude (m) Min Outdoor Range of Ambient Temperatures Min./Max / Electrical Classification CL Non Hazardous Div Gr (˚C) GENERAL REMARKS Hazardous (˚C) @ Flammable (kPa abs) Other 42 43 44 45 Corrosion/Erosion Caused By 46 % Solid 47 48 49 50 51 52 REV DATE Max Particle Size (mm) REASON FOR REVISION 35 BY CHECK APPROVED ASME B73.1-2001 NONMANDATORY APPENDIX A FORM A2 ASME CENTRIFUGAL PUMP RESP73 PAGE of November 2000 Data Sheet (SI Units) Job Number Item Number Req./Spec Number 53 54 / Purchase Order Number Date Inquiry Number By MECHANICAL DATA COUPLING BETWEEN PUMP AND DRIVER Impeller Type Manufacturer 55 Closed Open Type 56 Semi-open Other Size 57 Casing Mounting Model 58 Foot Centerline Spacer Length (mm) 59 Vertical Inline Close-coupled Coupling Guard Type 60 Bearings Manufacturer's Standard 61 Bearings Manufacturer 62 Radial Bearing Type No 63 Thrust Bearing Type No Baseplate Mounted 64 Bearing Isolators 65 Shaft Stiffness Ratio (L3/D4) Non-Spark Coupling Guard Required Remarks 66 Lubrication 67 Flood Pure Mist Shielded (Grease) 68 Grease Purge Mist Sealed (Grease) 69 Constant Level Oiler Required Centerline of Pump to Stilt Bottom 70 Housing Vent Required Vertical Pump Case Support Bracket 71 Magnetic Drain Plug in Housing Required 72 Oil Cooler Required Seal Spray Guard Required 74 Oil Viscosity ISO Grade 76 79 Size Facing Discharge Drain Required Aux Case Connection Size Threaded PIP Standard RESP002 (Data Sheet Attached) Pump Baseplate Manufacturer's Standard Manufacturer's Standard Other Other Shipment Domestic (mm) Welded and Flanged 82 83 Rating Suction 81 Export Export Boxing Required Number of Months of Storage MATERIALS Total Weight (kg) INSPECTION AND TESTING Material Class Code 84 Casing 85 Impeller Test 86 Cover Hydrostatic 87 Shaft Performance 88 Shaft Sleeve NPSHR 89 Baseplate Vibration 90 Casing Gasket Other Days Notification Required Final Inspection Required Non-Witnessed Witnessed 91 Impeller Gasket Dismantle and Inspect After Test 92 Casing Fasteners Casting Repair Procedure Approval Required 93 Bearing Housing 94 Bearing Housing Adapter Casing 95 Bearing Housing End Seals Other Certificate Material Certification Required 96 Coupling Guard 97 Mechanical Seal Gland 98 Mechanical Seal Gland Fasteners Cover Impeller Shaft Inspection Required for Connection Welds Manufacturer's Standard Manufacturer's Standard Horsepower Rating 102 Drive HP Selected or Max S.G 103 Remarks Visual Inspection Other DRIVER 101 Visual Inspection Inspection Required for Castings 99 100 (mm) PAINT AND SHIPMENT PREPARATION Other 80 Free Standing Remarks Nozzle Connections 77 78 Design Grounded Manufacturer's Standard 73 75 BASEPLATE Remarks (kW) Speed & Max Visc (rpm) (cp) MANUFACTURER DOCUMENTATION REQUIREMENTS For Vendor Data Requirements Refer to: Remarks 104 105 106 36 NONMANDATORY APPENDIX A ASME B73.1-2001 FORM A2 ASME CENTRIFUGAL PUMP RESP73 PAGE of November 2000 Data Sheet (SI Units) Job Number Item Number Req./Spec Number / 107 108 Supplied By MECHANICAL SEAL Pump Manufacturer 109 Mounted By Pump Manufacturer 110 Seal Classification Code 111 112 113 Purchase Order Number Date Inquiry Number By BARRIER/BUFFER FLUSH SYSTEM Purchaser Purchaser Barrier Flush Plan Barrier Flush Liquid Temperature Min./Max Manufacturer / Model Specific Heat 114 Manufacturer Code Seal Type Cartridge Component 115 Seal Design Single Dual Pressurized Unpressurized 116 (kJ/kg ˚C) Vapor Pressure Cylindrical Bore Secondary Seal Flush Piping 118 Seal Chamber Size Oversized Standard Material 122 / Temperature Required Min./Max Taper Bore 121 (kPa) (kPa) MAWP of Secondary Seal System Seal Chamber 120 / Pressure Required Min./Max Dry Gas (˚C) (kPa abs) @ 117 119 (˚C) Specific Gravity 316SS Tubing Pipe Carbon Steel Other Sleeve Material Pumping Ring Required Piping/Tubing Size Throat Bushing Required Remarks Materials Piping Assembly (mm) Threaded Unions Tube Type Fittings 123 Flanged Socket Welded Remarks 124 SEAL GLAND 125 126 Taps Required Quench 127 128 Flush Drain Primary Seals Other Throttle Bushing Temperature Secondary Seals External Flush Liquid 132 Supply Temperature Min./Max Specific Gravity 134 Specific Heat Flow / (˚C) Level Vapor Pressure 136 Flow Rate Required Min./Max 137 Pressure Required Min./Max / (kPa) 138 Temperature Required Min./Max / (˚C) (kPa abs) @ 139 Primary Seal Flush Piping 140 Tubing Material 142 143 144 / (m3/h) Other Name of Fluid Carbon Steel Piping/Tubing Size Piping Assembly COOLING OR HEATING PIPING PLANS Piping Plan No Other 145 146 Pipe 316SS Pressure (kJ/kg ˚C) Remarks (˚C) 135 141 Switches Pressure Primary Flush Plan No 131 133 Gauges Flow Materials SEAL FLUSHING 129 130 SEAL SYSTEM INSTRUMENTATION Unions Tube Type Fittings (˚C) Outlet Temperature (˚C) Rated Flow (m3/h) Flanged Supply Pressure (kPa) Socket Welded Max Allowable (mm) Threaded Inlet Temperature (kPa) P Remarks 147 Galvanized Pipe 148 Sight Flow Indicator 149 Outlet Shut-Off Valve 150 Remarks 151 37 SS Tubing (˚C) ASME Services ASME is committed to developing and delivering technical information At ASME’s Information Central, we make every effort to answer your questions and expedite your orders Our representatives are ready to assist you in the following areas: ASME Press Codes & Standards Credit Card Orders IMechE Publications Meetings & Conferences Member Dues Status Member Services & Benefits Other ASME Programs Payment Inquiries Professional Development Short Courses Publications Public Information Self-Study Courses Shipping Information Subscriptions/Journals/Magazines Symposia Volumes Technical Papers How can you reach us? 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