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API - API 11A - INFORMATION ON API STD 11-A: OIL WELL PUMPS Organization: API
Date: 1941-10-01
API - API STD 11E1 - API SPECIFICATION FOR RATING OF ROLLER-CHAIN SPEED REDUCERS FOR PUMPING MACHINES Organization: API
API - API STD 674 - POSITIVE DISPLACEMENT PUMPS-RECIPROCATING - THIRD EDITION; ERTA: MAY 2014; ERTA 2: APRIL 2015 Organization: API
Date: 2010-12-01
Description: Controlled-volume pumps, hydraulically driven pumps, and rotary pumps are not included. Note: See API 675 for controlled-volume pumps and API 676 for rotary pumps.
API - API STD 676 - POSITIVE DISPLACEMENT PUMPS - ROTARY - THIRD EDITION Organization: API
Date: 2009-11-01
Description: Controlled-volume pumps, hydraulically driven pumps and positive displacement reciprocating pumps are not included (see API 674 for positive displacement reciprocating pumps and API 675 for controlled-volume pumps). For rotary positive displacement pumps in auxiliary services (e.g. lube oil systems), manufacturer’s standard with demonstrated experience is acceptable.
API - API STD 11E - SPECIFICATION FOR PUMPING UNITS - ELEVENTH EDITION; SUPP 1: DECEMBER 1972; SUPP 2: MARCH 1981 Organization: API
Date: 1971-01-01
Description: This specification covers the design and rating of the following: a. Pumping-unit structure. b. Pumping-unit gear reducer. c. Pumping-unit chain reducer.
API - API SPEC 11E - SPECIFICATION FOR PUMPING UNITS - NINETEENTH EDITION; EFFECTIVE DATE: MAY 1, 2014; ERTA: AUGUST 2015 Organization: API
Date: 2013-11-01
Description: This includes the following: a) beam pump structures, b) pumping unit gear reducer, and c) pumping unit chain reducer.
PIP RECP001 - DESIGN OF PUMPING SYSTEMS THAT USE CENTRIFUGAL PUMPS Organization: PIP
Date: 2008-12-01
Description: Application limits for ASME B73 and API 610 OH1, OH2, OH3, and OH6 pumps are provided. Purpose This Practice provides requirements for design of pumping systems that use centrifugal pumps.
API - API STD 682 - PUMPS - SHAFT SEALING SYSTEMS FOR CENTRIFUGAL AND ROTARY PUMPS - FOURTH EDITION Organization: API
Date: 2014-05-01
Description: This standard is referenced normatively in API 610. It is applicable to both new and retrofitted pumps and to pumps other than API 610 pumps (e.g.
EEMUA PUB NO 164 - SEAL-LESS CENTRIFUGAL PUMPS: CLASS 1 - INCORPORTED AMENDMENT: MAY 23,2002 Organization: EEMUA
Date: 1993-01-01
Description: It is presented in the format of an API standard and uses selected clauses from API 610. It is intended to cover applications for which any of the following parameters are exceeded.
API - API STD 11AX - SPECIFICATION FOR SUBSURFACE PUMPS AND FITTINGS - SIXTH EDITION Organization: API
Date: 1971-03-01
Description: These specifications are not intended to inhibit purchasers and producers from purchasing or producing products made to specifications other than API, and nothing in any API specification is intended to in any way inhibit the purchase of products from companies not authorized to use the API program.
API - API BULL 11L3 - SUCKER ROD PUMPING SYSTEM DESIGN BOOK - FIRST EDITION; ERTA: NOVEMBER 1973; SUPP 1: FEBRUARY 1977 Organization: API
Date: 1970-05-01
Description: The purpose of this bulletin is to present tabular material derived from the application of a computer program to portions of the material in API RP 11L; Design Calculations for Sucker Rod Pumping Systems (First Edition, March 1967).
PIP RESP004 - LIQUID RING VACUUM PUMPS AND COMPRESSORS SPECIFICATION Organization: PIP
Date: 2014-01-01
Description: Comment: This Practice can be used in conjunction with API 681. A liquid ring machine data sheet, RESP004-DM/D, is included with this Practice.
DSF/PREN ISO 21049 - PUMPS - SHAFT-SEALING SYSTEMS FOR CENTRIFUGAL AND ROTARY PUMPS (ISO/DIS 21049:2010) Organization: DS
Description: It is applicable to both new and retrofitted pumps, and to pumps other than ISO 13709 pumps (e.g. ASME B73.1, ASME B73.2 and API 676 pumps). This International Standard might also be referenced by other machinery standards such as other pumps, compressors and agitators.
API - API BULL 2520 - API BULLETIN ON USE OF VARIABLE-VAPOR-SPACE SYSTEMS TO REDUCE EVAPORATION LOSS Organization: API
Date: 1964-09-01
Description: This is called balanced pumping. Filling losses are reduced in these systems whenever balanced pumping occurs. Also, there may be unused expansion capacity available during the filling of tanks which will further reduce loss.
ISO 13710 - PETROLEUM, PETROCHEMICAL AND NATURAL GAS INDUSTRIES RECIPROCATING POSITIVE DISPLACEMENT PUMPS - FIRST EDITION Organization: ISO
Date: 2004-07-01
Description: This International Standard is not applicable to controlled-volume pumps and rotary pumps. NOTE For controlled-volume pumps see API Std 675; for rotary pumps see API Std 676.
ISO DIS 13710 - PETROLEUM, PETROCHEMICAL AND NATURAL GAS INDUSTRIES — RECIPROCATING POSITIVE DISPLACEMENT PUMPS Organization: ISO
Date: 2010-11-11
Description: This International Standard is not applicable to controlled-volume pumps and rotary pumps. NOTE For controlled-volume pumps see API Std 675; for rotary pumps see API Std 676.
ISO 13709 - CENTRIFUGAL PUMPS FOR PETROLEUM, PETROCHEMICAL AND NATURAL GAS INDUSTRIES - SECOND EDITION; INCLUDES ACCESS TO ADDITIONAL CONTENT Organization: ISO
Date: 2009-12-15
Description: NOTE For sealless pumps, reference can be made to API Std 685. For heavy duty pump applications in industries other than petroleum, petrochemical and gas processing, reference can be made to ISO 9905.
DS/EN ISO 13709 CD-ROM - CENTRIFUGAL PUMPS FOR PETROLEUM, PETROCHEMICAL AND NATURAL GAS INDUSTRIES Organization: DS
Date: 2010-01-13
Description: Relevant industry operating experience suggests pumps produced to this International Standard are cost effective when pumping liquids at conditions exceeding any one of the following: . discharge pressure (gauge) 1 900 kPa (275 psi; 19,0 bar) . suction pressure (gauge) 500 kPa (75 psi; 5,17 bar) . pumping temperature 150 °C (300 °F) . rotative speed 3 600 r/min . rated total head 120 m (400 ft) . impeller diameter, overhung pumps 330 mm (13 in) NOTE For sealless pumps, reference can be made to API Std 685. For heavy duty pump applications in industries other than petroleum, petrochemical and gas processing, reference can be made to ISO 9905.
API - API STD 610 - CENTRIFUGAL PUMPS FOR PETROLEUM, PETROCHEMICAL AND NATURAL GAS INDUSTRIES - ELEVENTH EDITION; INCORPORATES ERRATA: JULY 2011; ISO 13709:2009 ADOPTION Organization: API
Date: 2010-09-01
Description: Relevant industry operating experience suggests pumps produced to this International Standard are cost effective when pumping liquids at conditions exceeding any one of the following: — discharge pressure (gauge) 1 900 kPa (275 psi; 19,0 bar) — suction pressure (gauge) 500 kPa (75 psi; 5,0 bar) — pumping temperature 150 °C (300 °F) — rotative speed 3 600 r/min — rated total head 120 m (400 ft) — impeller diameter, overhung pumps 330 mm (13 in) NOTE For sealless pumps, reference can be made to API Std 685. For heavy duty pump applications in industries other than petroleum, petrochemical and gas processing, reference can be made to ISO 9905.
API - API RP 11G - RECOMMENDED PRACTICE FOR INSTALLATION, MAINTENANCE, AND LUBRICATION OF PUMPING UNITS - FIFTH EDITION Organization: API
Date: 2013-11-01
Description: This recommended practice provides guidance related to the proper installation, care, and maintenance of surface mounted beam pumping units, varieties of which are described in API 11E. Information provided in this document is of a general nature and is not intended to replace specific instruction provided by the pumping unit manufacturer.

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