sjkocher 2020-06-25T11:18:07-05:00 Acrobat PDFMaker 17 for Word 2026-08-19T14:50:13+02:00 Adobe PDF Library 15.0 Engineering Office Revised Approve Process Equipment Skill Center 5-11 Centrifugal Pumps 5-11-13 Centrifugal Pumps https://pmtqualtrax.honeywell.com/ UOP 00009250 Standard Specifications Des Plaines 13 General D:20200625155656 6/25/2020 3:51:26 PM 1/22/2016 1:43:30 PM 6/25/2020 3:51:13 PM Van De Cotte, Michael R Varma, Naveen has not Approved, Van De Cotte, Michael R has not Approved, Daly, Phillip F has not Approved 3/16/2023 12:00:00 AM Varma, Naveen, Van De Cotte, Michael R, Daly, Phillip F Varma, Naveen has not Approved Van De Cotte, Michael R has not Approved Daly, Phillip F has not Approved https://pmtqualtrax.honeywell.com/ No Approvals on Record yet updated Header and Revision 5 Walter, William Christian Updated Header 9250 Office 2007 Word Document With Macros DOCM 2026-08-19T14:50:13+02:00 2020-06-25T11:18:07-05:00 2026-08-19T14:50:13+02:00 Acrobat PDFMaker 17 for Word uuid:3634d3ba-9053-4979-8b89-fe73748a2690 uuid:af2ed9ba-e0f2-4b2f-8602-7e6e049cdee2 4 application/pdf sjkocher Adobe PDF Library 15.0 D:20200625155656 UOP Varma, Naveen has not Approved, Van De Cotte, Michael R has not Approved, Daly, Phillip F has not Approved Varma, Naveen has not Approved Van De Cotte, Michael R has not Approved Daly, Phillip F has not Approved Varma, Naveen, Van De Cotte, Michael R, Daly, Phillip F 3/16/2023 12:00:00 AM 1/22/2016 1:43:30 PM 6/25/2020 3:51:26 PM 6/25/2020 3:51:13 PM Van De Cotte, Michael R Walter, William Christian Updated Header DOCM Office 2007 Word Document With Macros 9250 No Approvals on Record yet 5 updated Header and Revision https://pmtqualtrax.honeywell.com/ https://pmtqualtrax.honeywell.com/ Approve 5-11-13 Centrifugal Pumps 5-11 Centrifugal Pumps Revised Engineering Office Process Equipment Skill Center Standard Specifications Des Plaines General 13 00009250 4 engines={image=false textcolor=true vector=false text=true} tetml={filename={D:\drim\repository\projects\drim_13_0\metadata\6\a\6aaeee3a4f6a1e644e3315c43728ae8d\6aaeee3a4f6a1e644e3315c43728ae8d.para.xml} elements={annotations=false bookmarks=false destinations=false fields=false javascripts=false} } granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} Revision R e v i s i o n Indication I n d i c a t i o n UOP U O P Engineering E n g i n e e r i n g Department D e p a r t m e n t CENTRIFUGAL C E N T R I F U G A L PUMPS P U M P S STANDARD S T A N D A R D SPECIFICATION S P E C I F I C A T I O N 5-11-14 5 - 1 1 - 1 4 Page P a g e 1 1 of o f 6 6 DATE D A T E STATUS S T A T U S SPNSR S P N S R APVD A P V D 16JUN20 1 6 J U N 2 0 Reaffirmed R e a f f i r m e d MRV M R V PFD P F D 1. 1 . GENERAL G E N E R A L 1.1 1 . 1 Scope S c o p e CONFIDENTIAL C O N F I D E N T I A L – – The T h e information i n f o r m a t i o n in i n this t h i s document d o c u m e n t is i s confidential c o n f i d e n t i a l and a n d must m u s t not n o t be b e used u s e d for f o r any a n y purpose, p u r p o s e , duplicated, d u p l i c a t e d , or o r disclosed d i s c l o s e d to t o others o t h e r s without w i t h o u t UOP's U O P ' s written w r i t t e n permission. p e r m i s s i o n . a. a . This T h i s Standard S t a n d a r d Specification S p e c i f i c a t i o n covers c o v e r s the t h e design d e s i g n of o f American A m e r i c a n Petroleum P e t r o l e u m Institute I n s t i t u t e (API) ( A P I ) Standard S t a n d a r d 610, 6 1 0 , Centrifugal C e n t r i f u g a l Pumps P u m p s for f o r Petroleum, P e t r o l e u m , Petrochemical P e t r o c h e m i c a l and a n d Natural N a t u r a l Gas G a s Industries, I n d u s t r i e s , single s i n g l e stage s t a g e overhung, o v e r h u n g , between b e t w e e n bearing, b e a r i n g , multi-stage, m u l t i - s t a g e , and a n d high h i g h speed s p e e d integral i n t e g r a l gear g e a r pumps, p u m p s , and a n d hydraulic h y d r a u l i c power p o w e r recovery r e c o v e r y turbines. t u r b i n e s . b. b . Exceptions E x c e p t i o n s or o r variations v a r i a t i o n s shown s h o w n in i n the t h e UOP U O P Project P r o j e c t Specifications S p e c i f i c a t i o n s take t a k e precedence p r e c e d e n c e over o v e r requirements r e q u i r e m e n t s shown s h o w n herein. h e r e i n . 1.2 1 . 2 References R e f e r e n c e s 2. 2 . DESIGN D E S I G N Unless U n l e s s noted n o t e d below, b e l o w , use u s e the t h e edition e d i t i o n and a n d addenda a d d e n d a of o f each e a c h referenced r e f e r e n c e d document d o c u m e n t current c u r r e n t on o n the t h e date d a t e of o f this t h i s Standard S t a n d a r d Specification. S p e c i f i c a t i o n . When W h e n a a referenced r e f e r e n c e d document d o c u m e n t incorporates i n c o r p o r a t e s another a n o t h e r document, d o c u m e n t , use u s e the t h e edition e d i t i o n of o f that t h a t document d o c u m e n t required r e q u i r e d by b y the t h e referenced r e f e r e n c e d document. d o c u m e n t . a. a . American A m e r i c a n Petroleum P e t r o l e u m Institute I n s t i t u t e (API) ( A P I ) Standard S t a n d a r d 610, 6 1 0 , “Centrifugal “ C e n t r i f u g a l Pumps P u m p s for f o r Petroleum, P e t r o l e u m , Petrochemical P e t r o c h e m i c a l and a n d Natural N a t u r a l Gas G a s Industries” I n d u s t r i e s ” b. b . API A P I Standard S t a n d a r d 613, 6 1 3 , “Special “ S p e c i a l Purpose P u r p o s e Gear G e a r Units U n i t s for f o r Petroleum, P e t r o l e u m , Chemical C h e m i c a l and a n d Gas G a s Industry I n d u s t r y Services” S e r v i c e s ” c. c . API A P I Standard S t a n d a r d 677, 6 7 7 , “General “ G e n e r a l Purpose P u r p o s e Gear G e a r Units U n i t s for f o r Petroleum, P e t r o l e u m , Chemical C h e m i c a l and a n d Gas G a s Industry I n d u s t r y Services” S e r v i c e s ” d. d . American A m e r i c a n Society S o c i e t y for f o r Testing T e s t i n g and a n d Materials M a t e r i a l s (ASTM), ( A S T M ) , A A 193, 1 9 3 , A A 194, 1 9 4 , A A 216, 2 1 6 , A A 494, 4 9 4 , B B 865 8 6 5 e. e . American A m e r i c a n Society S o c i e t y of o f Mechanical M e c h a n i c a l Engineers E n g i n e e r s (ASME) ( A S M E ) B16.5, B 1 6 . 5 , “Pipe “ P i p e Flanges F l a n g e s and a n d Flanged F l a n g e d Fittings, F i t t i n g s , NPS N P S ½ ½ through t h r o u g h NPS N P S 24 2 4 Metric/Inch M e t r i c / I n c h Standard” S t a n d a r d ” f. f . ASME A S M E Boiler B o i l e r and a n d Pressure P r e s s u r e Vessel V e s s e l Code, C o d e , Section S e c t i o n VIII, V I I I , Division D i v i s i o n 1, 1 , Pressure P r e s s u r e Vessels V e s s e l s g. g . ASME A S M E B46.1,” B 4 6 . 1 , ” Surface S u r f a c e Texture T e x t u r e (Surface ( S u r f a c e Roughness, R o u g h n e s s , Waviness, W a v i n e s s , and a n d Lay)” L a y ) ” h. h . Standards S t a n d a r d s of o f the t h e Tubular T u b u l a r Exchanger E x c h a n g e r Manufacturers M a n u f a c t u r e r s Association A s s o c i a t i o n (TEMA) ( T E M A ) i. i . National, N a t i o n a l , state, s t a t e , and a n d local l o c a l governmental g o v e r n m e n t a l regulations r e g u l a t i o n s and a n d laws l a w s This T h i s standard s t a n d a r d is i s intended i n t e n d e d to t o be b e used u s e d as a s an a n addendum a d d e n d u m to t o API A P I Standard S t a n d a r d 610. 6 1 0 . Numbering N u m b e r i n g in i n this t h i s section s e c t i o n coincides c o i n c i d e s with w i t h actual a c t u a l paragraph p a r a g r a p h numbers n u m b e r s from f r o m API A P I Standard S t a n d a r d 610. 6 1 0 . 11 1 1 th t h Edition. E d i t i o n . Form F o r m QUA-03-5 Q U A - 0 3 - 5 Qualtrax Q u a l t r a x 9250 9 2 5 0 granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} Revision R e v i s i o n Indication I n d i c a t i o n UOP U O P Engineering E n g i n e e r i n g Department D e p a r t m e n t CENTRIFUGAL C E N T R I F U G A L PUMPS P U M P S STANDARD S T A N D A R D SPECIFICATION S P E C I F I C A T I O N 5-11-14 5 - 1 1 - 1 4 Page P a g e 2 2 of o f 6 6 DATE D A T E STATUS S T A T U S SPNSR S P N S R APVD A P V D 16JUN20 1 6 J U N 2 0 Reaffirmed R e a f f i r m e d MRV M R V PFD P F D 6.1 6 . 1 General G e n e r a l Paragraph P a r a g r a p h 6.1.1, 6 . 1 . 1 , Addition/Clarification A d d i t i o n / C l a r i f i c a t i o n CONFIDENTIAL C O N F I D E N T I A L – – The T h e information i n f o r m a t i o n in i n this t h i s document d o c u m e n t is i s confidential c o n f i d e n t i a l and a n d must m u s t not n o t be b e used u s e d for f o r any a n y purpose, p u r p o s e , duplicated, d u p l i c a t e d , or o r disclosed d i s c l o s e d to t o others o t h e r s without w i t h o u t UOP's U O P ' s written w r i t t e n permission. p e r m i s s i o n . Centrifugal C e n t r i f u g a l pumps p u m p s shall s h a l l comply c o m p l y with w i t h the t h e requirements r e q u i r e m e n t s of o f API A P I 610, 6 1 0 , except e x c e p t where w h e r e modified m o d i f i e d by b y the t h e UOP U O P Project P r o j e c t Specification(s). S p e c i f i c a t i o n ( s ) . Vendor's V e n d o r ' s offering o f f e r i n g shall s h a l l be b e a a size s i z e and a n d design d e s i g n which w h i c h has h a s a a successful s u c c e s s f u l record r e c o r d of o f proven p r o v e n field f i e l d service s e r v i c e at a t operating o p e r a t i n g conditions c o n d i t i o n s similar s i m i l a r to t o those t h o s e specified s p e c i f i e d (proto-types ( p r o t o - t y p e s are a r e not n o t acceptable). a c c e p t a b l e ) . An A n installation i n s t a l l a t i o n list l i s t shall s h a l l be b e submitted s u b m i t t e d upon u p o n request. r e q u e s t . Paragraph P a r a g r a p h 6.1.3, 6 . 1 . 3 , Addition A d d i t i o n Single S i n g l e and a n d two-stage t w o - s t a g e pumps p u m p s operating o p e r a t i n g at a t temperatures t e m p e r a t u r e s less l e s s than t h a n 300°F 3 0 0 ° F (150°C) ( 1 5 0 ° C ) and a n d multi-stage m u l t i - s t a g e pumps p u m p s operating o p e r a t i n g at a t temperatures t e m p e r a t u r e s less l e s s than t h a n 200°F 2 0 0 ° F (93°C) ( 9 3 ° C ) shall s h a l l be b e suitable s u i t a b l e for f o r instantaneous i n s t a n t a n e o u s startup s t a r t u p from f r o m ambient a m b i e n t to t o full f u l l operating o p e r a t i n g temperature. t e m p e r a t u r e . For F o r higher h i g h e r operating o p e r a t i n g temperatures t e m p e r a t u r e s the t h e vendor v e n d o r shall s h a l l provide p r o v i d e as a s part p a r t of o f the t h e operating o p e r a t i n g manual m a n u a l a a suitable s u i t a b l e startup s t a r t u p procedure p r o c e d u r e and a n d any a n y required r e q u i r e d monitoring m o n i t o r i n g equipment e q u i p m e n t (i.e., ( i . e . , skin s k i n thermocouples) t h e r m o c o u p l e s ) to t o assure a s s u r e that t h a t the t h e pump, p u m p , including i n c l u d i n g seal(s), s e a l ( s ) , does d o e s not n o t incur i n c u r damage d a m a g e due d u e to t o rapid r a p i d heat h e a t up. u p . Paragraph P a r a g r a p h 6.1.8, 6 . 1 . 8 , Addition A d d i t i o n UOP U O P requires r e q u i r e s an a n NPSH N P S H margin m a r g i n of o f 2 2 feet f e e t (0.6 ( 0 . 6 meters) m e t e r s ) or o r 15% 1 5 % of o f the t h e NPSH N P S H required, r e q u i r e d , whichever w h i c h e v e r is i s greater. g r e a t e r . This T h i s margin m a r g i n is i s included i n c l u d e d in i n the t h e system s y s t e m calculations. c a l c u l a t i o n s . It I t is i s not n o t included i n c l u d e d in i n the t h e NPSH N P S H available a v a i l a b l e reported r e p o r t e d in i n the t h e data d a t a sheets. s h e e t s . The T h e pump p u m p NPSH N P S H required r e q u i r e d must m u s t be b e less l e s s than t h a n or o r equal e q u a l to t o the t h e NPSH N P S H available a v a i l a b l e reported r e p o r t e d in i n the t h e data d a t a sheets. s h e e t s . Inducers I n d u c e r s are a r e not n o t permitted, p e r m i t t e d , except e x c e p t for f o r API A P I 610 6 1 0 pump p u m p type t y p e OH6. O H 6 . Paragraph P a r a g r a p h 6.1.9, 6 . 1 . 9 , Addition A d d i t i o n The T h e suction s u c t i o n specific s p e c i f i c speed s p e e d shall s h a l l not n o t exceed e x c e e d 11,000 1 1 , 0 0 0 (USGPM, ( U S G P M , ft.), f t . ) , 13000 1 3 0 0 0 (M3/hr, ( M 3 / h r , meters). m e t e r s ) . The T h e suction s u c t i o n specific s p e c i f i c speed s p e e d of o f pumps p u m p s over o v e r 100 1 0 0 HP H P (75 ( 7 5 kW) k W ) per p e r stage s t a g e in i n water, w a t e r , or o r aqueous a q u e o u s solution s o l u t i o n over o v e r 50% 5 0 % water, w a t e r , services s e r v i c e s shall s h a l l not n o t exceed e x c e e d 9500 9 5 0 0 (USGPM, ( U S G P M , ft.), f t . ) , 11000 1 1 0 0 0 (M3/hr, ( M 3 / h r , meters). m e t e r s ) . Suction S u c t i o n specific s p e c i f i c speeds s p e e d s of o f up u p to t o 24000 2 4 0 0 0 (USGPM, ( U S G P M , ft) f t ) are a r e acceptable a c c e p t a b l e for f o r high h i g h speed s p e e d integrally i n t e g r a l l y gear g e a r driven d r i v e n type t y p e pumps p u m p s (Pump ( P u m p type t y p e OH6) O H 6 ) Form F o r m QUA-03-5 Q U A - 0 3 - 5 Qualtrax Q u a l t r a x 9250 9 2 5 0 granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} Revision R e v i s i o n Indication I n d i c a t i o n UOP U O P Engineering E n g i n e e r i n g Department D e p a r t m e n t CENTRIFUGAL C E N T R I F U G A L PUMPS P U M P S STANDARD S T A N D A R D SPECIFICATION S P E C I F I C A T I O N 5-11-14 5 - 1 1 - 1 4 Page P a g e 3 3 of o f 6 6 DATE D A T E STATUS S T A T U S SPNSR S P N S R APVD A P V D 16JUN20 1 6 J U N 2 0 Reaffirmed R e a f f i r m e d MRV M R V PFD P F D Paragraph P a r a g r a p h 6.1.11, 6 . 1 . 1 1 , Addition A d d i t i o n Pumps P u m p s shall s h a l l have h a v e stable s t a b l e head/capacity h e a d / c a p a c i t y curves c u r v e s which w h i c h continuously c o n t i n u o u s l y rise r i s e to t o minimum m i n i m u m continuous c o n t i n u o u s flow. f l o w . CONFIDENTIAL C O N F I D E N T I A L – – The T h e information i n f o r m a t i o n in i n this t h i s document d o c u m e n t is i s confidential c o n f i d e n t i a l and a n d must m u s t not n o t be b e used u s e d for f o r any a n y purpose, p u r p o s e , duplicated, d u p l i c a t e d , or o r disclosed d i s c l o s e d to t o others o t h e r s without w i t h o u t UOP's U O P ' s written w r i t t e n permission. p e r m i s s i o n . Paragraph P a r a g r a p h 6.1.28, 6 . 1 . 2 8 , Clarification C l a r i f i c a t i o n Pumps P u m p s shall s h a l l be b e designed d e s i g n e d to t o operate o p e r a t e in i n a a totally t o t a l l y unprotected, u n p r o t e c t e d , outdoor o u t d o o r environment. e n v i r o n m e n t . Paragraph P a r a g r a p h 6.1.35, 6 . 1 . 3 5 , New N e w Pumps P u m p s shall s h a l l be b e designed d e s i g n e d for f o r continuous c o n t i n u o u s operation o p e r a t i o n at a t a a minimum m i n i m u m of o f 50°F 5 0 ° F (28°C) ( 2 8 ° C ) higher h i g h e r than t h a n specified s p e c i f i e d maximum m a x i m u m operating o p e r a t i n g temperature. t e m p e r a t u r e . 6.3 6 . 3 Paragraph P a r a g r a p h 6.1.36, 6 . 1 . 3 6 , New N e w Paragraph P a r a g r a p h 6.3.1, 6 . 3 . 1 , Addition A d d i t i o n Contractor C o n t r a c t o r to t o verify v e r i f y that t h a t downstream d o w n s t r e a m equipment, e q u i p m e n t , piping, p i p i n g , and a n d instrumentation i n s t r u m e n t a t i o n design d e s i g n pressures p r e s s u r e s are a r e adequate a d e q u a t e for f o r the t h e actual a c t u a l shutoff s h u t o f f pressure p r e s s u r e of o f purchased p u r c h a s e d pumps. p u m p s . The T h e design d e s i g n pressure p r e s s u r e of o f downstream d o w n s t r e a m equipment e q u i p m e n t was w a s established e s t a b l i s h e d by b y UOP U O P based b a s e d on o n estimated e s t i m a t e d pump p u m p shutoff s h u t o f f pressure. p r e s s u r e . Pump P u m p shutoff s h u t o f f pressure p r e s s u r e was w a s estimated e s t i m a t e d as a s follows: f o l l o w s : a. a . Fixed F i x e d speed s p e e d motor m o t o r driven d r i v e n pumps p u m p s Est. E s t . Shutoff S h u t o f f Pressure P r e s s u r e = = P P max. m a x . suction s u c t i o n + + 1.25*(∆P 1 . 2 5 * ( ∆ P rated). r a t e d ) . b. b . Steam S t e a m turbine t u r b i n e driven d r i v e n pumps p u m p s Est. E s t . Pump P u m p Shutoff S h u t o f f Pressure P r e s s u r e = = P P max. m a x . suction s u c t i o n + + 1.38*(∆P 1 . 3 8 * ( ∆ P rated) r a t e d ) NOTE: N O T E : The T h e rated r a t e d pump p u m p differential d i f f e r e n t i a l is i s based b a s e d on o n pumped p u m p e d fluid f l u i d maximum m a x i m u m specific s p e c i f i c gravity. g r a v i t y . 6.4 6 . 4 Nozzles N o z z l e s and a n d Pressure P r e s s u r e casing c a s i n g Connections C o n n e c t i o n s Paragraph P a r a g r a p h 6.4.2.3, 6 . 4 . 2 . 3 , Addition A d d i t i o n Flange F l a n g e classes c l a s s e s are a r e specified s p e c i f i e d in i n accordance a c c o r d a n c e with w i t h ASME A S M E B16.5. B 1 6 . 5 . Flange F l a n g e classes c l a s s e s listed l i s t e d in i n the t h e UOP U O P Project P r o j e c t Specifications S p e c i f i c a t i o n s are a r e based b a s e d upon u p o n design d e s i g n pressure p r e s s u r e and a n d temperature t e m p e r a t u r e conditions c o n d i t i o n s only, o n l y , and a n d do d o not n o t account a c c o u n t for f o r other o t h e r loads. l o a d s . The T h e final f i n a l design d e s i g n of o f all a l l flanges f l a n g e s shall s h a l l account a c c o u n t for f o r gasket g a s k e t seating s e a t i n g and a n d external e x t e r n a l loads. l o a d s . Differential D i f f e r e n t i a l thermal t h e r m a l expansion e x p a n s i o n of o f dissimilar d i s s i m i l a r joints j o i n t s and a n d transient t r a n s i e n t thermal t h e r m a l conditions c o n d i t i o n s such s u c h as a s start-up/shutdown s t a r t - u p / s h u t d o w n and a n d operational o p e r a t i o n a l upset u p s e t shall s h a l l be b e accommodated. a c c o m m o d a t e d . Flanges F l a n g e s intended i n t e n d e d for f o r use u s e with w i t h spiral s p i r a l wound w o u n d gaskets g a s k e t s shall s h a l l have h a v e a a flange f l a n g e surface s u r f a c e finish f i n i s h of o f 125 1 2 5 microinch m i c r o i n c h Ra R a minimum m i n i m u m to t o 250 2 5 0 microinch m i c r o i n c h Ra R a maximum. m a x i m u m . Flanges F l a n g e s intended i n t e n d e d for f o r Form F o r m QUA-03-5 Q U A - 0 3 - 5 Qualtrax Q u a l t r a x 9250 9 2 5 0 granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} Revision R e v i s i o n Indication I n d i c a t i o n UOP U O P Engineering E n g i n e e r i n g Department D e p a r t m e n t CENTRIFUGAL C E N T R I F U G A L PUMPS P U M P S STANDARD S T A N D A R D SPECIFICATION S P E C I F I C A T I O N 5-11-14 5 - 1 1 - 1 4 Page P a g e 4 4 of o f 6 6 DATE D A T E STATUS S T A T U S SPNSR S P N S R APVD A P V D 16JUN20 1 6 J U N 2 0 Reaffirmed R e a f f i r m e d MRV M R V PFD P F D use u s e with w i t h other o t h e r gaskets g a s k e t s shall s h a l l have h a v e a a flange f l a n g e surface s u r f a c e finish f i n i s h within w i t h i n the t h e optimal o p t i m a l range r a n g e for f o r the t h e specified s p e c i f i e d gasket. g a s k e t . Finishes F i n i s h e s shall s h a l l be b e judged j u d g e d by b y visual v i s u a l comparison c o m p a r i s o n with w i t h surface s u r f a c e finish f i n i s h roughness r o u g h n e s s standards s t a n d a r d s conforming c o n f o r m i n g to t o ASME A S M E B46.1. B 4 6 . 1 . Flange F l a n g e finishes f i n i s h e s shall s h a l l be b e protected p r o t e c t e d from f r o m damage d a m a g e during d u r i n g fabrication, f a b r i c a t i o n , heat h e a t treatment, t r e a t m e n t , shipping, s h i p p i n g , storage, s t o r a g e , and a n d installation. i n s t a l l a t i o n . CONFIDENTIAL C O N F I D E N T I A L – – The T h e information i n f o r m a t i o n in i n this t h i s document d o c u m e n t is i s confidential c o n f i d e n t i a l and a n d must m u s t not n o t be b e used u s e d for f o r any a n y purpose, p u r p o s e , duplicated, d u p l i c a t e d , or o r disclosed d i s c l o s e d to t o others o t h e r s without w i t h o u t UOP's U O P ' s written w r i t t e n permission. p e r m i s s i o n . 6.7 6 . 7 Wear W e a r Rings R i n g s and a n d Running R u n n i n g Clearances C l e a r a n c e s Paragraph P a r a g r a p h 6.7.4, 6 . 7 . 4 , Addition A d d i t i o n When W h e n non-metallic n o n - m e t a l l i c wear w e a r ring r i n g materials m a t e r i a l s are a r e specified, s p e c i f i e d , the t h e pump p u m p vendor v e n d o r shall s h a l l state s t a t e in i n his h i s proposal p r o p o s a l the t h e minimum m i n i m u m diametral d i a m e t r a l clearances c l e a r a n c e s when w h e n the t h e values v a l u e s are a r e less l e s s than t h a n API A P I Standard S t a n d a r d 610 6 1 0 Table T a b l e 5. 5 . 6.8 6 . 8 Mechanical M e c h a n i c a l Shaft S h a f t Seals S e a l s Paragraph P a r a g r a p h 6.8.4, 6 . 8 . 4 , New N e w A A dial d i a l type t y p e thermometer t h e r m o m e t e r shall s h a l l be b e provided p r o v i d e d when w h e n a a seal s e a l flush f l u s h cooler c o o l e r is i s provided. p r o v i d e d . Vent V e n t and a n d drain d r a i n connections c o n n e c t i o n s from f r o m the t h e mechanical m e c h a n i c a l seals s e a l s shall s h a l l be b e piped p i p e d to t o a a safe s a f e area. a r e a . Pumps P u m p s in i n water w a t e r service s e r v i c e shall s h a l l be b e designed d e s i g n e d so s o that t h a t the t h e water w a t e r temperature t e m p e r a t u r e at a t the t h e seal s e a l face f a c e does d o e s not n o t exceed e x c e e d 180°F 1 8 0 ° F (82°C). ( 8 2 ° C ) . A A non-sparking n o n - s p a r k i n g fixed f i x e d throttle t h r o t t l e bushing b u s h i n g shall s h a l l be b e provided p r o v i d e d for f o r Category C a t e g o r y 1 1 Arrangement A r r a n g e m e n t 1 1 seals. s e a l s . A A non-sparking n o n - s p a r k i n g fixed f i x e d throttle t h r o t t l e bushing b u s h i n g shall s h a l l be b e provided p r o v i d e d for f o r Category C a t e g o r y 2 2 Arrangement A r r a n g e m e n t 1 1 and a n d Arrangement A r r a n g e m e n t 2 2 seals s e a l s (when ( w h e n seal s e a l chamber c h a m b e r dimensions d i m e n s i o n s permit). p e r m i t ) . 6.10 6 . 1 0 Bearings B e a r i n g s and a n d Bearing B e a r i n g Housings H o u s i n g s Paragraph P a r a g r a p h 6.10.2.6, 6 . 1 0 . 2 . 6 , Addition A d d i t i o n Pumps P u m p s with w i t h bearing b e a r i n g housings h o u s i n g s lubricated l u b r i c a t e d by b y open o p e n or o r closed c l o s e d loop, l o o p , pure p u r e oil o i l mist m i s t shall s h a l l use u s e Inpro I n p r o Type T y p e OM-32 O M - 3 2 bearing b e a r i n g isolators i s o l a t o r s or o r equal, e q u a l , as a s a a minimum. m i n i m u m . Paragraph P a r a g r a p h 6.10.2.11, 6 . 1 0 . 2 . 1 1 , Clarification C l a r i f i c a t i o n Pumps P u m p s with w i t h anti-friction a n t i - f r i c t i o n bearings b e a r i n g s shall s h a l l have h a v e a a flat f l a t surface s u r f a c e at a t least l e a s t 1” 1 ” (25 ( 2 5 mm) m m ) in i n diameter d i a m e t e r for f o r the t h e location l o c a t i o n of o f magnetic m a g n e t i c based b a s e d vibration v i b r a t i o n measuring m e a s u r i n g equipment. e q u i p m e n t . Form F o r m QUA-03-5 Q U A - 0 3 - 5 Qualtrax Q u a l t r a x 9250 9 2 5 0 granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} Revision R e v i s i o n Indication I n d i c a t i o n UOP U O P Engineering E n g i n e e r i n g Department D e p a r t m e n t CENTRIFUGAL C E N T R I F U G A L PUMPS P U M P S STANDARD S T A N D A R D SPECIFICATION S P E C I F I C A T I O N 5-11-14 5 - 1 1 - 1 4 Page P a g e 5 5 of o f 6 6 DATE D A T E STATUS S T A T U S SPNSR S P N S R APVD A P V D 16JUN20 1 6 J U N 2 0 Reaffirmed R e a f f i r m e d MRV M R V PFD P F D 7.2 7 . 2 Couplings C o u p l i n g s and a n d Guards G u a r d s Paragraph P a r a g r a p h 7.2.2.a, 7 . 2 . 2 . a , Addition A d d i t i o n CONFIDENTIAL C O N F I D E N T I A L – – The T h e information i n f o r m a t i o n in i n this t h i s document d o c u m e n t is i s confidential c o n f i d e n t i a l and a n d must m u s t not n o t be b e used u s e d for f o r any a n y purpose, p u r p o s e , duplicated, d u p l i c a t e d , or o r disclosed d i s c l o s e d to t o others o t h e r s without w i t h o u t UOP's U O P ' s written w r i t t e n permission. p e r m i s s i o n . Disc D i s c coupling c o u p l i n g flexible f l e x i b l e discs d i s c s shall s h a l l be b e a a 300 3 0 0 series s e r i e s stainless s t a i n l e s s steel, s t e e l , except e x c e p t for f o r applications a p p l i c a t i o n s in i n a a wet w e t atmosphere a t m o s p h e r e in i n the t h e presence p r e s e n c e of o f chlorides, c h l o r i d e s , where w h e r e a a material m a t e r i a l resistant r e s i s t a n t to t o chloride c h l o r i d e stress s t r e s s corrosion c o r r o s i o n cracking c r a c k i n g shall s h a l l be b e used. u s e d . 7.5 7 . 5 Piping P i p i n g and a n d Appurtenances A p p u r t e n a n c e s Paragraph P a r a g r a p h 7.5.2.6, 7 . 5 . 2 . 6 , Addition A d d i t i o n Fluid F l u i d passages p a s s a g e s within w i t h i n the t h e pump p u m p shall s h a l l be b e arranged a r r a n g e d for f o r complete c o m p l e t e drainage d r a i n a g e where w h e r e practical. p r a c t i c a l . The T h e vendor v e n d o r shall s h a l l provide p r o v i d e 3/4" 3 / 4 " minimum m i n i m u m drain d r a i n piping p i p i n g with w i t h a a line l i n e size s i z e gate g a t e valve v a l v e for f o r each e a c h drain. d r a i n . Drain D r a i n valves v a l v e s shall s h a l l be b e located l o c a t e d as a s close c l o s e to t o the t h e pump p u m p as a s practical p r a c t i c a l and a n d still s t i l l be b e accessible. a c c e s s i b l e . Paragraph P a r a g r a p h 7.5.2.8, 7 . 5 . 2 . 8 , Addition A d d i t i o n 7.7 7 . 7 Gears G e a r s (NEW) ( N E W ) Balancing B a l a n c i n g lines l i n e s for f o r multi-stage m u l t i - s t a g e pumps p u m p s shall s h a l l utilize u t i l i z e flanged f l a n g e d joints; j o i n t s ; screwed s c r e w e d unions u n i o n s are a r e not n o t acceptable. a c c e p t a b l e . Pumps P u m p s equipped e q u i p p e d with w i t h a a tilting t i l t i n g shoe s h o e thrust t h r u s t bearing b e a r i n g shall s h a l l have h a v e a a forced f o r c e d feed f e e d lubrication l u b r i c a t i o n system. s y s t e m . Gears G e a r s shall s h a l l comply c o m p l y with w i t h API A P I Standard S t a n d a r d 677 6 7 7 for f o r spared s p a r e d pumping p u m p i n g services s e r v i c e s unless u n l e s s otherwise o t h e r w i s e specified. s p e c i f i e d . Gears G e a r s shall s h a l l comply c o m p l y with w i t h API A P I Standard S t a n d a r d 613 6 1 3 for f o r unspared u n s p a r e d pumping p u m p i n g services. s e r v i c e s . Gears G e a r s for f o r high h i g h speed s p e e d integrally i n t e g r a l l y geared g e a r e d type t y p e pumps p u m p s (OH6) ( O H 6 ) may m a y be b e produced p r o d u c e d to t o manufacturer’s m a n u f a c t u r e r ’ s standard. s t a n d a r d . 7.8 7 . 8 Oil O i l Coolers C o o l e r s (NEW) ( N E W ) Tubes T u b e s for f o r fresh f r e s h water w a t e r service s e r v i c e shall s h a l l be b e inhibited i n h i b i t e d admiralty. a d m i r a l t y . If I f ammonia a m m o n i a or o r hot h o t sulfides s u l f i d e s are a r e present, p r e s e n t , 70-30 7 0 - 3 0 Cu-Ni C u - N i or o r titanium t i t a n i u m only o n l y tubes t u b e s shall s h a l l be b e used. u s e d . For F o r sea s e a water w a t e r or o r brackish b r a c k i s h water w a t e r services s e r v i c e s the t h e tubes t u b e s shall s h a l l be b e aluminum-brass, a l u m i n u m - b r a s s , 90-10 9 0 - 1 0 Cu-Ni, C u - N i , 70-30 7 0 - 3 0 Cu-Ni, C u - N i , or o r titanium. t i t a n i u m . Form F o r m QUA-03-5 Q U A - 0 3 - 5 Qualtrax Q u a l t r a x 9250 9 2 5 0 granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} Revision R e v i s i o n Indication I n d i c a t i o n UOP U O P Engineering E n g i n e e r i n g Department D e p a r t m e n t CENTRIFUGAL C E N T R I F U G A L PUMPS P U M P S STANDARD S T A N D A R D SPECIFICATION S P E C I F I C A T I O N 5-11-14 5 - 1 1 - 1 4 Page P a g e 6 6 of o f 6 6 DATE D A T E STATUS S T A T U S SPNSR S P N S R APVD A P V D 16JUN20 1 6 J U N 2 0 Reaffirmed R e a f f i r m e d MRV M R V PFD P F D When W h e n a a steel s t e e l channel c h a n n e l without w i t h o u t non-ferrous n o n - f e r r o u s cladding c l a d d i n g or o r weld w e l d overlay o v e r l a y is i s used u s e d in i n sea s e a or o r brackish b r a c k i s h water w a t e r service, s e r v i c e , the t h e surface s u r f a c e of o f the t h e steel s t e e l channel c h a n n e l shall s h a l l be b e faced f a c e d and a n d coated c o a t e d as a s follows: f o l l o w s : CONFIDENTIAL C O N F I D E N T I A L – – The T h e information i n f o r m a t i o n in i n this t h i s document d o c u m e n t is i s confidential c o n f i d e n t i a l and a n d must m u s t not n o t be b e used u s e d for f o r any a n y purpose, p u r p o s e , duplicated, d u p l i c a t e d , or o r disclosed d i s c l o s e d to t o others o t h e r s without w i t h o u t UOP's U O P ' s written w r i t t e n permission. p e r m i s s i o n . 8.3 8 . 3 Testing T e s t i n g (1) ( 1 ) A A weld w e l d deposited d e p o s i t e d machined m a c h i n e d facing f a c i n g of o f aluminum a l u m i n u m bronze, b r o n z e , Monel, M o n e l , or o r Cu-Ni C u - N i shall s h a l l be b e applied a p p l i e d to t o the t h e contact c o n t a c t edges e d g e s of o f the t h e partition p a r t i t i o n plates p l a t e s at a t the t h e tubesheet t u b e s h e e t sides s i d e s and a n d the t h e face f a c e of o f the t h e channel c h a n n e l flange f l a n g e which w h i c h is i s adjacent a d j a c e n t to t o the t h e tubesheet. t u b e s h e e t . These T h e s e weld w e l d deposits d e p o s i t s shall s h a l l extend e x t e n d at a t least l e a s t 1 1 inch i n c h (25 ( 2 5 mm) m m ) back b a c k from f r o m the t h e tubesheet t u b e s h e e t contact c o n t a c t surface. s u r f a c e . (2) ( 2 ) Install I n s t a l l sacrificial s a c r i f i c i a l zinc z i n c anodes a n o d e s in i n the t h e channel c h a n n e l of o f exchangers e x c h a n g e r s in i n water w a t e r service. s e r v i c e . Anodes A n o d e s shall s h a l l be b e of o f sufficient s u f f i c i e n t size s i z e for f o r four f o u r years y e a r s of o f continuous c o n t i n u o u s operation. o p e r a t i o n . (3) ( 3 ) All A l l steel s t e e l surfaces, s u r f a c e s , including i n c l u d i n g nozzles n o z z l e s and a n d supports s u p p o r t s and a n d excluding e x c l u d i n g the t h e zinc z i n c anodes, a n o d e s , shall s h a l l be b e painted p a i n t e d with w i t h a a primer p r i m e r coating. c o a t i n g . (4) ( 4 ) ¼” ¼ ” OD O D tubes t u b e s are a r e acceptable a c c e p t a b l e for f o r lube l u b e oil o i l coolers c o o l e r s for f o r high h i g h speed s p e e d integrally i n t e g r a l l y geared g e a r e d type t y p e pumps. p u m p s . Paragraph P a r a g r a p h 8.3.4.3.1, 8 . 3 . 4 . 3 . 1 , Decision D e c i s i o n NPSH N P S H Required R e q u i r e d Test T e s t is i s required r e q u i r e d when w h e n the t h e NPSHA N P S H A does d o e s not n o t exceed e x c e e d the t h e predicted p r e d i c t e d NPSHR N P S H R at a t rated r a t e d flow f l o w by b y 2 2 feet f e e t (0.60 ( 0 . 6 0 meters) m e t e r s ) 9.1 9 . 1 Single-Stage S i n g l e - S t a g e Overhung O v e r h u n g Pumps P u m p s ANNEX A N N E X H H Paragraph P a r a g r a p h 9.1.1.3, 9 . 1 . 1 . 3 , Decision D e c i s i o n / / Addition A d d i t i o n The T h e shaft s h a f t flexibility f l e x i b i l i t y index i n d e x shall s h a l l be b e calculated c a l c u l a t e d in i n accordance a c c o r d a n c e with w i t h Annex A n n e x K.1 K . 1 and a n d reported r e p o r t e d in i n pump p u m p vendor’s v e n d o r ’ s proposal. p r o p o s a l . The T h e value v a l u e of o f the t h e overhung o v e r h u n g pump p u m p shaft s h a f t flexibility, f l e x i b i l i t y , I I SF, S F , for f o r the t h e given g i v e n pump p u m p size s i z e factor, f a c t o r , K K t t shall s h a l l not n o t exceed e x c e e d 1.2 1 . 2 times t i m e s the t h e equation e q u a t i o n K.4 K . 4 (SI ( S I units) u n i t s ) or o r K.5 K . 5 (US ( U S units). u n i t s ) . Table T a b l e H.4 H . 4 note n o t e a, a , Exception E x c e p t i o n All A l l piping p i p i n g between b e t w e e n the t h e casing c a s i n g and a n d the t h e drain d r a i n valve v a l v e shall s h a l l be b e Schedule S c h e d u l e 160. 1 6 0 . Form F o r m QUA-03-5 Q U A - 0 3 - 5 Qualtrax Q u a l t r a x 9250 9 2 5 0 000000 0.00