m0lzf 2026-06-05T18:03:13+02:00 Microsoft® Excel® 2016 2026-06-05T18:25:30+02:00 Microsoft® Excel® 2016 Microsoft® Excel® 2016 Microsoft® Excel® 2016 2026-06-05T18:03:13+02:00 2026-06-05T18:25:30+02:00 m0lzf engines={image=false textcolor=true vector=false text=true} tetml={filename={D:\drim\repository\projects\drim_26_0\metadata\6\1\61bd4eed044aceff3c1d35670d03f9af\61bd4eed044aceff3c1d35670d03f9af.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} Air A i r Liquide L i q u i d e Confidential C o n f i d e n t i a l Information I n f o r m a t i o n This T h i s print p r i n t is i s the t h e property p r o p e r t y of o f L’Air L ’ A i r Liquide L i q u i d e S.A. S . A . or o r its i t s (direct ( d i r e c t and a n d indirect) i n d i r e c t ) affiliates a f f i l i a t e s or o r subsidiaries s u b s i d i a r i e s and a n d contains c o n t a i n s valuable v a l u a b l e confidential c o n f i d e n t i a l information. i n f o r m a t i o n . Copyright C o p y r i g h t and a n d all a l l other o t h e r rights r i g h t s in i n this t h i s print p r i n t are a r e expressly e x p r e s s l y reserved. r e s e r v e d . No N o part p a r t of o f this t h i s print p r i n t may m a y be b e disclosed d i s c l o s e d by b y the t h e intended i n t e n d e d recipient r e c i p i e n t to t o a a third t h i r d party, p a r t y , reproduced, r e p r o d u c e d , copied, c o p i e d , lent, l e n t , or o r disposed d i s p o s e d of, o f , directly d i r e c t l y or o r indirectly, i n d i r e c t l y , nor n o r used u s e d for f o r any a n y purpose p u r p o s e other o t h e r than t h a n that t h a t for f o r which w h i c h it i t is i s expressly e x p r e s s l y furnished. f u r n i s h e d . This T h i s print p r i n t is i s lent l e n t subject s u b j e c t to t o return r e t u r n on o n demand. d e m a n d . Process P r o c e s s Process P r o c e s s Data D a t a Sheet S h e e t Cover C o v e r ●●CONFIDENTIAL-RESTRICTED ● ● C O N F I D E N T I A L - R E S T R I C T E D Business B u s i n e s s Owner O w n e r Process P r o c e s s Department D e p a r t m e n t Team T e a m Leader L e a d e r Distribution D i s t r i b u t i o n List L i s t Check C h e c k Project P r o j e c t ACL A C L (Access ( A c c e s s Control C o n t r o l List) L i s t ) 624001C39 6 2 4 0 0 1 C 3 9 / / 624001C39T01 6 2 4 0 0 1 C 3 9 T 0 1 / / 624001C39T02 6 2 4 0 0 1 C 3 9 T 0 2 PROCESS P R O C E S S DATA D A T A - - TAIL T A I L GAS G A S COMPANDER C O M P A N D E R - - NITROGEN N I T R O G E N WASTE W A S T E EXPANDER E X P A N D E R Derived D e r i v e d from f r o m G-TPL-13-0-1, G - T P L - 1 3 - 0 - 1 , Rev. R e v . 1, 1 , issued i s s u e d 26-Jun-18 2 6 - J u n - 1 8 Rev. R e v . 1 1 ●●CONFIDENTIAL-RESTRICTED ● ● C O N F I D E N T I A L - R E S T R I C T E D AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR A L _ C R Y O _ P R O C E S S _ D S _ T E M P L A T E _ C O M P R E S S O R 1 1 AFI A F I Approved A p p r o v e d for f o r Inquiry I n q u i r y All A l l 2026-06-05 2 0 2 6 - 0 6 - 0 5 M. M . JACQUEMIN J A C Q U E M I N F. F . PÈRE P È R E L. L . GRANADOS G R A N A D O S 0 0 AFI A F I Approved A p p r o v e d for f o r Inquiry I n q u i r y All A l l 2025-08-04 2 0 2 5 - 0 8 - 0 4 M. M . JACQUEMIN J A C Q U E M I N L. L . GRANADOS G R A N A D O S L. L . GRANADOS G R A N A D O S Rev. R e v . Status S t a t u s Description D e s c r i p t i o n Sheet S h e e t Date D a t e Prepared P r e p a r e d by b y Checked C h e c k e d by b y Approved A p p r o v e d by b y Project P r o j e c t Name N a m e ACCSION A C C S I O N Index I n d e x of o f Revisions R e v i s i o n s Project P r o j e c t No. N o . Document D o c u m e n t No. N o . Page P a g e / / of o f 53573 5 3 5 7 3 53573-62-01-PR-013739-KH 5 3 5 7 3 - 6 2 - 0 1 - P R - 0 1 3 7 3 9 - K H 1 1 / / 5 5 Case-Name: C a s e - N a m e : N/A N / A Printed P r i n t e d by b y / / date d a t e / / time: t i m e : RNETW R N E T W / / Revision R e v i s i o n 1 1 05/06/26 0 5 / 0 6 / 2 6 / / 18:02 1 8 : 0 2 granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} Air A i r Liquide L i q u i d e Confidential C o n f i d e n t i a l Information I n f o r m a t i o n This T h i s print p r i n t is i s the t h e property p r o p e r t y of o f L’Air L ’ A i r Liquide L i q u i d e S.A. S . A . or o r its i t s (direct ( d i r e c t and a n d indirect) i n d i r e c t ) affiliates a f f i l i a t e s or o r subsidiaries s u b s i d i a r i e s and a n d contains c o n t a i n s valuable v a l u a b l e confidential c o n f i d e n t i a l information. i n f o r m a t i o n . Copyright C o p y r i g h t and a n d all a l l other o t h e r rights r i g h t s in i n this t h i s print p r i n t are a r e expressly e x p r e s s l y reserved. r e s e r v e d . No N o part p a r t of o f this t h i s print p r i n t may m a y be b e disclosed d i s c l o s e d by b y the t h e intended i n t e n d e d recipient r e c i p i e n t to t o a a third t h i r d party, p a r t y , reproduced, r e p r o d u c e d , copied, c o p i e d , lent, l e n t , or o r disposed d i s p o s e d of, o f , directly d i r e c t l y or o r indirectly, i n d i r e c t l y , nor n o r used u s e d for f o r any a n y purpose p u r p o s e other o t h e r than t h a n that t h a t for f o r which w h i c h it i t is i s expressly e x p r e s s l y furnished. f u r n i s h e d . This T h i s print p r i n t is i s lent l e n t subject s u b j e c t to t o return r e t u r n on o n demand. d e m a n d . ●CONFIDENTIAL ● C O N F I D E N T I A L Process P r o c e s s Process P r o c e s s Data D a t a Sheet S h e e t Compressor C o m p r e s s o r client-logo.bmp c l i e n t - l o g o . b m p 01 0 1 Item I t e m Number N u m b e r 624001C39 6 2 4 0 0 1 C 3 9 / / 624001C39T01 6 2 4 0 0 1 C 3 9 T 0 1 / / 624001C39T02 6 2 4 0 0 1 C 3 9 T 0 2 02 0 2 03 0 3 Designation D e s i g n a t i o n PROCESS P R O C E S S DATA D A T A - - TAIL T A I L GAS G A S COMPANDER C O M P A N D E R - - NITROGEN N I T R O G E N WASTE W A S T E EXPANDER E X P A N D E R 04 0 4 05 0 5 Number N u m b e r required r e q u i r e d 1 1 Supplier/Type S u p p l i e r / T y p e 06 0 6 Driver D r i v e r Electrical E l e c t r i c a l Motor M o t o r 07 0 7 08 0 8 MACHINE M A C H I N E ARRANGEMENT A R R A N G E M E N T 09 0 9 10 1 0 11 1 1 12 1 2 13 1 3 14 1 4 15 1 5 16 1 6 17 1 7 18 1 8 19 1 9 20 2 0 21 2 1 22 2 2 23 2 3 24 2 4 25 2 5 26 2 6 27 2 7 28 2 8 29 2 9 30 3 0 31 3 1 32 3 2 33 3 3 Scheme S c h e m e is i s presented p r e s e n t e d for f o r illustrative i l l u s t r a t i v e purposes, p u r p o s e s , vendor v e n d o r to t o advise a d v i s e on o n number n u m b e r of o f compression c o m p r e s s i o n stages s t a g e s and a n d coolers. c o o l e r s . 2 2 34 3 4 The T h e turbine t u r b i n e preheater p r e h e a t e r is i s out o u t of o f vendor v e n d o r scope, s c o p e , but b u t turbine t u r b i n e inlet i n l e t temperature t e m p e r a t u r e is i s linked l i n k e d to t o this t h i s exchanger e x c h a n g e r which w h i c h is i s heated h e a t e d using u s i n g heat h e a t 2 2 35 3 5 recovery r e c o v e r y from f r o m the t h e Flue F l u e Gas G a s Compressor. C o m p r e s s o r . Refer R e f e r to t o document d o c u m e n t 53573-62-01-PR-013712 5 3 5 7 3 - 6 2 - 0 1 - P R - 0 1 3 7 1 2 for f o r details d e t a i l s on o n the t h e impact i m p a c t on o n Flue F l u e Gas G a s 2 2 36 3 6 Compressor. C o m p r e s s o r . 37 3 7 Process P r o c e s s scheme s c h e m e is i s based b a s e d on o n two t w o turbines t u r b i n e s in i n series s e r i e s but b u t supplier s u p p l i e r to t o recommend r e c o m m e n d optimized o p t i m i z e d number n u m b e r for f o r best b e s t economic e c o n o m i c solution. s o l u t i o n . 38 3 8 39 3 9 START-UP S T A R T - U P philosophy p h i l o s o p h y 40 4 0 41 4 1 Start-up S t a r t - u p is i s done d o n e with w i t h flue f l u e gas g a s (see ( s e e page p a g e 5 5 for f o r start-up s t a r t - u p composition). c o m p o s i t i o n ) . Compressor C o m p r e s s o r running r u n n i n g on o n its i t s recycle r e c y c l e line l i n e with w i t h discharge d i s c h a r g e pressure p r e s s u r e ≥6 ≥ 6 42 4 2 bar(a). b a r ( a ) . Minimum M i n i m u m flowrate f l o w r a t e and a n d outlet o u t l e t pressure p r e s s u r e should s h o u l d be b e calculated c a l c u l a t e d by b y vendor v e n d o r based b a s e d on o n machine m a c h i n e and a n d recycle r e c y c l e valve v a l v e sizing. s i z i n g . 43 4 3 44 4 4 On O n expander e x p a n d e r side, s i d e , gas g a s is i s available a v a i l a b l e by b y by-passing b y - p a s s i n g the t h e PSA P S A (available ( a v a i l a b l e flowrate f l o w r a t e and a n d pressure p r e s s u r e are a r e given g i v e n on o n page p a g e 4). 4 ) . Actual A c t u a l operating o p e r a t i n g 45 4 5 conditions c o n d i t i o n s should s h o u l d be b e calculated c a l c u l a t e d by b y vendor v e n d o r (lower ( l o w e r pressure p r e s s u r e if i f required r e q u i r e d and a n d lower l o w e r flowrate f l o w r a t e if i f required r e q u i r e d are a r e possible). p o s s i b l e ) . 46 4 6 PSA P S A constraint c o n s t r a i n t Derived D e r i v e d from f r o m G-TPL-13-0-1, G - T P L - 1 3 - 0 - 1 , Rev. R e v . 1, 1 , issued i s s u e d 26-Jun-18 2 6 - J u n - 1 8 Rev. R e v . AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR A L _ C R Y O _ P R O C E S S _ D S _ T E M P L A T E _ C O M P R E S S O R The T h e compressor c o m p r e s s o r and a n d expander e x p a n d e r are a r e placed p l a c e d after a f t e r a a Pressure P r e s s u r e Swing S w i n g Adsorber A d s o r b e r (PSA). ( P S A ) . The T h e cyclic c y c l i c nature n a t u r e of o f the t h e upstream u p s t r e a m process p r o c e s s induces i n d u c e s cyclic c y c l i c fluctuations f l u c t u a t i o n s (30 ( 3 0 sec) s e c ) of o f inlet i n l e t streams s t r e a m s of o f the t h e compander c o m p a n d e r : : +0.5% + 0 . 5 % / / -1.2% - 1 . 2 % on o n the t h e molecular m o l e c u l a r weight w e i g h t of o f the t h e tail t a i l gas g a s (see ( s e e page p a g e 5) 5 ) Line L i n e revised r e v i s e d under u n d e r Rev. R e v . No. N o . 1Project 1 P r o j e c t NameProject N a m e P r o j e c t No. N o . Document D o c u m e n t No. N o . Sheet S h e e t / / of o f Revision R e v i s i o n ACCSION A C C S I O N 53573 5 3 5 7 3 53573-62-01-PR-013739-KH 5 3 5 7 3 - 6 2 - 0 1 - P R - 0 1 3 7 3 9 - K H 2 2 / / 5 5 1 1 Case-Name: C a s e - N a m e : N/A N / A Printed P r i n t e d by b y / / date d a t e / / time: t i m e : RNETW R N E T W / / 20/07/23 2 0 / 0 7 / 2 3 / / 16:15 1 6 : 1 5 granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} SUCTION S U C T I O N TAIL T A I L GAS G A S COMPRESSOR C O M P R E S S O R Pressure P r e s s u r e Temperature T e m p e r a t u r e Pipe P i p e diameter d i a m e t e r Design D e s i g n pressure p r e s s u r e min. m i n . / / max. m a x . SIDE S I D E STREAM S T R E A M TAIL T A I L GAS G A S COMPRESSOR C O M P R E S S O R Available A v a i l a b l e Pressure P r e s s u r e (can ( c a n be b e lowered l o w e r e d for f o r optimization) o p t i m i z a t i o n ) Temperature T e m p e r a t u r e Pipe P i p e diameter d i a m e t e r Design D e s i g n pressure p r e s s u r e min. m i n . / / max. m a x . DISCHARGE D I S C H A R G E TAIL T A I L GAS G A S COMPRESSOR C O M P R E S S O R (2) ( 2 ) Molar M o l a r Flowrate F l o w r a t e (3) ( 3 ) Mass M a s s Flowrate F l o w r a t e Pressure P r e s s u r e Temperature T e m p e r a t u r e Pipe P i p e diameter d i a m e t e r Design D e s i g n pressure p r e s s u r e Design D e s i g n temperature t e m p e r a t u r e min. m i n . / / max. m a x . INTERCOOLERS I N T E R C O O L E R S TAIL T A I L GAS G A S COMPRESSOR C O M P R E S S O R (see ( s e e page p a g e 5 5 for f o r hot h o t water w a t e r conditions) c o n d i t i o n s ) Outlet O u t l e t Temperature T e m p e r a t u r e (gas ( g a s side) s i d e ) First F i r s t Intercooler I n t e r c o o l e r Outlet O u t l e t Temperature T e m p e r a t u r e (gas ( g a s side) s i d e ) Second S e c o n d Intercooler I n t e r c o o l e r Outlet O u t l e t Temperature T e m p e r a t u r e (gas ( g a s side) s i d e ) Aftercooler A f t e r c o o l e r SUCTION S U C T I O N NITROGEN N I T R O G E N WASTE W A S T E EXPANDER E X P A N D E R Molar M o l a r Flowrate F l o w r a t e Mass M a s s Flowrate F l o w r a t e Pressure P r e s s u r e Temperature T e m p e r a t u r e Pipe P i p e diameter d i a m e t e r Design D e s i g n pressure p r e s s u r e Design D e s i g n temperature t e m p e r a t u r e min. m i n . / / max. m a x . DISCHARGE D I S C H A R G E NITROGEN N I T R O G E N WASTE W A S T E EXPANDER E X P A N D E R (4) ( 4 ) Molar M o l a r Flowrate F l o w r a t e Mass M a s s Flowrate F l o w r a t e Pressure P r e s s u r e Temperature T e m p e r a t u r e Pipe P i p e diameter d i a m e t e r Design D e s i g n pressure p r e s s u r e Design D e s i g n temperature t e m p e r a t u r e min. m i n . / / max. m a x . Line L i n e revised r e v i s e d under u n d e r Rev. R e v . No. N o . °C ° C N/A N / A 1 1 1 1 1 1 1 1 1 1 18:02 1 8 : 0 2 / / / / 1 1 1 1 1 1 1 1 RNETW R N E T W ACCSION A C C S I O N AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR A L _ C R Y O _ P R O C E S S _ D S _ T E M P L A T E _ C O M P R E S S O R 36 3 6 41 4 1 3 3 / / 39 3 9 44 4 4 48 4 8 53 5 3 51 5 1 1 1 52 5 2 38 3 8 v.t.a v . t . a v.t.a v . t . a v.t.a v . t . a 43 4 3 1 1 1 1 36.4 3 6 . 4 24.0 2 4 . 0 v.t.a v . t . a -20 - 2 0 / / 65 6 5 1 1 1 1 29 2 9 28 2 8 35 3 5 31 3 1 41.7 4 1 . 7 25.6 2 5 . 6 Process P r o c e s s Data D a t a Sheet S h e e t 32 3 2 33.0 3 3 . 0 15 1 5 261 2 6 1 429 4 2 9 261 2 6 1 526 5 2 6 16 1 6 20 2 0 490 4 9 0 46.1 4 6 . 1 01 0 1 02 0 2 barg b a r g °C ° C Compressor C o m p r e s s o r 1 1 1 1 Fluid F l u i d 1 1 Mass M a s s Flowrate F l o w r a t e Designation D e s i g n a t i o n Number N u m b e r required r e q u i r e d 624001C39 6 2 4 0 0 1 C 3 9 / / 624001C39T01 6 2 4 0 0 1 C 3 9 T 0 1 / / 624001C39T02 6 2 4 0 0 1 C 3 9 T 0 2 Item I t e m Number N u m b e r client-logo.bmp c l i e n t - l o g o . b m p Process P r o c e s s 24.5 2 4 . 5 v.t.a v . t . a 0.0 0 . 0 12.3 1 2 . 3 1.013 1 . 0 1 3 1.013 1 . 0 1 3 v.t.a v . t . a 10.45 1 0 . 4 5 413 4 1 3 074 0 7 4 RATED R A T E D SUMMER S U M M E R see s e e page p a g e 5 5 for f o r detailed d e t a i l e d composition c o m p o s i t i o n and a n d properties p r o p e r t i e s Driver D r i v e r Supplier/Type S u p p l i e r / T y p e Electrical E l e c t r i c a l Motor M o t o r NOMINAL N O M I N A L SUMMER S U M M E R CASE C A S E (1) ( 1 ) NOMINAL N O M I N A L WINTER W I N T E R 03 0 3 04 0 4 PROCESS P R O C E S S DATA D A T A - - TAIL T A I L GAS G A S COMPANDER C O M P A N D E R - - NITROGEN N I T R O G E N WASTE W A S T E EXPANDER E X P A N D E R 05 0 5 06 0 6 1 1 START-UP S T A R T - U P 10 1 0 09 0 9 08 0 8 07 0 7 Nm N m 3 3 /h / h 282 2 8 2 946 9 4 6 249 2 4 9 170 1 7 0 bar(a) b a r ( a ) (5) ( 5 ) 1.013 1 . 0 1 3 kg/h k g / h 249 2 4 9 226 2 2 6 11 1 1 1 1 466 4 6 6 699 6 9 9 Molar M o l a r Flowrate F l o w r a t e 412 4 1 2 977 9 7 7 Design D e s i g n temperature t e m p e r a t u r e 12 1 2 356 3 5 6 104" 1 0 4 " 13 1 3 12 1 2 18 1 8 -0.2 - 0 . 2 / / 6 6 -20 - 2 0 / / 65 6 5 12.2 1 2 . 2 °C ° C DN D N 12.4 1 2 . 4 1 1 1.013 1 . 0 1 3 Nm N m 3 3 /h / h °C ° C 63 6 3 05/06/26 0 5 / 0 6 / 2 6 Printed P r i n t e d by b y / / date d a t e / / time: t i m e : 61 6 1 58 5 8 1 1 1 1 5 5 1Project 1 P r o j e c t No. N o . 53573-62-01-PR-013739-KH 5 3 5 7 3 - 6 2 - 0 1 - P R - 0 1 3 7 3 9 - K H 1 1 Document D o c u m e n t No. N o . Project P r o j e c t Name N a m e 53573 5 3 5 7 3 Revision R e v i s i o n Derived D e r i v e d from f r o m G-TPL-13-0-1, G - T P L - 1 3 - 0 - 1 , Rev. R e v . 1, 1 , issued i s s u e d 26-Jun-18 2 6 - J u n - 1 8 Case-Name: C a s e - N a m e : 62 6 2 60 6 0 Rev. R e v . 54 5 4 49 4 9 46 4 6 19 1 9 20 2 0 33 3 3 50 5 0 47 4 7 37 3 7 27 2 7 23 2 3 24 2 4 ●●CONFIDENTIAL-RESTRICTED ● ● C O N F I D E N T I A L - R E S T R I C T E D 14 1 4 30 3 0 17 1 7 Air A i r Liquide L i q u i d e Confidential C o n f i d e n t i a l Information I n f o r m a t i o n This T h i s print p r i n t is i s the t h e property p r o p e r t y of o f L’Air L ’ A i r Liquide L i q u i d e S.A. S . A . or o r its i t s (direct ( d i r e c t and a n d indirect) i n d i r e c t ) affiliates a f f i l i a t e s or o r subsidiaries s u b s i d i a r i e s and a n d contains c o n t a i n s valuable v a l u a b l e confidential c o n f i d e n t i a l information. i n f o r m a t i o n . Copyright C o p y r i g h t and a n d all a l l other o t h e r rights r i g h t s in i n this t h i s print p r i n t are a r e expressly e x p r e s s l y reserved. r e s e r v e d . No N o part p a r t of o f this t h i s print p r i n t may m a y be b e disclosed d i s c l o s e d by b y the t h e intended i n t e n d e d recipient r e c i p i e n t to t o a a third t h i r d party, p a r t y , reproduced, r e p r o d u c e d , copied, c o p i e d , lent, l e n t , or o r disposed d i s p o s e d of, o f , directly d i r e c t l y or o r indirectly, i n d i r e c t l y , nor n o r used u s e d for f o r any a n y purpose p u r p o s e other o t h e r than t h a n that t h a t for f o r which w h i c h it i t is i s expressly e x p r e s s l y furnished. f u r n i s h e d . This T h i s print p r i n t is i s lent l e n t subject s u b j e c t to t o return r e t u r n on o n demand. d e m a n d . 21 2 1 22 2 2 42 4 2 40 4 0 34 3 4 Molar M o l a r Flowrate F l o w r a t e 59 5 9 55 5 5 28" 2 8 " 56 5 6 45 4 5 v.t.a v . t . a DN D N 104" 1 0 4 " bar(g) b a r ( g ) 57 5 7 2 2 2 2 1.087 1 . 0 8 7 Mass M a s s Flowrate F l o w r a t e kg/h k g / h 21 2 1 191 1 9 1 20 2 0 785 7 8 5 bar(a) b a r ( a ) (6) ( 6 ) For F o r start-up, s t a r t - u p , expander e x p a n d e r available a v a i l a b l e flowrate f l o w r a t e is i s 179 1 7 9 178 1 7 8 Nm3/h N m 3 / h already a l r e a d y preheated p r e h e a t e d at a t the t h e right r i g h t temperature. t e m p e r a t u r e . Design D e s i g n temperature t e m p e r a t u r e °C ° C 433 4 3 3 564 5 6 4 v.t.a v . t . a 4.9 4 . 9 295 2 9 5 643 6 4 3 433 4 3 3 763 7 6 3 10.5 1 0 . 5 25 2 5 26 2 6 Nm N m 3 3 /h / h DN D N v.t.a v . t . a kg/h k g / h bar(a) b a r ( a ) °C ° C barg b a r g 487 4 8 7 889 8 8 9 bar(a) b a r ( a ) °C ° C 2 2 0.15 0 . 1 5 °C ° C -20 - 2 0 / / 180 1 8 0 1.080 1 . 0 8 0 1.080 1 . 0 8 0 1.080 1 . 0 8 0 v.t.a v . t . a 9.0 9 . 0 12 1 2 203 2 0 3 - - 10.57 1 0 . 5 7 12 1 2 698 6 9 8 9.99 9 . 9 9 Sheet S h e e t / / of o f 9.6 9 . 6 barg b a r g 10" 1 0 " 12.0 1 2 . 0 -20 - 2 0 / / 65 6 5 - - - - DN D N bar(g) b a r ( g ) kg/h k g / h 572 5 7 2 258 2 5 8 524 5 2 4 805 8 0 5 524 5 2 4 888 8 8 8 DN D N 72" 7 2 " v.t.a v . t . a 524 5 2 4 805 8 0 5 524 5 2 4 888 8 8 8 v.t.a v . t . a Nm N m 3 3 /h / h 447 4 4 7 520 5 2 0 410 4 1 0 909 9 0 9 410 4 1 0 973 9 7 3 v.t.a v . t . a bar(a) b a r ( a ) 6.83 6 . 8 3 6.83 6 . 8 3 v.t.a v . t . a v.t.a v . t . a °C ° C -20 - 2 0 / / 80 8 0 v.t.a v . t . a °C ° C v.t.a v . t . a v.t.a v . t . a v.t.a v . t . a v.t.a v . t . a °C ° C °C ° C kg/h k g / h 572 5 7 2 258 2 5 8 v.t.a v . t . a v.t.a v . t . a v.t.a v . t . a °C ° C v.t.a v . t . a v.t.a v . t . a v.t.a v . t . a Nm N m 3 3 /h / h 447 4 4 7 520 5 2 0 410 4 1 0 909 9 0 9 410 4 1 0 973 9 7 3 (6) ( 6 ) v.t.a v . t . a v.t.a v . t . a 6.83 6 . 8 3 6.87 6 . 8 7 1 1 1 1 1 1 1 1 1 1 (1) ( 1 ) The T h e RATED R A T E D case c a s e should s h o u l d be b e used u s e d for f o r the t h e sizing s i z i n g of o f the t h e machine, m a c h i n e , IGV I G V can c a n be b e set s e t to t o 0. 0 . The T h e NOMINAL N O M I N A L SUMMER S U M M E R case c a s e should s h o u l d be b e used u s e d for f o r the t h e power p o w e r consumption c o n s u m p t i o n optimization. o p t i m i z a t i o n . (2) ( 2 ) After A f t e r final f i n a l aftercooler. a f t e r c o o l e r . Aftercooler A f t e r c o o l e r should s h o u l d be b e sized s i z e d with w i t h an a n approach a p p r o a c h of o f 20°C 2 0 ° C between b e t w e e n water w a t e r inlet i n l e t and a n d gas g a s outlet. o u t l e t . (3) ( 3 ) No N o leaks l e a k s on o n the t h e compressor c o m p r e s s o r as a s it i t is i s accepted a c c e p t e d to t o contaminate c o n t a m i n a t e process p r o c e s s fluid f l u i d with w i t h seal s e a l gas g a s (4) ( 4 ) Intermediate I n t e r m e d i a t e pressure p r e s s u r e between b e t w e e n the t h e two t w o turbines t u r b i n e s should s h o u l d be b e optimized o p t i m i z e d on o n the t h e NOMINAL N O M I N A L SUMMER S U M M E R case c a s e to t o reach r e a c h 2°C 2 ° C at a t the t h e outlet o u t l e t of o f the t h e second s e c o n d wheel. w h e e l . (5) ( 5 ) For F o r start-up, s t a r t - u p , compressor c o m p r e s s o r flowrate f l o w r a t e with w i t h recycle r e c y c l e can c a n be b e around a r o u n d 80% 8 0 % of o f Nominal N o m i n a l flow. f l o w . To T o be b e defined d e f i n e d by b y vendor v e n d o r according a c c o r d i n g to t o available a v a i l a b l e gas g a s at a t Expander E x p a n d e r inlet. i n l e t . granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} Air A i r Liquide L i q u i d e Confidential C o n f i d e n t i a l Information I n f o r m a t i o n This T h i s print p r i n t is i s the t h e property p r o p e r t y of o f L’Air L ’ A i r Liquide L i q u i d e S.A. S . A . or o r its i t s (direct ( d i r e c t and a n d indirect) i n d i r e c t ) affiliates a f f i l i a t e s or o r subsidiaries s u b s i d i a r i e s and a n d contains c o n t a i n s valuable v a l u a b l e confidential c o n f i d e n t i a l information. i n f o r m a t i o n . Copyright C o p y r i g h t and a n d all a l l other o t h e r rights r i g h t s in i n this t h i s print p r i n t are a r e expressly e x p r e s s l y reserved. r e s e r v e d . No N o part p a r t of o f this t h i s print p r i n t may m a y be b e disclosed d i s c l o s e d by b y the t h e intended i n t e n d e d recipient r e c i p i e n t to t o a a third t h i r d ●●CONFIDENTIAL-RESTRICTED ● ● C O N F I D E N T I A L - R E S T R I C T E D Derived D e r i v e d from f r o m G-TPL-13-0-1, G - T P L - 1 3 - 0 - 1 , Rev. R e v . 1, 1 , issued i s s u e d 26-Jun-18 2 6 - J u n - 1 8 party, p a r t y , reproduced, r e p r o d u c e d , copied, c o p i e d , lent, l e n t , or o r disposed d i s p o s e d of, o f , directly d i r e c t l y or o r indirectly, i n d i r e c t l y , nor n o r used u s e d for f o r any a n y purpose p u r p o s e other o t h e r than t h a n that t h a t for f o r which w h i c h it i t is i s expressly e x p r e s s l y furnished. f u r n i s h e d . This T h i s print p r i n t is i s lent l e n t subject s u b j e c t to t o return r e t u r n on o n demand. d e m a n d . Rev. R e v . 1 1 01 0 1 Item I t e m Number N u m b e r 624001C39 6 2 4 0 0 1 C 3 9 / / 624001C39T01 6 2 4 0 0 1 C 3 9 T 0 1 / / 624001C39T02 6 2 4 0 0 1 C 3 9 T 0 2 02 0 2 03 0 3 Designation D e s i g n a t i o n PROCESS P R O C E S S DATA D A T A - - TAIL T A I L GAS G A S COMPANDER C O M P A N D E R - - NITROGEN N I T R O G E N WASTE W A S T E EXPANDER E X P A N D E R 04 0 4 RATED R A T E D NOMINAL N O M I N A L NOMINAL N O M I N A L 05 0 5 START-UP S T A R T - U P CASE C A S E SUMMER S U M M E R SUMMER S U M M E R WINTER W I N T E R 06 0 6 07 0 7 ENERGY E N E R G Y 08 0 8 Isothermal I s o t h e r m a l efficiency e f f i c i e n c y compressor c o m p r e s s o r % % 09 0 9 Thermodynamic T h e r m o d y n a m i c power p o w e r compressor c o m p r e s s o r kW k W 10 1 0 Mechanical M e c h a n i c a l losses l o s s e s (including ( i n c l u d i n g main m a i n oil o i l pump) p u m p ) kW k W 11 1 1 Power P o w e r at a t motor m o t o r coupling c o u p l i n g (including ( i n c l u d i n g losses) l o s s e s ) kW k W 12 1 2 Power P o w e r at a t motor m o t o r terminals t e r m i n a l s kW k W 13 1 3 Motor M o t o r rating r a t i n g kW k W 14 1 4 Surge S u r g e limit l i m i t in i n % % of o f nominal n o m i n a l flow f l o w (p=constant) ( p = c o n s t a n t ) % % 15 1 5 Driver D r i v e r rotating r o t a t i n g speed s p e e d RPM R P M 16 1 6 17 1 7 UTILITIES U T I L I T I E S 18 1 8 Seal S e a l gas g a s flowrate f l o w r a t e requirement r e q u i r e m e n t (operation ( o p e r a t i o n / / standstill) s t a n d s t i l l ) Nm N m 3 3 /h / h / / 19 1 9 Leakage L e a k a g e flowrate f l o w r a t e of o f seal s e a l gas g a s in i n the t h e process p r o c e s s gas g a s Nm N m 3 3 /h / h 20 2 0 Seal S e a l gas g a s vent v e n t flowrate f l o w r a t e Nm N m 3 3 /h / h 21 2 1 Instrument I n s t r u m e n t air a i r flowrate f l o w r a t e Nm N m 3 3 /h / h 22 2 2 Electrical E l e c t r i c a l frequency f r e q u e n c y Hz H z 50 5 0 23 2 3 24 2 4 HOT H O T WATER W A T E R CONDITIONS C O N D I T I O N S TO T O COMPRESSOR C O M P R E S S O R INTERCOOLERS I N T E R C O O L E R S 25 2 5 ME M E - - Glycol G l y c o l content c o n t e n t in i n hot h o t water w a t e r % % vol v o l 0% 0 % 1 1 26 2 6 Water W a t e r fouling f o u l i n g factor f a c t o r m2°C/W m 2 ° C / W 0.0001 0 . 0 0 0 1 27 2 7 Water W a t e r Inlet I n l e t Pressure P r e s s u r e bar(a) b a r ( a ) 19.5 1 9 . 5 1 1 28 2 8 Design D e s i g n Pressure P r e s s u r e bar(g) b a r ( g ) 25.0 2 5 . 0 1 1 29 2 9 Design D e s i g n Temperature T e m p e r a t u r e °C ° C -20 - 2 0 / / 230 2 3 0 1 1 30 3 0 Maximum M a x i m u m Allowable A l l o w a b l e Pressure P r e s s u r e Drop D r o p per p e r Intercooler I n t e r c o o l e r mbar m b a r 2 2 500 5 0 0 1 1 31 3 1 Hot H o t Water W a t e r (1) ( 1 ) (see ( s e e scheme) s c h e m e ) Flow F l o w m3/h m 3 / h 32 3 2 Hot H o t Water W a t e r (1) ( 1 ) (see ( s e e scheme) s c h e m e ) Intercooler I n t e r c o o l e r Inlet I n l e t Temperature T e m p e r a t u r e °C ° C 26.1 2 6 . 1 21.7 2 1 . 7 16.4 1 6 . 4 26.1 2 6 . 1 33 3 3 Hot H o t Water W a t e r (1) ( 1 ) (see ( s e e scheme) s c h e m e ) Intercooler I n t e r c o o l e r Outlet O u t l e t Temperature T e m p e r a t u r e °C ° C T T Gas G a s in i n - - 6°C 6 ° C T T Gas G a s in i n - - 6°C 6 ° C 1 1 34 3 4 Hot H o t Water W a t e r (2) ( 2 ) (see ( s e e scheme) s c h e m e ) Flow F l o w m3/h m 3 / h 35 3 5 Hot H o t Water W a t e r (2) ( 2 ) (see ( s e e scheme) s c h e m e ) Intercooler I n t e r c o o l e r Inlet I n l e t Temperature T e m p e r a t u r e °C ° C 26.1 2 6 . 1 21.7 2 1 . 7 16.4 1 6 . 4 26.1 2 6 . 1 36 3 6 Hot H o t Water W a t e r (2) ( 2 ) (see ( s e e scheme) s c h e m e ) Intercooler I n t e r c o o l e r Outlet O u t l e t Temperature T e m p e r a t u r e °C ° C T T Gas G a s in i n - - 6°C 6 ° C T T Gas G a s in i n - - 6°C 6 ° C 1 1 37 3 7 Hot H o t Water W a t e r (3) ( 3 ) (see ( s e e scheme) s c h e m e ) Flow F l o w m3/h m 3 / h 38 3 8 Hot H o t Water W a t e r (3) ( 3 ) (see ( s e e scheme) s c h e m e ) Intercooler I n t e r c o o l e r Inlet I n l e t Temperature T e m p e r a t u r e °C ° C 26.1 2 6 . 1 21.7 2 1 . 7 16.4 1 6 . 4 26.1 2 6 . 1 39 3 9 Hot H o t Water W a t e r (3) ( 3 ) (see ( s e e scheme) s c h e m e ) Intercooler I n t e r c o o l e r Outlet O u t l e t Temperature T e m p e r a t u r e °C ° C T T Gas G a s in i n - - 6°C 6 ° C T T Gas G a s in i n - - 6°C 6 ° C 1 1 40 4 0 Overdesign O v e r d e s i g n on o n heat h e a t transfer t r a n s f e r area a r e a % % 10 1 0 41 4 1 42 4 2 COOLING C O O L I N G WATER W A T E R (for ( f o r auxiliary a u x i l i a r y equipment) e q u i p m e n t ) 43 4 3 Cooling C o o l i n g water w a t e r flowrate f l o w r a t e m m 3 3 /h / h v.t.g v . t . g 1 1 44 4 4 Water W a t e r fouling f o u l i n g factor f a c t o r m2h°C/kcal m 2 h ° C / k c a l 0.0002 0 . 0 0 0 2 1 1 45 4 5 Water W a t e r inlet i n l e t temperature t e m p e r a t u r e °C ° C 23.1 2 3 . 1 18.7 1 8 . 7 13.4 1 3 . 4 23.1 2 3 . 1 46 4 6 Maximum M a x i m u m allowable a l l o w a b l e water w a t e r temperature t e m p e r a t u r e increase i n c r e a s e °C ° C 15.0 1 5 . 0 47 4 7 Water W a t e r inlet i n l e t pressure p r e s s u r e bar(a) b a r ( a ) 4.0 4 . 0 48 4 8 Allowable A l l o w a b l e water w a t e r pressure p r e s s u r e drop d r o p (skid) ( s k i d ) mbar m b a r 1 1 000 0 0 0 49 4 9 50 5 0 OPTIMIZATION O P T I M I Z A T I O N CRITERIA C R I T E R I A 51 5 1 Running R u n n i n g time t i m e h/year h / y e a r 52 5 2 Power P o w e r evaluation e v a l u a t i o n €/MWh € / M W h AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR A L _ C R Y O _ P R O C E S S _ D S _ T E M P L A T E _ C O M P R E S S O R v.t.a v . t . a : : values v a l u e s to t o be b e advised a d v i s e d by b y vendor. v e n d o r . Process P r o c e s s Item I t e m Specifications S p e c i f i c a t i o n s & & Data D a t a Sheets S h e e t s Process P r o c e s s Data D a t a Sheet S h e e t Compressor C o m p r e s s o r : : values v a l u e s to t o be b e guaranteed g u a r a n t e e d by b y vendor v e n d o r with w i t h the t h e following f o l l o w i n g tolerances t o l e r a n c e s : : Pressure P r e s s u r e (- ( - 0 0 %) % ) ; ; Power P o w e r construction c o n s t r u c t i o n tolerances t o l e r a n c e s (+ ( + 0 0 %) % ) ; ; Power P o w e r measurement m e a s u r e m e n t tolerances t o l e r a n c e s (< ( < 1.5 1 . 5 %, % , advise a d v i s e if i f different) d i f f e r e n t ) ; ; Discharged D i s c h a r g e d flow f l o w (- ( - 0 0 %) % ) ; ; Temperature T e m p e r a t u r e (+ ( + 1°C) 1 ° C ) ; ; Water W a t e r flow f l o w (+ ( + 5 5 %) % ) ; ; Leakage L e a k a g e flowrate f l o w r a t e of o f process p r o c e s s gas g a s (+ ( + 0 0 %) % ) Project P r o j e c t Name N a m e ACCSION A C C S I O N Line L i n e revised r e v i s e d under u n d e r Rev. R e v . No. N o . Project P r o j e c t No. N o . Document D o c u m e n t No. N o . Sheet S h e e t / / of o f 53573 5 3 5 7 3 53573-62-01-PR-013739-KH 5 3 5 7 3 - 6 2 - 0 1 - P R - 0 1 3 7 3 9 - K H 4 4 / / 5 5 Revision R e v i s i o n 1 1 granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true} SUCTION S U C T I O N TAIL T A I L GAS G A S COMPRESSOR C O M P R E S S O R Composition C o m p o s i t i o n Carbon C a r b o n dioxide d i o x i d e (CO ( C O 2 2 ) ) %mol % m o l Water W a t e r (H ( H 2 2 O) O ) %mol % m o l Nitrogen N i t r o g e n (N ( N 2 2 ) ) %mol % m o l Oxygen O x y g e n (O ( O 2 2 ) ) %mol % m o l Argon A r g o n (Ar) ( A r ) %mol % m o l Carbon C a r b o n monoxide m o n o x i d e (CO) ( C O ) ppm p p m Nitric N i t r i c oxide o x i d e (NO) ( N O ) ppm p p m Nitric N i t r i c dioxide d i o x i d e (NO2) ( N O 2 ) ppm p p m Sulfure S u l f u r e dioxide d i o x i d e (SO2) ( S O 2 ) ppm p p m Methane M e t h a n e (CH4) ( C H 4 ) ppm p p m Density D e n s i t y (1) ( 1 ) kg/m3 k g / m 3 Molecular M o l e c u l a r Weight W e i g h t (1) ( 1 ) g/mol g / m o l Molar M o l a r Heat H e a t Capacity C a p a c i t y (1) ( 1 ) kcal/Nm3/°C k c a l / N m 3 / ° C Viscosity V i s c o s i t y (1) ( 1 ) kg/m/h k g / m / h SIDE S I D E STREAM S T R E A M TAIL T A I L GAS G A S COMPRESSOR C O M P R E S S O R Composition C o m p o s i t i o n Carbon C a r b o n dioxide d i o x i d e (CO ( C O 2 2 ) ) %mol % m o l Water W a t e r (H ( H 2 2 O) O ) %mol % m o l Nitrogen N i t r o g e n (N ( N 2 2 ) ) %mol % m o l Oxygen O x y g e n (O ( O 2 2 ) ) %mol % m o l Argon A r g o n (Ar) ( A r ) %mol % m o l Carbon C a r b o n monoxide m o n o x i d e (CO) ( C O ) ppm p p m Nitric N i t r i c oxide o x i d e (NO) ( N O ) ppm p p m Nitric N i t r i c dioxide d i o x i d e (NO2) ( N O 2 ) ppm p p m Sulfure S u l f u r e dioxide d i o x i d e (SO2) ( S O 2 ) ppm p p m Methane M e t h a n e (CH4) ( C H 4 ) ppm p p m Density D e n s i t y (1) ( 1 ) kg/m3 k g / m 3 Molecular M o l e c u l a r Weight W e i g h t (1) ( 1 ) g/mol g / m o l Molar M o l a r Heat H e a t Capacity C a p a c i t y (1) ( 1 ) kcal/Nm3/°C k c a l / N m 3 / ° C Viscosity V i s c o s i t y (1) ( 1 ) kg/m/h k g / m / h NITROGEN N I T R O G E N WASTE W A S T E EXPANDER E X P A N D E R Composition C o m p o s i t i o n Carbon C a r b o n dioxide d i o x i d e (CO ( C O 2 2 ) ) %mol % m o l Water W a t e r (H ( H 2 2 O) O ) %mol % m o l Nitrogen N i t r o g e n (N ( N 2 2 ) ) %mol % m o l Oxygen O x y g e n (O ( O 2 2 ) ) %mol % m o l Argon A r g o n (Ar) ( A r ) %mol % m o l Carbon C a r b o n monoxide m o n o x i d e (CO) ( C O ) %mol % m o l Nitric N i t r i c oxide o x i d e (NO) ( N O ) ppm p p m Nitric N i t r i c dioxide d i o x i d e (NO2) ( N O 2 ) ppm p p m Sulfure S u l f u r e dioxide d i o x i d e (SO2) ( S O 2 ) ppm p p m Methane M e t h a n e (CH4) ( C H 4 ) ppm p p m Density D e n s i t y (1) ( 1 ) kg/m3 k g / m 3 Molecular M o l e c u l a r Weight W e i g h t (1) ( 1 ) g/mol g / m o l Molar M o l a r Heat H e a t Capacity C a p a c i t y (1) ( 1 ) kcal/Nm3/°C k c a l / N m 3 / ° C Viscosity V i s c o s i t y (1) ( 1 ) kg/m/h k g / m / h (1) ( 1 ) Physical P h y s i c a l properties p r o p e r t i e s at a t suction s u c t i o n Line L i n e revised r e v i s e d under u n d e r Rev. R e v . No. N o . 50 5 0 47 4 7 28 2 8 32 3 2 37 3 7 33 3 3 - - N/A N / A Printed P r i n t e d by b y / / date d a t e / / time: t i m e : RNETW R N E T W / / 34 3 4 41 4 1 44 4 4 49 4 9 05/06/26 0 5 / 0 6 / 2 6 Sheet S h e e t / / of o f Revision R e v i s i o n Case-Name: C a s e - N a m e : 18:02 1 8 : 0 2 / / 1 1 Rev. R e v . 53573 5 3 5 7 3 53573-62-01-PR-013739-KH 5 3 5 7 3 - 6 2 - 0 1 - P R - 0 1 3 7 3 9 - K H 5 5 / / 5 5 ACCSION A C C S I O N 1 1 1 1 48 4 8 1Project 1 P r o j e c t No.Document N o . D o c u m e n t No. N o . 1 1 AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR A L _ C R Y O _ P R O C E S S _ D S _ T E M P L A T E _ C O M P R E S S O R 40 4 0 1 1 1 1 1 1 9.3 9 . 3 164.6 1 6 4 . 6 1 1 42 4 2 1 1 1 1 1 1 45 4 5 46 4 6 - - Derived D e r i v e d from f r o m G-TPL-13-0-1, G - T P L - 1 3 - 0 - 1 , Rev. R e v . 1, 1 , issued i s s u e d 26-Jun-18 2 6 - J u n - 1 8 38 3 8 1 1 39 3 9 1 1 1 1 1 1 43 4 3 Project P r o j e c t Name N a m e 1 1 35 3 5 1 1 36 3 6 1 1 1 1 1 1 - - - - - - 1 1 1 1 30 3 0 1 1 31 3 1 1 1 - - - - 27 2 7 1 1 1 1 1 1 25 2 5 0.36 0 . 3 6 ●●CONFIDENTIAL-RESTRICTED ● ● C O N F I D E N T I A L - R E S T R I C T E D 21 2 1 1 1 22 2 2 26 2 6 1 1 1 1 29 2 9 1 1 1 1 40.86% 4 0 . 8 6 % 1 1 20 2 0 1 1 19 1 9 1 1 1 1 18 1 8 1 1 17 1 7 16 1 6 12 1 2 1 1 14 1 4 1 1 13 1 3 1 1 0.00% 0 . 0 0 % 07 0 7 08 0 8 11 1 1 10 1 0 09 0 9 Supplier/Type S u p p l i e r / T y p e 06 0 6 Driver D r i v e r Electrical E l e c t r i c a l Motor M o t o r Item I t e m Number N u m b e r 624001C39 6 2 4 0 0 1 C 3 9 / / 624001C39T01 6 2 4 0 0 1 C 3 9 T 0 1 / / 624001C39T02 6 2 4 0 0 1 C 3 9 T 0 2 PROCESS P R O C E S S DATA D A T A - - TAIL T A I L GAS G A S COMPANDER C O M P A N D E R - - NITROGEN N I T R O G E N WASTE W A S T E EXPANDER E X P A N D E R 02 0 2 04 0 4 03 0 3 client-logo.bmp c l i e n t - l o g o . b m p Process P r o c e s s Process P r o c e s s Data D a t a Sheet S h e e t Compressor C o m p r e s s o r Air A i r Liquide L i q u i d e Confidential C o n f i d e n t i a l Information I n f o r m a t i o n This T h i s print p r i n t is i s the t h e property p r o p e r t y of o f L’Air L ’ A i r Liquide L i q u i d e S.A. S . A . or o r its i t s (direct ( d i r e c t and a n d indirect) i n d i r e c t ) affiliates a f f i l i a t e s or o r subsidiaries s u b s i d i a r i e s and a n d contains c o n t a i n s valuable v a l u a b l e confidential c o n f i d e n t i a l information. i n f o r m a t i o n . Copyright C o p y r i g h t and a n d all a l l other o t h e r rights r i g h t s in i n this t h i s print p r i n t are a r e expressly e x p r e s s l y reserved. r e s e r v e d . No N o part p a r t of o f this t h i s print p r i n t may m a y be b e disclosed d i s c l o s e d by b y the t h e intended i n t e n d e d recipient r e c i p i e n t to t o a a third t h i r d party, p a r t y , reproduced, r e p r o d u c e d , copied, c o p i e d , lent, l e n t , or o r disposed d i s p o s e d of, o f , directly d i r e c t l y or o r indirectly, i n d i r e c t l y , nor n o r used u s e d for f o r any a n y purpose p u r p o s e other o t h e r than t h a n that t h a t for f o r which w h i c h it i t is i s expressly e x p r e s s l y furnished. f u r n i s h e d . This T h i s print p r i n t is i s lent l e n t subject s u b j e c t to t o return r e t u r n on o n demand. d e m a n d . CASES C A S E S 01 0 1 Designation D e s i g n a t i o n 05 0 5 Number N u m b e r required r e q u i r e d 1 1 6.97% 6 . 9 7 % 70.38% 7 0 . 3 8 % 23 2 3 24 2 4 15 1 5 1 1 574 5 7 4 0.92% 0 . 9 2 % 0.50% 0 . 5 0 % 0.47% 0 . 4 7 % 164.6 1 6 4 . 6 39.8 3 9 . 8 55.72% 5 5 . 7 2 % 4.00% 4 . 0 0 % 0.47% 0 . 4 7 % 0.00% 0 . 0 0 % 0.00% 0 . 0 0 % 21.55% 2 1 . 5 5 % - - 0.34 0 . 3 4 - - - - - - - - 54.60% 5 4 . 6 0 % 52.94% 5 2 . 9 4 % 0.00% 0 . 0 0 % 22.8 2 2 . 8 26.0 2 6 . 0 23.7 2 3 . 7 42.50% 4 2 . 5 0 % 39.71% 3 9 . 7 1 % 3.89% 3 . 8 9 % 4.00% 4 . 0 0 % 12.2 1 2 . 2 12.2 1 2 . 2 9.3 9 . 3 18.5 1 8 . 5 - - - - 31.85 3 1 . 8 5 10.03 1 0 . 0 3 0.06 0 . 0 6 1 1 016 0 1 6 0.06 0 . 0 6 0.06 0 . 0 6 0.06 0 . 0 6 36.97 3 6 . 9 7 36.70 3 6 . 7 0 37.15 3 7 . 1 5 0.36 0 . 3 6 0.36 0 . 3 6 11.9 1 1 . 9 0.32 0 . 3 2 0.32 0 . 3 2 0.06 0 . 0 6 1.06% 1 . 0 6 % 1.06% 1 . 0 6 % 905 9 0 5 905 9 0 5 31.85 3 1 . 8 5 0.34 0 . 3 4 18.5 1 8 . 5 10.03 1 0 . 0 3 1 1 574 5 7 4 39.8 3 9 . 8 6.97% 6 . 9 7 % 0.92% 0 . 9 2 % 0.00% 0 . 0 0 % 70.38% 7 0 . 3 8 % 21.55% 2 1 . 5 5 % - - START-UP S T A R T - U P RATED R A T E D NOMINAL N O M I N A L SUMMER S U M M E R NOMINAL N O M I N A L WINTER W I N T E R NMW N M W LMW L M W NMW N M W 0.0 0 . 0 0.0 0 . 0 89.18% 8 9 . 1 8 % 8.81% 8 . 8 1 % 8.82% 8 . 8 2 % 8.82% 8 . 8 2 % 0.38 0 . 3 8 0.38 0 . 3 8 25.3 2 5 . 3 24.7 2 4 . 7 0.00% 0 . 0 0 % 500 5 0 0 500 5 0 0 92.3 9 2 . 3 67.0 6 7 . 0 0.00% 0 . 0 0 % 303.3 3 0 3 . 3 1.58 1 . 5 8 1.57 1 . 5 7 1.59 1 . 5 9 38.06% 3 8 . 0 6 % 35.37% 3 5 . 3 7 % 35.77% 3 5 . 7 7 % 66.7 6 6 . 7 424.6 4 2 4 . 6 304.7 3 0 4 . 7 55.78% 5 5 . 7 8 % 58.69% 5 8 . 6 9 % 58.22% 5 8 . 2 2 % 0.00% 0 . 0 0 % 5.13% 5 . 1 3 % 5.04% 5 . 0 4 % 5.10% 5 . 1 0 % 0.95% 0 . 9 5 % 0.86% 0 . 8 6 % 0.87% 0 . 8 7 % 748 7 4 8 352 3 5 2 355.5 3 5 5 . 5 0.0 0 . 0 0.0 0 . 0 0.0 0 . 0 0.0 0 . 0 0.0 0 . 0 0.0 0 . 0 0.0 0 . 0 0.38 0 . 3 8 0.06 0 . 0 6 24.9 2 4 . 9 17.37 1 7 . 3 7 17.41 1 7 . 4 1 16.89 1 6 . 8 9 37.25 3 7 . 2 5 37.70 3 7 . 7 0 37.63 3 7 . 6 3 89.18% 8 9 . 1 8 % 1.16% 1 . 1 6 % 0.19% 0 . 1 9 % 0.06 0 . 0 6 0.06 0 . 0 6 0.99% 0 . 9 9 % 0.85% 0 . 8 5 % 0.85% 0 . 8 5 % 0.0 0 . 0 5.54 5 . 5 4 5.44 5 . 4 4 0.00% 0 . 0 0 % 0.00% 0 . 0 0 % 0.00% 0 . 0 0 % 0.0 0 . 0 0.0 0 . 0 0.0 0 . 0 88.85% 8 8 . 8 5 % 0.09 0 . 0 9 5.45 5 . 4 5 28.66 2 8 . 6 6 28.63 2 8 . 6 3 28.63 2 8 . 6 3 6.4 6 . 4 4.5 4 . 5 4.5 4 . 5 0.0 0 . 0 0.0 0 . 0 1 1 1 1 1 1 0.32 0 . 3 2 22.2 2 2 . 2 22.0 2 2 . 0 22.0 2 2 . 0 0.09 0 . 0 9 0.06 0 . 0 6 0.00 0.00 0.00 1.00 0.00 0.69 0.31 1.00 0.00 0.00 0.20 0.20 0.60 0.00 0.50 0.00