WPC0M k]BiaZĜXESr$?QO=,oS2>N= dXX0gڭ>$Oke"ʰT E1׀d^0ܮwrk (c?D.>jD#@,X?Q b#ZtX続TM\\^or9,ހ6j+!:c$"Small Circle"0 ($$   1  4 d,#(&A<< CLevel 1Level 2Level 3Level 4Level 5( $ Figure  1  %#-& I&mage <=8C HKKKK M $"  `Q XXkam\.\ LK:\0089-03\029\001\REPORT\TIER2RPT.RV3\K:\0089-03\029\001\REPORT\TIER2RPT.RV3/  #X6OX `Q#@  2-  2  A  `Q XX6O  )  kam\.\ LK:\0089-03\029\001\REPORT\TIER2RPT.RV3\K:\0089-03\029\001\REPORT\TIER2RPT.RV3/  TABLE AddWPCBK q6(z%4"519Ȑ2G\  `Times NewG        @ Figure2-1.TypicalRefineryDesulfurizationSystem + !x7 + "k G\  `Times NewGAAA        @Hydrogen #w5 G\  `Times NewGAAA        @Plant $G\  `Times NewGAAA        @(w/heaters)+ % + &R G\  `Times NewGAAA        @Hydrotreater ' G\  `Times NewGAAA        @Unit (G\  `Times NewGAAA        @(w/heaters)+ )GG`+ *DG\  `Times NewGAAA        @Amine +TG\  `Times NewGAAA        @Unit+ ,h + -G\  `Times NewGAAA        @Sulfur .KeG\  `Times NewGAAA        @Recovery /gG\  `Times NewGAAA        @Unit+ 0z~+ 1/xG\  `Times NewGAAA        @TailGas 2*G\  `Times NewGAAA        @Unit+ 3K| + 4G\  `Times NewGAAA        @Power 5>4G\  `Times NewGAAA        @Plant+ 6  `7o k2 k  8~  `9| } }; + :Y ; <+n = >@ ? @U `A i+ B  `Cd  Ds s  `Es '  F  `GZ  H _  `I G  J  `K8  L  `Mo   N d  `Ow w I w  P\ i\  `Q \   R*  `SQPPc+ TT U V&i W X;~ Y  ZP `[B+ \   `] W + ^N G\  `Times NewGwww        @Gasoline+ _|%|W  ``|I0EE+ aG\  `Times NewGwww        @Steam bG\  `Times NewGwww        @Steam cbTG\  `Times NewGwww        @Electricity+ d@@*  `e@+ fnG\  `Times NewGwww        @Electricity g G\  `Times NewGwww        @Fuelgas h/ G\  `Times NewGwww        @Naphtha iI G\  `Times NewGwww        @Hydrogen jg@G\  `Times NewGwww        @Heater kQFG\  `Times NewGwww        @fluegas lb2G\  `Times NewGwww        @Heater mL9G\  `Times NewGwww        @fluegas n{UG\  `Times NewGwww        @Fugitive oB;G\  `Times NewGwww        @Fugitive p G\  `Times NewGwww        @Lowsulfurgasoline+ q ~+ rhG\  `Times NewGAAA        @Sour s G\  `Times NewGAAA        @Water te G\  `Times NewGAAA        @Stripper+ u@T `vM wh `xPTT+ y[ z) {q |? } ~T  `^__G+ 'I'I1 `;     1 ` #  + VNG\  `Times NewGwww        @Steam+ Bt `fb<b+ KG\  `Times NewGwww        @Electricity+ V7 ` H  + b 5 5  50 5 x 5 5  5E 5  5 5  5[ 5  5 5 ` 3 + mG\  `Times NewGwww        @Steam+ F _ `I %V% >c7 `y:ww+ G\  `Times NewGwww        @Water /G\  `Times NewGwww        @Sourgas  G\  `Times NewGwww        @Sourwater 0 G\  `Times NewGwww        @Sourgas+ M' `688/ "W `GKKh -"A `:  < `!!!/ -"/+ !G\  `Times NewGwww        @Fuelgas B>G\  `Times NewGwww        @Fuelgas+ G: e `N Z Z `Z mm `m"+ G\  `Times NewGwww        @Air+ Z `~,~+ G\  `Times NewGwww        @Electricity+ DD `D o+ G\  `Times NewGwww        @Sulfur+ f\fW  `"%%o  `a 70 `E2HH xx `x,+ OG\  `Times NewGwww        @Reactor MG\  `Times NewGwww        @fluegas >G\  `Times NewGwww        @Tailgas+ e `wu-u syT `w+ EmE `E+ 5G\  `Times NewGwww        @H N5G\  `Times NewGlll        @2 5G\  `Times NewGwww        @S uG\  `Times NewGwww        @H HuG\  `Times NewGlll        @2 uG\  `Times NewGwww        @S $G\  `Times NewGwww        @Fuelgas gG\  `Times NewGwww        @Sourwater+ s% `I::+ @G\  `Times NewGwww        @Fuelgas+ ^ ^  `^  + G\  `Times NewGwww        @Fluegas+    R    $ g    :}  ` K + (G\  `Times NewGwww        @Steam+ *N[ `W + G\  `Times NewGwww        @Electricity 'FG\  `Times NewGwww        @Sourwater+   9 ` + '<'+ G\  `Times NewGwww        @Electricity+ b  d89*OLE*WPC'  9! ƚ <X 9  .1   & & MathType "-<<k Times New Roman)-2 @Burner_ 2 eCostk2  $5000 2 N 2 N [Times New RomanU- 2 0.9p8pPSymbol- 2 = 2   & "Systemn-WPWin 6.0/OLE 1.0 Prefix Information MarkerEquation.COEE2ࡱ> Root EntryF1O+K@Ole 9CompObjjBOlePart )F! WPWin61[1] FMicrosoft Equation 2.0 DS EquationEquation.COEE29q3,r 9  .1   & & MathType "-<<k OlePres000Equation Native Times New Roman)-2 @Burner_ 2 eCostk2  $5000 2 N 2 N [Times New RomanU- 2 0.9p8pPSymbol- 2 = 2   & "Systemn-dXkCY Burner_Cost=$5000N 0.9 N  METAFILEPICTtz 9  .1   & & MathType "-<<k Times New Roman)-2 @Burner_ 2 eCostk2  $5000 2 N 2 N [Times New RomanU- 2 0.9p8pPSymbol- 2 = 2   & "Systemn-Table_A / O$    *    Hydrogenistypicallyproducedusingasteamreformingprocess.Theprocessincludes  feedinglighthydrocarbons(C1'sthroughC4's)andsteamthroughcatalystfilledtubesinaspecializedheatercalledareformer.t(c(3$ !  3- Table_ATABLE ATABLE A   PQ*OLE*  O$    *    Hydrogenistypicallyproducedusingasteamreformingprocess.Theprocessincludes  feedinglighthydrocarbonsandsteamthroughcatalystfilledtubesinaspecializedheatercalledareformer.Hydrogencanalsobeproducedusingacatalyticreformingprocess.Theprocessincludesfeedingheavyhydrocarbons,suchasnaphthas,overacatalystunderhighheat. N $"  `Q XXkam\.\ LK:\0089-03\029\001\REPORT\TIER2RPT.RV3\K:\0089-03\029\001\REPORT\TIER2RPT.RV3/  XXX#X6OX `Q#@  3-  11  A  `Q XX6O((3$ !      0  WPC'  9! ƚ <X 9  .1   & & MathType "-<<k Times New Roman)-2 @Burner_ 2 eCostk2  $5000 2 N 2 N [Times New RomanU- 2 0.9p8pPSymbol- 2 = 2   & "Systemn-`DWPWin 6.0/OLE 1.0 Prefix Information MarkerEquation.COEE2ࡱ> Root EntryFN|n@Ole 9CompObjjBOlePart )F! WPWin61[1] FMicrosoft Equation 2.0 DS EquationEquation.COEE29q3,r 9  .1   & & MathType "-<<k OlePres000Equation Native Times New Roman)-2 @Burner_ 2 eCostk2  $5000 2 N 2 N [Times New RomanU- 2 0.9p8pPSymbol- 2 = 2   & "Systemn-dXkCY Burner_Cost=$5000N 0.9 N  METAFILEPICTtz 9  .1   & & MathType "-<<k Times New Roman)-2 @Burner_ 2 eCostk2  $5000 2 N 2 N [Times New RomanU- 2 0.9p8pPSymbol- 2 = 2   & "Systemn-(5hCEKQW]cioAutoList11.1.1.1.1.1.1.1. N $"  `Q XXkam\.\ LK:\0089-03\029\001\REPORT\TIER2RPT.RV3\K:\0089-03\029\001\REPORT\TIER2RPT.RV3/  XX#X6OX `Q#@  3-  12  A  `Q XX6O3#37=CIQYag1.a.i.(1)(a)(i)1)a)(;3$2#  0  .3  0    )  kam\.\ LK:\0089-03\029\001\REPORT\REPORT6A.WPD\K:\0089-03\029\001\REPORT\REPORT6A.WPD/   N $"  `Q XXkam\.\ LK:\0089-03\029\001\REPORT\TIER2RPT.RV3\K:\0089-03\029\001\REPORT\TIER2RPT.RV3/  XX#X6OX `Q#@  3-  13  A  `Q XX6O d d1  d4-  N $"  `Q XXkam\.\ LK:\0089-03\029\001\REPORT\TIER2RPT.RV3\K:\0089-03\029\001\REPORT\TIER2RPT.RV3/  XX#X6OX `Q#@  3-  14  A  `Q XX6O   Table_A ='    Table42._BACT_ԀControlHierarchyforEquipmentLeaks(Continued)  N $"  `Q XXkam\.\ LK:\0089-03\029\001\REPORT\TIER2RPT.RV3\K:\0089-03\029\001\REPORT\TIER2RPT.RV3/  XX#X6OX `Q#@  3-  15  A  `Q XX6OTable_A M $"  N XXkam\.\ LK:\0089-03\029\001\REPORT\REPORT6A.WPD\K:\0089-03\029\001\REPORT\REPORT6A.WPD/  XXX#X X N#@  4-  12  A  N XX &0 d dg WPC))ll!lR]ƚj.-"_ .U&,\  & &$TNPPMicrosoft PowerPoint & TNPPf & &TNPP , l1x`X45&gpTimes New Romanq-.  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"-K --'- $^5^ & &grB--B "-dm--'- $jG & &q@lH--l "-@W@~--'- $r@c & &kDs8--8D "-Xkk--' & &BdTimes New Romanq-.  2 "Fuel gas50+0*& & &~Times New Roman=-.  2 < Fuel gas50+0*& & &&---B "---' & &--(` "-(V--'- $$\$ &  & &w--:[w "-W--'- $%n% & &:B--W "-::w--'- $:] & &aTimes New Romanq-.   2 =AirE  & &---7Z "-d--'- $l & &i}u2Times New Romanq-.  2  Electricity;++ *0 & &&---> "-(--'- $s & &$--| "-p --' &  & & Times New Romanq-.  2 fZSulfur50 0  & &CK--- "-VClC--' & &CS--\C "-;S--'- $K & &EM--< "-E7E--'- $Eyh" & &--L "---'- $pp & &_g-- "-\__--'- $_<   & &DTimes New Romanq-.  2 Reactor@+*+0 Times New Roman=-.  2 wflue gas 0*0+% & &Y)Times New Roman4-.  2 Tail gas;*0*& & &---> "---'- $JJ & &--iN "-F--'- $ & &--JE "-:x--'- $  & &W Times New Romanq-.   2 HETimes New Roman=-  2 $2Times New Roman4-  2 @S5 & &u*Times New Roman=-.   2 HETimes New Roman4-  2 2Times New Roman=-  2 *S5 & &M Times New Roman4-.  2 bFuel gas50+0*& & &Times New Roman=-.  2  Sour water500 F*+  & &q5e>---!q "-47I--'- $]6Y & &TBTimes New Romanq-.  2 Fuel gas50+0*& & &Sh[T---T "-0SS--'- $Sg0v & &>Times New Romanq-.  2 JFlue gas50+0*& & &Q---?QQQ "-p0Qp--'- $qq & &]1Times New Romanq-.  2 Steam5+*K & &Mlv---M "-pj]--'- $l^J^ & &Times New Romanq-.  2  Electricity;++ *0 & &'wF,Times New Roman=-.  2 a Sour water500 F*+  & &)5&ow---  "-oo--'- $oLGG & &)5Times New Romanq-.  2 >c Electricity;++ *0 &  & &S---8S "---' & &TNPP & --#M -, dc    N $"  `Q XXkam\.\ LK:\0089-03\029\001\REPORT\TIER2RPT.RV3\K:\0089-03\029\001\REPORT\TIER2RPT.RV3/  XX#X6OX `Q#@  3-  17  A  `Q XX6O N ='  X6OXXX@ #X6OXXX6O#q+m=-)b| ` @EdVq Table33.SummaryofTopDown_BACT_ԀImpactAnalysisResults(Continued)  M $"  `Q XXkam\.\ LK:\0089-03\029\001\REPORT\TIER2RPT.RV3\K:\0089-03\029\001\REPORT\TIER2RPT.RV3/  XX#X6OX `Q#@  3-  17  A  `Q XX6O`TABLE A(#$  0  Table_ALevel 1Level 2Level 3Level 4Level 5Level 1Level 2Level 3Level 4Level 5Level 1Level 2Level 3Level 4Level 5%#-&&OLE 2.0 Box <=8C HKKKKwx*OLE*WPC'+&5\+&5\9!+&5\BƚC.Ab     4<' """)))UUUMMMBBB999|PP3f333f3333f3ffffff3f̙3ff333f333333333f33333333f33f3ff3f3f3f3333f33̙33333f333333f3333f3ffffff3f33ff3f3f3f3fff3ffffffffff3ffff̙fff3fffff3fff333f3f3ff3ff33f̙̙3̙ff̙̙̙3f̙3f333f3333f3ffffff3f̙3f3f3f333f3333f3ffffff3f̙3f3ffffffffff!___www45'  Arial-----Arial5-----Arial$------------"Systemn-'- 4<-'- 4<8- "- $<ii < <i "-i<i  <i< "-i< <- # <J #J < # <#<#<i#i< <  < <     y  y    L L       "---'--- !!---'---  T'---'---  T'8- - "-  $#---'---   T'B  $- B W B - ---'---   T'  $     ---'---   T'---'---   T'---'---  4<--------'---  gn 2 ! Figure 4-1.==='88!8v2 JEquipment Leak Control Levels for Large Hydrotreaters- Cost and ReductionsC===Y8=!=888H==!'==8688!='=8'=8H5='=!'88!8'8!H=8!8==H8==8!==8----'---  4<---'---  4<----'---  4< 2 R 20,000.....2  25,000.....2 30,000.....2 35,000.....2 q40,000.....2 945,000.....---'---  4<---'---  4<  2 90.. 2 x95.. 2 100... 2 4 105... 2 110... 2 115... 2 p120... 2 125... 2 C130...---'---  4<------'---  `?e  32 Uq VOC Emission Reductions (tpy)7A<7J..33<.33.33.3-----'---  4<-----'---   4d Arial-2 wAnnualized Cost ($/yr)-----'---  4<---'---  4<--  45- "- M Q --- -  -8 Y --  2 \ NSPS<777' 4<--- - [q--- -  -Fy--  2 |HON<A<' 4<--- -  p --- -  - x -- !2 { New Source NESHAP<.;7..*.<77<77' 4<-- -' 4< '  'WPWin 6.0/OLE 1.0 Prefix Information MarkerExcel.Sheet.8ࡱ> -\  !"#$%&'()*+,/0123456789:<=>?@ABCDEFGHIJKLMNOPQRSTUVWXYZ[Root Entry F`_QnOle CompObjbWorkbookuP  FMicrosoft Excel ChartBiff8Excel.Sheet.89q?8o՜.+,D՜.+,`HP X`hp x 1 Sheet1Large HydrotreaterSmall Hydrotreaters IBa= '()*&<=xZX/Y8X1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial"$"#,##0_);\("$"#,##0\)!"$"#,##0_);[Red]\("$"#,##0\)""$"#,##0.00_);\("$"#,##0.00\)'""$"#,##0.00_);[Red]\("$"#,##0.00\)7*2_("$"* #,##0_);_("$"* \(#,##0\);_("$"* "-"_);_(@_).))_(* #,##0_);_(* \(#,##0\);_(* "-"_);_(@_)?,:_("$"* #,##0.00_);_("$"* \(#,##0.00\);_("$"* "-"??_);_(@_)6+1_(* #,##0.00_);_(* \(#,##0.00\);_(* "-"??_);_(@_)83_(* #,##0.000_);_(* \(#,##0.000\);_(* "-"??_);_(@_)4/_(* #,##0.0_);_(* \(#,##0.0\);_(* "-"??_);_(@_)0+_(* #,##0_);_(* \(#,##0\);_(* "-"??_);_(@_)                + ) , *    8 ``i̜̙3f3333f3ffff333ff333f33f33BBB\nLarge HydrotreaterSmall Hydrotreaters+Large Hydrogen8Small Hydrogen&GSheet1rj03  @@  TAC HON Reg Neg Mod. Reg NegPet Ref NESHAPBAAQMD-2SCAQMD-2BAAQMD-1SCAQMD-1NSPSERLargeSmall HydrotreatersHydrogen  % l8*~H~ bPbexbHbD~H~ e}`T0   be `T0D~b}}bNe `T0b85~5~$ bbd~bTb{Apd~ ~lb{ApApLd~b]d~ ~ bDI\be8e beDbb{ApWBApLP (b}e ~!p!Apeb<(0b}l~be}ee85~l~?}`T0$? ?be`T0L5~,b zel6~5~}ǹeb@@b֜z0Pbd{0cT0`btbb}0RT0bbbbz0brbb%00br` 0r0bQ` 0~  IMHP LaserJet 5/5M PostScriptw odXX]p?gRdCustom page 1|CCCustom page 2|CCCustom page 3|CC"d??3` 4#` 4#` 4#` 4#` 4#( 333ff3 r  0L-  @& ]L-< <NSPS<$rr  0-  @  ]- <HON<ll  s *-  @ & G ]- <New Source NESHAP<0 0 3d 3QQ ; Q ; Q3_4E4D$% M 3O&Q4$% M 3O&Q4FAx p 3O- 3*V@@`@@#M43*@@@@@@#M4% M3O&Q >VOC Emission Reductions (tpy)'4% 3HgMZ3O&Q 0Annualized Cost ($/yr)'4523  NM43d" 3_ M NM  MM<444% R$ JM03O70&Q VFigure 4-1. 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Reg NegPet Ref NESHAPBAAQMD-2SCAQMD-2BAAQMD-1SCAQMD-1NSPSERLargeSmall HydrotreatersHydrogen  % l7~}bPbexbHbD~} 8e}`T0   be`T0D~b}}bNe`T0bp}}H bb>>G?|N'|>T0btebb{ApWBApLP b}eh}eDbb{ApWBApLP (b}eh}pApeb<(0b}0}be}e&ep}0}?}`T0H? ?be&`T0},b ze~}}ǹeb@@b֜z0Pbd{0cT0`btbb}0RT0bbbbz0brbb%00br` 0r0bQ` 0~  IMHP LaserJet 5/5M PostScriptw od]p?gRdCustom page 1|CCCustom page 2|CCCustom page 3|CC"d??3` 4#` 4#` 4#` 4#` 4#( 333ff3 r  0L-  @& ]L-< <NSPS<$rr  0-  @  ]- <HON<ll  s *-  @ , ]- <New Source NESHAP<0 0 3d 3QQ ; Q ; Q3_4E4D$% M 3O&Q4$% M 3O&Q4FAx p 3O- 3*V@@`@@#M43*@@@@@@#M4% M3O&Q >VOC Emission Reductions (tpy)'4% 3HgMZ3O&Q 0Annualized Cost ($/yr)'4523  NM43d" 3_ M NM  MM<444% R$ JM03O70&Q VFigure 4-1. Equipment Leak Control Levels for Large Hydrotreaters- Cost and Reductions'44e6'"̍ _@I؅(^@?o[@e'Sc@\S'@@e>   IMHP LaserJet 5/5M PostScriptw od]p?gRdCustom page 1|CCCustom page 2|CCCustom page 3|CC"d??3` 4#` 4# ` 4#` 4#` 4#  ( 333ff3  l  s *3  @"Q]3 <NSPS<$rr  0@4  @  X ]@4 <HON<ll  s *4  @  r ]4@  <New Source NESHAP<.g0 0 3d 3QQ ; Q ; Q3_4E4 3QQ ; Q ; Q3_4E4D$% M 3O&Q4$% M 3O& Q4FAx p 3O- 3*I@R@@?D@#M43*@X@@@@@@#M4% M3O&Q >VOC Emission Reductions (tpy)'4% 3HgMZ3O&Q 0Annualized Cost ($/yr)'4523  NM43d" 3_ M NM  MM<444% R< JM03O>0&Q WFigure 4-2. Equipment Leak Control Levels for Small Hydrotreaters- Costs and Reductions'44ecpQ@cpQ@M4cQ@M4cQ@$p+O@$p+O@e1Q@_@T@@_@X@\@e>   IMHP LaserJet 5/5M PostScriptw od]p?gRdCustom page 1|CCCustom page 2|CCCustom page 3|CC"d??3` 4# ` 4# ` 4#` 4#` 4#0( 333ff3 r  0:  @V]:  <NSPS <.ll  s *;  @ )  ];L  <HON<ll  s *X;  @ j  ]X;  <New Source NESHAP<.g0 0 3d 3QQ ; Q ; Q3_4E4D$% M 3O& Q4$% M 3O& Q4FAx p 3O- 3*W@@`@@?W@#M43*@@@@@@@#M4% M3O&Q >VOC Emission Reductions (tpy)'4% 34gMZ3O&Q 2Annualized Costs ($/yr)'4523  NM43d" 3_ M NM  MM<444% R JM03OR0&Q YFigure 4-3. 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Figure 4-4.==='88!8{2 MEquipment Leak Control Levels for Small Hydrogen Units - Costs and ReductionsC===Y8=!=888H==!'==8688!='CY8H5='==8=H=!8!H=8!88==H8==8!==8----'---  4<---'---  4<----'---  4< 2 Y 45,000....2 % 46,000....2 47,000....2 48,000....2 49,000....2 W10,000.....---'---  4<---'---  4<  2 50.. 2 55.. 2 60.. 2 65.. 2 70.. 2 q75..---'---  4<------'---  nFs  32 \ VOC Emission Reductions (tpy)7A<7J..33<.33.33.3-----'---  4<-----'---   0i Arial-2 |Annualized Costs ($/yr)-----'---  4<---'---  4<--  45- "- _`  --- -  -VK  --  2  NSPS<7772 g ' 4<--- - Y --- -  -P --  2 HON<A<' 4<--- - \  t--- -  ---- - Z e --- -  -Q P -- !2 New Source NESHAP<.;7..*.<77<77' 4<-- -' 4< '  '*OLE*WPC'+&5\+&5\9!+&5\$ƚC.Ab 8    4<' """)))UUUMMMBBB999|PP3f333f3333f3ffffff3f̙3ff333f333333333f33333333f33f3ff3f3f3f3333f33̙33333f333333f3333f3ffffff3f33ff3f3f3f3fff3ffffffffff3ffff̙fff3fffff3fff333f3f3ff3ff33f̙̙3̙ff̙̙̙3f̙3f333f3333f3ffffff3f̙3f3f3f333f3333f3ffffff3f̙3f3ffffffffff!___www45'  Arial$---Arial-----Arial----------"Systemn-'- 4<-'- 4<8- "- $<}} < < "-<} } << "-< <- # < # < # <* #* <#<D#D<#<^#^<#< < } < <     t  t    E E     } } "---'--- !!---'---  '---'---  '8-  "-t     r r q q   || r rtt - "-  $_ )t  t _ ---'---   '  $l   x l ---'---   '  $     ---'---   'r  $ ] r r ] ---'---   'q  $\ q  q \ ---'---   '  $   ---'---   '| $g||g---'---   ' r $r r ] r---'---   ' $---'---   't $tt_t---'---   '---'---   '---'---  4<------'---  n y2 LFigure 3-1. NOx Control Levels for 10 MMBtu/hr Heaters-Costs and Reductions==='88!8HN8H==!'==8688!='88SSH!=='H88!8'8!H=8!88==H8==8!==8----'---  4<---'---  4<----'---  4<  2 S 0.2 /5,000....2 m 10,000.....2 15,000.....2 20,000.....2 25,000.....2 30,000.....2 .35,000.....2 40,000.....---'---  4<---'---  4<  2 2.5.. 2 k3.5.. 2 4.5.. 2 ; 5.5.. 2 6.5.. 2 7.5.. 2 t8.5.. 2 9.5.. 2 -10.5...---'---  4<------'---  >@z  12 V NOx Emission Reduction (tpy)<A.7J..33<.33.333-----'---  4<-----'---  x d Arial-2 l wAnnualized Cost ($/yr)-----'---  4<---'---  4<--  45- "-   )--- -  -  =--  2 =LNB.<7' 4<--- -  T >--- -  - ? R--  2 RULNB<.<7' 4<--- - R--- -  -I--  2 SCR7<<' 4<--- - O--- -  -F-- 2  ULNB+ SCR<.<707<<' 4<--- - .  --- -  -% | --  2 FGR3A<' 4<--- - . --- -  -% ! -- 2 ! FGR+LNB3A<0.<7' 4<--- - z V --- -  -e j --  2 j SNCR7<<<' 4<--- - Q --- -  -Y -- 2 \ LNB+SNCR.<707<<<' 4<--- - Qk--- -  -Y-- 2 \ ULNB+SNCR<.<707<<<' 4<--- - ,--- -  -@-- 2 @LNB+SCR.<707<<' 4<-- -' 4< '  '-WPWin 6.0/OLE 1.0 Prefix Information MarkerExcel.Sheet.8bࡱ> .  !"#$%&'()*+,-./0123456789:;<=>?@ABCDEFGHIJKLMNOPQRSTUVWXYZ[\]^_`abcdefghijklmnopqrstuvwxyz{|}~Root Entry F61oOle CompObjbWorkbook@'  FMicrosoft Excel ChartBiff8Excel.Sheet.89qGcOh+'0HPl ERG - MorrisvilleeERG - MorrisvilleeMicrosoft Excel@$'o@7?@h      !"#$%&'()*+,-/ I@Ba=     <=. 8 X1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1 Arial1$Arial1QTahoma1QTahoma1Arial"$"#,##0_);\("$"#,##0\)!"$"#,##0_);[Red]\("$"#,##0\)""$"#,##0.00_);\("$"#,##0.00\)'""$"#,##0.00_);[Red]\("$"#,##0.00\)7*2_("$"* #,##0_);_("$"* \(#,##0\);_("$"* "-"_);_(@_).))_(* #,##0_);_(* \(#,##0\);_(* "-"_);_(@_)?,:_("$"* #,##0.00_);_("$"* \(#,##0.00\);_("$"* "-"??_);_(@_)6+1_(* #,##0.00_);_(* \(#,##0.00\);_(* "-"??_);_(@_)0.0 0.00000 0.000000 0.0000 0.000 #,##0.0"Yes";"Yes";"No""True";"True";"False""On";"On";"Off" 0.0000000 0.00000000                + ) , *             " "0 "0@   ( "0@  "0@ "4@  " " "4  $  $  $`  `  $`  `@ @   d@   d@     @@  @   @  @   $   @  $   $  $  $ # "0  $  @   @  $@  $ @  $@  $  $ @  $@  $ @ (0@ *0@  `@  $`@  $`@  $`  $`@  @  @@ *0  @  $@  $@ "0@ "0@@ *0@  $@  $@  $@@  $`@  @@  @  @@  `@  "@ @ *0"@  $"@  $"@  $"@ @  $"`@ "0@@  $   $ ` "0@ "0@  "@ "0"@ "0"@ "0` *0  "0"@ @ "0"`@ "0   $ @ "0 @ "0 "0`@   @ "" ""8 ""8`  $" @ 0@ *0  @  "@ @ *0"@   @ "0@@ "0 @ "0@@ "0@ "0  @ "0@@ "0@ "0  @ "0@ "0 "0  " "0 "0 0 0 0 0 0`  * SCRAmmrateNDLNB&ULNB aFGR zSCRSCRvend1  SCRvend2&TAC 4SNCR^c Efficiencyq INCREMENTAL 10 +50 75 F150 350:summary8 ph@'M      0e0e      A@@ A5% 8c8c     ?1 d0u0@Ty2 NP'p<'pA)BCD|E||@   Heater Capacity (MMBtu/hr)Cost Capital CostLowHigh InstallationTaxesTaxes and FreightTotalTotal Capital CostCapital Recovery equipmentCapital Recovery-catAmmoniaTaxes, Ins, AdminWasteDisposal Storage TanksTACCap and FreightStorage TankTCI EngineeringCap RecEquipmCatTax, InsAdmin ElectricityULNBLNBHeater Size (MMBtu)NoxAverage IncrementalEmission AnnualizedCost-Heater Emissions Reductions EffectivenessSizeControl Alternative(tpy)($/yr) ($/ton NOx) 10 MMBtu/hrBaselineLow Nox BurnerSCRUltra Low Nox Burner 50 MMBtu/hr 75 MMBtu/hr 150 MMBtu/hr 350 MMBtu/hr TAC summarySCR+ULNBSCR AVGUltra Low Nox Burner and SCRVendor 1--179 ppmVendor 1--33 ppmVendor 2--179 ppmVendor 2--33 ppmOld Avgvendor comparison (lb NH3/hr) % differenceSCR+LNBSCR TechnologyNOx ppmNOx (lb/MMBtu)% Redux UncontrolledFGRFGR+LNBSNCRLNB+SNCRLNB+SCR ULNB+SNCRULNB+SCRHeater Size (GJ/hr)Heater Size (MMBtu/hr)Fuel penalty($/yr) SNCR + LNB SNCR + ULNBNOxLow Nox Burner (LNB)Ultra Low Nox Burner (ULNB)Flue Gas Recirculation (FGR)Ultra Low Nox Burner and SNCRCase LNB level ULNB level(ppmv) (lb/MMBtu)Ammonia feedrate (lb NH3/hr)a"Ammonia Cost ($/yr)b" Total Annual Cost ($/yr) Annual CostsControlsCapital Cost (July 1999 $)a"Electricity Cost ($/yr)c"Maintenance Cost ($/yr)d"Capital Recoverye"Total Annual Cost ($/yr)f"SNCR Total Annual Cost ($/yr) Heater SizeElectricity Costs Maintenance Costs ($/yr)Capital (July 1999 $)a "($/yr)b" Costs ($/yr)c "Recovery ($/yr)d" Costs ($/yr)e " Capital CostsNumber of Burnersa"Vendor 1 EquipmentCatalyst179 ppmv33 ppmvVendor 2CapitalCapacity Taxes andAmmonia Taxes, Ins,Annual Annual Cost'Annual Cost Calculated from Vendor DataASummary of Total Annual Costs for Control Technology CombinationsVendora"Levelb" Cost ($)c" Cost ($)d" Shipping ($)e " Storage ($)f "jCapital Recovery($/yr)d" Cost ($/yr)e " Admin ($/yr)f "SCRg" SCR Costh" LNB Costi" SCR Costj" ULNB Costk "NOx Inlet LevelPrice per Burner ($)b"Purchased Equipment Cost ($)c"Total Capital Cost ($)d"Annual Costs ($/yr)e"Price per Burner ($)f" NOx InletStandard Burner Price ($)Purchased Equipment Cost ($)Annual Costs ($/yr)Standard Burner Annual Cost Differential ($/yr) e>1dGP\?{ap&7{-pa AE!L!64'G"]"4'x#$u $N be`T0b|Bmmbe`T0bbmbe&n`T0b@.n.nub  bv* /yr) Admin ($/yr)f "bdbDT0bt00ApApzm00b E000bbb߿0bDeLbb{ApWBApL0b}e&npApe(mm(#nhb\e dbe(mH#nbe(me.e@.nXm`T0u   be.`T0T.n4b zet/n.nmǹePQt/ne`T0`T0H;m&nPb&nXbÆ0t/n`T0dbtb`T0b|bŕ0`T0`T0)0`T0`T0by0pbb%00bp` 0p0b.Lbx~b Pb,b0Heater Capacity (MMBtu/hr)Cost Capital CostLo I@  dMbP?_*+%B?&CAppendix A.2.1 Calculation of Ammonia Cost for Control Cases&?'?MHP LaserJet 4V/4MV PostScriptg odXX ^ RdCustom page 1BBCustom page 2BBCustom page 3BB"d??U} }  } $ }  } $} $+[8I@bbbbbb bb      b 0 OPNOx Inlet LevelPOOP CaseHHeater Size (MMBtu/hr)(ppmv) (lb/MMBtu),IAmmonia feedrate (lb NH3/hr)a"&vendor comparison (lb NH3/hr) % difference#IAmmonia Cost ($/yr)b"?$@?`f@MA2K?7D.A.= ףpx@fffff4@fffff1@")C[c?DD.~ P@-D}`1@DDDd'Fu)}@D8",?I@?`f@MA2K?7D.A.= ףpx@fffff4@fffff1@")C17^@DD.~ t@-D#}`1@DDDd'FԳ\@D8", Uncontrolled?R@?`f@MA2K?7D.A.= ףpx@fffff4@fffff1@")CʥR@DD.~ ~@-Dis O4@DDDd'FC@D8",?b@?`f@MA2K?7D.A.= ףpx@fffff4@fffff1@")CʥR(@DD.~ @-D"}`1@DDDd'FC@D8",8@u@@`f@MB2K?7D.A.= ףpx@fffff4@fffff1@")El$<@DD.~ 8@->S32@DDDd'GY<@D8",?$@?T@MA/1&|?7D.A.= ףpx@fffff4@fffff1@")Cq?DD. D'F(6~@D8",?I@?T@MA/1&|?7D.A.= ףpx@fffff4@fffff1@")CVn?DD. D'FcZx5@D8",  LNB level ?R@?T@M A/1&|? 7D .A.= ףpx@fffff4@fffff1@") Cb@ D D . D' F4fPS@D 8",  ?b@?T@M A/1&|? 7D .A.= ףpx@fffff4@fffff1@") Cb@ D D . D' F4fPS@ D 8", 8 @u@@T@M B/1&|? 7D .A.= ףpx@fffff4@fffff1@") E)@ D D . 8>' GOI@ D 8",  ?$@?@@M A? 7D .A.= ףpx@fffff4@fffff1@") Ccn:? D D .~ 6@- DڥKHD D D d' FzQh@ D 8",  ?I@?@@M A? 7D .A.= ףpx@fffff4@fffff1@") C n? D D .~ P@- DgfiYذ%@ D D D d' FOYQe@ D 8", ULNB level?R@?@@MA?7D.A.= ףpx@fffff4@fffff1@")C}ǦR?DD.~ [@-D5? DDDd'F=kl̖@ D8",?b@?@@MA?7D.A.= ףpx@fffff4@fffff1@")C}ǦR@DD.~ k@-D5?DDDd'F=kl̦@D8",*Ju@J@@MK?7D.A.= ףpx@fffff4@fffff1@")L`@DD.~ *@-M;.D @DDDd'N&.')@D8",(cT>h(  hr h 0,G  @ ]`,GT  >(<?a Calculated assuming 1:1 ratio of NOx to ammonia, ammonia MW of 17, and NOx MW of 46. This calculation assumes that additional ammonia will be injected beyond the amount that would react with NOx to achieve the estimated emission reduction. This was done to account for ammonia slip and incomplete mixing of ammonia and flue gas. b Calculated using $300/ton cost for annhydrous ammonia. This value is the midpoint of the range of costs as reported in the "Status Report on NOx Control Technologies and Cost Effectiveness for Utility Boilers," NESCAUM/MARAMA, June 1998.<("y1gN"yOR#g>>@  I@  dMbP?_*+%30&CAppendix A.2.2 ULNB and LNB Cost CalculationsMHP LaserJet 4V/4MV PostScriptg od ^ RdCustom page 1BBCustom page 2BBCustom page 3BB"d??U} } $ } I }  }  } $ } I } $ } } } }   T0 b b     b  b :   b b  b     mn b`E ,@b !pStandard Burner  =l Capital Costs~ QHeater Size (MMBtu)!aNumber of Burnersa""QStandard Burner Price ($)%QPurchased Equipment Cost ($)oTotal Capital CostAnnual Costs ($/yr) $@l?#( @ D !( @ DD %5Ҫ@D{Gz?!bY:TE~@ DD((( I@l@#(Kw+@ D!(ޞ@ DD%5[U@D{Gz?!bnSA@ DD((( R@l@#(J@D{Gz?!hVlj@ DD(((    !p ULNB  LNB  =l  Capital Costs ~  Capital Costs 3  QHeater Size (MMBtu)! aNumber of Burnersa"$ WPrice per Burner ($)b", QPurchased Equipment Cost ($)c"& }Total Capital Cost ($)d"# oAnnual Costs ($/yr)e"( aAnnual Cost Differential ($/yr)$ WPrice per Burner ($)f", QPurchased Equipment Cost ($)c"& QTotal Capital Cost ($)d"# WAnnual Costs ($/yr)e"( oAnnual Cost Differential ($/yr) $@l?X@! (@  D D % 5@ D {Gz?! 5,@  D D! V:TEn@  D D- X@ D (\?! (@ D D % (n@ D {Gz?! X,=F1@ D D! 5okT=@ D DI@l@2X@D D?D!(&C@ DD%5Á;1h@D{Gz?!5$kfb@ DD!lSA@  DD-X"@D(\?!(eDX+`@ DD% (jT>A@ D{Gz?! XK;@ D D! 5@NE6_@  D DR@l@2X-)4@D D?D!(㛿"@ DD%5CA@D{Gz?!5A6@ DD!Ev@ DD-X62@D(\?!(O|7@ DD% (7z@ D{Gz?! X,%xS@ D D! 5CE e@ D Db@l.@2X C˭@D D?D!(n~@ DD%5hs@D{Gz?!5Ȳb@ DD!`إ@ DD-X5@D(\?!(cQ@ DD% (ڏ]HT@ D{Gz?! X^Ĺ(@ D D! 5Хl6t@ D Dnu@qA@2[;J_@D D?D!)@ DD%h]@D{Gz?!eAg>@ DD!eXlj@ DD-[ƻLOX@D(\?!)`(@ DD% )V"@ D{Gz?! [=O@ D D! hpnh(1{@ D D  L,9m9?6Q?Q? Q?   .HD""Sf}"x (  r  0[  @ $]`[ 1h<2a As per vendor advice. b See Appendix A.1 for vendor supplied information. Burner price was calculated by multiplying the single burner price by: [(# burners)^0.9/(# burners)] to account for economy of scale pricing, per vendor data. c Calculated by multiplying price per burner and number of burners. Assumes no installation in excess of standard burner installation costs. d Calculated assuming 3% tax rate on PEC. e The only annual costs expected for LNBs and ULNBs are capital recovery costs (e.g., no additional operating and maintenance costs over a standard burner). Capital recovery costs were calculated assuming 7% interest rate over 10 year life. f Calculated assuming that standard burner costs 2/3 the price of ULNBs, and LNBs would cost 6% more than a standard burner per vendor information.<h"""5" ""k1>@  2     I@  dMbP?_*+%63&CAppendix A.2.3 FGR and FGR+LNB Cost CalculationsMHP LaserJet 4V/4MV PostScriptg odXX ^ RdCustom page 1BBCustom page 2BBCustom page 3BB"d??U} I} } I } }  } $} I } m T0bbbb  :  OO` Annual Costs\lj== =FGRjFGR+LNB Heater Sizel Capital CostjElectricity Costs= Maintenance =Capital = Total Annualj Total Annual (MMBtu/hr)Heater Size (GJ/hr)m(July 1999 $)a "i($/yr)b" Costs ($/yr)c "Recovery ($/yr)d" Costs ($/yr)i Costs ($/yr)e "~ $@%%@DzG?@bD9@*2D333333?fffff~x@̔v@RX2> b@<D?8"Q?fffff~x@̔v@%(?{@D)\(?!(ǃ@ DD'([r@DDD#Xӧb@ DZ ~ I@%`J@DzG?@b4LA*2D333333?fffff~x@̔v@RXGݳ@<D?8"Q?fffff~x@̔v@%(W[@D)\(?!(ӖnL3@ DD'(+9?u @DDD#Xy*+@ DZ ~ R@%S@DzG?@bH >WA*2D333333?fffff~x@̔v@RXO @<D?8"Q?fffff~x@̔v@%(TB6@D)\(?!(/@ DD'(nq*@DDD#X6J@ DZ ~ b@%c@DzG?@b6cA*2D333333?fffff~x@̔v@RXO @<D?8"Q?fffff~x@̔v@%(8!@D)\(?!(>8 c%@ DD'(偓M@DDD#X1[w@ DZ ~ nu@%*w@DzG?@ezhA*2D333333?fffff~x@̔v@R[L=:@<D?8"Q?fffff~x@̔v@%))g@D)\(?!)ÿ@ DD')K`J@DDD#[w@ DZ   L,9m9?6Q?Q? Q?  ;:qqqqq0p(  px p 6nXPP?  Rx]4@n #T"W :<;JJHuck: Assumed CRF was the same as that for LNB and ULNB.<!0 F: xx p 6XoXPP? Z ]4@Xo $T"WX <JJHuck: FGR TAC + LNB TAC<!0 xx p 6oXPP? ZK]4@ol  'ppWX V<WJJHuck: July 1999 CE: 391.9 1991 Annual CE: 361.3 Formula from the ACT, Section 6.a.v.<!0 V@xx p 6XPP? Z]4@ &T"WX (<)JJHuck: Formula from ACT, Section 6.a.v.<!0 ( p H  @?  ]`  X<a Capital costs were calculated using the algorithm in "Alternative Control Techniques Document-Nox emissions from Process Heaters" (EPA-453-/R-93-034)(ACT). Costs were scaled from 1991 dollars to 1999 dollars using CE index. b Electricity costs were calculated using the algorithm in the ACT. c Maintenance costs were calculated using the ACT factor of 2.75% of SNCR capital costs. d Capital recovery costs were calculated assuming the same inputs used for LNBs and ULNBs systems: 7% interest rate and a 10 year life. e Total annual costs are the sum of the FGR annual costs and annual costs for control combinations. See Appendix A.2.2 for LNB and ULNB costs.<X"N")"*": " SJJHuckJJHuckJJHuckJJHuck>@    I@  dMbP?_*+%*'&CAppendix A.2.4 SCR Cost Calculations&?'?MHP LaserJet 4V/4MV PostScriptg oGU ^ RGCustom page 1BBCustom page 2BBCustom page 3BB"G??U} I } } } m} $} } } } I } } m }  }  &T0b bbb :  b b b {bmnb,mnmUnn nmeQe0'Annual Cost Calculated from Vendor Data$&O\OOOV Capital CostUUUp  Annual Cost  j=Heater jAverage === lTotal 3===Totalj NOx InletCapacity Capital CostjCapital Installation Taxes andAmmonia  lCapital& Capital Recovery($/yr)d"   Ammonia Taxes, Ins,AnnualVendora"iLevelb" (MMBtu/hr) Low Highi Cost ($)c" Cost ($)d" Shipping ($)e " Storage ($)f " m Cost ($)c" ] Equipment Catalyst Total  Cost ($/yr)e " Admin ($/yr)f " Cost ($/yr)Vendor 1j179 ppmv$@OA\A&X ADD% @?D% @Q?D%@ D?# b*A %h/ Xy)L@ 333333?D #*?/ d;O <@ ?D $7?" |a1@ D D  u)}@%@{Gz?D #hmjz@ % 0 jI@\A A&XADD%@?D%@Q?D%@ D?# b&A %h/ X*5{Z@ 333333?D #*?/  AL A&X` ADD%`@?D%@Q?D%7@ D?# b$A %h/ X(>~@ 333333?D #*?/ ܵ@ ?D $7?" ZGUE@ D D  C@%@{Gz?D #,}[@ % 0 j b@L A@A& X,A D D % ,A ?D % @ Q?D % @ D ?# b8]A % h/ XE$]@ 333333?D #*?/ ( j@ ?D $7?" ػ?^B@  D D  C@% @ {Gz?D # ͺW@ % 0 i u@:OA:`A& YpA D D % :pA ?D % :@ Q?D % :z@ D ?# c A % h/ Y?1m@ 333333?D #*?/ :4@ ?D $7?" :=9@  D D  :Y<@% :@}@ {Gz?D # :,kA % 0  j33 ppmv $@OA\A& X A D D %  @ ?D %  @ Q?D % @ D ?# b*A % h/ Xy)L@ 333333?D #*?/ d;O <@ ?D $7?" |a1@  D D  zQh@% @ {Gz?D # #75@ % 0 j I@\A A& XA D D % @ ?D % @ Q?D % @ D ?# b&A % h/ X*5{Z@ 333333?D #*?/  AL A& X` A D D % `@ ?D % @ Q?D % 7@ D ?# b$A % h/ X(>~@ 333333?D #*?/ ܵ@ ?D $7?" ZGUE@  D D  =kl̖@% @ {Gz?D # W{@ % 0 jb@L A@A&X,ADD%,A?D%@Q?D%@ D?# b8]A %h/ XE$]@ 333333?D #*?/ ( j@ ?D $7?" ػ?^B@ D D  =kl̦@%@{Gz?D #0@ % 0 8tuu@7OA7`A&spADD%7pA?D%7@Q?D%7z@ D?# { A %h/ s?1m@ 333333?D #*?/ 74@ ?D $7?" 7=9@ D D  7&.')@%7@}@{Gz?D #7bLn@ % 0Vendor 2j179 ppmv~ $@ ~ 3@ xj%@Q?D%@ D?# b@ %h+ X)@ D #*?# Gz|@ $7?" .4ׅu@ D D  u)}@%V@Q?D #9-gM@ % 0 j~ I@ ~ 3@A xj%6@Q?D%@ D?# bA %h+ X.9.@ D 8J#*?# \@ 8J$7?" ѩ+@ D D  Գ\@%ffff@Q?D #Blb@! % 0 j~ R@ ~ 3R A xj%0@Q?D%@ D?# b@A %h+ X BN@ D y#*?# p= @ y$7?" 5ct@ D D  C@%̸@Q?D #\}< @" % 0 j~ b@ ~ 3=A xj%d@Q?D%@ D?# b`A %h+ XV+~@ D `#*?# 3333@ `$7?" xb֋@ D D  C@% @Q?D #'va3@# % 0 i~ u@ ~ ]UA yj%@Q?D%D@ D?# c#!A %h0 Yr3܀l@ D [A#*?) := ףP@ [A$7?" :HciJ@ D D  :Y<@%:3333t@Q?D #:'Է@$ % 0j33 ppmv~ $@ ~ 3@ xj%ب@Q?D%@ D?# b@>@ %h+ X}"Op@ D  #*?# R묊@  $7?" ht@ D D  zQh@%@Q?D #9Mʀ@ % 0 j~ I@ ~ 3A xj%ܴ@Q?D%b@ D?# bA %h+ Xa@ D hB#*?# {G!2@ hB$7?" 5 @ D D  OYQe@%33333@Q?D #@! % 0 j~ R@ ~ 3 A xj%@Q?D%D@ D?# b@sA %h+ XsLZ@ D e#*?# q= #Ÿ@ e$7?" h@ D D  =kl̖@%333331@Q?D ##~TB@" % 0 j~ b@ ~ 3A xj% @Q?D%@ D?# bpA %h+ XB}@ D P#*?# @@ P$7?" !>?v@ D D  =kl̦@%ffff@Q?D #S`?@# % 0 *v~ nu@ **~ _A zj%*@Q?D%*@ D?# e85 A %h0 [ho@ D @#*?) )@ @$7?" )gT@ D D  )&.')@%)@Q?D #)/}@$ % 0& JASummary of Total Annual Costs for Control Technology Combinations & !Heater OO`\Ow\OO Capacityk  SCR+LNB   SCR+ULNB   (MMBtu/hr) mSCRg" i SCR Costh"  LNB Costi" rTotal i SCR Costj" ULNB Costk "TotalD,l\*k;**E T0!b"b#$ %~ $@ ' b}@ DD* Xב5ٛ@ D D Z (okT=@Z " 5fF@! D D ' XY< k@ D D (V:TEn@$ Z # (*@  % ~ !I@!'! b/|[@DD*! X)@! D! D Z! (@NE6_@ Z "! 5aw@" D! D! '! X~-}@!D D!(lSA@ Z#!(1@  %!! ~ "R@"'" b&؉@DD*" X:q@" D" D Z " (CE e@! Z "" 5UTZ܆@# D" D" '" Xci@"D D"(Ev@!Z#"(q@  %"" ~ #b@#'# b!*+@D D*# XX2o@# D# D Z # (Хl6t@" Z "# 5Chh(@$ D# D# '# X︊@#DD#(`إ@"Z##(+Rj@  %## ~ $nu@$**'$ e+A D D*$ [Iq%@$ D$ D Z $ )pnh(1{@# Z "$ heR@# D$ D$ '$ [ru$@$DD$)Xlj@#Z#$)k%@ %$$ "%d99999@( 3f3f3   H @?&F]` R<Sa Information from vendors is provided in Appendix A.1. b Inlet levels correspond to uncontrolled NOx from process heaters (179 ppmv) and controlled using an ULNB (33 ppmv). c Total capital cost components include purchased equipment, installation, taxes and freight, and ammonia storage. Purchased equipment costs include ammonia injection grid, blower, control valves, controls, and catalyst. Purchased equipment costs for vendor 1 were calculated as the average of the range of costs provided by vendor 1. Installation costs were included in vendor 2 quotes, and calculated for vendor 1 to be 50% of purchased costs (based on vendor data). Taxes and freight costs were calculated as 3% of purchased equipment costs. Ammonia storage costs were calculated to be 10% of purchased equipment costs based on data provided by vendor 1. d Capital recovery was calculated assuming 7% interest rate over life of equipment and life of catalyst. Based on vendor data equipment life was assumed to be 20 years and catalyst life was assumed to be 5 years. Catalyst costs for vendor 1 are 40% of capital costs and equipment costs are 60%, based on vendor 1 data. Catalyst costs for vendor 2 were provided for each heater size. e Ammonia costs are calculated in Appendix A.2.1. f Taxes, insurance, and administration costs were assumed to be 4 % of the total capital cost. g SCR costs are the average of the costs provided by vendors for inlet NOx levels of 179 ppmv (uncontrolled). h SCR costs are the costs of the SCR system with the ammonia costs for the LNB level of control instead of the uncontrolled level of control. i LNB costs are from LNB calculations in Appendix A.2.2. j SCR costs are the average of the costs provided by vendors for an inlet NOx level of 33 ppmv (ULNB level of control). k ULNB costs are from ULNB calculations in Appendix A.2.2.<"I9":";I"J";"5b"c"<b"ca""_R>@$$$2     I@  dMbP?_*+%# &CSCR-Vender 1 Cost CalculationsMHP LaserJet 2100 Series PSg oA3%peJXVHACustom page 1XCCCustom page 2XCCCustom page 3XCC"A??U} 4T0bbb b :  bbbmnbEbnbeEmQT0TVendor 1--179 ppm,Heater Capacity Capital Cost  Installation Taxes and Freight    Storage Tanks    Total Capital Cost (MMBtu/hr) Low HighAverage Low HighAverage Low High Average  Low  High Average  Low HighAverage$@OA\A& A"DD%O@?D%\@?D% @?D%@ Q?D%@ Q?D%  @Q?D% L@ D?% @D?% @ D?.  A DDDD .iA DDDD .*A DDD D I@\A A&ADD%\@?D%@?D%@?D%@ Q?D%@ Q?D% @ Q?D% @ D?% @D?% @ D?. iA DDDD .pA DDDD .&ADDD D R@> AL A&` ADD%>@?D%L@?D%`@?D%2@ Q?D% @ Q?D% @ Q?D% @ D?% p@D?% 7@ D?. cADDDD .ADDDD .$ADDD D b@L A@A&,ADD%L@?D%@A?D%,A?D% @ Q?D%@ Q?D% @ Q?D% p@ D?% R@D?% @ D?. ADDDD .ADDDD .8]ADDD D u@OA`A&pADD%OA?D%`A?D%pA?D%@ Q?D%@ Q?D% @ Q?D% L@ D?% O@D?% z@ D?. ADDDD .d"ADDDD . ADDD D  Heater Capacity# Capital Recovery equipment  Capital Recovery-cat  Total ~ @F  "*?0D D D D D   (MMBtu/hr) Low High Average Low High Average Low High Average ~ 4@ ~ $@/ H. @ 333333?D #*?/ e`T@ 333333?D#*?/ y)L@2 333333?D#*?/ 5^IK@ ?D $7?/ V,@ ?D$7?/ d;O <@?D$7?" U|h@ D D " 6y@ D D " |a1@ D D  ~ I@/ e`T@ 333333?D #*?/ 9̛@ 333333?D#*?/ *5{Z@333333?D#*?/ V,@ ?D $7?/ Af-N@ ?D$7?/ ~@ 333333?D#*?//n@?D $7?/^K}@?D$7?/ܵ@ ?D$7?"b@ DD""s@ DD" ZGUE@ DD ~ b@/m2@333333?D #*?/Ͻ$@333333?D#*?/E$]@333333?D#*?/^K}@?D $7?/W@?D$7?/( j@?D$7?""s@ DD"vkg@ DD" ػ?^B@ DD ~ u@/H. @333333?D #*?/|?T@333333?D#*?/?1m@333333?D#*?/5^IK@?D $7?/(\@?D$7?/4@?D$7?"U|h@ DD"͛@ DD" =9@ DD Heater CapacityAmmonia ElectricityTaxes, Ins, Admin Waste TAC (MMBtu/hr) Cost Cost Low HighAverageDisposal Low High ,Average ~ $@u)}@~ %@Q?D %I@{Gz?D%@ {Gz?D~ 4A]E@D DDDD4/(x@ D DDDD4 -hmjz@ D DDDD ~ I@Գ\@~ %@Q?D %@{Gz?D%@{Gz?D~ 4^[";@D DDDD4,|sC@D DDDD4 -mP*@D DDDD ~ R@C@~ %@Q?D %@{Gz?D%@{Gz?D~ 4& @DDDDD4z@DDDDD4 -,}[@ D DDDD ~ b@C@~ %@Q?D %w@{Gz?D%@{Gz?D~ 4t@DDDDD4WsxF@DDDDD4 -ͺW@ D DDDD ~ u@Y<@~ %@Q?D %@{Gz?D%@}@{Gz?D~ 4@C@DDDDD4+#6ADDDDD4 .,kA D DDDD &Vendor 1--33 ppm$Heater Capacity Capital Cost  Installation Taxes and Freight   Storage Tanks    Total Capital Cost  (MMBtu/hr) Low HighAverage Low HighAverage Low High Average  Low  High Average  Low HighAverage$@OA\A& A DD%O@?D%\@?D% @"?D%@ Q?D%@ Q?D%  @"Q?D% L@ D?% @D?% @" D?.  A&DDDD .iA&DDDD .*A" DDD D I@\A A&ADD%\@?D%@?D%@?D%@ Q?D%@ Q?D% @ Q?D% @ D?% @D?% @ D?. iA'DDDD .pA'DDDD .&ADDD D <Q+N2_____uuuuu*E M T0!b"b$%&'(b)b*:,-b.b/0b123 R@> AL A& ` AD D % >@ ?D % L@ ?D % `@?D % 2@ Q?D %  @ Q?D % @ Q?D % @ D ?% p@ D ?% 7@ D ?. cA(D D D D . A(D D D D . $AD D D D  !b@L A@A&!,A D!D!%!L@!?D!%!@A!?D!%!,A ?D!%! @! Q?D!%!@! Q?D!%! @ Q?D!%! p@! D!?%! R@!D!?%! @ D!?.! A)D!D!D!D! .!A)D!D!D!D! .!8]A D!D!D! D! !"u@OA`A&"pA!D"D"%"OA"?D"%"`A"?D"%"pA!?D"%"@" Q?D"%"@" Q?D"%" @! Q?D"%" L@" D"?%" O@"D"?%" z@! D"?." A*D"D"D"D" ."d"A*D"D"D"D" ." A!D"D"D" D" "$Heater Capacity#$Capital Recovery equipment $$Capital Recovery-cat $$Total$~ $@F$ "*?0D$D$D%D$D%% (MMBtu/hr) %Low %High%Average %Low %High%Average %Low %High% Average% ~ %4@%~ &$@/&H. @&333333?D #*?/&e`T@&333333?D#*?/&y)L@"333333?D#*?/&5^IK@&?D $7?/&V,@&?D$7?/&d;O <@*?D$7?"&U|h@. D&D&"&6y@. D&D&"& |a1@* D&D&& ~ 'I@/'e`T@'333333?D #*?/'9̛@'333333?D#*?/'*5{Z@&333333?D#*?/'V,@'?D $7?/'Af-N@'?D$7?/'~@'333333?D #*?/(/n@(?D $7?/(^K}@(?D $7?/(ܵ@'?D $7?"(b@0 D(D("("s@0 D(D("( ZGUE@' D(D(( ~ )b@/)m2@)333333?D! #*?/)Ͻ$@)333333?D!#*?/)E$]@(333333?D!#*?/)^K}@)?D! $7?/)W@)?D!$7?/)( j@(?D!$7?")"s@1 D)D)")vkg@1 D)D)") ػ?^B@( D)D)) ~ *u@/*H. @*333333?D" #*?/*|?T@*333333?D"#*?/*?1m@)333333?D"#*?/*5^IK@*?D" $7?/*(\@*?D"$7?/*4@)?D"$7?"*U|h@2 D*D*"*͛@2 D*D*"* =9@) D*D** ,Heater Capacity,Ammonia, Electricity,Taxes, Ins, Admin ,,Waste ,TAC,- (MMBtu/hr) -Cost -Cost -Low -High-Average-Disposal -Low -High- ,Average- Old Avg- ~ .$@.zQh@~ .%.@.Q?D %.I@.{Gz?D%.@* {Gz?D~ .4.h_)@D&D.D.D.D.4.^Dx$@. D&D.D.D.D.4. -#75@2D& D.D.D.D.&. #7@$D.D.. ~ /I@/OYQe@~ /%/@/Q?D %/@/{Gz?D%/@.{Gz?D~ /4/H|W.!@D'D/D/D/D/4/>rIw@/ D'D/D/D/D/4/ -Ł(:@. D' D/D/D/D/&/ Ł@D/D// ~ 0R@0=kl̖@~ 0%0@0Q?D %0@0{Gz?D %0@/{Gz?D ~ 040V:{@ D(D0D0D0D0403/@0 D(D0D0D0D040 -W{@/ D( D0D0D0D0&0 W{`@D0D00 ~ 1b@1=kl̦@~ 1%1@1Q?D! %1w@1{Gz?D!%1@0{Gz?D!~ 141)M@!D)D1D1D1D141^Rϊ@1 D)D1D1D1D141 -0@0 D) D1D1D1D1&1 @ D1D11 ~ 2u@2&.')@~ 2%2@2Q?D" %2@2{Gz?D"%2@}@1{Gz?D"~ 24274%7@"D*D2D2D2D242dO`N@2 D*D2D2D2D242 .bLn@1 D* D2D2D2D2&2 bL˞%@!D2D22 $3(hT___>@  *  I@  dMbP?_*+%&?'MHP LaserJet 2100 Series PSg od%3mJXVHdCustom page 1XCCCustom page 2XCCCustom page 3XCC"d??U} I }  } $} 2  T0 b b     b b :  b b  b    mn bE b nb m nbVendor 2--179 ppmHeater CapacityCap and TaxesStorage  (MMBtu/hr) InstallationFreight Tank Engineering TCI $@@%@Q?D%@D?.@ DDDD I@@A%6@Q?D%@D?.ADDDD R@R A%0@Q?D%@D?.@ADDDD b@=A%d@Q?D%@D?.`ADDDD u@UA%@Q?D%D@D?.#!ADDDD  Heater Capacity Cap Rec Cap Rec  Ammonia  Electricity Tax, Ins Waste   (MMBtu/hr) Equipm Cat Total Cost Cost Admin Disposal ,TAC~ $@+ )@ D#*?# Gz|@  $7?" .4ׅu@  D D  u)}@~ % V@&Q?D~ 4 -8-gM@&D D D D D ~ I@+.9.@D8J#*?#\@ 8J$7?"ѩ+@ DDԳ\@~ %ffff@Q?D~ 4-Blb@ DDDDD~ R@+ BN@Dy#*?#p= @ y$7?"5ct@ DDC@~ %̸@Q?D~ 4-\}< @DDDDD~ b@+V+~@D`#*?#3333@ `$7?"xb֋@ DDC@~ % @Q?D~ 4-'va3@DDDDD ~ u@0r3܀l@D[A#*?)= ףP@[A$7?"HciJ@ DDY<@~ %3333t@Q?D~ 4.'Է@DDDDD  Vendor 2--33 ppm Heater CapacityCap and TaxesStorage   (MMBtu/hr) InstallationFreight Tank Engineering TCI $@@%ب@Q?D%@D?~ .@>@"DDDD I@A%ܴ@Q?D%b@D?~ .A#DDDD R@ A%@Q?D%D@D?~ .@sA$DDDD b@A% @Q?D%@D?~ .pA%DDDD u@A%@Q?D%@D?~ .85 A&DDDD 4w8l#.9n T0! b" b# $ % & ( b ) b* :+ , b- b. / b0 1   Heater Capacity Cap Rec Cap Rec  Ammonia  Electricity Tax, Ins Waste  ! (MMBtu/hr)!Equipm !Cat!Total !Cost !Cost!Admin!Disposal !,TAC! ~ "$@+"}"Op@"D #*?#"R묊@"  $7?""ht@- D"D""zQh@~ "%"@Q?D~ "4"-9Mʀ@D"D"D"D"D"" ~ #I@+#a@#DhB#*?##{G!2@# hB$7?"#5 @# D#D##OYQe@~ #%#33333@Q?D~ #4#-@. D#D#D#D#D## ~ $R@+$sLZ@$De#*?#$q= #Ÿ@$ e$7?"$h@$ D$D$$=kl̖@~ $%$333331@Q?D~ $4$-#~TB@/ D$D$D$D$D$$ ~ %b@+%B}@%DP#*?#%@@% P$7?"%!>?v@% D%D%%=kl̦@~ %%%ffff@Q?D~ %4%-S`?@0 D%D%D%D%D%% ~ &u@0&ho@&D@#*?)&@&@$7?"&gT@& D&D&&&.')@~ &%&@Q?D~ &4&./}@1 D&D&D&D&D&& ( )0 TAC summary)111111112 *34 +3Heater Capacity ++SCR+LNB ++SCR+ULNB + ,3 (MMBtu/hr),SCR AVG, ,SCR  ,LNB,Total, ,SCR ,ULNB, 4Total~ -3$@(-(}@-D Z -+-(ב5ٛ@-D-ZZ-(okT=@1Z !-(fF@- D-D--(-(Y< k@1D"Z. -(V:TEn@1Z !- 5*@ D-D-~ .3I@(.(/|[@.DZ .+.()@.D.ZZ.(@NE6_@-Z !.(aw@- D.D..(.(~-}@"D#Z/ .(lSA@-Z!. 51@" D.D.~ /3R@(/(&؉@/DZ /+/(:q@/D/ZZ /(CE e@.Z !/(UTZ܆@. D/D//(/(ci@.D$Z0 /(Ev@.Z!/ 5q@# D/D/~ 03b@(0(!*+@0DZ 0+0(X2o@0D0ZZ 0(Хl6t@/Z !0(Chh(@/ D0D00(0(︊@/D%Z1 0(`إ@/Z!0 5+Rj@$ D0D0~ 16u@(17+A1DZ 18+17Iq%@1D1ZZ 1(pnh(1{@0Z !17eR@0 D1D118(17su$@0D&Z2 1(Xlj@0Z!1 9k%@% D1D1&@####.4q5555Pl(  lx l 6XPP? +Z0]4@t "T"W F<GJMH: calculated by SCR TAC - 179ppm ammonia cost + 82ppm ammonia cost <!E F ,JJHuck>!@111++++ I@  dMbP?_*+%XU&CAppendix A.2.5 SNCR and Control Combinations- Capital and Annual Cost CalculationsMHP LaserJet 4V/4MV PostScriptg od,, ` = ^ RdCustom page 1BBCustom page 2BBCustom page 3BB"d,??U} m }  }  } m }  } I }  }  } $ }   T0 b b     b b :  b b  b    O\O` Annual Costsf ControlsWHeater Size (MMBtu/hr)QHeater Size (GJ/hr)*aCapital Cost (July 1999 $)a"#WAmmonia Cost ($/yr)b"'QElectricity Cost ($/yr)c"Fuel penalty($/yr)'QMaintenance Cost ($/yr)d" QCapital Recoverye"& QSNCR Total Annual Cost ($/yr)( WTotal Annual Cost ($/yr)f" SNCR~ 3$@%%@DzG?Ob5Y_&@9j|D333333?ffffff?fffff~x@̔v@Xu)}@ ZOD@  "   I@  dMbP?_*+%MHP LaserJet 2100 Series PSg od,,` WJXVHdCustom page 1XCCCustom page 2XCCCustom page 3XCC"d,X??U} m } } m } I% Redux T0bbbb :  b TechnologyNOx ppmNOx (lb/MMBtu)% Redux UncontrolledaWWf@KD.A.= ףpx@"fffff4@fffff4@/-?-DDDd FGRaG_@KD.A.= ףpx@"fffff4@fffff4@%/R!uq? Dffffff?~ >@ LNBaOT@KD.A.= ףpx@"fffff4@fffff4@~ /$@-aJ@DDDd SNCRa/Q@KD.A.= ףpx@"fffff4@fffff4@+/JY8?DDd~ N@FGR+LNBaEhL@KD.A.= ףpx@"fffff4@fffff4@+/Ʊ?DdD~ Q@ ULNBaم,rfy@@ KD.A.= ףpx@"fffff4@fffff4@~ /@-FdT@DDDdLNB+SNCRaxgq@@KD.A.= ףpx@"fffff4@fffff4@//&c\qq?Dq= ףp??-gfffffT@DDDd SCR~ 1@W/W5"?AD.A.= ףpx@"fffff4@fffff4@-tPV@DDDd  ULNB+SNCRa 0>D)@CRKD .A.= ףpx@"fffff4@fffff4@/ /PBy? D ףp= ??- 433333W@DD Dd LNB+SCR~  @W /aWX? AD .A.= ףpx@"fffff4@fffff4@~ <W@ ULNB+SCR~ @W /:mnvx? AD .A.= ףpx@"fffff4@fffff4@- ȁakLX@ DD Dd* ZPHp 0( @A@A >@ I@  dMbP?_*+%63&C&20Table 2 Incremental Costs for Superior OptionsMHP LaserJet 4V/4MV PostScriptg odXX ^ RdCustom page 1BBCustom page 2BBCustom page 3BB"dXX??U} } } I} I } $ }  } $ }  !T0b b  b b b bbbb{bb{ z0  nb* !!! "Nox!Total#Average# Incremental Incremental  $NoxEmission Annualized%Cost- %Cost CostHeater Emissions Reductions Cost% Effectiveness% Effectiveness Effectiveness SizeControl Alternative(tpy)(tpy)($/yr)& ($/ton NOx)& ($/ton NOx) ($/ton NOx)  10 MMBtu/hr% Ultra Low Nox Burner and SCR  :z"@ Z *@ Z ! 7裬@  D D / VD * D * / Y%q@ D D D D  & Ultra Low Nox Burner and SNCR  ۫E!@ Z uYpB@ Z ! r@ D D  / ޱ)@D D D D   Ultra Low Nox Burner  JVE@ Z V:TEn@ Z ! ݛ?@  D D  / E'oT@D D D D   Low Nox Burner  St$@Z  okT=@ Z ! r @  D D ~ @Y@ r @ D   50 MMBtu/hr%Ultra Low Nox Burner and SCRiG@Z1@Z!!fY L@ DD/~yW D*D*/9Ǵ<@DDDD&Ultra Low Nox Burner and SNCRX4 F@ZA+J@Z !K&r@ DD/}:㻽@ DDDDUltra Low Nox Burner)t^cC@ ZlSA@Z!ܯ:@ DD/7>fQ@DDDDLow Nox BurnerWS:9@Z@NE6_@Z !I}@ DDI}@DI}@D 75 MMBtu/hr%Ultra Low Nox Burner and SCR@  I@MHP LaserJet 5/5M PostScriptw odXX]p?gRdCustom page 1|CCCustom page 2|CCCustom page 3|CC"dXX??3` 4#` 4#` 4#` 4# ` 4#  (  :N l  s *  @ i ]d$ <LNB< ll  s *  @ ] % <ULNB< rr  0(  @  }](% <SCR< xx  6x  @8 n]x\&  < ULNB+ SCR<' ll  s *  @  ]' <FGR< ll  s *  @ ]' <FGR+LNB< ll   s *h  @@p] hT( <SNCR< ll   s *  @ Q 2 ] ( < LNB+SNCR<& ll   s *  @ 9 2 ] )  < ULNB+SNCR<+ ll   s *X  @ %k ] XL* <LNB+SCR<! 0 0 3 d  3Q 10 MMBTUQ ; Q ; Q3_43_ M NM   d43_ M NM   d4E4D$% rM 3O&Q4$% rM 3O&Q4FA 3O 3*@#M43*#M4% 6OM3Oc & Q <NOx Emission Reduction (tpy)'4% 3hoMZ3O J& Q 0Annualized Cost ($/yr)'4523  NM43d" 3_ M NM  MM<444% Kt M03O:& Q LFigure 3-1. NOx Control Levels for 10 MMBtu/hr Heaters-Costs and Reductions'44 erCQ@St$@rCQ@r9>@ @JVE@+^3!@۫E!@ "@ :z"@e[r@okT=@Ψ魞v@ӧb@V:TEn@0Wg@}@uYpB@fF@ *@e> *   I@MHP LaserJet 5/5M PostScriptw odXXn p?gRdCustom page 1|CCCustom page 2|CCCustom page 3|CC"dXX??3` 4#` 4# ` 4# ` 4#` 4# ( 3f3f3 l  s *p  @ b ]p, <LNB< rr  0  @ d i ]X- <ULNB< ll  s *  @  /]. <SCR< rr  0`  @C`u]`.  < ULNB +SCR<( ll  s *  @(g]P/ <FGR< ll  s *  @>8 ]/ <FGR+LNB< ll   s *P  @-] P0 <SNCR< ll   s *  @8 _] H1 <LNB+SCR<! ll   s *  @A  v] 1 < LNB+SNCR<& ll   s *@  @u X] @2  < ULNB+SNCR<+ 0 0 3 d  3Q 50Q ;Q ;Q3_43_ M NM   d43_ M NM   d4E4D$% rM 3O& Q4$% rM 3O& Q4FA 3O 3*,@#M43*#M4% 6OM3Oc &Q <NOx Emission Reduction (tpy)'4% 3hoMZ3O J&Q 0Annualized Cost ($/yr)'4523  NM43d" 3_ M NM  MM<444% Kt M03O:&Q LFigure 3-2. NOx Control Levels for 50 MMBtu/hr Heaters-Costs and Reductions'44 eQn,@WS:9@Qn<@Gx $(@@ YaC@)t^cC@NhXAE@X4 F@OnF@ iG@e+9?u @@NE6_@$@y*+@lSA@ 3@/|[@A+J@aw@ 1@e> 1   I@MHP LaserJet 5/5M PostScriptw odXXn p?gRdCustom page 1|CCCustom page 2|CCCustom page 3|CC"dXX??3` 4# ` 4#` 4#` 4#` 4# ( 3f3f3  l  s *P  @r  ]P 4 <LNB< gll  s *  @ Q ] 5 <ULNB< gll  s *  @  2] L6 <SCR< gll  s *@  @ EX]@ 6 < ULNB+SCR< gll  s *  @Gr] 7 <FGR< grr  0   @|E] D8 <FGR+LNB< gll  s *0  @ 1[ ] 0 8 <LNB+SCR< gll  s *  @N1,]  9 <SNCR< gll  s *  @  z]  <: < LNB+SNCR< gll  s *  @8  ]  :  < ULNB+SNCR< g 0 0 3 d  3Q 75Q ;"+Q ;"+Q3_43_ M NM   d43_ M NM   d4E4D$% M 3O&Q4$% M 3O&Q4FA 3O 3*4@#M43*#M4% GOM3Oc &Q <NOx Emission Reduction (tpy)'4% 3hoMZ3O J&Q 0Annualized Cost ($/yr)'4523  NM43d" 3_ M NM  MM<444% Kt M03O:&Q LFigure 3-3. NOx Control Levels for 75 MMBtu/hr Heaters-Costs and Reductions'44 eMb5@+1N7C@MbE@46 M@:N1 P@B5vP@P@  q   I@MHP LaserJet 5/5M PostScriptw odXXn p?gRdCustom page 1|CCCustom page 2|CCCustom page 3|CC"dXX??3` 4#` 4#` 4#` 4#` 4# ( @A@A l  s *\  @p  ]\H= <LNB<gll  s *  @ E ]= <ULNB<gll  s *  @K  Y]> <SCR<gll  s *L  @ W]L@? < ULNB+SCR<gll  s *,  @px],? <FGR<gll  s *h  @8}1]h@ <FGR+LNB<gll   s *  @X6] 8A <SNCR<gll   s *  @h  ] A < LNB+SNCR<gll   s *X  @ X ] XB  < ULNB+SNCR<g ll   s *  @~  ] 0C <LNB+SCR<g0 0 3 d  3QQ ;.7Q ;.7Q3_43_ M NM   d43_ M NM   d4E4D$% M 3O&Q4$% M 3O&Q4FA} 3O 3*D@#M43*#M4% OOM3Oc &Q <NOx Emission Reduction (tpy)'4% 3hoMZ3O J&Q 0Annualized Cost ($/yr)'4523  NM43d" 3_ M NM  MM<444% gK GM03O?&Q MFigure 3-4. NOx Control Levels for 150 MMBtu/hr Heaters-Costs and Reductions'44 e bE@7S@ bU@#lxz +   I@MHP LaserJet 5/5M PostScriptw odXXn p?gRdCustom page 1|CCCustom page 2|CCCustom page 3|CC"dXX??3` 4#` 4#` 4#` 4#` 4# <( C6 <l < s *  @  ]E <LNB<gll < s *8  @ Y E ]8 k  I@  dMbP?_*+%*'&C&20Table 1 Summary of Control OptionsMHP LaserJet 4V/4MV PostScriptg oLXXAt ^ RLCustom page 1BBCustom page 2BBCustom page 3BB"LXX??U} } }  } I } $ }  } $  (1) 0F bbbb bb bb   b0bbbmnbmnmEnn nm!eQ !!! "NOx!Total#Average# Incremental  $NOxEmission Annualized%Cost- %CostHeater Emissions Reductions Cost% Effectiveness% Effectiveness SizeControl Alternative(tpy)(tpy)($/yr)& ($/ton NOx)& ($/ton NOx)  10 MMBtu/hr Baseline cZ#@   % Flue Gas Recirculation (FGR) ( rCQ@*D Zd [r@ Z! EL@C D D    Low Nox Burner (LNB) ' St$@ D Zd okT=@?Z ! r @ D D ~ @Y@   SNCR ' rCQ@CD Zd Ψ魞v@ Z ! '@  D D    FGR+LNB ' r9>@ D Zd ӧb@ Z! Kc@  D D  $Ultra Low Nox Burner (ULNB)' @ D ZdV:TEn@ Z !q+܆?@ DD LNB+SNCR'JVE@D Zd0Wg@Z !mu\@  DD  SCR'+^3!@ D Zd}@7Z-!97l@  DD/?k@DD DD  ULNB+SNCR'۫E!@D Z duYpB@Z !r@ DD LNB+SCR' "@D Z dfF@Z-!YFv@ DD %Ultra Low Nox Burner and SCR':z"@D Z d*@Z- !7裬@ DD/PYCDDDD 50 MMBtu/hrBaseline@ %Flue Gas Recirculation (FGR)(Qn,@DZd+9?u @Z!QL@ DD Low Nox Burner (LNB)'WS:9@DZd@NE6_@Z !I}@ DDI}@=D SNCR'Qn<@DZd$@Z !,W@ DD FGR+LNB'Gx $(@@DZdy*+@Z!k.@  DD $Ultra Low Nox Burner (ULNB)' YaC@DZdlSA@Z!#{:@ DD/b9N^@DDDDLNB+SNCR')t^cC@DZd 3@Z !YI@ DD  SCR'NhXAE@DZd/|[@Z.!S-O @ DD  ULNB+SNCR'X4 F@DZ dA+J@Z !K&r@ DD LNB+SCR'OnF@DZ daw@Z.!r IzQ@ DD %Ultra Low Nox Burner and SCR'iG@DZ d1@Z. !fY L@ DD/.RDDDD ! 75 MMBtu/hr!Baseline!ػ@ !BXhweY"#$b%b&b'b(bb)bb*+,-./012b30456bb7b8m9nb:;mn<mE=nn>?nm@eQAe"%"Flue Gas Recirculation (FGR)"("Mb5@D!Zd"nq*@"Z!"統k@ D"D" "##Low Nox Burner (LNB)#'#+1N7C@"D!Zd#CE e@Z !#@# D#D##@D##$ $SNCR$'$MbE@D!Zd$Xɗ,}@$Z !$WP@" D$D$ $%%FGR+LNB%'%46 M@&D!Zd'*Lz@'Z !'g/,"@$ D'D' '( (SCR('(:N1 P@#D!Zd(&؉@Z/!(g 7'M@& D(D( ()) ULNB+SNCR)')B5vP@(D!Z d)cY}~&@)Z !)Љ-@' D)D) )**LNB+SCR*'*P@)D!Z d*UTZ܆@*Z/!*aon@+ D*D* *+%+Ultra Low Nox Burner and SCR+'+@ 9:%:Flue Gas Recirculation (FGR):(:QnX@7D9Zd:K`J@:Z!:Ժލ~@5 D:D: :;;Low Nox Burner (LNB);';.E&kf@:D9Zd;pnh(1{@2Z !;,{, @; D;D;;,{, @7D;;< <SNCR<'<Qnh@3D9Zd<RA<Z !<O^@: D<D< <==FGR+LNB='=lV}Fl@<D9Zd=w@=Z!=$zO}@1 D=D= =>$>Ultra Low Nox Burner (ULNB)>'>: eqp@=D9Zd>(Xlj@;Z!>6@; D>D>/>(.H@@D@D;D@D;>??LNB+SNCR?'?-g~5p@>D9Zd?/#|A?Z !?jX3@< D?D? ?@ @SCR@'@z&ZXr@;D9Zd@+ABZ1!@XZxK|@> D@D@ @(AA ULNB+SNCRA'AUKs@@D9Z dAԯZAAZ !AR+6?R|@B DADA ADlZZBC DbEbBBLNB+SCRB'BOns@AD9Z dBeR@AZ1!B$tv@? DBDB BC%CUltra Low Nox Burner and SCRC'C_[5t@BD9Z dC(k%@4Z1 !C(] ttt@> DCDC/C)3 CDCD@DCD@CDE <>@   BOlePartOlePres000$SummaryInformation(DocumentSummaryInformation8d ^\@p$ 8    4<' """)))UUUMMMBBB999|PP3f333f3333f3ffffff3f̙3ff333f333333333f33333333f33f3ff3f3f3f3333f33̙33333f333333f3333f3ffffff3f33ff3f3f3f3fff3ffffffffff3ffff̙fff3fffff3fff333f3f3ff3ff33f̙̙3̙ff̙̙̙3f̙3f333f3333f3ffffff3f̙3f3f3f333f3333f3ffffff3f̙3f3ffffffffff!___www45'  Arial$---Arial-----Arial----------"Systemn-'- 4<-'- 4<8- "- $<}} < < "-<} } << "-< <- # < # < # <* #* <#<D#D<#<^#^<#< < } < <     t  t    E E     } } "---'--- !!---'---  '---'---  '8-  "-t     r r q q   || r rtt - "-  $_ )t  t _ ---'---   '  $l   x l ---'---   '  $     ---'---   'r  $ ] r r ] ---'---   'q  $\ q  q \ ---'---   '  $   ---'---   '| $g||g---'---   ' r $r r ] r---'---   ' $---'---   't $tt_t---'---   '---'---   '---'---  4<------'---  n y2 LFigure 3-1. NOx Control Levels for 10 MMBtu/hr Heaters-Costs and Reductions==='88!8HN8H==!'==8688!='88SSH!=='H88!8'8!H=8!88==H8==8!==8----'---  4<---'---  4<----'---  4<  2 S 0.2 /5,000....2 m 10,000.....2 15,000.....2 20,000.....2 25,000.....2 30,000.....2 .35,000.....2 40,000.....---'---  4<---'---  4<  2 2.5.. 2 k3.5.. 2 4.5.. 2 ; 5.5.. 2 6.5.. 2 7.5.. 2 t8.5.. 2 9.5.. 2 -10.5...---'---  4<------'---  >@z  12 V NOx Emission Reduction (tpy)<A.7J..33<.33.333-----'---  4<-----'---  x d Arial-2 l wAnnualized Cost ($/yr)-----'---  4<---'---  4<--  45- "-   )--- -  -  =--  2 =LNB.<7' 4<--- -  T >--- -  - ? R--  2 RULNB<.<7' 4<--- - R--- -  -I--  2 SCR7<<' 4<--- - O--- -  -F-- 2  ULNB+ SCR<.<707<<' 4<--- - .  --- -  -% | --  2 FGR3A<' 4<--- - . --- -  -% ! -- 2 ! FGR+LNB3A<0.<7' 4<--- - z V --- -  -e j --  2 j SNCR7<<<' 4<--- - Q --- -  -Y -- 2 \ LNB+SNCR.<707<<<' 4<--- - Qk--- -  -Y-- 2 \ ULNB+SNCR<.<707<<<' 4<--- - ,--- -  -@-- 2 @LNB+SCR.<707<<' 4<-- -' 4< '  '՜.+,D՜.+, PXx  KEastern Research GroupN1  SCRAmmrate LNB&ULNBFGRSCR SCRvend1 SCRvend2&TACSNCR Efficiency INCREMENTALsummary105075150350  Worksheets Charts 6> _PID_GUIDAN{870E0B01-DAFA-11D3-94F1-F382C0481DE4} METAFILEPICT ^x$ ^\@ 8    4<' """)))UUUMMMBBB999|PP3f333f3333f3ffffff3f̙3ff333f333333333f33333333f33f3ff3f3f3f3333f33̙33333f333333f3333f3ffffff3f33ff3f3f3f3fff3ffffffffff3ffff̙fff3fffff3fff333f3f3ff3ff33f̙̙3̙ff̙̙̙3f̙3f333f3333f3ffffff3f̙3f3f3f333f3333f3ffffff3f̙3f3ffffffffff!___www45'  Arial$---Arial-----Arial----------"Systemn-'- 4<-'- 4<8- "- $<}} < < "-<} } << "-< <- # < # < # <* #* <#<D#D<#<^#^<#< < } < <     t  t    E E     } } "---'--- !!---'---  '---'---  '8-  "-t     r r q q   || r rtt - "-  $_ )t  t _ ---'---   '  $l   x l ---'---   '  $     ---'---   'r  $ ] r r ] ---'---   'q  $\ q  q \ ---'---   '  $   ---'---   '| $g||g---'---   ' r $r r ] r---'---   ' $---'---   't $tt_t---'---   '---'---   '---'---  4<------'---  n y2 LFigure 3-1. NOx Control Levels for 10 MMBtu/hr Heaters-Costs and Reductions==='88!8HN8H==!'==8688!='88SSH!=='H88!8'8!H=8!88==H8==8!==8----'---  4<---'---  4<----'---  4<  2 S 0.2 /5,000....2 m 10,000.....2 15,000.....2 20,000.....2 25,000.....2 30,000.....2 .35,000.....2 40,000.....---'---  4<---'---  4<  2 2.5.. 2 k3.5.. 2 4.5.. 2 ; 5.5.. 2 6.5.. 2 7.5.. 2 t8.5.. 2 9.5.. 2 -10.5...---'---  4<------'---  >@z  12 V NOx Emission Reduction (tpy)<A.7J..33<.33.333-----'---  4<-----'---  x d Arial-2 l wAnnualized Cost ($/yr)-----'---  4<---'---  4<--  45- "-   )--- -  -  =--  2 =LNB.<7' 4<--- -  T >--- -  - ? R--  2 RULNB<.<7' 4<--- - R--- -  -I--  2 SCR7<<' 4<--- - O--- -  -F-- 2  ULNB+ SCR<.<707<<' 4<--- - .  --- -  -% | --  2 FGR3A<' 4<--- - . --- -  -% ! -- 2 ! 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NOx Control Levels for 50 MMBtu/hr Heaters-Costs and Reductions==='88!8HN8H==!'==8688!='88SSH!=='H88!8'8!H=8!88==H8==8!==8----'---  4<---'---  4<----'---  4<  2 S 0.2 d 10,000.....2 v 20,000.....2 30,000.....2 40,000.....2 50,000.....2 60,000.....---'---  4<---'---  4<  2 14.0... 2 19.0... 2 l24.0... 2 , 29.0... 2 34.0... 2 39.0... 2 m44.0... 2 -49.0...---'---  4<------'---  >@z  12 V NOx Emission Reduction (tpy)<A.7J..33<.33.333-----'---  4<-----'---  x d Arial-2 l wAnnualized Cost ($/yr)-----'---  4<---'---  4<--  45- "- +  --- -  -"  3--  2 3LNB.<7' 4<--- -  #e --- -  - m --  2 p ULNB<.<7' 4<--- - v --- -  -~--  2 &SCR7<<' 4<--- - M`C2--- -  -DKKF----  2 NZULNB<.<7 2 Y+SCR07<<' 4<--- - tj--- -  -kU--  2 FGR3A<' 4<--- - n  --- -  -Y  -- 2  FGR+LNB3A<0.<7' 4<--- -   --- -  -  --  2  SNCR7<<<' 4<--- - -t--- -  -$_-- 2 LNB+SCR.<707<<' 4<--- - ;~--- -  -2i-- 2 LNB+SNCR.<707<<<' 4<--- - --- -  - -- 2  ULNB+SNCR<.<707<<<' 4<-- -' 4< '  '-'-naphthasventb LNBssystems.refsystem.ref1980sMorrisville analysis,24,27WPWin 6.0/OLE 1.0 Prefix Information MarkerExcel.Sheet.8bࡱ> .  !"#$%&'()*+,-./0123456789:;<=>?@ABCDEFGHIJKLMNOPQRSTUVWXYZ[\]^_`abcdefghijklmnopqrstuvwxyz{|}~Root Entry FG1oOle CompObjbWorkbook@'  FMicrosoft Excel ChartBiff8Excel.Sheet.89qGcOh+'0HPl ERG - MorrisvilleeERG - MorrisvilleeMicrosoft Excel@$'o@7?@h      !"#$%&'()*+,-/ I@Ba=     <=. 8 X1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1Arial1 Arial1$Arial1QTahoma1QTahoma1Arial"$"#,##0_);\("$"#,##0\)!"$"#,##0_);[Red]\("$"#,##0\)""$"#,##0.00_);\("$"#,##0.00\)'""$"#,##0.00_);[Red]\("$"#,##0.00\)7*2_("$"* #,##0_);_("$"* \(#,##0\);_("$"* "-"_);_(@_).))_(* #,##0_);_(* \(#,##0\);_(* "-"_);_(@_)?,:_("$"* #,##0.00_);_("$"* \(#,##0.00\);_("$"* "-"??_);_(@_)6+1_(* #,##0.00_);_(* \(#,##0.00\);_(* "-"??_);_(@_)0.0 0.00000 0.000000 0.0000 0.000 #,##0.0"Yes";"Yes";"No""True";"True";"False""On";"On";"Off" 0.0000000 0.00000000                + ) , *             " "0 "0@   ( "0@  "0@ "4@  " " "4  $  $  $`  `  $`  `@ @   d@   d@     @@  @   @  @   $   @  $   $  $  $ # "0  $  @   @  $@  $ @  $@  $  $ @  $@  $ @ (0@ *0@  `@  $`@  $`@  $`  $`@  @  @@ *0  @  $@  $@ "0@ "0@@ *0@  $@  $@  $@@  $`@  @@  @  @@  `@  "@ @ *0"@  $"@  $"@  $"@ @  $"`@ "0@@  $   $ ` "0@ "0@  "@ "0"@ "0"@ "0` *0  "0"@ @ "0"`@ "0   $ @ "0 @ "0 "0`@   @ "" ""8 ""8`  $" @ 0@ *0  @  "@ @ *0"@   @ "0@@ "0 @ "0@@ "0@ "0  @ "0@@ "0@ "0  @ "0@ "0 "0  " "0 "0 0 0 0 0 0`  * SCRAmmrateNDLNB&ULNB aFGR zSCRSCRvend1  SCRvend2&TAC 4SNCR^c Efficiencyq INCREMENTAL 10 +50 75 F150 350:summary8 ph@'M      0e0e      A@@ A5% 8c8c     ?1 d0u0@Ty2 NP'p<'pA)BCD|E||@   Heater Capacity (MMBtu/hr)Cost Capital CostLowHigh InstallationTaxesTaxes and FreightTotalTotal Capital CostCapital Recovery equipmentCapital Recovery-catAmmoniaTaxes, Ins, AdminWasteDisposal Storage TanksTACCap and FreightStorage TankTCI EngineeringCap RecEquipmCatTax, InsAdmin ElectricityULNBLNBHeater Size (MMBtu)NoxAverage IncrementalEmission AnnualizedCost-Heater Emissions Reductions EffectivenessSizeControl Alternative(tpy)($/yr) ($/ton NOx) 10 MMBtu/hrBaselineLow Nox BurnerSCRUltra Low Nox Burner 50 MMBtu/hr 75 MMBtu/hr 150 MMBtu/hr 350 MMBtu/hr TAC summarySCR+ULNBSCR AVGUltra Low Nox Burner and SCRVendor 1--179 ppmVendor 1--33 ppmVendor 2--179 ppmVendor 2--33 ppmOld Avgvendor comparison (lb NH3/hr) % differenceSCR+LNBSCR TechnologyNOx ppmNOx (lb/MMBtu)% Redux UncontrolledFGRFGR+LNBSNCRLNB+SNCRLNB+SCR ULNB+SNCRULNB+SCRHeater Size (GJ/hr)Heater Size (MMBtu/hr)Fuel penalty($/yr) SNCR + LNB SNCR + ULNBNOxLow Nox Burner (LNB)Ultra Low Nox Burner (ULNB)Flue Gas Recirculation (FGR)Ultra Low Nox Burner and SNCRCase LNB level ULNB level(ppmv) (lb/MMBtu)Ammonia feedrate (lb NH3/hr)a"Ammonia Cost ($/yr)b" Total Annual Cost ($/yr) Annual CostsControlsCapital Cost (July 1999 $)a"Electricity Cost ($/yr)c"Maintenance Cost ($/yr)d"Capital Recoverye"Total Annual Cost ($/yr)f"SNCR Total Annual Cost ($/yr) Heater SizeElectricity Costs Maintenance Costs ($/yr)Capital (July 1999 $)a "($/yr)b" Costs ($/yr)c "Recovery ($/yr)d" Costs ($/yr)e " Capital CostsNumber of Burnersa"Vendor 1 EquipmentCatalyst179 ppmv33 ppmvVendor 2CapitalCapacity Taxes andAmmonia Taxes, Ins,Annual Annual Cost'Annual Cost Calculated from Vendor DataASummary of Total Annual Costs for Control Technology CombinationsVendora"Levelb" Cost ($)c" Cost ($)d" Shipping ($)e " Storage ($)f "jCapital Recovery($/yr)d" Cost ($/yr)e " Admin ($/yr)f "SCRg" SCR Costh" LNB Costi" SCR Costj" ULNB Costk "NOx Inlet LevelPrice per Burner ($)b"Purchased Equipment Cost ($)c"Total Capital Cost ($)d"Annual Costs ($/yr)e"Price per Burner ($)f" NOx InletStandard Burner Price ($)Purchased Equipment Cost ($)Annual Costs ($/yr)Standard Burner Annual Cost Differential ($/yr) e>1dGP\?{ap7{-pa AE!L!6$G"]"$x#$u $N be`T0b|BmmbeJ`T0bbmbenJ`T0bnnb  bv* bb7bbdbDT0bt00ApApzm00b E000bbb߿0bDeLbb{ApWBApL0b}enpApe(mm-nhb\e dbe(m-nbe(me6enJXm`T0   be6`T0n4b zeLnnmǹePQLne`T0`T0H;m/nPb/nXbÆ0Ln`T0dbtb`T0b|bŕ0`T0`T0)0`T0`T0by0pbb%00bp` 0p0b.Lbx~b Pb,b0Heater Capacity (MMBtu/hr)Cost Capital CostLo I@  dMbP?_*+%B?&CAppendix A.2.1 Calculation of Ammonia Cost for Control Cases&?'?MHP LaserJet 4V/4MV PostScriptg odXX ^ RdCustom page 1BBCustom page 2BBCustom page 3BB"d??U} }  } $ }  } $} $+[8I@bbbbbb bb      b 0 OPNOx Inlet LevelPOOP CaseHHeater Size (MMBtu/hr)(ppmv) (lb/MMBtu),IAmmonia feedrate (lb NH3/hr)a"&vendor comparison (lb NH3/hr) % difference#IAmmonia Cost ($/yr)b"?$@?`f@MA2K?7D.A.= ףpx@fffff4@fffff1@")C[c?DD.~ P@-D}`1@DDDd'Fu)}@D8",?I@?`f@MA2K?7D.A.= ףpx@fffff4@fffff1@")C17^@DD.~ t@-D#}`1@DDDd'FԳ\@D8", Uncontrolled?R@?`f@MA2K?7D.A.= ףpx@fffff4@fffff1@")CʥR@DD.~ ~@-Dis O4@DDDd'FC@D8",?b@?`f@MA2K?7D.A.= ףpx@fffff4@fffff1@")CʥR(@DD.~ @-D"}`1@DDDd'FC@D8",8@u@@`f@MB2K?7D.A.= ףpx@fffff4@fffff1@")El$<@DD.~ 8@->S32@DDDd'GY<@D8",?$@?T@MA/1&|?7D.A.= ףpx@fffff4@fffff1@")Cq?DD. D'F(6~@D8",?I@?T@MA/1&|?7D.A.= ףpx@fffff4@fffff1@")CVn?DD. D'FcZx5@D8",  LNB level ?R@?T@M A/1&|? 7D .A.= ףpx@fffff4@fffff1@") Cb@ D D . D' F4fPS@D 8",  ?b@?T@M A/1&|? 7D .A.= ףpx@fffff4@fffff1@") Cb@ D D . D' F4fPS@ D 8", 8 @u@@T@M B/1&|? 7D .A.= ףpx@fffff4@fffff1@") E)@ D D . 8>' GOI@ D 8",  ?$@?@@M A? 7D .A.= ףpx@fffff4@fffff1@") Ccn:? D D .~ 6@- DڥKHD D D d' FzQh@ D 8",  ?I@?@@M A? 7D .A.= ףpx@fffff4@fffff1@") C n? D D .~ P@- DgfiYذ%@ D D D d' FOYQe@ D 8", ULNB level?R@?@@MA?7D.A.= ףpx@fffff4@fffff1@")C}ǦR?DD.~ [@-D5? DDDd'F=kl̖@ D8",?b@?@@MA?7D.A.= ףpx@fffff4@fffff1@")C}ǦR@DD.~ k@-D5?DDDd'F=kl̦@D8",*Ju@J@@MK?7D.A.= ףpx@fffff4@fffff1@")L`@DD.~ *@-M;.D @DDDd'N&.')@D8",(cT>h(  hr h 0,G  @ ]`,GT  >(<?a Calculated assuming 1:1 ratio of NOx to ammonia, ammonia MW of 17, and NOx MW of 46. This calculation assumes that additional ammonia will be injected beyond the amount that would react with NOx to achieve the estimated emission reduction. This was done to account for ammonia slip and incomplete mixing of ammonia and flue gas. b Calculated using $300/ton cost for annhydrous ammonia. This value is the midpoint of the range of costs as reported in the "Status Report on NOx Control Technologies and Cost Effectiveness for Utility Boilers," NESCAUM/MARAMA, June 1998.<("y1gN"yOR#g>>@  I@  dMbP?_*+%30&CAppendix A.2.2 ULNB and LNB Cost CalculationsMHP LaserJet 4V/4MV PostScriptg od ^ RdCustom page 1BBCustom page 2BBCustom page 3BB"d??U} } $ } I }  }  } $ } I } $ } } } }   T0 b b     b  b :   b b  b     mn b`E ,@b !pStandard Burner  =l Capital Costs~ QHeater Size (MMBtu)!aNumber of Burnersa""QStandard Burner Price ($)%QPurchased Equipment Cost ($)oTotal Capital CostAnnual Costs ($/yr) $@l?#( @ D !( @ DD %5Ҫ@D{Gz?!bY:TE~@ DD((( I@l@#(Kw+@ D!(ޞ@ DD%5[U@D{Gz?!bnSA@ DD((( R@l@#(J@D{Gz?!hVlj@ DD(((    !p ULNB  LNB  =l  Capital Costs ~  Capital Costs 3  QHeater Size (MMBtu)! aNumber of Burnersa"$ WPrice per Burner ($)b", QPurchased Equipment Cost ($)c"& }Total Capital Cost ($)d"# oAnnual Costs ($/yr)e"( aAnnual Cost Differential ($/yr)$ WPrice per Burner ($)f", QPurchased Equipment Cost ($)c"& QTotal Capital Cost ($)d"# WAnnual Costs ($/yr)e"( oAnnual Cost Differential ($/yr) $@l?X@! (@  D D % 5@ D {Gz?! 5,@  D D! V:TEn@  D D- X@ D (\?! (@ D D % (n@ D {Gz?! X,=F1@ D D! 5okT=@ D DI@l@2X@D D?D!(&C@ DD%5Á;1h@D{Gz?!5$kfb@ DD!lSA@  DD-X"@D(\?!(eDX+`@ DD% (jT>A@ D{Gz?! XK;@ D D! 5@NE6_@  D DR@l@2X-)4@D D?D!(㛿"@ DD%5CA@D{Gz?!5A6@ DD!Ev@ DD-X62@D(\?!(O|7@ DD% (7z@ D{Gz?! X,%xS@ D D! 5CE e@ D Db@l.@2X C˭@D D?D!(n~@ DD%5hs@D{Gz?!5Ȳb@ DD!`إ@ DD-X5@D(\?!(cQ@ DD% (ڏ]HT@ D{Gz?! X^Ĺ(@ D D! 5Хl6t@ D Dnu@qA@2[;J_@D D?D!)@ DD%h]@D{Gz?!eAg>@ DD!eXlj@ DD-[ƻLOX@D(\?!)`(@ DD% )V"@ D{Gz?! [=O@ D D! hpnh(1{@ D D  L,9m9?6Q?Q? Q?   .HD""Sf}"x (  r  0[  @ $]`[ 1h<2a As per vendor advice. b See Appendix A.1 for vendor supplied information. Burner price was calculated by multiplying the