© 2007 chevron and john zink company, llc
TRANSCRIPT
© 2007 Chevron and John Zink Company, LLC
© 2007 Chevron and John Zink Company, LLC
Session 10Session 10Thursday, December 7, 8:00Thursday, December 7, 8:00--9:309:30
NOx Reduction Implementation TechnologyNOx Reduction Implementation Technology
PlantPlant--wide NOx Reduction Strategies:wide NOx Reduction Strategies:ChevronChevron ––John Zink ExperienceJohn Zink Experience
Ed Shepherd, Chevron (Richmond, CA)Ed Shepherd, Chevron (Richmond, CA)JimJim SeeboldSeebold, retired from Chevron (Richmond, CA), retired from Chevron (Richmond, CA)
Chuck Baukal, John Zink (Tulsa, OK)Chuck Baukal, John Zink (Tulsa, OK)
© 2007 Chevron and John Zink Company, LLC
Factors to Consider
•Existing & future permitted NOx levels•Existing equipment emissions performance•Capital & operating costs•Complexity & reliability•Emission credits costs•Planned equipment shutdowns•Future production levels•Future process modifications•Space availability & requirements•Timing•Heating equipment loading (base vs. peaking)•Environmental considerations of any new equipment
© 2007 Chevron and John Zink Company, LLC
NOx Reduction Efficiency
0.006 –0.01590 –97%Selective Catalytic Reduction (SCR)
0.033 –0.08540%Selective Noncatalytic Reduction(SNCR)
0.02555%Flue Gas Recirculation
0.007 –0.0380 –95%Ultra-Low-NOx-Burners (ULNB)
0.0660%Low-NOx Burners (LNB)
0.14Base CaseStandard Burners
ApproximateEmissions(lb/MMBtu)
ApproximateReduction
(%)Technology
Source: M. Bradford et al., Controlling NOx Emissions –Part 1, Chem. Eng. Prog., Vol. 98, No. 3, pp. 42-46, 2002.
© 2007 Chevron and John Zink Company, LLC
NOx Reduction in Process Heaters
Control TechnologyControlledEmissions
PercentReduction
Low-NOx Burners 0.1 –0.3 lb/106 Btu 25-65*
Staged Air Lances Not Available 35-51
Ammonia Injection Not Available 43-70
Urea Injection + Low NOx Burner Not Available 55-70
Selective Catalytic Reduction 20 –40 ppm 65-90
Selective Catalytic Reduction +Low NOx Burner
25 –40 ppm 70-90
*Reductions of up to 90% have been demonstrated.
Source: J. Bluestein, NOx Controls for Gas-Fired Industrial Boilers & Combustion Equipment:A Survey of Practices, Gas Research Institute (Chicago), Report GRI-92/0374, 1992.
© 2007 Chevron and John Zink Company, LLC
NOx Reduction Cost Effectiveness ($/ton)
0 500 1000 1500 2000 2500 3000 3500
Current Generation LowNOx Burners
Fuel Dilution onConventional Burners
Next Generation Low -NOx Burners
SCR + Low -NOx Burners
SCR System
$/Ton NOx Reduced
Source: J. McAdams et al., Minimize NOx emissions cost-effectively, Hydrocarbon Processing,Vol. 80, No. 6, pp. 51-58, 2001.
© 2007 Chevron and John Zink Company, LLC
NOx Reduction RetrofitsCost Impact of Reduction Mandates
•Shape of curveconfirmed in everycapital project we haveeither done or studied
•Significant differencebetween 65% and 85%
•That kind of differenceroughly DOUBLES thecost
•Paying public &stockholders like thelower cost better0
50
100
150
200
0 250 500 750 1000 1500 2000 2500 500065% 85%NOx Reduction
Cost
Major Processing ComplexNOx Reduction ProjectsCost vs. Percent ReductionLeast-Cost Technology Mix
© 2007 Chevron and John Zink Company, LLC
Most cost-effective approach to plant-wide NOx reductionbenefits both consuming public & corporate shareholders
•Negotiate a bubble rule on emissions fromthe entire processing complex
•Try to negotiate a cost-effective overallreduction under the bubble
•Control major sources to the max leavingsmaller sources alone
•Favor ultra low NOx burner retrofits avoidingthe proliferation of smaller SCRs
•But provide at least one huge SCR on amajor source (e.g., boiler house, steammethane reformer) as a “dial”control on totalemissions under the bubble
© 2007 Chevron and John Zink Company, LLC
What we wouldWhat we wouldlikelike NOTNOT to doto do!!
What we wouldWhat we wouldLIKELIKE to doto do!!
© 2007 Chevron and John Zink Company, LLC
35-mm slideconversion coming!ItIt’’s onlys only
moneymoney!!
Why we donWhy we don’’t liket likeSCRs too much . . .SCRs too much . . .
© 2007 Chevron and John Zink Company, LLC
Selective Catalytic Reduction (SCR) System
FlueGas
Flue gascontainingNOX fromanotherprocess
CatalystAmmonia in carrier gas
© 2007 Chevron and John Zink Company, LLC
OK, fine, you may prefer to do burners,but which SCRs make the most sense?
•Really BIG ones …•The bigger the better …•They’re all highly effective …•But the bigger they are the more cost-
effective they become!
© 2007 Chevron and John Zink Company, LLC
5
10
15
20
25
30
35
0 500 1000 1500 2000 2500 3000Fir ing Rat e, mmBt u/ hr
(mmBtu)1/2
Build reallyBuild really BIGBIG SCRsSCRs!!
© 2007 Chevron and John Zink Company, LLC
CapExCapEx OpExOpExNo SCR at the boiler house! …...…….…. ~$10m ~$2m/yr
No SCR at crude unit F1100/F1160! … ~$10m ~$2m/yr
No SCR at hydrogen reformer F355! ... ~$10m ~$2m/yr
Chevron RichmondChevron Richmond’’s NOx Project Highlightss NOx Project HighlightsHuge Savings Accrued to the Shareholders by Inspiring &
Supporting the Development of Extremely Low-NOx Burners
Intense collaboration with burner suppliersIntense collaboration with burner suppliers
Crude unit burners installedCrude unit burners installed onon--thethe--runrunFavorable margins — NONO shutdown contributed torefinery profitability
~$30m~$30m ~$6m/yr~$6m/yr
SavingsSavings
© 2007 Chevron and John Zink Company, LLC
Chevron RichmondChevron Richmond#4 Crude Unit#4 Crude Unit
Ultra Low NOx Burner RetrofitUltra Low NOx Burner Retrofit
© 2007 Chevron and John Zink Company, LLCUltra low NOx burners installed on the run!
© 2007 Chevron and John Zink Company, LLC
180 ppm 0 ppm
© 2007 Chevron and John Zink Company, LLC
180 ppm 14 ppm
© 2007 Chevron and John Zink Company, LLCBefore 180 ppmBefore 180 ppm After 14 ppmAfter 14 ppm
SCR Reduction (92%) at a Burner PriceSCR Reduction (92%) at a Burner Price!!For process heating youFor process heating you DONDON’’TT need a selective catalytic reduction flue gas treatmentneed a selective catalytic reduction flue gas treatment
plant but you reallyplant but you really DODO need burners so why not superneed burners so why not super--low NOx burnerslow NOx burners
© 2007 Chevron and John Zink Company, LLC
Rel
ativ
eN
Ox
Em
issi
on
s
Fuel leancombustion
Fuel richcombustion
Diffusion Flame
Premix Flame
FlammabilityFlammabilityLimitLimit
Region ofStoichiometricCombustion
Design burner toDesign burner tooperate in this regionoperate in this region
The Trick?Deep penetration into the
low-Btu regime whilstmaintaining flame
stability!
ULTRA LEAN PREMIXULTRA LEAN PREMIX
© 2007 Chevron and John Zink Company, LLC
On the other hand, you’ll stillneed at least one monster SCR… whether you like it or not!
© 2007 Chevron and John Zink Company, LLC
……II’’llll KILLKILL youyou !!Be Safe or ...
Free-standing stack lift withmonster low-temperature SCRin the background (on one of two
SMR furnaces) illustrates whywe don’t like SCRs too much…
© 2007 Chevron and John Zink Company, LLC
PrePre--lift Safety Talklift Safety Talk
© 2007 Chevron and John Zink Company, LLC
3 Cell Terrace WallSteam Methane Reformer
228 burners
The other SMR furnace got ultra low NOx burners!
© 2007 Chevron and John Zink Company, LLC
Chevron Richmond Boiler HouseChevron Richmond Boiler HouseNote hills thatNote hills that wouldwould have beenhave been
the central duct supportsthe central duct supportsfor two monster SCRs ...for two monster SCRs ...
© 2007 Chevron and John Zink Company, LLC
Poor ManPoor Man’’s SCR:s SCR:Fuel ConditioningFuel Conditioning!!
“Fuel Induced Recirculation”(FIR) or “Fuel Dilution”
PERF Fuel DilutionConstant Firing Rate
55
60
65
70
75
80
85
90
95
100
105
0 5 10 15 20 25 30 35Nitrogen in Fuel Gas, vol%
NO
x,p
pm
•Reaction rate limited!
•Reduce flame temperature,reduce NOx!
•“Cool”Fuel!
•Ain’t science wunaful?
© 2007 Chevron and John Zink Company, LLC
TThehe BIGBIG IIdea:dea:
““Deep penetration into the low-Btu regime… while still maintaining flame stability!”
ItIt’’s all about making a lows all about making a low--Btu fuelBtu fuelPremixed “FIR”(Fuel Induced Recirculation) Example
One way to do it …
flue gas
fuel gas
primaryair
secondaryair
flameflame
© 2007 Chevron and John Zink Company, LLC
~ 93% NOx Reduction!
© 2007 Chevron and John Zink Company, LLC
DIAL-A-NOX in action !!!
#4 Boiler Sub#4 Boiler Sub--1010 ppmppm DemonstrationDemonstration
~ 98% NOx Reduction!
© 2007 Chevron and John Zink Company, LLC
© 2007 Chevron and John Zink Company, LLC
Recent photograph of an expert alertly seeking breakthrough soluRecent photograph of an expert alertly seeking breakthrough solutions ...tions ...
QuestionsQuestions??