Upload
quinton-broughton
View
225
Download
3
Tags:
Embed Size (px)
Citation preview
1
What’s Up With Cement Plant Permitting?
What’s BACT?
Presented byA. A. Linero, P.E. AdminstratorNew Source Review Section
June 27, 2001
AWMA Conference, June 2001 2
Overview
Kiln Construction is BackFocus on Preheater/Calciner
ProcessFormation and Control of PollutantsWhat’s Going on in Europe Some BACT and LAER RangesLook at a Current ProjectWhat Next? Questions?
AWMA Conference, June 2001 3
Views are Author’s !
Not Opinions of Florida DEPWe do Case-by-Case ReviewsLiterature Search, Not a Technical
PaperAs Seen by a Permitting EngineerThere are Very Diverse OpinionsGreatly Simplified
AWMA Conference, June 2001 4
Dry Process Preheater Calciner Kilns
AWMA Conference, June 2001 5
Limited to New Dry Process Preheater Calciner Kilns
Rinker Photo By FDEP
AWMA Conference, June 2001 6
From Top of Preheater
Devil’s Slide Photos by FDEP
AWMA Conference, June 2001 7
Leaning Tower of Polysius?
Florida Rock Photo by A. Linero
AWMA Conference, June 2001 8
Lot’s of Projects
Production is up Nationwide. 80 Million TPYFlorida Rock – First New Kiln in a Dozen YearsNew Plants – CO, FL, MS, NY, TXModernizations and ExpansionsAL, AZ, CA, CO, FL, IN, MS, SC, TX, UTMost Require PSD Review and BACT (or LAER)Others “Net Out” – Switch Wet to Dry Process
AWMA Conference, June 2001 9
Pollutant Formation - NOX
Thermal NOX Temp. > 1200 OCKiln Burner ~ 2000 OCOxidizing ConditionsCalciner ~ 1000 OCFuel NOX
Kiln and CalcinerDevils’ Slide Photo by FDEP
AWMA Conference, June 2001 10
Pollutant Control - NOX
Minimize T and Raw Materials Fluctuations
Optimum Process and Raw Mix ControlIntelligent Systems – Linkman, PyroExpertMinimize Primary Air from Coal MillMaximize Hot Air From Clinker CoolerAll New Projects Do These Things
AWMA Conference, June 2001 11
Kiln Burner NOX
Graphic Source: F.L.Smidth/Fuller Multi-channel BurnerPyrojet, Swirlax, Duoflex, GyroTherm, RotoflamFlame Shaping and Localized Reducing
Conditions High Momentum Primary Air EnvelopeCompatible with Low NOX. All New Projects Do.
AWMA Conference, June 2001 12
SC Calciner
Staged Combustion (SC)Lower Stage – Reducing ZoneTires (15%), TDF, DDF, Bottle CapsTertiary Air and FuelUpper Stage – Top AirFlorida Rock InstallingMaybe 30 – 45% ReductionAll New Projects Do This
Graphic Source: Polysius
AWMA Conference, June 2001 13
Diaper Derived Fuel?
Devil’s Slide Filmed by FDEP
AWMA Conference, June 2001 14
Tire Gasification and SC
Whole TiresMaybe 40% TiresJura Cement - WildeggPossible at Suwannee, FL
Graphic Source: Polysius
AWMA Conference, June 2001 15
SNCR
Ammonia or Urea Injection
High T, Near Calciner15+ Kilns in EuropeTaiwanMost Without SCZero in U.S.
Graphic Source: Fueltec
AWMA Conference, June 2001 16
SNCR – Problems?
Much Resistance in U.S.“Slip” and Possibility of Detached
PlumeOften Occurs Even w/o SNCRAmmonia Sulfates and ChloridesCompatibility Question With SC
Graphic Source: EnviroCare
AWMA Conference, June 2001 17
SNCR – Opacity?
No Steam Plume in Dry Preheater Calciner Process Baghouse Will Help Ameliorate Problem Author saw No Plume at Siggenthal Still Getting Plume? Manage and Solve Detached Plume Problem Well Described by EnviroCare and CTL, Inc. Incorporate Into SO2 Control Hydrated Lime MicroMist, Avoid Aluminum Dross
Siggenthal Photo by A. Linero
AWMA Conference, June 2001 18
SNCR – SC Compatibility
For SNCR to Work, Need High T and O2
In SC Calciner, T is High where O2 is “Low”Outside of Calciner, O2 is “High” and T is “Low” Is Lower End of Window 800 or 900 OC Jura Zement Has SC and SNCR and Gasification!“No Effect on (Pre-SNCR) Excellent Plume
Opacity”No Ammonia Slip (Low Removal Objective?)
Graphic Source: Jura Zement
AWMA Conference, June 2001 19
Selective Catalytic Reduction
Catalyst and Low T Ammonia InjectionDemonstration Stage at SolnhofenExtremely Dusty EnvironmentOr Need to Re-heat Stack GasMaybe Exotic Compared to Other OptionsBetter to See What SC, SNCR, Achieve
First
AWMA Conference, June 2001 20
European Emission Limits
Polysius Graphic Modified by A. Linero
AWMA Conference, June 2001 21
SNCR at Leimen Plant - Germany
Graphic Source: Heidelberger
2.3 lb/ton
3.7 lb/ton
~1.3 ?
AWMA Conference, June 2001 22
What is BACT?
2.5 lb/ton at Kiln Built Circa 1980! Slug of 2.3 – 2.9 lb/ton BACTs, e.g. FRI 2.8 in
1996 ~ 1 lb/ton in Slite, Sweden (80% Reduction) ~ 1 lb/ton in Taiwan by SNCR ~ 1 lb/ton in 1994 Ash Grove SNCR Test ~ 1.2 lb/ton Annual Limit at Holnam Midlothian European IPPC BAT (200 – 500 mg/m3) Equals 0.9 to 2.3 lb/ton LAER? Must Be Near 1 lb/ton. Lower if SCR
Photo Source: RMC Lonestar
AWMA Conference, June 2001 23
Pollutant Formation – SO2
Fuel Sulfur – Kiln/CalcinerRoasting of Pyrites in PH
Graphic Source: F.L.Smidth/Fuller
AWMA Conference, June 2001 24
Pollutant Control – SO2
Raw Material Selection (Avoid Pyrites!) Fine CaO in Calciner Scrubs Kiln ~ 100% Move CaO by P to Upper Preheater Can Reduce Pyritic Emissions ~ 20-30% Capitol Cement and Ash Grove Chanute Need More Fuel, Balance Heat Capital Investment Looks Low
Graphic Source: F.L.Smidth/Fuller
AWMA Conference, June 2001 25
Pollutant Control – SO2
CaCO3 and Moisture on Raw Mill Surface Some of the CaO from D-SOX
Maybe Together 70+ Percent of Residual SO2
When Raw Mill Out – Control Gas Temperature Spray Fine Ca(OH)2 Mist into Conditioning Tower Not Enough - More Conventional Scrubbers Achieve as much as 90 Percent Removal
Pfeiffer Raw Mill
AWMA Conference, June 2001 26
Effect of Raw Materials & Process on SO2
PH/Calciner Kilns in TX – 1000’s of TPY of SO2
High Pyrites in Raw Materials Wet Kilns in Florida – 1000’s of TPY of SO2
Fuel Sulfur, No Calciner - less Self Scrubbing PH/Calciner Kilns in Florida – << 100 TPY No Pyrites in Raw Materials Florida Rock Kiln, Rinker Modernization From 1000+ TPY to ~ 20 TPY
Florida Rock Photo By FDEP
AWMA Conference, June 2001 27
What is BACT?
< 0.23 (or Better) in Florida With No Controls ~ 0.05 at Siggenthal by (Incidental) Coke
Filter ~ 1.3 lb/ton at TXI Midlothian to Avoid PSD < 1 lb/ton at Slite, Sweden (90% Reduction) European IPPC BAT (200 – 400 mg/m3) Equals 0.9 to 1.8 lb/ton D-SOx & Lime Mist With Moderate Pyrites 90 % Scrubber Control With Very High Pyrites
AWMA Conference, June 2001 28
Pollutant Formation - CO & VOC
CO From Incomplete CombustionVery Little VOC From Kiln and
CalcinerEvolution in PreheaterOrganic Carbon from Raw MaterialsCarbon from Coal AshVOC from Mill Scale, etc.
AWMA Conference, June 2001 29
Pollutant Control - CO & VOC
Hot Excess Air, Mixing Tertiary Air After Calcining E.G. Pyrotop after SC Raw Material Selection – e.g. Millscale ~ 70% VOC Reduction at Florida Rock Must Install Continuous Monitor Grind and Introduce Directly into Kiln
Graphic Source: KHD
AWMA Conference, June 2001 30
Regenerative Thermal Oxidation
Texas Cement MidlothianAbout 10 ModulesArea of a Football FieldEnter Market at Earliest DateAvoid PSD Delays “up to 3
Years”$17,500,000 for RTO$13,000,000 for SO2 Scrubber
Graphic Sources: Durr/Reeco
AWMA Conference, June 2001 31
Active Coke Filter
Siggenthal Switzerland In Conjunction with Dried Sludge Burning$15,000,000 Partly Funded by Zurich“Environmentally Friendly Dried Sludge
Burning”Concern Was Thallium and Mercury (on Cows?)Also Cleans up, SO2, dioxin/furan, and AmmoniaWith SNCR Constitutes POLVITEC by Polysius
AWMA Conference, June 2001 32
What is BACT?
VOC = ~ 0.1 lb/ton in Florida (Hard to Meet!)VOC = ~ 0.026 lb/ton at TXI (By RTO - LAER?)CO = ~ 2 – 3.6 lb/ton in Florida CO = ~ 6 – 8 lb/ton in SC CO = ~ 0.37 lb/ton at TXI (By RTO - LAER?)
AWMA Conference, June 2001 33
European Rule 2000/76/EG
Pollutant Concentration Process LimitDust 30 mg/m3 ~ 0.14 lb/ton
NOX 500 mg/m3 * ~ 2.3 lb/ton *800 mg/m3 ** ~ 3.7 lb/ton **
SO2 50 mg/m3 *** ~ 0.23 lb/ton ***Mercury 0,05 mg/m3 ~ 0.00023 lb/tonFluorides 1 mg/m3 ~ 0.0046 TOC 10 mg/m3 *** ~ 0.046 lb/ton ***CO _
* New Sources ** Existing Sources (Swedish non-EU standard is 200 mg/m3 ~ 0.9 lb/ton)*** Non Raw Material-Specific Emission
AWMA Conference, June 2001 34
Pollutant Concentration Process Limit
Chlorides 10 mg/m3 ~ 0.046 lb/ton
Cd and Thallium 0.05 mg/m3 ~ 0.00023 lb/ton
Sb+As+Pb+Cr+
Co+Cu+Mn+Ni+V 0.5 mg/m3 ~ 0.0023 lb/ton
Dioxin and Furan 0.1 ng ITEQ/m3
European Rule 2000/76/EG
AWMA Conference, June 2001 35
Ozone Non-Attainment Area
Pollutant
Requirement
Top Limit
Technology
Draft Limit
Proposed Control
NOX (4121 tpy)
LAER ~ 1 SNCR 3.61 2.82,3
SC SC &
SNCR(?)
VOC (129 tpy)
LAER 0.026 RTO ~0.11
Materials?
SO2 (850 tpy)
BACT 0.23 Varies ~0.74
Scrubbers
CO (3983 tpy)
BACT 0.37 RTO ~3.5 Materials?1. Initial Limit is 3.6 lb/ton during first two years by Staged Combustion 12-Month Average2. Limit is stepped down from 3.6 to 2.8 lb/ton between years 2 and 3 3. Company proposes LAER after 38 months of operation. Department sets LAER (2007 ??)
AWMA Conference, June 2001 36
Final Thoughts
4000 TPY of NOX equates to 50 Gas-fired Combined Cycle Plants = to 12,500
MW At 3 million Btu/ton of Clinker 3.6 lb NOX /ton limit equates to
1.2 lb NOX/million Btu heat input Order of magnitude > than new coal power plant Two orders > greater than gas-fired power plant Some low hanging fruit to pick here.
AWMA Conference, June 2001 37