GHG BACT Analysis Deanna L. Duram, P.E., C.M. August 4, 2011 Air & Waste Management Association Southern Section Meeting trinityconsultants.com
Dec 14, 2015
GHG BACT Analysis
Deanna L. Duram, P.E., C.M.August 4, 2011
Air & Waste Management AssociationSouthern Section Meeting
trinityconsultants.com
Outline
EPA Guidance and 5-Step Process Differences from traditional BACT
approach Highlight a biomass case study
throughout
EPA BACT Guidance Case-by-case determination Performed by applicant; approved by agency EPA recommends 5-Step top-down BACT evaluation
process Emission limits achievable considering…
Economic impacts Environmental and energy impacts
EPA guidance materials PSD and Title V Permitting Guidance for GHGs White Papers on GHG Control Measures On-Demand Video Training Materials, including sample
BACT assessments Enhanced RBLC
5-Step Top-Down BACT Process
Step 0 – Define the Source Step 1 – Identify available control options Step 2 – Eliminate technically infeasible options Step 3 – Rank options by control effectiveness Step 4 – Evaluate most effective controls and
emission limits achievable Step 5 – Select BACT
Step 0 – Define the Source
Applicant defines goals, objectives, purpose, and basic design
Source definition generally provides key design elements that are not under consideration through the BACT process
Define in permit application Permit issuer must discern which
design elements are inherent to that purpose and objectives and which may be changed for pollutant reductions
Step 0 Case StudyNew Combined Heat and Power System at
existing pulp and paper mill 620 MMBtu/hr bubbling fluidized bed boiler 40 MW Steam turbine generator Biomass combustion (bark, mill residuals) Natural gas for startup burners and some load
burning, < 250 MMBtu/hr Installation allows for shutdown of 1 coal/oil/gas
power boiler; removal of coal/oil from a second power boiler, retaining only gas combustion
Objective is to generate renewable energy to replace fossil fuel energy on site and for potential sale to the utility grid
Identify all control technologies available to the source, including: Inherently lower-emitting processes
and designs Add-on technologies Control methods applied at similar
emissions sources Feasible combinations of these
technologies Considers facility-level impacts
No off-site impacts considered, technology must represent emissions reduction at facility
Step 1: Identify
Available Control Options
(1/2)
Not required to include options that “fundamentally redefine the nature of the source”
No clear guidance re: which technologies redefine nature of source
Fuel type as BACT? EPA guidance considers: Cleaner versions of primary fuel Increased usage of secondary fuel Alternative fuel for which source is not
already configured EPA guidance leaves door open for
stricter interpretations by permitting authority
Use relevant white papers as starting point
Step 1: Identify
Available Control Options
(2/2)
EPA Guidance Potential carbon neutrality (based on life-cycle of biofuel)
not considered At facility-level, CO2 emissions from biofuels similar to
fossil fuels Biofuels must represent emissions reduction at facility
level to be considered viable GHG BACT option Biogenic carbon deferral
3/21/2011: EPA proposes deferral of GHG permitting requirements for CO2 emissions from biogenic sources
EPA issued guidance for determining BACT for bioenergy production
Promulgated 7/20/2011 Effective immediately for delegated states SIP approved states may incorporate into rules
Step 1 Biofuel Considerations
Step 1 Energy Efficiency Considerations (1/2)
EPA BACT guidance stresses importance of energy efficiency Primary Step 1 option(s) for combustion sources
Construction of new facilities GHG BACT evaluated on facility-wide basis, including
energy efficiency Evaluate emissions from non-emitting, energy
consuming equipment Modification to existing facilities
BACT applies to new or modified emission unit, not necessarily to energy consuming equipment
EPA guidance still encourages permitting agencies to consider energy efficiency
EPA guidance recommends benchmarking evaluation Collectively assess small energy saving
measures by benchmarking efficiency of new unit of similar design
EPA resources to support benchmarking analyses ENERGY STAR program Sector-specific tools, Energy Performance
Indicators (EPIs), etc.
Step 1 Energy Efficiency Considerations (2/2)
Step 1 CCS Considerations Carbon Capture and Storage (CCS) One of primary distinctions between traditional BACT
and GHG BACT Per EPA, consider CCS in Step 1 for large CO2
emitters, sources emitting high-purity CO2 streams Hydrogen production Ammonia production Natural gas processing Ethanol production Ethylene oxide production Cement production Iron and steel manufacturing
Even if non high-purity CO2 stream, may need to include as a “possible” control option
Step 1 Case Study CCS
High-purity stream? Not on EPA list Limited industrial applications
Efficient Boiler Design Technology selection of BFB boiler over other designs Redefining source?
Lowest Carbon Fuel Consideration of back-up fuels as primary (natural
gas) Source redefining concerns – not evaluating any other
fuel possibilities Energy Efficiency Options
Number of options in EPA guidance documents New boiler – state of the art
Step 2: Eliminate
Technically Infeasible
Options
Is technology available? Reached licensing and
commercial development stage Compliance with BACT limit
demonstrated at similar facility Is technology applicable based
on physical, chemical, and engineering principles?
Per EPA, absence of a commercial guarantee for GHG emissions not sufficient to eliminate option from consideration
Step 2 CCS Considerations
Must consider technical feasibility of each step Capture, transport and storage
If any step infeasible, CCS considered technically infeasible Low-purity stream? Space Right-of-ways Access to storage reservoir
May suffice to demonstrate difference between CCS considerations at applicant’s facility and demonstrated CCS
Many state agencies prefer to monetize everything (eliminate from Step 4 instead)
Step 2 Case Study CCS
Low-purity stream? No available storage/pipeline
Boiler design Addressed supercritical steam design (greater than
3,200 psig operating pressure) as infeasible for this boiler size
Fluidized bed, suspension, stoker, and pile combustion feasible options
Lowest carbon fuel Use of natural gas feasible
Efficiency options Feasible
Step 3: Rank
Remaining Control Options
Ranked by effectiveness of control Traditionally presented as:
Percent pollutant removal Controlled emission rate Reduction in emissions over time
For GHG, EPA advocating efficiency-based control effectiveness Consider thermal efficiency by using
emissions per unit of output (rather than per unit of fuel input)
Must rank logical combinations of the technologies
Can be challenging given variety of iterations on energy efficiencies
Step 3 Case Study Compared boiler efficiencies
In this case, ranked based on energy efficiency – fluidized bed is the clear choice
What if proposing to install a new stoker boiler with a lower energy efficiency?
Is this an area an agency can look at – redefining the source?
Did not do a straight comparison between remaining options
Proceeded to Step 4 with a BFB boiler, and lowest carbon fuel and energy efficiency options to be reviewed
Step 4: Evaluate
Most Effective Controls
(1/3)
Ranked by effectiveness of control Traditionally presented as:
Percent pollutant removal Controlled emission rate Reduction in emissions over time
Top-down – Start with most effective control option
Consider economic, environmental, and energy-related impacts BACT typically focuses on economic
considerations But EPA guidance suggests other
collateral impacts increasingly important for GHG BACT
Step 4: Evaluate
Most Effective Controls
(2/3)
Economic considerations Evaluated on a per ton CO2 equivalent
basis instead of per ton individual GHG EPA guidance considers average cost
effectiveness and incremental cost of adding compatible control technology
No cost effectiveness threshold ($/ton CO2e) in EPA guidance Work Group’s Interim Phase I Report
identifies cost effectiveness range from $3-$150/ton CO2e
Additional local economic factors (new for GHGs) High control cost relative to project cost Potential movement to overseas
production Local job losses
Step 4: Evaluate
Most Effective Controls
(3/3)
Additional considerations Direct energy costs (e.g.
combustion sources) Indirect energy usage (e.g.
purchased electricity) For CCS, consider parasitic load On-site and off-site environmental
implications (e.g., life cycle of biofuels)
Step 4 Case Study Environmental benefits of project
Combustion of plant residuals - Identified by EPA as a CH4 control measure for on-site landfills, so used that logic as a benefit for the project
Significant reduction in coal generated power on-site Reduction in wastewater through scrubber removal Off-site benefit – generation of renewable energy, sale of
renewable energy to grid, likely displacing fossil-fuel generated electricity
Natural gas is a non-renewable fuel Higher costs than biomass Biomass carbon-neutrality? Recent EPA guidance –
biomass combustion is BACT State of the art energy efficiency options for new
unit
Step 5: Select BACT
(1/2)
Select BACT based on most efficient control option or combination of options not eliminated by Step 4
Permitted BACT standards vary Emission limits (output basis,
accounting for energy efficiency) Averaging time periods Equipment specifications Work practices Associated monitoring, recordkeeping,
and reporting EPA advocates BACT limits with
longer averaging periods to address GHG emissions and load variations inherent in combustion equipment
Step 5: Select BACT
(2/2)
May include work practices such as an Environmental Management System (EMS) focused on energy efficiency ENERGY STAR provides guidance BACT limit may include implementation
of energy saving measures identified by EMS
EPA’s Sample GHG BACT assessments Municipal solid waste landfill Natural gas-fired boiler Hydrogen plant at petroleum refinery Coal-fired electricity generating facility Kiln at a cement plant Natural gas compressor station Gas-fired combined cycle power plant
Step 5 Case Study Proposed BACT limit based on vendor provided data 0.45 lb CO2e per lb steam on a 12-month rolling
average basis Anticipated CEM for monitoring for CO2, and
subsequent calculations for CH4 and N2O Since application submittal, EPA released biomass
deferral proposal and bioenergy GHG BACT guidance
State agency was considering a range of options, even having mentioned the possibility of “good combustion practices” as BACT
Stay tuned...