CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):8,564,794.6
CO2 equivalent emissions from supplier subparts LL-QQ (metric tons):
Biogenic CO2 emissions from facility subparts C-II, SS, and TT (metric tons):0
Cogeneration Unit Emissions Indicator:Y
GHG Report Start Date:2021-01-01
GHG Report End Date:2021-12-31
Description of Changes to Calculation Methodology:
Plant Code Indicator:Y
Primary NAICS Code:325211
Second Primary NAICS Code:325199
Additional NAICS Codes: 325311 325120
Parent Company Details:
Parent Company Name:Ascend Performance Materials Holdings Inc
Address:1010 Travis Street Suite 900,
Huston,
TX 77002-3014
Percent Ownership Interest:100
Subpart C: General Stationary Fuel Combustion
Gas Information Details
| Gas Name | Carbon Dioxide |
| Gas Quantity | 1,001,033.3 (Metric Tons) |
| Own Result? | |
| Gas Name | Biogenic Carbon dioxide |
| Gas Quantity | 0 (Metric Tons) |
| Own Result? | |
| Gas Name | Methane |
| Gas Quantity | 15.68 (Metric Tons) |
| Own Result? | |
| Gas Name | Nitrous Oxide |
| Gas Quantity | 1.568 (Metric Tons) |
| Own Result? | |
Unit Details:
Unit Name : CP-1
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name :
Plant Code : 10416 (numeric, maximum of 6 digits)
Common Pipe Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity:
911.7
Cumulative Maximum Rated Heat Input Capacity:
3249.6
Emission Details:
Annual Biogenic CO2 Emissions:
0
(metric tons)
Annual Fossil fuel based CO2 Emissions:
863175.9
(metric tons)
Tier Fuel Details:
Fuel :
Natural Gas (Weighted U.S. Average)
Tier Name :
Tier 3 (Equation C-5, gaseous fuel)
Tier Methodology Start Date :
2021-01-01
Tier Methodology End Date :
2021-12-31
Fuel Emission Details :
| Total CO2 emissions | Total CH4 emissions | Total N2O emissions | Total CH4 emissions CO2e | Total N2O emissions CO2e |
|
847947.7
(Metric Tons)
|
15.68
(Metric Tons)
|
1.568
(Metric Tons)
|
392.0
(Metric Tons)
|
467.3
(Metric Tons)
|
Carbon Content Substitute Data Information :
Total number of valid carbon content determinations :
365
Total number of carbon content substitute data values :
0
Frequency of carbon content determinations :
Daily
Total number of operating hours in the reporting year for which missing data substitution was used for fuel usage :
0
Molecular Weight Information :
Total number of valid molecular weight determinations :
365
Total number of molecular weight substitute data values :
0
Frequency of molecular weight determinations :
Daily
Molar Volume Constant (MVC) used :
836.6 (scf/kg-mole)
Unit Name : CP-2
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name :
Plant Code : 10416 (numeric, maximum of 6 digits)
Common Pipe Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity:
258
Cumulative Maximum Rated Heat Input Capacity:
774
Emission Details:
Annual Biogenic CO2 Emissions:
0
(metric tons)
Annual Fossil fuel based CO2 Emissions:
0
(metric tons)
Tier Fuel Details:
Fuel :
Residual Fuel Oil No. 6
Tier Name :
Tier 3 (Equation C-4, liquid fuel)
Tier Methodology Start Date :
2021-01-01
Tier Methodology End Date :
2021-12-31
Fuel Emission Details :
| Total CO2 emissions | Total CH4 emissions | Total N2O emissions | Total CH4 emissions CO2e | Total N2O emissions CO2e |
|
0
(Metric Tons)
|
0
(Metric Tons)
|
0
(Metric Tons)
|
0
(Metric Tons)
|
0
(Metric Tons)
|
Carbon Content Substitute Data Information :
Total number of valid carbon content determinations :
1
Total number of carbon content substitute data values :
0
Frequency of carbon content determinations :
Once per fuel lot
Total number of operating hours in the reporting year for which missing data substitution was used for fuel usage :
0
Unit Name : EU-003
Unit Type : OB (Boiler, other)
Unit Description :
Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity:
388
(mmBtu/hr)
Plant Code : 10416 (numeric, maximum of 6 digits)
Emission Details:
Annual CO2 mass emissions from sorbent: 0 (Metric Tons)
Annual Biogenic CO2 Emissions:
0
(metric tons)
Tier Fuel Details:
Fuel :
Maleic Fuel Gas (Other (gas))
Tier Name :
Tier 3 (Equation C-5, gaseous fuel)
Tier Methodology Start Date :
2021-01-01
Tier Methodology End Date :
2021-12-31
Fuel Emission Details :
| Total CO2 emissions | Total CH4 emissions | Total N2O emissions | Total CH4 emissions CO2e | Total N2O emissions CO2e |
|
76130.2
(Metric Tons)
|
()
|
()
|
()
|
()
|
Carbon Content Substitute Data Information :
Total number of valid carbon content determinations :
40
Total number of carbon content substitute data values :
5
Frequency of carbon content determinations :
Weekly
Total number of operating hours in the reporting year for which missing data substitution was used for fuel usage :
0
Molecular Weight Information :
Total number of valid molecular weight determinations :
40
Total number of molecular weight substitute data values :
5
Frequency of molecular weight determinations :
Weekly
Molar Volume Constant (MVC) used :
849.5 (scf/kg-mole)
Unit Name : EU-004
Unit Type : OB (Boiler, other)
Unit Description :
Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity:
388
(mmBtu/hr)
Plant Code : 10416 (numeric, maximum of 6 digits)
Emission Details:
Annual CO2 mass emissions from sorbent: 0 (Metric Tons)
Annual Biogenic CO2 Emissions:
0
(metric tons)
Tier Fuel Details:
Fuel :
Maleic Fuel Gas (Other (gas))
Tier Name :
Tier 3 (Equation C-5, gaseous fuel)
Tier Methodology Start Date :
2021-01-01
Tier Methodology End Date :
2021-12-31
Fuel Emission Details :
| Total CO2 emissions | Total CH4 emissions | Total N2O emissions | Total CH4 emissions CO2e | Total N2O emissions CO2e |
|
69940.1
(Metric Tons)
|
()
|
()
|
()
|
()
|
Carbon Content Substitute Data Information :
Total number of valid carbon content determinations :
48
Total number of carbon content substitute data values :
5
Frequency of carbon content determinations :
Weekly
Total number of operating hours in the reporting year for which missing data substitution was used for fuel usage :
0
Molecular Weight Information :
Total number of valid molecular weight determinations :
48
Total number of molecular weight substitute data values :
5
Frequency of molecular weight determinations :
Weekly
Molar Volume Constant (MVC) used :
849.5 (scf/kg-mole)
Unit Name : EU-014
Unit Type : OB (Boiler, other)
Unit Description :
Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity:
258
(mmBtu/hr)
Plant Code : 10416 (numeric, maximum of 6 digits)
Emission Details:
Annual CO2 mass emissions from sorbent: 0 (Metric Tons)
Annual Biogenic CO2 Emissions:
0
(metric tons)
Tier Fuel Details:
Fuel :
KATT Fuel 2018 (Other (liquid))
Tier Name :
Tier 3 (Equation C-4, liquid fuel)
Tier Methodology Start Date :
2021-01-01
Tier Methodology End Date :
2021-12-31
Fuel Emission Details :
| Total CO2 emissions | Total CH4 emissions | Total N2O emissions | Total CH4 emissions CO2e | Total N2O emissions CO2e |
|
7015.3
(Metric Tons)
|
0
Y
(Metric Tons)
|
0
Y
(Metric Tons)
|
0
(Metric Tons)
|
0
(Metric Tons)
|
Carbon Content Substitute Data Information :
Total number of valid carbon content determinations :
12
Total number of carbon content substitute data values :
0
Frequency of carbon content determinations :
Monthly
Total number of operating hours in the reporting year for which missing data substitution was used for fuel usage :
0
Unit Name : EU-015
Unit Type : OB (Boiler, other)
Unit Description :
Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity:
258
(mmBtu/hr)
Plant Code : 10416 (numeric, maximum of 6 digits)
Emission Details:
Annual CO2 mass emissions from sorbent: 0 (Metric Tons)
Annual Biogenic CO2 Emissions:
0
(metric tons)
Tier Fuel Details:
Fuel :
KATT Fuel 2018 (Other (liquid))
Tier Name :
Tier 3 (Equation C-4, liquid fuel)
Tier Methodology Start Date :
2021-01-01
Tier Methodology End Date :
2021-12-31
Fuel Emission Details :
| Total CO2 emissions | Total CH4 emissions | Total N2O emissions | Total CH4 emissions CO2e | Total N2O emissions CO2e |
|
0
(Metric Tons)
|
0
Y
(Metric Tons)
|
0
Y
(Metric Tons)
|
0
(Metric Tons)
|
0
(Metric Tons)
|
Carbon Content Substitute Data Information :
Total number of valid carbon content determinations :
12
Total number of carbon content substitute data values :
0
Frequency of carbon content determinations :
Monthly
Total number of operating hours in the reporting year for which missing data substitution was used for fuel usage :
0
Subpart E: Adipic Acid Production
Gas Information Details
| Gas Name | Nitrous Oxide |
| Gas Quantity | 22,741.33 (Metric Tons) |
| Own Result? | |
Method used to estimate N2O emissions: Administrator Approved
Annual N2O sold or transferred off site: ()
Number of distinct abatement technologies: 1
Was NSCR used: N
Number of months missing data procedures were used to measure: 0
"Other" abatement technologies were used:
Yes
Description of "other" abatement technologies that were used: Thermal Reduction
Annual quantity of Cyclohexane or cyclohexanone/cyclohexanol mixture used to produce adipic acid: ()
Annual percent emission reduction:
81.9
(Percent)
Administrator Approved details
Is this a previously approved alternate method: yes
Name of alternate method: Continuous Process analyzers
Alternate method description: Use of process analyzers to monitor N2O to control units in real time.
Alternate method request date: 2017-01-10
Alternate method approval date: 2017-01-10
Unit Name : EU-002
Unit Type : Adipic Acid Production Unit
Unit Description :
Subpart P: Hydrogen Production
CEMS Monitoring Location (CML) Details
Gas Information Details
| Gas Name | Carbon Dioxide |
| Gas Quantity | 215,158.3 (Metric Tons) |
| Own Result? | |
| Gas Name | Biogenic Carbon dioxide |
| Gas Quantity | 0 (Metric Tons) |
| Own Result? | |
| Gas Name | Methane |
| Gas Quantity | 0 (Metric Tons) |
| Own Result? | |
| Gas Name | Nitrous Oxide |
| Gas Quantity | 0 (Metric Tons) |
| Own Result? | |
Annual quantity of carbon, other than CO2, collected and transferred off site in either gas, liquid, or solid forms, excluding methanol:
()
No Cems Hydrogen Unit Details:
Unit Name: EU-103
Unit Type: Hydrogen production process unit
Unit Description:
CO2Emissions: 104836.6 (Metric Tons)
Annual Quantity of Hydrogen Produced: ()
Annual quantity of ammonia intentionally produced as a desired product, if applicable:
()
Annual quantity of methanol intentionally produced as a desired product, if applicable:
()
Fuel/FeedStock Details:
Fuel/FeedStock Name:
Fuel/FeedStock Type:
Annual Fuel/Feedstock Consumed: ()
No Cems Hydrogen Unit Details:
Unit Name: EU-049
Unit Type: Hydrogen production process unit
Unit Description:
CO2Emissions: 110321.7 (Metric Tons)
Annual Quantity of Hydrogen Produced: ()
Annual quantity of ammonia intentionally produced as a desired product, if applicable:
()
Annual quantity of methanol intentionally produced as a desired product, if applicable:
()
Fuel/FeedStock Details:
Fuel/FeedStock Name:
Fuel/FeedStock Type:
Annual Fuel/Feedstock Consumed: ()
Subpart V: Nitric Acid Production
Gas Information Details
| Gas Name | Nitrous Oxide |
| Gas Quantity | 1,914.076 (Metric Tons) |
| Own Result? | |
SubpartVFacilityInformationDetails:
| Total Number of Nitric Acid Trains at the Facility [§98.226(f)] | 1 |
| Total Annual Nitric Acid Production for the Facility [§98.226(e)] (short tons) | |
| Total Annual Percent N2O Emission Reduction for All Nitric Acid Trains Combined [§98.226(q)] (percent) | percent |
NitricAcidTrainInformationDetails:
NitricAcidTrainInfoRowDetails:
| Nitric Acid Train ID [§98.226(a)] | EU-042 |
| Description of the Nitric Acid Train (Optional) | |
| Number of Months that a Missing Data Procedure Was Used to Determine a Monthly Quantity of Nitric Acid Production [§98.226(l)] | 0 |
| Type of Nitric Acid Process Used by the Train [§98.226(k)] | |
| Are N2O Emissions Estimated Using an Administrator-Approved Alternative Method? [§98.226] | No |
| If yes, is this a previously approved alternative method? [§98.223(a)(2)] | |
| If yes, enter the name of the Alternative Method [§98.226(n)(1)] | |
| If yes, provide a description of the Alternative Method [§98.226(n)(2)] | |
| If yes, enter the request date [§98.226(n)(3)] (mm/dd/yyyy) | |
| If yes, enter the approval date [§98.226(n)(4)] (mm/dd/yyyy) | |
| Number of Times in the Reporting Year that a Performance Test had to be Repeated [§98.226(m)(7)] | 0 |
| Performance Test (1 of 3): ID/Description [§98.226(m)] | 010AS-547799 |
| Performance Test (1 of 3): Test Method Used [§98.226(m)(2)] | EPA Method 320 |
| Performance Test (2 of 3): ID/Description (if applicable) [§98.226(m)] | |
| Performance Test (2 of 3): Test Method Used (if applicable) [(98.226(m)(2)] | |
| Performance Test (3 of 3): ID/Description (if applicable) [§98.226(m)] | |
| Performance Test (3 of 3): Test Method Used (if applicable) [(98.226(m)(2)] | |
| Does Nitric Acid Train Exhaust to an N2O Abatement Technology? [§98.226(h)] | No |
| Was Nonselective catalytic reduction (NSCR) used as an abatement technology? [§98.226(h)] | |
| Were any "other" abatement technologies used? [§98.226(h)] | |
| If yes, provide a description of the "Other" Abatement Technology [§98.226(h)] | |
| Date of Installation of Abatement Technology [§98.226(h)] (mm/dd/yyyy) | |
| Annual N2O Emissions for the Nitric Acid Train [§98.226(b)] (metric tons) | 1914.076214300667223308 |
Subpart TT: Industrial Waste Landfills
Gas Information Details
| Gas Name | Carbon Dioxide |
| Gas Quantity | 0 (Metric Tons) |
| Own Result? | |
| Gas Name | Biogenic Carbon dioxide |
| Gas Quantity | 0 (Metric Tons) |
| Own Result? | |
| Gas Name | Methane |
| Gas Quantity | 17.31 (Metric Tons) |
| Own Result? | |
| Gas Name | Nitrous Oxide |
| Gas Quantity | 0 (Metric Tons) |
| Own Result? | |
Landfill Details:
| Was the landfill open or closed |
Closed
|
| First year the landfill accepted waste | 1953 |
| If the landfill is closed, the last year that the landfill received waste | 1980 |
| Landfill Capacity | 145000 (Metric Tons) |
| Does the landfill have a landfill gas collection system | N |
| Passive vents and/or flares are present (vents or flares that are not considered part of the gas collection system) | N |
| An indication of whether leachate recirculation was used during the reporting year | N |
| The typical frequency of use of leachate recirculation over the past ten (10) years | Not used for the past ten (10) years |
| Each type of cover material used and Landfill surface area containing waste |
| Organic cover | 62150 (Square Meters) |
| Clay cover | 189052 (Square Meters) |
|
| Number of waste streams | 1 |
| Annual modeled methane generation TT1 | 19.24 (Metric Tons) |
| Annual modeled methane generation TT1 user overrided value | N |
Equation TT-1 Details:
| The fraction of CH4 in landfill gas (F), is it based on a measured value or default value | Default |
| Fraction by volume of CH4 in landfill gas | () |
| An MCF value other than the default of 1 was used | N |
Waste Stream For Method3 Details:
| Capacity of the landfill used (or the total quantity of waste-in-place) at the end of the "YrData" from design drawings or engineering estimates | () |
| Do you know the year when the landfill opened? | No |
| The year the landfill first received waste from company records, or 1960 (whichever is more recent) | |
Methane Generation and Emissions for Landfills without LFG Collection Systems
Methane Oxidation Fraction
|
Methane Oxidation Fraction TT-6
| 0.10 |
Gas Collection Systems details
| Methane Generation Equation TT6 | 17.31 (Metric Tons) |
Waste Stream Summary:
Stream Identification and Method(s) used to determine historical waste stream quantity for Misc
| Stream Name | Misc |
| Stream Description | Chemical Intermediates, spent catalysts, C&D |
| Type(s) Of Waste Present In The Waste Stream |
| other industrial solid waste |
| construction and demolition |
| inert waste |
|
| Range of years for which both disposal and production data were used in Equation TT-2 to calculate the average waste disposal factor for the landfill | 2010-2011 |
| First year this waste stream was placed in the landfill | 1960 |
| Last year this waste stream was placed in the landfill | 1980 |
| Method(s) used to determine historical waste stream quantity |
| Reporting Year | Method #1 | Method #2 | Method #3 | Method #4 | Decayrate | Waste disposed quantity (UOM) | Waste stream DOC value (UOM) | Is defaulted value from table TT1 | Is value measured using 60 day anaerobic biodegradation test | Is based on total volatile solids measurements |
| 1960 | N | Y | N | N | 0.06 | 5934.5 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1961 | N | Y | N | N | 0.06 | 5934.5 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1962 | N | Y | N | N | 0.06 | 6303.7 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1963 | N | Y | N | N | 0.06 | 6303.7 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1964 | N | Y | N | N | 0.06 | 5934.5 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1965 | N | Y | N | N | 0.06 | 5934.5 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1966 | N | Y | N | N | 0.06 | 5565.4 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1967 | N | Y | N | N | 0.06 | 5565.4 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1968 | N | Y | N | N | 0.06 | 5196.2 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1969 | N | Y | N | N | 0.06 | 5196.2 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1970 | N | Y | N | N | 0.06 | 4827.0 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1971 | N | Y | N | N | 0.06 | 4827.0 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1972 | N | Y | N | N | 0.06 | 4457.9 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1973 | N | Y | N | N | 0.06 | 4457.9 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1974 | N | Y | N | N | 0.06 | 4088.7 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1975 | N | Y | N | N | 0.06 | 4088.7 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1976 | N | Y | N | N | 0.06 | 3701.3 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1977 | N | Y | N | N | 0.06 | 3719.5 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1978 | N | Y | N | N | 0.06 | 3350.4 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1979 | N | Y | N | N | 0.06 | 2907.4 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
| 1980 | N | Y | N | N | 0.06 | 2907.4 (Metric Tons) | 0.2 (Metric Tons) | Y | N | N |
|
- Method #1: Used one of the waste quantity measurement methods specified in 98.463(a)(2)(i): direct mass measurements, direct volume measurements multiplied by waste stream density, mass balance procedures (difference between the mass of process inputs and the mass of process outputs), or the number of loads multiplied by the mass of waste per load based on the working capacity of the vehicle or container.
- Method #2: Calculated the average waste disposal rate per Equation TT-2 and calculated the waste disposal quantities for historic years in which direct waste disposal measurements are not available using historical production data per Equation TT-3.
- Method #3: Calculated an average annual bulk waste disposal quantity for historic years when waste quantity data as determined by other methods are available consecutively for the most recent disposal years (Equation TT-4a).
- Method #4: Calculated an average annual bulk waste disposal quantity for historic years when waste quantity data as determined by other methods are available for sporadic (non-consecutive) years (Equation TT-4b).