Unit Details:
Unit Name : GP-001
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name :
Small Unit Aggregation Details:
Use Ivt Indicator: N
Highest Maximum Rated Heat Input Capacity:
142.8
Cumulative Maximum Rated Heat Input Capacity:
501.6
Emission Details:
Annual CO2 mass emissions from sorbent: 0 (Metric Tons)
Annual Biogenic CO2 Emissions:
0
(metric tons)
Annual Fossil fuel based CO2 Emissions:
157143
(metric tons)
Tier Fuel Details:
Fuel :
Natural Gas (Weighted U.S. Average)
Tier Name :
Tier 1 (Equation C-1b, natural gas billing in mmBtu)
Tier Methodology Start Date :
2020-01-01
Tier Methodology End Date :
2020-12-31
Fuel Emission Details :
Total CO2 emissions | Total CH4 emissions | Total N2O emissions | Total CH4 emissions CO2e | Total N2O emissions CO2e |
157143.0
(Metric Tons)
|
2.96
(Metric Tons)
|
0.296
(Metric Tons)
|
74
(Metric Tons)
|
88.3
(Metric Tons)
|
Equation C1b/C8b Inputs :
Natural Gas Usage :
2961610
(mmBtu/year)
Unit Name : GP-002
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name :
Small Unit Aggregation Details:
Use Ivt Indicator: N
Highest Maximum Rated Heat Input Capacity:
45
Cumulative Maximum Rated Heat Input Capacity:
45
Emission Details:
Annual CO2 mass emissions from sorbent: 0 (Metric Tons)
Annual Biogenic CO2 Emissions:
10.5
(metric tons)
Annual Fossil fuel based CO2 Emissions:
0
(metric tons)
Tier Fuel Details:
Fuel :
Other Biomass Gases
Tier Name :
Tier 1 (Equation C-1)
Tier Methodology Start Date :
2020-01-01
Tier Methodology End Date :
2020-12-31
Fuel Emission Details :
Total CO2 emissions | Total CH4 emissions | Total N2O emissions | Total CH4 emissions CO2e | Total N2O emissions CO2e |
10.5
(Metric Tons)
|
0.00
(Metric Tons)
|
0.000
(Metric Tons)
|
0
(Metric Tons)
|
0
(Metric Tons)
|
Equation C1/C8 Inputs :
Fuel Quantity :
308688
(scf/year)
Name or ID: | Anaerobic Digester-Biomethanator |
Anaerobic Process: | Anaerobic Reactor |
Is biogas generated in the process recovered? | Yes |
Number of weeks that the system was operational: | 52 |
Document or diagram that pertains to this process: | |
Average depth of the lagoon: | |
Does the facility measure COD or BOD5 concentration of the wastewater entering the anaerobic process? | COD |
Does the facility perform an ethanol production processing operation? If yes, which process is used? | Dry milling process |
How does the facility monitor the CH4 concentration in the biogas collected for destruction? | Weekly monitoring |
Is the biogas temperature incorporated into the monitoring equipment internal calculations? | Yes |
Is the biogas pressure incorporated into the monitoring equipment internal calculations? | Yes |
Is the biogas moisture content incorporated into the monitoring equipment internal calculations? | Yes |
Was biogas flow measured on a wet or dry basis? | |
Was biogas CH4 concentration measured on a wet or dry basis? | |
Does CH4 destruction occur at the facility, off-site, or both? | On-Site |
CH4 collection efficiency (based on cover type): | 0.99 |
Annual mass of CH4 generated from anaerobic wastewater treatment process: | 0 (Metric Tons) |
Annual mass of CH4 emissions from anaerobic wastewater treatment process: | 0.20 (Metric Tons) |
Rn: Annual quantity of CH4 recovered from the Anaerobic Process: | 3.49 (Metric Tons) |
Annual operating hours for the primary destruction device: | 8476 |
Destruction efficiency for the primary destruction device: | 0.98 |
Fraction of hours the primary destruction device was operating: | 0.965 |
Is a back-up destruction device present at the facility? | Yes |
Annual operating hours for the back-up destruction device: | 75 |
Destruction efficiency for the back-up destruction device: | 0.98 |
Fraction of hours the back-up destruction device was operating: | 0.009 |