Facility Name:Pennsylvania Grain Processing, LLC
Facility Identifier:
Facility Reporting Year:2020
Facility Location:
Address: 250 Technology Drive
City: Clearfield
State: PA
Postal Code: 16830

Facility Site Details:
CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):157,310.2
CO2 equivalent emissions from supplier subparts LL-QQ (metric tons):
Biogenic CO2 emissions from facility subparts C-II, SS, and TT (metric tons):10.5
Cogeneration Unit Emissions Indicator:N
GHG Report Start Date:2020-01-01
GHG Report End Date:2020-12-31
Description of Changes to Calculation Methodology:
Plant Code Indicator:N
Primary NAICS Code:325193
Second Primary NAICS Code:

Parent Company Details:
Parent Company Name:PENNSYLANIA GRAIN PROCESSING LLC
Address:250 Technology Drive, Clearfield,  PA 16830
Percent Ownership Interest:100

Subpart C: General Stationary Fuel Combustion

Gas Information Details

Gas NameCarbon Dioxide
Gas Quantity157,143 (Metric Tons)
Own Result?

Gas NameBiogenic Carbon dioxide
Gas Quantity10.5 (Metric Tons)
Own Result?

Gas NameMethane
Gas Quantity2.96 (Metric Tons)
Own Result?

Gas NameNitrous Oxide
Gas Quantity0.296 (Metric Tons)
Own Result?

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 emissionsTotal CH4 emissionsTotal N2O emissionsTotal CH4 emissions CO2eTotal 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 emissionsTotal CH4 emissionsTotal N2O emissionsTotal CH4 emissions CO2eTotal 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)


Subpart II: Industrial Wastewater Treatment

Gas Information Details

Gas NameMethane
Gas Quantity0.2 (Metric Tons)
Own Result?


Anaerobic Process Information:
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)


Equation II-1 Inputs:
WeekFloww (m3)MDP?CODw (kg/m3)MDP?B0 (kg CH4/kg COD)ALT?MCFALT?
1000.250.8
2000.250.8
3000.250.8
4000.250.8
5000.250.8
6000.250.8
7000.250.8
8000.250.8
9000.250.8
10000.250.8
11000.250.8
12000.250.8
13000.250.8
14000.250.8
15000.250.8
16000.250.8
17000.250.8
18000.250.8
19000.250.8
20000.250.8
21000.250.8
22000.250.8
23000.250.8
24000.250.8
25000.250.8
26000.250.8
27000.250.8
28000.250.8
29000.250.8
30000.250.8
31000.250.8
32000.250.8
33000.250.8
34000.250.8
35000.250.8
36000.250.8
37000.250.8
38000.250.8
39000.250.8
40000.250.8
41000.250.8
42000.250.8
43000.250.8
44000.250.8
45000.250.8
46000.250.8
47000.250.8
48000.250.8
49000.250.8
50000.250.8
51000.250.8
52000.250.8

Equation II-4 Inputs:
WeekVolumetric Biogas Flow (acf)MDP?Biogas CH4 Concentration (%)MDP?Biogas Temperature (°R)Biogas Pressure (atm)Biogas Moisture (cfw/cfb)
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52

Equation II-6 Inputs:
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