GHG Summary Report

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):21,370.6
CO2 equivalent emissions from supplier subparts LL-QQ (metric tons):
Biogenic CO2 emissions from facility subparts C-II, SS, and TT (metric tons):5,319.7
Cogeneration Unit Emissions Indicator:N
GHG Report Start Date:2023-01-01
GHG Report End Date:2023-12-31
Description of Changes to Calculation Methodology:
Plant Code Indicator:N
Primary NAICS Code:311411
Second Primary NAICS Code:

Parent Company Details:

Parent Company Name:MCCAIN USA INC
Address:1 Tower Lane, Oakbrook Terrace, IL 60181
Percent Ownership Interest:100

Subpart C: General Stationary Fuel Combustion

Gas Information Details

Gas Name	Carbon Dioxide
Gas Quantity	20,040.2 (Metric Tons)
Own Result?

Gas Name	Biogenic Carbon dioxide
Gas Quantity	5,319.7 (Metric Tons)
Own Result?

Gas Name	Methane
Gas Quantity	0.72 (Metric Tons)
Own Result?

Gas Name	Nitrous Oxide
Gas Quantity	0.107 (Metric Tons)
Own Result?

Unit Details:

Unit Name : Biogas Flare Stack
Unit Type : FLR (Flare)
Unit Description :

Individual Unit Details:
Use Ivt Indicator: N
Maximum Rated Heat Input Capacity: 26.5 (mmBtu/hr)

Emission Details:
Annual Biogenic CO2 Emissions: 419.4 (metric tons)

Tier Fuel Details:

Fuel : Other Biomass Gases
Tier Name : Tier 1 (Equation C-1)
Tier Methodology Start Date : 2023-01-01
Tier Methodology End Date : 2023-12-31

Fuel Emission Details :

Total CO2 emissions	Total CH4 emissions	Total N2O emissions	Total CH4 emissions CO2e	Total N2O emissions CO2e
419.4 (Metric Tons)	0.03 (Metric Tons)	0.005 (Metric Tons)	0.6 (Metric Tons)	1.5 (Metric Tons)

Equation C1/C8 Inputs :
Fuel Quantity : 12296077 (scf/year)

Unit Name : GP-Boilers
Unit Description :

Small Unit Aggregation Details:
Use Ivt Indicator: N
Highest Maximum Rated Heat Input Capacity: 98.5
Cumulative Maximum Rated Heat Input Capacity: 197.644

Emission Details:
Annual Biogenic CO2 Emissions: 4836.7 (metric tons)
Annual Fossil fuel based CO2 Emissions: 20040.2 (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 : 2023-01-01
Tier Methodology End Date : 2023-12-31

Fuel Emission Details :

Total CO2 emissions	Total CH4 emissions	Total N2O emissions	Total CH4 emissions CO2e	Total N2O emissions CO2e
19278.3 (Metric Tons)	0.36 (Metric Tons)	0.036 (Metric Tons)	9.1 (Metric Tons)	10.8 (Metric Tons)

Equation C1b/C8b Inputs :
Natural Gas Usage : 363331 (mmBtu/year)

Fuel : Distillate Fuel Oil No. 2
Tier Name : Tier 1 (Equation C-1)
Tier Methodology Start Date : 2023-01-01
Tier Methodology End Date : 2023-12-31

Fuel Emission Details :

Total CO2 emissions	Total CH4 emissions	Total N2O emissions	Total CH4 emissions CO2e	Total N2O emissions CO2e
761.9 (Metric Tons)	0.03 (Metric Tons)	0.006 (Metric Tons)	0.8 (Metric Tons)	1.8 (Metric Tons)

Equation C1/C8 Inputs :
Fuel Quantity : 74649 (gallons/year)

Fuel : Other Biomass Gases
Tier Name : Tier 1 (Equation C-1)
Tier Methodology Start Date : 2023-01-01
Tier Methodology End Date : 2023-12-31

Fuel Emission Details :

Total CO2 emissions	Total CH4 emissions	Total N2O emissions	Total CH4 emissions CO2e	Total N2O emissions CO2e
4836.7 (Metric Tons)	0.30 (Metric Tons)	0.059 (Metric Tons)	7.4 (Metric Tons)	17.4 (Metric Tons)

Equation C1/C8 Inputs :
Fuel Quantity : 141814766 (scf/year)

Unit Name : Sludge Digester Heater
Unit Type : PRH (Process Heater)
Unit Description :

Individual Unit Details:
Use Ivt Indicator: N
Maximum Rated Heat Input Capacity: 2 (mmBtu/hr)

Emission Details:
Annual CO₂ mass emissions from sorbent: 0 (Metric Tons)
Annual Biogenic CO2 Emissions: 63.6 (metric tons)

Tier Fuel Details:

Fuel : Other Biomass Gases
Tier Name : Tier 1 (Equation C-1)
Tier Methodology Start Date : 2023-01-01
Tier Methodology End Date : 2023-12-31

Fuel Emission Details :

Total CO2 emissions	Total CH4 emissions	Total N2O emissions	Total CH4 emissions CO2e	Total N2O emissions CO2e
63.6 (Metric Tons)	0.00 (Metric Tons)	0.001 (Metric Tons)	0.1 (Metric Tons)	0.2 (Metric Tons)

Equation C1/C8 Inputs :
Fuel Quantity : 1865396 (scf/year)

Subpart II: Industrial Wastewater Treatment

Gas Information Details

Gas Name	Methane
Gas Quantity	51.22 (Metric Tons)
Own Result?

Anaerobic Process Information:

Name or ID:	Covered Anaerobic Lagoon
Anaerobic Process:	Anaerobic Deep Lagoon
Is biogas generated in the process recovered?	Yes
Number of weeks that the system was operational:	52
Number of hours the biogas collection system was operational:	8784
Document or diagram that pertains to this process:
Average depth of the lagoon:	7(Meters)
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?	No ethanol production processing operations are performed at this facility
How does the facility monitor the CH₄ concentration in the biogas collected for destruction?	Daily averaging of continuous 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):	0.975
Annual mass of CH₄ generated from anaerobic wastewater treatment process:	1975.28 (Metric Tons)
Annual mass of CH₄ emissions from anaerobic wastewater treatment process:	29.28 (Metric Tons)

Equation II-1 Inputs:

Week	Flow_w (m³)	MDP?	COD_w (kg/m³)	MDP?	B₀ (kg CH₄/kg COD)	ALT?	MCF	ALT?
1	47451		4.2		0.25		0.8
2	45580		2.0		0.25		0.8
3	48687		3.4		0.25		0.8
4	51520		4.9		0.25		0.8
5	40897		5.8		0.25		0.8
6	42954		5.8		0.25		0.8
7	45216		5.8		0.25		0.8
8	37048		6.7		0.25		0.8
9	48119		5.9		0.25		0.8
10	48200		5.9		0.25		0.8
11	44037		5.0		0.25		0.8
12	45043		3.4		0.25		0.8
13	47318		3.4		0.25		0.8
14	42073		3.4		0.25		0.8
15	50472		4.0		0.25		0.8
16	51912		5.1		0.25		0.8
17	47348		4.9		0.25		0.8
18	49529		4.8		0.25		0.8
19	49882		4.7		0.25		0.8
20	35695		4.5		0.25		0.8
21	27247		3.0		0.25		0.8
22	41890		2.9		0.25		0.8
23	39598		2.7		0.25		0.8
24	47851		3.7		0.25		0.8
25	51054		4.6		0.25		0.8
26	38167		5.7		0.25		0.8
27	48696		4.8		0.25		0.8
28	45771		7.7		0.25		0.8
29	44682		4.8		0.25		0.8
30	45552		5.1		0.25		0.8
31	47510		5.2		0.25		0.8
32	36804		5.3		0.25		0.8
33	6485		4.3		0.25		0.8
34	35689		4.7		0.25		0.8
35	44685		4.7		0.25		0.8
36	42372		4.7		0.25		0.8
37	45239		5.0		0.25		0.8
38	40993		2.9		0.25		0.8
39	44535		4.4		0.25		0.8
40	46216		5.0		0.25		0.8
41	46997		5.7		0.25		0.8
42	45881		3.3		0.25		0.8
43	47196		3.5		0.25		0.8
44	43314		3.7		0.25		0.8
45	38574		4.2		0.25		0.8
46	36436		4.3		0.25		0.8
47	35881		4.3		0.25		0.8
48	48381		3.6		0.25		0.8
49	39915		3.0		0.25		0.8
50	49288		4.1		0.25		0.8
51	14696		5.3		0.25		0.8
52	2077		5.3		0.25		0.8

Equation II-4 Inputs:

Week	Volumetric Biogas Flow (acf)	MDP?	Biogas CH₄ Concentration (%)	MDP?	Biogas Temperature (°R)	Biogas Pressure (atm)	Biogas Moisture (cfw/cfb)
1				Yes
2				Yes
3				Yes
4				Yes
5
6
7
8
9
10				Yes
11				Yes
12				Yes
13				Yes
14				Yes
15				Yes
16				Yes
17				Yes
18				Yes
19				Yes
20				Yes
21				Yes
22				Yes
23				Yes
24				Yes
25				Yes
26				Yes
27				Yes
28				Yes
29				Yes
30				Yes
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:

R_n: Annual quantity of CH₄ recovered from the Anaerobic Process:	763.6 (Metric Tons)
Annual operating hours for the primary destruction device:	7234
Destruction efficiency for the primary destruction device:	0.99
Fraction of hours the primary destruction device was operating:	0.824
Is a back-up destruction device present at the facility?	Yes
Annual operating hours for the back-up destruction device:	1526
Destruction efficiency for the back-up destruction device:	0.99
Fraction of hours the back-up destruction device was operating:	0.174

Anaerobic Process Information:

Name or ID:	White Waste Digester
Anaerobic Process:	Anaerobic Sludge Digester
Is biogas generated in the process recovered?	Yes
Number of weeks that the system was operational:	52
Number of hours the biogas collection system was operational:	8784
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?
Does the facility perform an ethanol production processing operation? If yes, which process is used?	No ethanol production processing operations are performed at this facility
How does the facility monitor the CH₄ concentration in the biogas collected for destruction?	Daily averaging of continuous 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 emissions from anaerobic wastewater treatment process:	21.94 (Metric Tons)

Equation II-4 Inputs:

Week	Volumetric Biogas Flow (acf)	MDP?	Biogas CH₄ Concentration (%)	MDP?	Biogas Temperature (°R)	Biogas Pressure (atm)	Biogas Moisture (cfw/cfb)
1				Yes
2				Yes
3				Yes
4				Yes
5
6
7
8
9
10				Yes
11				Yes
12				Yes
13				Yes
14				Yes
15				Yes
16				Yes
17				Yes
18				Yes
19				Yes
20				Yes
21				Yes
22				Yes
23				Yes
24				Yes
25				Yes
26				Yes
27				Yes
28				Yes
29				Yes
30				Yes
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:

R_n: Annual quantity of CH₄ recovered from the Anaerobic Process:	859.9 (Metric Tons)
Annual operating hours for the primary destruction device:	7210
Destruction efficiency for the primary destruction device:	0.99
Fraction of hours the primary destruction device was operating:	0.821
Is a back-up destruction device present at the facility?	Yes
Annual operating hours for the back-up destruction device:	1526
Destruction efficiency for the back-up destruction device:	0.99
Fraction of hours the back-up destruction device was operating:	0.174