GHG Summary Report

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):59,444.3
CO2 equivalent emissions from supplier subparts LL-QQ (metric tons):
Biogenic CO2 emissions from facility subparts C-II, SS, and TT (metric tons):10,709
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:311611
Second Primary NAICS Code:

Parent Company Details:

Parent Company Name:JBA USA HOLDINGS LLC
Address:1770 promontory circle, greeley, CO 80634
Percent Ownership Interest:100

Subpart C: General Stationary Fuel Combustion

Gas Information Details

Gas Name	Carbon Dioxide
Gas Quantity	56,241 (Metric Tons)
Own Result?

Gas Name	Biogenic Carbon dioxide
Gas Quantity	10,709 (Metric Tons)
Own Result?

Gas Name	Methane
Gas Quantity	1.72 (Metric Tons)
Own Result?

Gas Name	Nitrous Oxide
Gas Quantity	0.236 (Metric Tons)
Own Result?

Unit Details:

Unit Name : GP-24352
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name :

Small Unit Aggregation Details:
Use Ivt Indicator: Y
Highest Maximum Rated Heat Input Capacity: 95
Cumulative Maximum Rated Heat Input Capacity: 258.5

Emission Details:
Annual CO₂ mass emissions from sorbent: 0 (Metric Tons)
Annual Biogenic CO2 Emissions: 10709 (metric tons)
Annual Fossil fuel based CO2 Emissions: 56241 (metric tons)

Tier Fuel Details:

Fuel : Natural Gas (Weighted U.S. Average)
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
56241.0 (Metric Tons)	1.06 (Metric Tons)	0.106 (Metric Tons)	26.5 (Metric Tons)	31.6 (Metric Tons)

Fuel : Other Biomass Gases
Tier Name : Tier 2 (Equation C-2a)
Tier Methodology Start Date : 2020-01-01
Tier Methodology End Date : 2020-12-31
Frequency of HHV determinations : Monthly

Tier 2 Monthly HHV Details :

January	February	March	April	May	June	July	August	September	October	November	December
N	N	N	N	N	N	N	N	N	N	N	N

Fuel Emission Details :

Total CO2 emissions	Total CH4 emissions	Total N2O emissions	Total CH4 emissions CO2e	Total N2O emissions CO2e
10709.0 (Metric Tons)	0.66 (Metric Tons)	0.130 (Metric Tons)	16.5 (Metric Tons)	38.6 (Metric Tons)

Subpart II: Industrial Wastewater Treatment

Gas Information Details

Gas Name	Methane
Gas Quantity	123.6 (Metric Tons)
Own Result?

Anaerobic Process Information:

Name or ID:	Anaerobic
Anaerobic Process:	Anaerobic Deep Lagoon
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:	6(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?	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):	0.975
Annual mass of CH₄ generated from anaerobic wastewater treatment process:	3658.89 (Metric Tons)
Annual mass of CH₄ emissions from anaerobic wastewater treatment process:	123.60 (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	65866.1		3.467		0.25		0.8
2	59809.5		5.243		0.25		0.8
3	67191.0		4.428		0.25		0.8
4	64730.5		3.964		0.25		0.8
5	60453.0		3.592		0.25		0.8
6	66396.1		2.490		0.25		0.8
7	58408.9		4.183		0.25		0.8
8	67039.6		3.448		0.25		0.8
9	66244.7		5.676		0.25		0.8
10	64881.9		4.472		0.25		0.8
11	72187.8		5.885		0.25		0.8
12	71884.9		5.096		0.25		0.8
13	73323.4		4.586		0.25		0.8
14	69651.5		5.381		0.25		0.8
15	49853.8		2.526		0.25		0.8
16	53866.4		2.870		0.25		0.8
17	53563.6		3.426		0.25		0.8
18	57916.8		3.568		0.25		0.8
19	57311.1		3.383		0.25		0.8
20	74156.2		3.786		0.25		0.8
21	84149.7		4.499		0.25		0.8
22	65904.0		3.329		0.25		0.8
23	89714.2		3.892		0.25		0.8
24	80477.8		5.191		0.25		0.8
25	73701.9		4.397		0.25		0.8
26	91947.6		5.818		0.25		0.8
27	65487.6		7.385		0.25		0.8
28	70938.6		4.766		0.25		0.8
29	69651.5		4.731		0.25		0.8
30	69159.4		13.748		0.25		0.8
31	77335.9		8.713		0.25		0.8
32	76806.0		6.620		0.25		0.8
33	83127.6		8.550		0.25		0.8
34	78963.7		5.827		0.25		0.8
35	80212.8		5.875		0.25		0.8
36	71468.5		5.258		0.25		0.8
37	58295.3		5.713		0.25		0.8
38	82294.8		6.380		0.25		0.8
39	76768.1		6.022		0.25		0.8
40	78282.3		5.826		0.25		0.8
41	77298.1		5.546		0.25		0.8
42	83619.7		3.650		0.25		0.8
43	94938.1		4.045		0.25		0.8
44	85663.8		2.082		0.25		0.8
45	72225.6		2.273		0.25		0.8
46	69651.5		2.312		0.25		0.8
47	76086.7		2.292		0.25		0.8
48	83657.6		3.990		0.25		0.8
49	80364.3		4.214		0.25		0.8
50	75291.8		4.970		0.25		0.8
51	92742.5		4.337		0.25		0.8
52	79872.2		6.002		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
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23		Yes		Yes
24		Yes		Yes
25		Yes		Yes
26		Yes		Yes
27		Yes		Yes
28		Yes		Yes
29		Yes		Yes
30		Yes		Yes
31		Yes		Yes
32		Yes		Yes
33		Yes		Yes
34		Yes		Yes
35		Yes		Yes
36		Yes		Yes
37		Yes		Yes
38		Yes		Yes
39		Yes		Yes
40		Yes		Yes
41		Yes		Yes
42		Yes		Yes
43		Yes		Yes
44
45
46
47
48
49
50
51
52

Equation II-6 Inputs:

R_n: Annual quantity of CH₄ recovered from the Anaerobic Process:	3467.86 (Metric Tons)
Annual operating hours for the primary destruction device:	1884
Destruction efficiency for the primary destruction device:	0.99
Fraction of hours the primary destruction device was operating:	0.215
Is a back-up destruction device present at the facility?	Yes
Annual operating hours for the back-up destruction device:	6900
Destruction efficiency for the back-up destruction device:	0.99
Fraction of hours the back-up destruction device was operating:	0.786