GHG Summary Report

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):66,865.8
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: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:311613

Parent Company Details:

Parent Company Name:TYSON FOODS INC
Address:2200 Don Tyson Parkway, Springdale, AR 72762
Percent Ownership Interest:100

Subpart C: General Stationary Fuel Combustion

Gas Information Details

Gas Name	Carbon Dioxide
Gas Quantity	20,317 (Metric Tons)
Own Result?

Gas Name	Biogenic Carbon dioxide
Gas Quantity	0 (Metric Tons)
Own Result?

Gas Name	Methane
Gas Quantity	0.38 (Metric Tons)
Own Result?

Gas Name	Nitrous Oxide
Gas Quantity	0.038 (Metric Tons)
Own Result?

Unit Details:

Unit Name : Generators
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name : G (generator)

Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity: 0.5 (mmBtu/hr)

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

Tier Fuel Details:

Fuel : Distillate Fuel Oil No. 2
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
0.5 (Metric Tons)	0.00 (Metric Tons)	0.000 (Metric Tons)	0 (Metric Tons)	0 (Metric Tons)

Unit Name : GP-Gas Fired Equipment
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: 31.4
Cumulative Maximum Rated Heat Input Capacity: 127.69

Emission Details:
Annual CO₂ mass emissions from sorbent: 0 (Metric Tons)
Annual Biogenic CO2 Emissions: 0 (metric tons)
Annual Fossil fuel based CO2 Emissions: 20316 (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
20316.5 (Metric Tons)	0.38 (Metric Tons)	0.038 (Metric Tons)	9.6 (Metric Tons)	11.4 (Metric Tons)

Subpart II: Industrial Wastewater Treatment

Gas Information Details

Gas Name	Methane
Gas Quantity	1,861.12 (Metric Tons)
Own Result?

Anaerobic Process Information:

Name or ID:	Anarobic Lagoons
Anaerobic Process:	Anaerobic Deep Lagoon
Is biogas generated in the process recovered?	No
Number of weeks that the system was operational:	52
Document or diagram that pertains to this process:
Average depth of the lagoon:	6.1(Meters)
Does the facility measure COD or BOD₅ concentration of the wastewater entering the anaerobic process?	BOD
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?
Is the biogas temperature incorporated into the monitoring equipment internal calculations?
Is the biogas pressure incorporated into the monitoring equipment internal calculations?
Is the biogas moisture content incorporated into the monitoring equipment internal calculations?
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?
CH₄ collection efficiency (based on cover type):
Annual mass of CH₄ generated from anaerobic wastewater treatment process:	1861.12 (Metric Tons)
Annual mass of CH₄ emissions from anaerobic wastewater treatment process:	1861.12 (Metric Tons)

Equation II-2 Inputs:

Week	Flow_w (m³)	MDP?	BOD_w (kg/m³)	MDP?	B₀ (kg CH₄/kg COD)	ALT?	MCF	ALT?
1	33652		2.181		0.60		0.8
2	33917		4.074		0.60		0.8
3	30738		2.881		0.60		0.8
4	34447		2.643		0.60		0.8
5	31003		2.650		0.60		0.8
6	30208		2.810		0.60		0.8
7	28618		2.950		0.60		0.8
8	32857		3.161		0.60		0.8
9	30738		4.086		0.60		0.8
10	30208		2.493		0.60		0.8
11	30208		4.051		0.60		0.8
12	31797		2.884		0.60		0.8
13	34447		3.240		0.60		0.8
14	31797		2.138		0.60		0.8
15	12189		1.037		0.60		0.8
16	13249		0.167		0.60		0.8
17	25703		1.168		0.60		0.8
18	32857		1.747		0.60		0.8
19	33387		1.847		0.60		0.8
20	34182		2.591		0.60		0.8
21	33652		4.236		0.60		0.8
22	29943		2.8		0.60		0.8
23	35242		2.62		0.60		0.8
24	32327		2.75		0.60		0.8
25	34712		3.013		0.60		0.8
26	35507		3.116		0.60		0.8
27	21198		2.407		0.60		0.8
28	32062		2.03		0.60		0.8
29	35772		1.919		0.60		0.8
30	32857		2.161		0.60		0.8
31	35242		2.28		0.60		0.8
32	28883		1.229		0.60		0.8
33	29148		2.024		0.60		0.8
34	30473		1.296		0.60		0.8
35	31003		1.496		0.60		0.8
36	28353		3.779		0.60		0.8
37	28883		2.106		0.60		0.8
38	29943		2.346		0.60		0.8
39	30473		1.496		0.60		0.8
40	30473		10.27		0.60		0.8
41	30738		1.473		0.60		0.8
42	32592		1.394		0.60		0.8
43	31532		1.923		0.60		0.8
44	34447		2.334		0.60		0.8
45	33917		1.521		0.60		0.8
46	33387		1.573		0.60		0.8
47	31797		1.337		0.60		0.8
48	30208		1.201		0.60		0.8
49	38422		0.892		0.60		0.8
50	36302		1.173		0.60		0.8
51	27028		1.9		0.60		0.8
52	18549		0.259		0.60		0.8