GHG Summary Report

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):443,548.2
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:324110
Second Primary NAICS Code:

Parent Company Details:

Parent Company Name:CHEVRON CORP
Address:6001 Bollinger Canyon Rd, San Ramon, CA 94583
Percent Ownership Interest:100

Subpart C: General Stationary Fuel Combustion

Gas Information Details

Gas Name	Carbon Dioxide
Gas Quantity	349,329.7 (Metric Tons)
Own Result?

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

Gas Name	Methane
Gas Quantity	20.57 (Metric Tons)
Own Result?

Gas Name	Nitrous Oxide
Gas Quantity	4.097 (Metric Tons)
Own Result?

Unit Details:

Unit Name : No. 7 NG
Unit Type : OB (Boiler, other)
Unit Description :

Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity: 225 (mmBtu/hr)

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

Tier Fuel Details:

Fuel : Natural Gas (Weighted U.S. Average)
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 : Daily

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
183.2 (Metric Tons)	0.00 (Metric Tons)	0.000 (Metric Tons)	0.1 (Metric Tons)	0.1 (Metric Tons)

Unit Name : Alkyl Polymer F3617
Unit Type : PRH (Process Heater)
Unit Description :

Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity: 2.6 (mmBtu/hr)

Emission Details:
Annual Biogenic CO2 Emissions: 0 (metric tons)

Tier Fuel Details:

Fuel : Residual Fuel Oil No. 6
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
1293.0 (Metric Tons)	0.05 (Metric Tons)	0.010 (Metric Tons)	1.3 (Metric Tons)	3.1 (Metric Tons)

Unit Name : CP-1 Total RFG Flow
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name :

Common Pipe Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity: 172
Cumulative Maximum Rated Heat Input Capacity: 1440.5

Emission Details:
Annual Biogenic CO2 Emissions: 0 (metric tons)
Annual Fossil fuel based CO2 Emissions: 340621.4 (metric tons)

Tier Fuel Details:

Fuel : Fuel Gas
Tier Name : Tier 3 (Equation C-5, gaseous fuel)
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
339415.4 (Metric Tons)	20.35 (Metric Tons)	4.070 (Metric Tons)	508.7 (Metric Tons)	1212.7 (Metric Tons)

Carbon Content Substitute Data Information :
Total number of valid carbon content determinations : 12
Total number of carbon content substitute data values : 0
Frequency of carbon content determinations : Monthly
Total number of operating hours in the reporting year for which missing data substitution was used for fuel usage : 0

Molecular Weight Information :
Total number of valid molecular weight determinations : 12
Total number of molecular weight substitute data values : 0
Frequency of molecular weight determinations : Monthly
Molar Volume Constant (MVC) used : 836.6 (scf/kg-mole)

Unit Name : Nat Gas to Disulfide Settler
Unit Type : PRH (Process Heater)
Unit Description :

Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity: 105.4 (mmBtu/hr)

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

Tier Fuel 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
322.2 (Metric Tons)	0.01 (Metric Tons)	0.001 (Metric Tons)	0.2 (Metric Tons)	0.2 (Metric Tons)

Unit Name : Nat Gas to SRU Main Burner
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name : Nat Gas to SRU Main Burner

Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity: 4.5 (mmBtu/hr)

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

Tier Fuel 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
526.1 (Metric Tons)	0.01 (Metric Tons)	0.001 (Metric Tons)	0.2 (Metric Tons)	0.3 (Metric Tons)

Unit Name : CP-2 NG to Ref Compressors
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name :

Common Pipe Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity: 16
Cumulative Maximum Rated Heat Input Capacity: 48

Emission Details:
Annual Biogenic CO2 Emissions: 0 (metric tons)
Annual Fossil fuel based CO2 Emissions: 0 (metric tons)

Tier Fuel 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
4337.9 (Metric Tons)	0.08 (Metric Tons)	0.008 (Metric Tons)	2.0 (Metric Tons)	2.4 (Metric Tons)

Unit Name : NG to RTO
Unit Type : RTO (Regenerative thermal oxidizer)
Unit Description :

Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity: 2.5 (mmBtu/hr)

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

Tier Fuel 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
297.0 (Metric Tons)	0.01 (Metric Tons)	0.001 (Metric Tons)	0.1 (Metric Tons)	0.2 (Metric Tons)

Unit Name : Octane Engines for Lab
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name : Octane Engines for Lab

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

Emission Details:
Annual Biogenic CO2 Emissions: 0 (metric tons)

Tier Fuel Details:

Fuel : Motor Gasoline
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
10.9 (Metric Tons)	0.00 (Metric Tons)	0.000 (Metric Tons)	0.0 (Metric Tons)	0.0 (Metric Tons)

Unit Name : Nat Gas to SRU Reheater
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name : Nat Gas to SRU Reheater

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

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

Tier Fuel 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
409.7 (Metric Tons)	0.01 (Metric Tons)	0.001 (Metric Tons)	0.2 (Metric Tons)	0.2 (Metric Tons)

Unit Name : No. 5 NG
Unit Type : OB (Boiler, other)
Unit Description :

Individual Unit Details:
Use Ivt Indicator: Y
Maximum Rated Heat Input Capacity: 172 (mmBtu/hr)

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

Tier Fuel 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
307.1 (Metric Tons)	0.01 (Metric Tons)	0.001 (Metric Tons)	0.1 (Metric Tons)	0.2 (Metric Tons)

Unit Name : Nat Gas to F68250
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name : Nat Gas to F68250

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

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

Tier Fuel 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
1722.5 (Metric Tons)	0.03 (Metric Tons)	0.003 (Metric Tons)	0.8 (Metric Tons)	1 (Metric Tons)

Unit Name : Nat Gas to F68220
Unit Type : OCS (Other combustion source)
Unit Description :
Other Unit Name : Nat Gas to F68220

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

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

Tier Fuel 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
504.7 (Metric Tons)	0.01 (Metric Tons)	0.001 (Metric Tons)	0.2 (Metric Tons)	0.3 (Metric Tons)

Subpart Y: Petroleum Refineries

Gas Information Details

Gas Name	Carbon Dioxide
Gas Quantity	85,897.3 (Metric Tons)
Own Result?

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

Gas Name	Methane
Gas Quantity	79.9 (Metric Tons)
Own Result?

Gas Name	Nitrous Oxide
Gas Quantity	0.568 (Metric Tons)
Own Result?

Flare Gas Details

Name or ID: Coker Flare
Description:
Type: Flare
Is the flare serviced by a flare gas recovery system ? Y
Type of flare: Steam assisted
Other Flare type:

Flare service type: General facility flare
Other Flare service type:

Basis for the fraction of carbon in the flare gas contributed by methane value: Engineering calculations
Other Basis for the fraction of carbon in the flare gas contributed by methane value:

Emissions Details

CO2 Emissions Calculation Method: 98.253(b)(1)(iii) - Equation Y-3 Start-up, Shutdown, Malfunction

Name	Value	Own Result?
CO2Emissions	2781.1 (Metric Tons)	N

Name	Value	Own Result?
CH4Emissions	8.39 (Metric Tons)	N

Name	Value	Own Result?
N2OEmissions	0.028 (Metric Tons)	N

Y3 Equation Details

Total number of start-up, shutdown, or malfunction (SSM) events exceeding 500,000 scf/day: 4

Name or ID: FCC Flare
Description:
Type: Flare
Is the flare serviced by a flare gas recovery system ? Y
Type of flare: Steam assisted
Other Flare type:

Flare service type: General facility flare
Other Flare service type:

Basis for the fraction of carbon in the flare gas contributed by methane value: Engineering calculations
Other Basis for the fraction of carbon in the flare gas contributed by methane value:

Emissions Details

CO2 Emissions Calculation Method: 98.253(b)(1)(iii) - Equation Y-3 Start-up, Shutdown, Malfunction

Name	Value	Own Result?
CO2Emissions	2488.6 (Metric Tons)	N

Name	Value	Own Result?
CH4Emissions	7.51 (Metric Tons)	N

Name	Value	Own Result?
N2OEmissions	0.025 (Metric Tons)	N

Y3 Equation Details

Total number of start-up, shutdown, or malfunction (SSM) events exceeding 500,000 scf/day: 4

Name or ID: AIR Flare
Description:
Type: Flare
Is the flare serviced by a flare gas recovery system ? N
Type of flare: Steam assisted
Other Flare type:

Flare service type: General facility flare
Other Flare service type:

Basis for the fraction of carbon in the flare gas contributed by methane value: Engineering calculations
Other Basis for the fraction of carbon in the flare gas contributed by methane value:

Emissions Details

CO2 Emissions Calculation Method: 98.253(b)(1)(iii) - Equation Y-3 Start-up, Shutdown, Malfunction

Name	Value	Own Result?
CO2Emissions	12817.6 (Metric Tons)	N

Name	Value	Own Result?
CH4Emissions	38.69 (Metric Tons)	N

Name	Value	Own Result?
N2OEmissions	0.128 (Metric Tons)	N

Y3 Equation Details

Total number of start-up, shutdown, or malfunction (SSM) events exceeding 500,000 scf/day: 0

Catalytic Cracking and Reforming Units

FCCU (Description: Type: Fluid Catalytic Cracking Unit)

Name	Value	Own Result?
CO2Emissions	66121.1 (Metric Tons)

Method used to calculate CO2 emissions:Equation Y-6 and Y-7a - 98.253(c)(2)

Name	Value	Own Result?
CH4Emissions	1.94 (Metric Tons)

Method used to calculate CH4 emissions:Equation Y-9 with a default emission factor

Name	Value	Own Result?
N2OEmissions	0.387 (Metric Tons)

Method used to calculate N2O emissions:Equation Y-10 with a default emission factor

Name	Value	Substitute Indicator	Times Substituted
AnnualAverageExhaustGasFlowRate	()

Manufacturer's method for annual average volumetric flow rate of exhaust gas:

Name	Value	Substitute Indicator	Times Substituted
PercentCO2	()		523

Manufacturer's method for annual average percent CO2 in exhaust gas stream:Exhaust CO2 Analyzer

Name	Value	Substitute Indicator	Times Substituted
PercentCO	()		76

Manufacturer's method for annual average percent CO in exhaust gas stream:CEMS Analyzer

Name	Value	Substitute Indicator	Times Substituted
PercentO2ExhaustGas	()		76

Manufacturer's method for annual average percent O2 in exhaust gas stream:CEMS Analyzer

Name	Value	Substitute Indicator	Times Substituted
PercentO2Inlet	()

Reformer Regen (Description: Type: Catalytic Reforming Unit)

Name	Value	Own Result?
CO2Emissions	28.1 (Metric Tons)

Method used to calculate CO2 emissions:Equation Y-11 - 98.253(e)(3)

Name	Value	Own Result?
CH4Emissions	0.00 (Metric Tons)

Method used to calculate CH4 emissions:Equation Y-9 with a default emission factor

Name	Value	Own Result?
N2OEmissions	0.000 (Metric Tons)

Method used to calculate N2O emissions:Equation Y-10 with a default emission factor
Total number of regeneration cycles or measurement periods:
Average coke burn-off quantity per cycle or measurement period: (kg coke/cycle or kg coke/measurement period)

Sulfur Recovery Details

Sour Gas Details

is Sour Gas Stream Sent Off Site Indicator :N
Annual Volumetric Flow Method :
Average Mole Fraction of Carbon in Sour Gas Method :

Sulfur Recovery Unit Details

Unit Name :SRU1
Unit Type :Sulfur Recovery Plant
Unit Description :

Sulfur Recovery Plant Description :Claus
Other Sulfur Recovery Plant Description :

Name	Value	Own Result?
CalculatedCO2Emissions	712.7 (Metric Tons)

CO2 Emission Method :Equation Y-12

Process Vent Method Details

Cumulative Annual Volume Flow Discharged Method :
Other Annual Volume Metric Flow Method List :
Cumulative Venting Time :

is Recycled Tailgas Included Indicator :Y

Name	Value	Substitute Indicator	Times Substituted
AnnualVolumetricFlow	()		0

Annual Volumetric Flow Method :Metered
Annual Average Mole Fraction of Carbon Method in the Sour Gas Method :Other (specify)
Number of hours missing data procedures were used for annual average mole fraction of carbon method in the sour gas :0

Recycle Tail Gas Details

Tail Gas Recycled Flow Rate Carbon Content Included :Y
Tail Gas Correction for CO2 Used :Y

Name	Value	Substitute Indicator	Times Substituted
RecycleTailGasVolume	()		0

Recycled Tail Gas Method Details
Recycled Tail Gas Method :Engineering estimates
Other Recycled Tail Gas Method :

Name	Value	Substitute Indicator	Times Substituted
AnnualAverageMoleFractionofCarbon	()		0

Annual Average Mole Fraction of Carbon Method :Engineering calculations
Other Annual Average Mole Fraction of Carbon Method :
Basis for Correction :Default correction factor (95%)
Value of Correction : ()
Approach Used for Correction :
Other Approach Used for Correction :

Sulfur Recovery Unit Details

Unit Name :SRU2
Unit Type :Sulfur Recovery Plant
Unit Description :

Sulfur Recovery Plant Description :Claus
Other Sulfur Recovery Plant Description :

Name	Value	Own Result?
CalculatedCO2Emissions	948.1 (Metric Tons)

CO2 Emission Method :Equation Y-12

Process Vent Method Details

Cumulative Annual Volume Flow Discharged Method :
Other Annual Volume Metric Flow Method List :
Cumulative Venting Time :

is Recycled Tailgas Included Indicator :Y

Name	Value	Substitute Indicator	Times Substituted
AnnualVolumetricFlow	()		0

Tail Gas Recycled Flow Rate Carbon Content Included :Y
Tail Gas Correction for CO2 Used :Y

Name	Value	Substitute Indicator	Times Substituted
RecycleTailGasVolume	()		0

Recycled Tail Gas Method Details
Recycled Tail Gas Method :Engineering estimates
Other Recycled Tail Gas Method :

Name	Value	Substitute Indicator	Times Substituted
AnnualAverageMoleFractionofCarbon	()		0

Delayed Coking Details

Unit Name: Coker
Unit Type: Delayed Coking Unit
Unit Description:

Total number of associated delayed coking vessels (or coke drums): 2
Basis for the typical dry mass of coke at the end of the coking cycle: calculated using Equation Y-18a
Method used to estimate the average temperature of the coke bed, T_init: pressure correlation and Equation Y-18d
Type of emission factor was used in Equation Y-18f: default factor

Name	Value	Own Result?
CH4Emissions	8.25 (Metric Tons)	N

Uncontrolled Blowdown Systems

Methane emissions: ()
Methane emissions calculation method:No uncontrolled blowdown systems

Equipment Leak Details

Name	Value	Own Result?
TotalCH4Emissions	13.34 (Metric Tons)

Method to Calculate Equipment Leak Emission:98.253(l)(2) method

Storage Tank Details

Name	Value	Own Result?
StabilizedCrudeTotalCH4Emissions	1.78 (Metric Tons)

Stored Liquids Other Than Unstabilized Crude Oil Calculation Method:Equation Y-22
is Stored Liquids Other Than Unstabilized Crude Oil Received Stored Indicator:
UnStabilized Crude Calculation Method:
is UnStablized Crude Received Stored Indicator:
UnStabilized Crude Basis for Mole Fraction:
Other UnStabilized Crude Basis for Mole Fraction:

Subpart TT: Industrial Waste Landfills

Gas Information Details

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

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

Gas Name	Methane
Gas Quantity	176.77 (Metric Tons)
Own Result?

Gas Name	Nitrous Oxide
Gas Quantity	0 (Metric Tons)
Own Result?

Landfill Details:

Was the landfill open or closed

Closed

First year the landfill accepted waste

1960

If the landfill is closed, the last year that the landfill received waste

1998

Landfill Capacity

322892 (Metric Tons)

Does the landfill have a landfill gas collection system

Passive vents and/or flares are present (vents or flares that are not considered part of the gas collection system)

An indication of whether leachate recirculation was used during the reporting year

The typical frequency of use of leachate recirculation over the past ten (10) years

Not used for the past ten (10) years

Each type of cover material used and Landfill surface area containing waste

Clay cover	60705 (Square Meters)
Other soil mixture	60705 (Square Meters)
Sand cover	60705 (Square Meters)

Number of waste streams

Annual modeled methane generation TT1

196.41 (Metric Tons)

Annual modeled methane generation TT1 user overrided value

Equation TT-1 Details:

The fraction of CH4 in landfill gas (F), is it based on a measured value or default value	Default
Fraction by volume of CH4 in landfill gas	()
An MCF value other than the default of 1 was used	N

Waste Stream For Method3 Details:

Capacity of the landfill used (or the total quantity of waste-in-place) at the end of the "YrData" from design drawings or engineering estimates	322892 (Metric Tons)
Are waste quantity data available?	waste quantity data are not available for any years
The year in which the landfill last received waste(YrData)	1998
Do you know the year when the landfill opened?	Yes
The year the landfill first received waste from company records, or 1960 (whichever is more recent)	1960

Methane Generation and Emissions for Landfills without LFG Collection Systems

Methane Oxidation Fraction

Methane Oxidation Fraction TT-6

0.10

Gas Collection Systems details

Methane Generation Equation TT6

176.77 (Metric Tons)

Waste Stream Summary:

Stream Identification and Method(s) used to determine historical waste stream quantity for LWMA Wastes

Stream Name

LWMA Wastes

Stream Description

The Landfill Waste Management Area (LWMA) at the Salt Lake Refinery contains waste under a RCRA Post Closure Permit.

Type(s) Of Waste Present In The Waste Stream

construction and demolition

industrial sludge

other industrial solid waste

Range of years for which both disposal and production data were used in Equation TT-2 to calculate the average waste disposal factor for the landfill

First year this waste stream was placed in the landfill

1960

Last year this waste stream was placed in the landfill

1998

Method(s) used to determine historical waste stream quantity

Reporting Year	Method #1	Method #2	Method #3	Method #4	Decayrate	Waste disposed quantity (UOM)	Waste stream DOC value (UOM)	Is defaulted value from table TT1	Is value measured using 60 day anaerobic biodegradation test	Is based on total volatile solids measurements
1960	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1961	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1962	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1963	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1964	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1965	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1966	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1967	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1968	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1969	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1970	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1971	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1972	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1973	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1974	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1975	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1976	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1977	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1978	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1979	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1980	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1981	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1982	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1983	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1984	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1985	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1986	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1987	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1988	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1989	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1990	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1991	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1992	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1993	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1994	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1995	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1996	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1997	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N
1998	N	N	Y	N	0.02	8279 (Metric Tons)	0.2 (Metric Tons)	Y	N	N

Method #1: Used one of the waste quantity measurement methods specified in 98.463(a)(2)(i): direct mass measurements, direct volume measurements multiplied by waste stream density, mass balance procedures (difference between the mass of process inputs and the mass of process outputs), or the number of loads multiplied by the mass of waste per load based on the working capacity of the vehicle or container.
Method #2: Calculated the average waste disposal rate per Equation TT-2 and calculated the waste disposal quantities for historic years in which direct waste disposal measurements are not available using historical production data per Equation TT-3.
Method #3: Calculated an average annual bulk waste disposal quantity for historic years when waste quantity data as determined by other methods are available consecutively for the most recent disposal years (Equation TT-4a).
Method #4: Calculated an average annual bulk waste disposal quantity for historic years when waste quantity data as determined by other methods are available for sporadic (non-consecutive) years (Equation TT-4b).