Aluminum Production

Subpart F, Greenhouse Gas Reporting Program

oEFft

United Stales
ErrvircnnwiBl Protection
Agency

Under the Mandator)' Reporting of Greenhouse Gases (GHGs) rule, owners or operators of aluminum
production facilities (as defined below) must report emissions from processes that produce primary
aluminum and any other source categories located at the facility for which methods are defined in the
rule. Owners and operators are required to collect emission data; calculate GHG emissions; and follow
the specified procedures for quality assurance, missing data, recordkeeping, and reporting per the
requirements of 40 CFR Part 98 Subpart F - Aluminum Production.

How Is This Source Category Defined?

The aluminum production source category consists of facilities that manufacture primary aluminum using
the Hall-Heroult manufacturing process. The primary aluminum manufacturing process consists of the
following operations:

•	Electrolysis in prebake and Soderberg cells

•	Anode baking for prebake cells

This source category does not include experimental cells or research and development process units.

What Greenhouse Gases Must Be Reported?

Each aluminum production facility must report:

•	Perfluoromethane (CF4) and perfluoroethane (C2F6) emissions from anode effects in all prebake
and Soderberg electrolysis cells combined.

•	Carbon dioxide (CO2) emissions from anode consumption during electrolysis in all prebake and
Soderberg cells.

•	All CO2 emissions from onsite anode baking.

In addition, each facility must report GHG emissions for other source categories for which calculation
methods are provided in the rule. For example, facilities must report CO2, nitrous oxide (N2O), and
methane (CFU) emissions from each stationary combustion unit on site by following the requirements of
40 CFR part 98, subpart C (General Stationary Fuel Combustion Sources). Please refer to the relevant
information sheet for a summary of the rule requirements for calculating and reporting emissions from
any other source categories at the facility.

How Must Greenhouse Gas Emissions Be Calculated?

Facilities must calculate GHG process emissions using the following methods:

•	CF4 from anode effects. Calculate annual CF4 emissions based on the frequency and duration
of anode effects in the aluminum electrolytic reduction process for each prebake and Soderberg
electrolysis cell using the following parameters:

o Anode effect minutes (AEM) per cell-day calculated monthly,
o Aluminum metal production calculated monthly.

o A slope coefficient relating CF4 emissions to anode effect minutes per cell-day
and aluminum production. The slope coefficient is specific to each smelter.

Smelters that have never measured the slope coefficient must measure it within
one year of rule publication. Smelters that have measured it must re-measure it

February 2018

Page 1

40 CFR 98, Subpart F


-------
within three years of rule publication. Thereafter, all smelters must measure it
at least once every 10 years, or whenever there is a major technological or
process change. The slope coefficient must be measured in accordance with the
protocol specified in the rule. Under certain conditions, high-efficiency smelters
may use a default slope coefficient from Table F-l in the rule.

•	C2F6 from anode effects. Estimate annual C2F6 emissions from anode effects from each
prebake and Soderberg electolysis cell using the estimated CF4 emissions and the mass ratio of
C2F6 to CF4 emissions, as determined during the same test during which the slope coefficient is
determined.

•	Process CO2 emissions. Reporters can elect to calculate and report process CO2 emissions from
anode consumption during electrolysis and from anode baking by using one of two methods:

o Installing and operating a continuous emission monitoring system (CEMS) and following the

Tier 4 methodology (in 40 CFR part 98, subpart C).
o Using the calculation procedures specified below.

•	CO2 emissions from anode consumption in prebake cells. Estimate annual CO2 emissions at
the facility level using a mass balance equation based on measurements of the following
parameters:

o Net prebaked anode consumption rate per metric ton of aluminum metal produced,
o Ash and sulfur contents of the anodes.

o Total mass of aluminum metal produced per year for all prebake cells.

•	CO2 emissions from Soderberg cells. Estimate CO2 emissions from paste consumption in
Soderberg cells using a mass balance equation at the facility level based on the following
parameters:

o Paste consumption rate per metric ton of aluminum metal produced and the annual mass of

aluminum metal produced for all Soderberg cells,
o Emissions of cyclohexane-soluble matter per metric ton of aluminum produced,
o Binder content of the anode paste.

o Sulfur, ash, and hydrogen contents of the coal tar pitch used as the binder in the anode paste,
o Sulfur and ash contents of the calcined coke used in the anode paste,
o Carbon in the skimmed dust from the cell, per metric ton of aluminum produced.

•	CO2 emissions from anode baking of prebake cells. Estimate CO2 emissions at the facility
level separately from pitch volatiles and from bake furnace packing material.

o To estimate CO2 emissions from the pitch volatiles, use a mass balance equation based on the
following parameters:

•	Initial weight of the green anodes.

•	Mass of hydrogen in the green anodes.

•	Mass of the baked anodes.

•	Mass of waste tar collected.

o To estimate CO2 emissions from bake furnace packing material, use a mass balance equation
based on the following parameters:

•	Packing coke consumption rate per ton of baked anode production

•	Sulfur and ash contents of the packing coke.

Measure the smelter-specific values used to estimate CO2 emissions from anode and paste consumption
(e.g., sulfur, ash, and hydrogen contents), or use default values listed in the rule.

February 2018

Page 2

40 CFR 98, Subpart F


-------
If process CO2 emissions from anode consumption during electrolysis or anode baking are emitted
through the same stack as a combustion unit or process equipment that uses a CEMS and follows the Tier
4 methodology in the rule to report CO2 emissions, then the CEMS must be used to measure and report
combined CO2 emissions from that stack, instead of using the calculation procedures specified above.

A checklist for data that must be monitored is available at: https://www .epa.gov/ghgrcporting/subpart-f-
checklist.

What Information Must Be Reported?

In addition to the information required by the General Provisions at 40 CFR 98.3(c) each aluminum
production facility must report the following information at the facility level:

•	Type of smelter technology used.

•	The following PFC-specific information on an annual basis:

o CF4 and C2F6 emissions from anode effects in all prebake and Soderberg electrolysis cells
combined.

o Anode effect minutes per cell-day, anode effect frequency, anode effect duration, if

estimating CF4 emissions from anode effect duration,
o Anode effect overvoltage factor, potline overvoltage, and current efficiency, if estimating CF4
from overvoltage.

o Smelter-specific slope coefficients (or overvoltage emission factors) and the last date when
the smelter-specific-slope coefficients (or overvoltage emission factors) were measured, if
estimating CF4 emissions from overvoltage.

•	Method used to measure the frequency and duration of anode effects (or overvoltage).

•	The following CO2 -specific information for prebake cells on an annual basis:
o Anode consumption if using the method is 98.63(g).

o CO2 emissions from the smelter.

•	The following CO2 -specific information for Soderberg cells on an annual basis:
o Paste consumption if using the method in 98.63(g).

o CO2 emissions from the smelter.

•	Smelter-specific inputs to the CO2 process equations (e.g., levels of sulfur and ash) that were
used in the calculation.

Facilities must enter required data into the electronic Greenhouse Gas Reporting Tool (e-GGRT) to be
reported in the annual report, and must also enter into e-GGRT" s Inputs Verifier Tool (IVT) the inputs to
emission equations for which reporting is not required. IVT uses these entered data to calculate the
equation results.

When and How Must Reports Be Submitted?

Annual reports must be submitted by March 31 of each year, unless the 31st is a Saturday, Sunday, or
federal holiday, in which case the reports are due on the next business day. Annual reports must be
submitted electronically using e-GGRT. the GHGRP's online reporting system. Additional information
on setting up user accounts, registering a facility and submitting annual reports is available at
https ://ccdsupport. com/ confluence/.

February 2018

Page 3

40 CFR 98, Subpart F


-------
When Can a Facility Stop Reporting?

There are several scenarios under which a facility may discontinue reporting. These scenarios are
summarized in the Subpart A Information Sheet as well as in an FAQ.

For More Information

For additional information on Subpart F, visit the Subpart F Resources webpage. For additional
information on the Greenhouse Gas Reporting Program, visit the Greenhouse Gas Reporting Program
Website, which includes information sheets on other rule subparts, data previously reported to the
Greenhouse Gas Reporting Program, training materials, and links to frequently asked questions.

This document is provided solely for informational purposes. It does not provide legal advice, have
legally binding effect, or expressly or implicitly create, expand, or limit any legal rights, obligations,
responsibilities, expectations, or benefits in regard to any person. The series of information sheets is
intended to assist reporting facilities/owners in understanding key provisions of the Greenhouse Gas
Reporting Program.

February 2018

Page 4

40 CFR 98, Subpart F


-------