Technical Support Document for the
Lead Production Sector: Proposed Rule for
Mandatory Reporting of Greenhouse Gases

Office of Air and Radiation
U.S. Environmental Protection Agency

January 22, 2009


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Technical Support Document for the Lead Production Sector: Proposed Rule for Mandatory Reporting of

Greenhouse Gases

CONTENTS

1.	Industry Description	1

2.	Total Emissions	1

2.1	Process Emissions	1

2.2	Combustion Emissions	2

3.	Review of Existing Programs and Methodologies	2

3.1	2006 IPCC Guidelines	2

3.2	U.S. EPA's Inventory of U.S. Greenhouse Gas Emissions and Sinks	4

3.3	Australian National Government's Greenhouse and Energy Reporting Program... 4

3.4	Canadian Mandatory Greenhouse Gas Reporting Program	4

4.	Options for Reporting Threshold	5

4.1	Options Considered	5

4.2	Emissions and Facilities Covered Per Option	5

4.2.1	Combustion Emissions	5

4.2.2	Process Emissions	6

4.2.3 Emissions Thresholds	8

5.	Options for Monitoring Methods	8

5.1	Option 1: Simplified Emission Calculation	9

5.2	Option 2: Facility-Specific Carbon Balance Calculation	9

5.3	Option 3: Facility-Specific Emission Factor Using Stack Test Data	9

5.4	Option 4: Direct Measurement Using CEMS	10

6.	Procedures for Estimating Missing Data	11

6.1	Procedures for Option 1: Simplified Emission Calculation	11

6.2	Procedures for Option 2: Facility-Specific Carbon Balance Calculation	11

6.3	Procedures for Option 3: Facility-Specific Emission Factor Using Stack Test Data
	11

7.4	Procedures for Option 4: Direct Measurement Using CEMS	12

7.	QA/QC Requirements	12

7.1	Combustion Emissions	12

7.2	Process Emissions	12

7.2.1	Equipment Maintenance	12

7.2.2	Stack Test Data	13

7.2.3	CEMS	13

7.3	Data Management	13

8.	Types of Emission Information to be Reported	14

8.1 Additional Data to be Retained Onsite	14

9.	References	15

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Technical Support Document for the Lead Production Sector: Proposed Rule for Mandatory Reporting of

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1.	Industry Description

Lead is a metal used to produce various products such as batteries, ammunition, construction
materials, electrical components and accessories, and vehicle parts. Approximately, 89 percent of
lead is used to produce batteries. The lead production source category is defined to consist of
primary lead smelters and secondary lead smelters. A primary lead smelter produces lead metal
from lead sulfide ore concentrates through the use of pyrometallurgical processes. A secondary
lead smelter produces lead and lead alloys from lead-bearing scrap metal.

For the primary lead smelting process used in the United States, lead sulfide ore concentrate is
first fed to a sintering process to burn sulfur from the lead ore. The sinter is smelted with a
carbonaceous reducing agent in a blast furnace to produce molten lead bullion. From the furnace,
the bullion is transferred to dross kettle furnaces to remove copper and other metal impurities.
Following further refining steps to obtain high purity lead metal, the lead is cast into ingots or
used to produce alloy products.

The feed materials predominately processed at U.S. secondary lead smelters are used lead-acid
automobile batteries. These facilities can also process other lead-bearing scrap materials
including wheel balance weights, pipe, solder, drosses, and lead sheathing. These incoming lead
scrap materials are first pre-treated to partially remove metal and nonmetal contaminants. The
resulting lead scrap is smelted (U.S. secondary lead smelters typically use either a blast furnace
or reverberatory furnace). The molten lead from the smelting furnace is refined in kettle
furnaces, and then casted into ingots or used to produce lead alloy products

Most of the lead produced in the United States is from secondary lead production. In 2006, U.S.
secondary lead production totaled 1,161,000 metric tons, primarily from the recycling of lead-
acid batteries (USGS 2007). There are approximately 26 U.S. secondary lead smelters with
annual lead production capacities ranging from 130,000 metric tons to less than 1,000 metric
tons (USGS 2007). An additional 153,000 metric tons of lead was produced in 2006 by the sole
operating U.S. primary lead smelter.

2.	Total Emissions

Lead production results in both combustion and process-related greenhouse gas (GHG)
emissions (discussed further in Sections 4 and 5). Table 5 in section 5.2 presents the estimated
GHG emissions from U.S. facilities in 2006. Total nationwide GHG emissions from lead
production in the United States were estimated to be approximately 0.9 million metric tons CO2
equivalent (MMTCC^e) in 2006. These emissions include both on-site stationary combustion
emissions (CO2, CH4, and N2O) and process-related emissions (CO2). The majority of these
emissions were from the combustion of natural gas and other carbon-based fuels burned to
produce heat for the lead smelting processes. Combustion GHG emissions were estimated to be
0.6 MMTC02e emissions (69 percent of the total emissions). The remaining estimated 0.3
MMTC02e were process-related GHG emissions (31 percent of the total emissions).

2.1 Process Emissions

Process-related CO2 emissions are released from the lead smelting process due to the addition of
a carbonaceous reducing agent such as metallurgical coke or coal to the smelting furnace. The
reduction of lead oxide to lead metal during the process produces the CO2 emissions. At the

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Technical Support Document for the Lead Production Sector: Proposed Rule for Mandatory Reporting of

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primary lead smelter, sinter roast which consists of lead oxides and other metallic oxides, is feed
into a blast furnace for smelting together with smelter by-products and metallurgical coke. The
reduction of lead oxide during this process produces CO2 emissions. Secondary lead production
consists primarily of recycling lead acid batteries by either crushing the recycled lead batteries
using a hammer mill and entering into a smelter or by directly entering the batteries in a smelter
whole (with or without desulphurization). Several different furnace types can be used for
smelting the batteries as well as other recycled scrap lead. In the U.S., the majority of secondary
lead smelting is conducted using a blast furnace or reverberatory furnace.

2.2 Combustion Emissions

For most of the metallurgical process equipment used at primary and secondary lead smelters,
the only source of carbon is the natural gas or another fuel the burned in the unit to produce heat
for drying, roasting, sintering, calcining, melting, or casting operations. These types of
combustion devices can include roasters, furnaces (other than induction furnaces which use
electricity to produce heat for melting), refining kettles, sinter machines, rotary kilns, casting
machines, boilers, and space heaters. The blast furnace also consumes metallurgical coke as a
charge for the reduction process. Emissions associated with metallurgical coke consumption are
considered process emissions. For a full discussion of stationary combustion, please refer to
(EPA-HQ-OAR-2008-0508-004).

3. Review of Existing Programs and Methodologies

Four existing GHG emissions reporting programs and methodologies were identified for
calculating GHG emissions from lead production: the 2006 Intergovernmental Panel on Climate
Change (IPCC) Guidelines for National Greenhouse Gas Inventories, the U.S. EPA's Inventory

of U.S. Greenhouse Gas Emissions and Sinks: 1990-2006, the Australian National Greenhouse
Gas Reporting Program, and the Canadian Mandatory Greenhouse Gas Reporting Program.

3.1 2006 IPCC Guidelines

The 2006 IPCC Guidelines for National Greenhouse Gas Inventories considers three different
methods for calculating emissions from lead production (IPCC 2006). The IPCC Tier 1 method
uses a default emission factor by production type listed in Table 1 multiplied by lead production
quantity. The equation is as follows:

ECo2 = (DS x EFa) + (ISF x EFb) + (S x EFC)

Where:

ECo2 = Emissions of CO2, metric ton

DS	= Lead produced by direct smelting, metric ton

ISF	= Lead produced from the Imperial smelting furnace, metric ton

S	= Lead produced from secondary materials, metric ton

EFa.b.c	= Applicable emission factor, metric tons CCVmetric ton product

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Technical Support Document for the Lead Production Sector: Proposed Rule for Mandatory Reporting of

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Table 1. Default Emission Factors for Lead Production

Production Type

Emission Factor
(metric ton CCVmetric ton product)

Imperial Smelt Furnace (ISF)

0.59

Direct Smelting (DS)

0.25

Treatment of Secondary Raw Materials

0.20

Source: 2006 IPCC Guidelines for National Greenhouse Gas Inventories

The IPCC Tier 2 method calculates emission factors specific to each production type (e.g.,
secondary lead production) based on country-specific information about the use of reducing
agents, furnace types, and other process materials. Carbon contents presented in Table 2 can be
used to develop emission factors. IPCC Tier 2 is more accurate than IPCC Tier 1 because it
accounts for the materials and furnace types used by the country rather than assuming a world-
wide production average.

Table 2. Material-Specific Carbon Content for Lead Production

Process Materials

Carbon Content
(kg carbon/kg material)

Blast Furnace Gas

0.17

Charcoal*

0.91

Coal3

0.67

Coal Tar

0.62

Coke

0.83

Coke Oven Gas

0.47

Coking Coal

0.73

EAF Carbon Electrodes'3

0.82

EAF Charge Carbon0

0.83

Fuel Oild

0.86

Gas Coke

0.83

Natural Gas

0.73

Petroleum Coke

0.87

a Assumed other bituminous coal

b Assumed 80 percent petroleum coke and 20 percent coal tar
c Assumed coke oven coke
d Assumed gas/diesel fuel

* Charcoal if derived from biomass emissions are zero, but above carbon
content should be used to calculate emissions and should be reported as a
memo item

Source: 2006 IPCC Guidelines for national Greenhouse Gas Inventories

The IPCC Tier 3 method consists of either direct measurement of CO2 emissions at lead
production facilities (aggregated for national reporting) or calculating plant-specific emissions
based on plant-specific data on reducing agents and process materials. IPCC Tier 3 is more
accurate than IPCC Tier 2 because individual smelters can differ substantially in the furnaces and
other process equipment used.

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Technical Support Document for the Lead Production Sector: Proposed Rule for Mandatory Reporting of

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3.2	U.S. EPA's Inventory of U.S. Greenhouse Gas Emissions and Sinks

The protocol used for the U.S. EPA's Inventory of U.S. Greenhouse Gas Emissions and Sinks
(US EPA 2008) to estimate GHG emissions from U.S. primary and secondary lead production
facilities was the IPCC Tier 1 method (described in Section 3.1).

3.3	Australian National Government's Greenhouse and Energy Reporting Program

The Australian National Government's Greenhouse and Energy Reporting Program (Australian
DCC 2007) requires reporting of CO2 emissions from lead producing facilities that emit at least
25,000 mtC02e, or produce or consume at least 100 terajoules of energy; or their corporate group
emits at least 125,000 mtCC^e, or it produces or consumes at least 500 terajoules of energy. The
program uses a method for estimating emissions from lead production facilities based on the
National Greenhouse Account (NGA) default method. This method calculates emissions based
on the following equation:

Ei = XQc x ECc x EFC / 1000

Where:

Ei = emissions of CO2 from the production of the metal, metric tons
Qc = the quantity of each carbon reductant used, metric tons
ECc = the energy content of the reductant, gigajoule per metric ton
EFC= the emission factor of the fuel used, kilogram per gigajoule

The program protocol encourages the development of facility-specific emission factors from the
carbon content of the reducing agent. This higher accuracy method is similar to the method
specified by the IPCC Tier 3 method (described in Section 3.1).

3.4	Canadian Mandatory Greenhouse Gas Reporting Program

The Canadian Mandatory Greenhouse Gas Reporting Program (Environment Canada 2008)
requires reporting of CO2 emissions from lead producing facilities if they emit 100,000 mtCC^e.
The method used for estimating emissions is based on the following equation:

EmissionSC02 = EFra X Mra + M C in Metal Ore x (44/12)

Where:

Emissionsco2	= Emissions of CO2 from the production of the metal, metric ton

EFra	= Emission factor for the reducing agent, mtCCVmt reducing agent

Mra	= Mass of reducing agent consumed, metric ton

M c in Metal Ore	= Mass of carbon in the metal ore feed, metric ton

44/12	= Stoichiometric ratio of CO2/C

The protocol suggests that facility-specific emission factors be developed for the reducing agent
consumed and used to ensure accuracy of the estimates. However, they also provide the IPCC
default emissions factors in the case that facility-specific emission factors can not be calculated.

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Technical Support Document for the Lead Production Sector: Proposed Rule for Mandatory Reporting of

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4. Options for Reporting Threshold

4.1	Options Considered

Options considered for the reporting threshold include mandatory GHG reporting from primary
and secondary smelters based on emission thresholds of 1,000, 10,000, 25,000, and 100,000
mtC02e. For this analysis, process and combustion emissions were estimated for primary and
secondary lead smelters as presented in Section 5.2.

4.2	Emissions and Facilities Covered Per Option
4.2.1 Combustion Emissions

Nationwide combustion GHG emissions from lead production facilities were estimated using
data collected from Title V air permits for the primary lead smelter and a representative
secondary lead smelter (Tables 3 and 4). The combustion devices at each facility are natural-gas
fired. The GHG emissions were estimated by multiplying the combustion device heat rating
(MMBtu/year) by the carbon content of natural gas (14.47 Tg C/QBtu) and using the default CH4
and N2O emission factors for stationary combustion in manufacturing industries and construction
obtained from the 2006 IPCC Guidelines for National Greenhouse Gas Inventories (IPCC 2006).
For the purpose of estimating annual GHG emissions, each combustion device was assumed to
operate 24 hours/day, 365 days/year at 90% of capacity. To estimate facility-level combustion
CO2 emissions for secondary lead smelters, the annual estimated combustion emissions value
calculated for the secondary lead smelter used to prepared Table 4 was divided by the
corresponding facility's annual lead production to obtain a combustion GHG emissions factor for
secondary lead smelters in terms of lead production (metric tons C02e emitted per metric ton of
lead produced). This emissions factor was then applied to each of the facilities listed in Table 5
using the facility's annual lead production capacity presented in the table.

Table 3. Primary Lead Smelter Stationary Combustion Sources

Combustion Device3

Fuel Burned3

Heat Rating3
(MMBtu/Hour)

Estimated
GHG Emissions
(metric tons C02e)b

Kettle burners

Natural Gas

5.04

25,325

Dross kettle burners

Natural Gas

5.04

4,221

Office boiler

Natural Gas

2.84

1,189

Furnace vent

Natural Gas

5.05

2,115

Space heater

Natural Gas

10

4,187

Strip mill kettle burners

Natural Gas

5.04

4,221

Change house boilers

Natural Gas

5.46

4,573

Low alpha smelting system

Natural Gas

2.94

1,231

Acid plant preheater

Natural Gas

5.88

2,462

Silver dross liquation kettles

Natural Gas

3.36

1,407

Total





50,930

a Facility data from Missouri DNR (2006) Part 70 Operating Permit Number OP2006-011
b Estimate assumes combustion device operated 24 hours/day, 365 days/year at 90% of capacity.

Table 4. Secondary Lead Smelter Stationary Combustion Sources

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Technical Support Document for the Lead Production Sector: Proposed Rule for Mandatory Reporting of

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Combustion Device3

Fuel Burned3

Heat Rating3
(MMBtu/Hour)

Estimated
GHG Emissions
(metric tons C02e)

Reverberatory furnace

Natural Gas

32

13,399

Refining kettle

Natural Gas

4

13,399

Refining kettle

Natural Gas

4.25

1,780

Casting machine

Natural Gas

0.3

126

Rotary dryer

Natural Gas

14

5,862

HVAC

Natural Gas

0.07

29

Total





34,596

a Air permit data for selected facility from Indiana DOEM (2007) Administrative Amendment to Part 70

Operating Permit TO97-6201-00079.
b Estimate assumes combustion device operated 24 hours/day, 365 days/year at 90% of capacity.

4.2.2 Process Emissions

Nationwide process CO2 emissions from lead smelters were estimated using the IPCC Tier 1
method (see Section 3.1). Total national primary and secondary lead production was multiplied
by the emission factors provided in Table 1 for direct smelting and secondary production,
respectively. Facility-level emission estimates were made to better characterize the distribution
of emissions within the sector. To estimate facility-level process CO2 emissions for secondary
lead smelters, the total estimated nationwide emissions value for secondary production was
prorated among the facilities listed in Table 5 based on annual lead production capacity for each
facility.

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Technical Support Document for the Lead Production Sector: Proposed Rule for Mandatory Reporting of

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Table 5. Estimated 2006 U.S. Lead smelter GHG Emissions

Facility

Smelter Type

Annual
Production
Capacity
(metric tons)

Estimated
Process CO2
Emissions
(metric tons)

Estimated
Combustion
C02e Emissions
(metric tons)

Estimated
Total C02e
Emissions
(metric tons)

Plant 1

Primary

220,000

38,250

50,930

89,180

Plant 2

Secondary

130,000

25,538

59,966

85,503

Plant 3

Secondary

110,000

21,609

50,740

72,349

Plant 4

Secondary

110,000

21,609

50,740

72,349

Plant 5

Secondary

110,000

21,609

50,740

72,349

Plant 6

Secondary

90,000

17,680

41,515

59,195

Plant 7

Secondary

88,000

17,287

40,592

57,879

Plant 8

Secondary

80,000

15,715

39,208

55,906

Plant 9

Secondary

85,000

15,715

36,902

52,617

Plant 10

Secondary

75,000

14,733

34,596

49,329

Plant 11

Secondary

75,000

14,733

34,596

49,329

Plant 12

Secondary

66,000

12,965

30,444

43,409

Plant 13

Secondary

58,000

11,394

26,754

38,148

Plant 14

Secondary

30,000

5,893

13,838

19,732

Plant 15

Secondary

30,000

5,893

13,838

19,732

Plant 16

Secondary

24,000

4,715

11,071

15,785

Plant 17

Secondary

10,000

1,964

4,613

6,577

Plant 18

Secondary

1.000E

196

461

658

Plant 19

Secondary

1.000E

196

461

658

Plant 20

Secondary

1.000E

196

461

658

Plant 21

Secondary

1.000E

196

461

658

Plant 22

Secondary

1.000E

196

461

658

Plant 23

Secondary

1.000E

196

461

658

Plant 24

Secondary

1.000E

196

461

658

Plant 25

Secondary

1.000E

196

461

658

Plant 26

Secondary

1.000E

196

461

658

Plant 27

Secondary

1.000E

196

461

658

Primary Lead Smelter Total

220,000

38,250

50,930

89,180

Secondary Lead Smelter Total

1,181,000

232,000

544,765

776,765

Nationwide Total

1,401,000

270,250

595,695

865,945

Note: Information on specific lead production plant capacity is proprietary.

E - Estimated. There are ten small secondary lead production plants whose annual capacity ranges from <1,000 to
approximately 4,000 metric tons per year. In total, these plants do not exceed lead production capacity of 10,000
metric tons per year. This value (10,000 metric tons) was divided equally among the ten plants.

Source: Guberman 2008.

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Technical Support Document for the Lead Production Sector: Proposed Rule for Mandatory Reporting of

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4.2.3 Emissions Thresholds

As presented in Table 5, total nationwide lead production capacity is approximately 1,401,000
metric tons with approximately 16 percent coming from primary lead production and 84 percent
coming from secondary lead production. Estimated process and combustion emissions from lead
production total 0.9 MMTCC^e. These emissions originate from approximately 26 secondary
lead smelters and one primary lead smelter. In developing the threshold for lead smelters, annual
GHG emissions-based threshold levels of 1,000, 10,000, 25,000 and 100,000 Mt C02e were
considered. Table 6 presents the estimated emissions and number of facilities that would be
subject to GHG emissions reporting, based on existing facility lead production capacities, under
these various threshold levels.

Table 6. Threshold Analysis for Lead Production

Threshold

Level
(mtC02e/yr)

Nationwide Annual GHG Emissions
(mtC02e/yr)

Total
Number
of

Facilities

Subject to GHG Reporting

Process
Emissions

Combustion
Emissions

Total

GHG Emissions

Facilities

mtC02e/yr

Percent

Number

Percent

100,000

270,250

595,695

865,945

0

0

0

0

0%

25,000

270,250

595,695

865,945

13

859,368

92%

13

48%

10,000

270,250

595,695

865,945

16

852,791

98%

16

59%

1,000

270,250

595,695

865,945

17

797,543

99%

17

63%

As presented in Table 6, no facility exceed a threshold of 100,000 mtCC^e/year, approximately
48 percent (13) of all facilities exceed a threshold of 25,000 mtCC^e/year, approximately 59
percent (16 facilities) of all facilities exceed a threshold of 10,000 mtCC^e/year, and
approximately 63 percent (17 facilities) exceed a threshold of 1,000 mtCC^e/year. Based on
these estimates, approximately 92 percent of emissions result from facilities that emit more than
25,000 mtC02e annually, approximately 98 percent of emissions result from facilities that emit
more than 10,000 mtCC^e annually, and approximately 99 percent of emissions result facilities
that emit more than 1,000 mtCC^e annually. To include all facilities in the reporting framework,
a threshold of approximately 500 mtCC^e would be required.

5. Options for Monitoring Methods

As described in Section 4, lead smelters can release both combustion and process-related GHG
emissions. The process-related GHG emissions are produced at primary and secondary lead
smelters operating smelting furnaces (e.g., blast furnace) in which coke or another carbonaceous
reducing agent is charged. This section describes monitoring method options for estimating
process-related GHG emissions from the lead production source category.

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5.1	Option 1: Simplified Emission Calculation

The monitoring method is a simplified emission calculation method using only default emission
factors to estimate CO2 emissions. The method requires multiplying the amount of lead produced
for a specific reporting period (e.g., annual) by the appropriate default emission factors
applicable to the lead smelter operations obtained from the 2006 IPCC guidelines. This option is
the IPCC Tier 1 method described in Section 3.1. Implementation of this method requires facility
owners and operators to keep records of metric tons of lead produced. As these records are
expected to already be maintained, this method is the easiest option for the facility owner or
operator to implement. However, because lead smelters can differ substantially in the number
and types of furnaces operated and other site-specific factors, use of default emission factors
introduces the greatest level of uncertainty to the annual GHG emissions determinations for
individual facilities.

5.2	Option 2: Facility-Specific Carbon Balance Calculation

The monitoring method requires performing monthly measurements of the carbon content of
specific process inputs and the mass rate of these inputs. This is the IPCC Tier 3 method and the
higher order methods in the Canadian and Australian reporting programs. This method requires
facility owners and operators to determine the carbon contents of materials added to the source
by analysis of representative samples collected of the material or from information provided by
the material suppliers. In addition, the quantities of these materials consumed during lead
production are measured and recorded. To obtain the process-related CO2 emission estimate, the
material carbon content would be multiplied by the corresponding mass of material consumed
and a conversion of carbon to CO2 assuming that all of the carbon is converted during the
reduction process. This method is more accurate than Option 1 because it accounts for the
process materials actually used by the each individual facility. However, the method does require
more recordkeeping and computations on the part of the facility owner or operator.

For this method, the facility owner or operator would report in addition to GHG emissions, the
facility lead product produced, carbon content of reducing agents consumed, and quantity of
carbon recovered for downstream use, if any. In addition, each facility owner or operator would
be required to conduct quality assurance (QA) of supplier-provided information on the carbon
content of the input materials by collecting a composite sample of material and sending it to a
third-party, independent laboratory for chemical analysis to verify the supplier's information.
This QA procedure would be required to be conducted on a periodic basis (e.g., annually).

5.3	Option 3: Facility-Specific Emission Factor Using Stack Test Data

This monitoring method is applicable to lead smelter sources for which the GHG emissions are
contained within a stack or vent. The monitoring method uses stack test data to develop a site-
specific process emissions factor which is then applied to quantity measurement data of feed
material or product for the specified reporting period. For this method, a CO2 emissions
measurement stack test would be performed concurrently with measuring the input material feed
rate or product output rate during the test, and the fuel usage during the test (if applicable to the
unit) to determine the site-specific CO2 process emissions factor for the source (e.g., metric ton
of CO2 emitted per metric ton of lead product produced). The total annual CO2 process emissions
for the source would be calculated by multiplying this site-specific CO2 process emission factor

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by the total amount of the appropriate input material or product, as applicable to the emissions
factor, recorded for the operation of the source during the specified reporting period.

For stack testing, sampling equipment would be periodically brought to the site and installed
temporarily in the stack to collect a sample of the stack gas for analysis to determine the CO2
concentration in the gas stream. During the test, the flow rate of the stack gas would also be
measured allowing the calculation of the CO2 mass emission rate for the source. For a lead
smelter source for which both combustion and process-related emissions are released by the
source (e.g. blast furnace), measuring fuel usage during the stack test would allow an emissions
factor for process-related emissions to be calculated by subtracting the contribution due to the
carbon in the fuel burned from the total emissions measured by the test.. The performing of a
stack test requires additional cost and time to implement the method compared to Options 1 and
2.

In general, the facility-specific emission factor should be re-established on a periodic basis by
performing a new stack test. The facility owner or operator would report for each stack test
conducted the measured GHG concentrations in the stack gas, the monitored stack gas flow rate
for each monitored emission point, and the time period during which the stack test was
conducted. The process operating conditions (e.g., raw material feed rates) during the time
period when the test was conducted would be reported.

This method can offer a higher level of accuracy than either Options 1 or 2 since actual stack test
data are used for each facility to obtain facility-specific GHG emission factors. However, the
method may not be appropriate for all lead smelters depending on the site-specific operations
conducted at the facility. A method using periodic, short-term stack testing would be appropriate
for those facilities where process inputs (e.g., feed materials, carbonaceous reducing agents) and
process operating parameters remain relatively consistent over time. In cases where there is the
potential for significant variations in the process input characteristics or operating conditions,
continuous or more frequent measurements would be needed to accurately record changes in the
actual GHG emissions from the sources resulting from any process variations.

5.4 Option 4: Direct Measurement Using CEMS

Another monitoring method applicable to lead smelter sources for which the GHG emissions are
contained within a stack or vent is direct measurement using a continuous emissions monitoring
system (CEMS). The CEMS measures total CO2 emissions in the exhaust gas stream from a
source so the recorded results would represent the combined combustion and process-related
emissions for those lead smelter sources in which a fossil-fuel is burned.

Direct measurements of the GHG concentration in the stack gas and the flow rate of the stack gas
can be made using a CEMS. The difference between this option and Option 3 is using a CEMS
provides a continuous measurement of the emissions while a stack test provides a periodic
measurement of the emissions. Because a CEMS would continuously measure actual CO2
emissions from a given lead smelter source when it is in operation, this method is the most
accurate monitoring method for determining GHG emissions from a specific source. The costs
for installing and operating a CEMS for direct measurements of GHG emissions from a given
lead smelter would be higher than for using one of the other monitoring method options.

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Elements of a CEMS include a platform and sample probe within the stack to withdraw a sample
of the stack gas, an analyzer to measure the concentration of the GHG (e.g., CO2) in the stack
gas, and a flow meter within the stack to measure the flow rate of the stack gas. The emissions
are calculated from the concentration of GHGs in the stack gas and the flow rate of the stack gas.
The CEMS continuously withdraws and analyzes a sample of the stack gas and continuously
measures the GHG concentration and flow rate of the stack gas. Under a CEMS approach, the
results of the recorded emissions measurement data would be reported annually.

6. Procedures for Estimating Missing Data

Procedures for estimating missing data vary depending on the monitoring method used for
determining annual GHG emissions from a source. Each of the options described in Section 6
would require a complete record of measured parameters as well as parameters determined from
company records that are used in the GHG emissions calculations (e.g., reducing agent carbon
contents). Therefore, whenever a quality-assured value of a required parameter is unavailable, a
substitute data value for the missing parameter must be used in the calculations.

6.1	Procedures for Option 1: Simplified Emission Calculation

If facility-specific production data is missing for one year, an average value using the production
data from the year prior and the year after the missing year may be calculated. Default emission
factors are available from the IPCC guidelines (IPCC 2006).

6.2	Procedures for Option 2: Facility-Specific Carbon Balance Calculation

When assuming a 100% conversion of C to CO2, no missing data procedures would apply
because this factor would be multiplied by the materials input, which are readily available. If this
amount of carbonaceous agent input is not available, a facility owner or operator would need to
extrapolate a value from previous years operating data taking into consideration any changes in
production or process.

6.3	Procedures for Option 3: Facility-Specific Emission Factor Using Stack Test Data

For a method requiring measurement of CO2 emissions using stack testing, "missing data" is not
generally anticipated. Stack testing conducted for the purposes of compliance determination is
subject to quality assurance guidelines and data quality objectives established by the U.S. EPA,
including the Clean Air Act National Stack Testing Guidance (US EPA 2005). The 2005
Guidance Document states that stack tests should be conducted in accordance with a pre-
approved site-specific test plan to ensure that a complete and representative test is conducted. In
addition, according to the 2005 Guidance Document, a site-specific test plan should generally
include chain of custody documentation from sample collection through laboratory analysis
including transport, and should recognize special sample transport, handling, and analysis
instructions necessary for each set of field samples. The test plan for a stack test used to obtain
data for the purposes of emissions reporting would be made available for review prior to
performing the stack test, and the stack test results would be reviewed with respect to the test
plan prior to the data being deemed acceptable for the purposes of emissions reporting. Results
of stack tests that do not meet pre-established quality assurance guidelines and data quality
objectives would generally not be acceptable for use in emissions reporting, and any such stack
test would need to be re-conducted to obtain acceptable data.

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7.4 Procedures for Option 4: Direct Measurement Using CEMS

For a method requiring direct measurement of CO2 emissions using CEMS, procedures for
management of missing data established by the U.S. EPA in 40 CFR Part 75 could be used.

These procedures for management of missing data are described in Part 75.35(a), (b), and (d). In
general, missing data from operation of the CEMS may be replaced with substitute data to
determine the CO2 flow rates or CO2 emissions during the period in which CEMS data are
missing.

7. QA/QC Requirements

Facility owners and operators should conduct quality assurance (QA) and quality control (QC) of
the information used for each GHG emissions determination including production and
consumption data, supplier information (e.g., carbon contents), and emission estimates
calculations performed. Facility owners and operators are encouraged to prepare an in-depth
quality assurance and quality control plan which would include checks on production data, the
carbon content information received from the supplier and from the lab analysis, and calculations
performed to estimate GHG emissions. Several examples of QA/QC procedures are described
below.

7.1	Combustion Emissions

Facility owner and operators can find more information on the QA/QC requirements associated
with methods for estimating CO2, CH4, and N2O emissions from stationary combustions in the
General Stationary Combustion Source Technical Support Document at EPA-HQ-OAR-2008-
0508-004.

7.2	Process Emissions

The QA/QC requirements vary depending on the monitoring method used for determining annual
GHG emissions from a source. Each option would require QA/QC measures appropriate to the
particular methodology used to ensure proper emission monitoring and reporting.

7.2.1 Equipment Maintenance

For methods using data obtained from flow meters to directly measure the flow rate of fuels, raw
materials, products, or process byproducts, flow meters should be calibrated on a scheduled basis
according to equipment manufacturer specifications and standards. Flow meter calibration is
generally conducted at least annually. A written record of procedures needed to maintain the
flow meters in proper operating condition and a schedule for those procedures should be part of
the QA/QC plan for the capture or production unit.

An equipment maintenance plan should be developed as part of the QA/QC plan. Elements of a
maintenance plan for equipment include the following: (1) conduct regular maintenance of
equipment, e.g. flow meters; (2) maintain a written record of procedures needed to maintain the
monitoring system in proper operating condition and a schedule for those procedures; and (3)
maintain a record of all testing, maintenance, or repair activities performed on any monitoring
system or component in a location and format suitable for inspection. A maintenance log may be
used for this purpose.

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7.2.2	Stack Test Data

For a method requiring measurement of CO2 emissions using stack testing, the stack test should
be performed according to the quality assurance guidelines and data quality objectives
established by the U.S. EPA, including the Clean Air Act National Stack Testing Guidance (US
EPA 2005).

7.2.3	CEMS

For a method requiring direct measurement of CO2 emissions using CEMS, the equipment
should be tested for accuracy and calibrated as necessary by a certified third party vendor. These
procedures should be consistent in stringency and data reporting and documentation adequacy
with the QA/QC procedures for CEMS described in Part 75 of the Acid Rain Program (EPA
2008a).

7.3 Data Management

Data management procedures should be included in the QA/QC Plan. Elements of the data
management procedures plan are as follows:

•	For measurements of carbon content of reducing agents, assess representativeness of the
carbon content measurement of reducing agents and other process inputs by comparing
values received from supplier and/or laboratory analysis with IPCC default values.

•	Check for temporal consistency in production data, process inputs, and emission estimate.
If outliers exist, they should be explained by changes in the facility's operations or other
factors. A monitoring error is probable if differences between annual data cannot be
explained by:

o Changes in activity levels,
o Changes concerning process inputs material,

o Changes concerning the emitting process (e.g. energy efficiency improvements)
(European Commission 2007).

•	Determine the "reasonableness" of the emission estimate by comparing it to previous
year's estimates and relative to national emission estimate for the industry:

o Comparison of data on fuel or input material consumed by specific sources with

fuel or input material purchasing data and data on stock changes,
o Comparison of fuel or input material consumption data with fuel or input material

purchasing data and data on stock changes,
o Comparison of emission factors that have been calculated or obtained from the fuel
or input material supplier, to national or international reference emission factors of
comparable fuels or input materials
o Comparison of emission factors based on fuel analyses to national or international

reference emission factors of comparable fuels, or input materials,
o Comparison of measured and calculated emissions (European Commission 2007).

•	Maintain data documentation, including comprehensive documentation of data received
through personal communication:

o Check that changes in data or methodology are documented

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8. Types of Emission Information to be Reported

Lead smelter owners and operators would report annual process CO2 emissions. Depending on
the monitoring method used (discussed in Section 6), additional information could be reported to
assist in the verification of the reported emissions. Such information could include facility
operation information routinely recorded at the facility such as the total number of smelting
furnaces operated at the facility, lead product production quantities, raw material quantities
purchased and consumed, and fossil fuel usage. In addition, facility owners and operators could
report additional information to assist in QA/QC of any site-specific GHG emissions data used
for the reported emissions determination.

For a full discussion of stationary combustion reporting options, please refer to (EPA-HQ-OAR-
2008-0508-004).

8.1 Additional Data to be Retained Onsite

Owners and operators of facilities reporting GHG emissions should be required to retain certain
process configuration information and operating data used for their GHG emissions
determinations onsite for a period of at least three years from the reporting year. Process
configuration information would include combustion device types, numbers, and sizes, and
identification of process equipment using carbonaceous input materials. Process operating data
would include process raw material feed rates and carbon contents, and lead product production
quantities. These data could be used to conduct trend analyses and potentially to develop process
or activity-specific emission factors for lead smelters. For method using stack testing, these data
would include stack test reports and associated sampling and chemical analytical data for the
stack test. For method using emission monitoring systems, data would include measured GHG
concentrations and stack gas flow rates, calibration and quality assurance records.

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9. References

Australian DCC (2007). National Greenhouse and Energy Reporting System: Technical
Guidelines for the Estimation of Greenhouse Emissions and Energy at Facility Level.
Commonwealth of Australia. Canberra, Australia.

Doe Run (2004) The Doe Run Company. Herculaneum, MO. Available at:
http ://www. doerun. com/index, aspx

Environment Canada (2008) GHG Quantification Guidance: Protocols and Guidance Manuals.
Section 3. Available at:

http://www.ee. gc.ca/pdb/ghg/guidance/protocols/2005_metal_mining/base_metals/s3_e.cfm#3.4.
32

Guberan (2008). Personal Communication between David E. Guberman of the US Geological
Survey and Charles Cebul of ICF International. April 15th, 2008.

Indiana DOEM (2007) Administrative Amendment to Part 70 Operating Permit TO97-6201-
00079. Indiana Department of Environmental Management. Indianapolis, Indiana.
http ://permits. air, idem, in. gov/6201 f.pdf

IPCC (2006) 2006 IPCC Guidelines for National Greenhouse Gas Inventories. The National
Greenhouse Gas Inventories Programme, The Intergovernmental Panel on Climate Change, H.S.
Eggleston, L. Buenida, K. Miwa, T Ngara, and K. Tanabe (eds.). Hayama, Kanagawa, Japan.

Missouri DNR (2006) Part 70 Operating Permit Number OP2006-011. State of Missouri
Department of Natural Resources, Air Pollutant Control Program. Herculaneum, MO.

Sjardin, M. (2003) CO2 Emission Factors for Non-Energy Use in the Non-Ferrous Metal,
Ferroalloys and Inorganics Industry. Copernicus Institute. Utrecht, the Netherlands.

US EPA (2003). Part 75, Appendix Bl. Available at
http ://www. epa. gov/ airmarkt/spm/rule/001000000B. htm.

U.S. EPA (2005). Clean Air Act National Stack Testing Guidance, U.S. Environmental
Protection Agency Office of Enforcement and Compliance Assurance, September 30, 2005, Page
11. Available at:

http://www.epa.gov/compliance/resources/policies/monitoring/caa/stacktesting.pdf

U.S. EPA (2008) Inventory of U.S. Greenhouse Gas Emissions and Sinks. April 15, 2008.
Available at: http://www.epa.gov/climatechange/ emissions/usinventorvreport.html

USGS (2007) 2006 Minerals Yearbook: Lead Annual Report. U.S. Geological Survey, Reston,
VA. Available at: http://minerals.usgs.gov/minerals/pubs/commoditv/lead/mvbl-2006-lead.pdf

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