Part 70 Air Quality Permit

Holcim (US) Inc. – Holly Hill Plant

200 Safety Street

Holly Hill, South Carolina 29059

(permit updated 6/27/05 and 8/19/05)

In accordance with the provisions of the Pollution Control Act, Sections
48-1-50(5) and 48-1-110(a), and the 1976 Code of Laws of South Carolina,
as amended, Regulation 61-62, the above named permittee is hereby
granted permission to discharge air contaminants into the ambient air.
The Bureau of Air Quality authorizes the operation of this facility and
its applicable equipment specified herein in accordance with the plans,
specifications and other information submitted in the Title V permit
application dated April 1996, August 2000, November 2000, and November
2002.

This permit is subject to and conditioned upon the terms, limitations,
standards, and schedules contained in or specified on the 106 pages,
with the accompanying attachments, of this permit.

Permit Number:	TV-1860-0005	Effective Date:	July 1, 2003

Issue Date:		April 15, 2003	Expiration Date:	June 30, 2008

Director, Engineering Services Division

Bureau of Air Quality

RECORD OF REVISIONS

Revision

Number	Final

Revision

Date	Type of Revision

(AA, MM, SM)	Description of Change (Specific Parts,

Sections, and Tables Revised or Added)

1	5/14/03	AA	Updated sections 5 through 10 for missing equipment;
updated attachment B for insignificant activities; updated attachment C
for regulations not applicable to the facility.

2	9/23/03	AA	Changing the control device description for BH85 within
table 5.6 control devices unit ID 06- Cement Loadout Equipment

2	9/23/03	MM	Reflect changes done to the piping system to Tank 146
(Table 5.14 unit ID 07 - Tank Equipment).

3	10/22/03	AA	R170, R171, R174, R175, R178, R180, R195, R204 has been
moved from Table 5.16 and Table 5.9 into Table 5.15 and Table 5.8, to
reflect applicability to NSPS, Subpart OOO and not MACT, Subpart LLL.

R183 and R185 has moved from Table 5.15 and Table 5.9 into Table 5.16
and Table 5.8, to reflect applicability to MACT, Subpart LLL and not
NSPS, Subpart OOO.

4	6/27/05	MM	Adding construction permit 1860-0005-CZ:

1. Truck Load Out Silo System. W902 through W905 has been added to
Tables 5.13, 5.20 and 6.7. Condition 5.E.6(g) has been added to reflect
a process weight rate limitation for the system.

4	6/27/05	MM	Adding construction permit 1860-0005-DA:

1. Adding the Sampson Feeder System to Table 5.4, 5.11, 5.18, and 6.5.
Condition 5.E.4(ii) has been added to reflect a process weight rate
limitation for the system.

4	6/27/05	MM	Adding construction permit 1860-0005-DB:

1. Relocate an existing 100,000 gallon No.6 Fuel Oil Storage Tank and
modify it to serve as a non-hazardous waste derived fuel (NHWDF) storage
tank.

2. Addition of three new 60,000 gallon NHWDF storage tanks and a new 5.0
million Btu/hr boiler to heat two of the four NHWDF storage tank lines.

Changes have been made to Tables 5.1, 5.7, 5.14, 5.21, 6.8, and
conditions 5.E.7(j)(k)(l)(m) and 6.B.8(m) have been added.

4	6/27/05	MM	Adding construction permit 1860-0005-DC:

1. Cement Dome Bucket Elevator Retrofit Project (Aliviator project), to
improve the product recovery associated with the transfer of cement from
Finishing Mills 5 and 6 to the existing dome, truck surge bin, rail
silos and the new cement silos. Two new dust collectors (S188 and S189)
will be installed for PM/PM10 control. The existing cement dome emission
source, C319 (S85). Changes have been made to Tables 5.5, 5.12, 5.19 and
6.6 and condition 5.E.4(d) has been added

4	6/27/05	MM	Adding conditions to allow for maintenance activities to be
perform on the inlet pressure port without shutting off the HWDF.

4	6/27/05	MM	Voiding out all references to the old facility in Parts 8.0
and 9.0.

4	6/27/05	AA	Updated condition 4.B.6.

5	8/19/05	AA	Removing of all non-applicable 40 CFR 63, Subpart DD
requirements, originally added through construction permit 1860-0005-CB.

AA	= Administrative Amendment

MM	= Minor Modification

SM	= Significant Modification

Send copies of all revisions to Permit File, Main File, District EQC
Office, US EPA, and Facility Contact.

TABLE OF CONTENTS

Part 1.0	GENERAL INFORMATION

A.	Applicable Permit Dates

B.	Facility Information

C.	Facility Address

D.	Facility Billing Address

Part 2.0	APPLICABILITY

Part 3.0	GENERAL CONDITIONS

A.	Permit Issuance

B.	Permit Expiration and Renewal

C.	Severability

D.	Fee Assessment and Payment

E.	Submittal of Information

F.	Public Participation

G.	Permit Reopening

H.	Temporary Sources

I.	Emergency Provisions

J.	Property Rights

K.	Economic Incentives, Marketable Permits, Emission Trading

L.	Title IV Sources

M.	Administrative Permit Amendments

N.	Minor Permit Modifications

O.	Significant Modification Procedures

P.	Duty to Comply

Q.	Inspection and Entry

R.	Compliance Requirements

S.	Schedule of Compliance

T.	Need to Halt or Reduce Activity Not a Defense

U.	Operational Flexibility

Part 4.0	FACILITY WIDE REQUIREMENTS

A.	Emissions Limits and Standards

B.	Facility Wide Conditions

Part 5.0	EMISSION UNIT REQUIREMENTS

A.	Emission Unit Description

B.	Control Devices Description

C.	Equipment Description

D.	Emissions Limits and Standards

E.	Emission Unit Conditions

Part 6.0	MONITORING AND REPORTING REQUIREMENTS

A.	Monitoring and Reporting

B.	Monitoring and Reporting Conditions

Part 7.0	ADDITIONAL CONDITIONS

A.	Specific Conditions

B.	Operational Flexibility

C.	Compliance Schedule

D.	Permit Shield

ATTACHMENT A - Modeled Emission Rates

ATTACHMENT B - Insignificant Activities

ATTACHMENT C - Applicable and Non-applicable Federal and State
Regulations

PART 1.0  GENERAL INFORMATION

A.	APPLICABLE PERMIT DATES

ISSUE DATE					: April 15, 2003

EFFECTIVE DATE				: July 1, 2003

EXPIRATION DATE				: June 30, 2008

RENEWAL APPLICATION DUE		: December 31, 2007

B.	FACILITY INFORMATION

ENVIRONMENTAL CONTACT		: Glenn Raynor

CONTACT TELEPHONE NUMBER	:<PHONE_NUMBER>

INTERNET E-MAIL ADDRESS<EMAIL_ADDRESS>
FACILITY LOCATION			: 200 Safety Street / Highway 453

COUNTY					: Orangeburg

SIC CODE(S)					: 3241

AFS CODE					:<PHONE_NUMBER>

C.	FACILITY ADDRESS

FACILITY NAME				: Holcim (US) Inc. – Holly Hill Plant

ADDRESS					: 200 Safety Street / Highway 453

						: Holly Hill, South Carolina 29059

D.	FACILITY BILLING ADDRESS

FACILITY BILLING NAME			: Holcim (US) Inc. – Holly Hill Plant

ADDRESS					: 200 Safety Street / highway 453

						: Holly Hill, South Carolina 29059

PART 2.0  APPLICABILITY [SC Regulation 61-62.70.3(a)]

The following sources are subject to permitting requirements of Part 70:

1.	Any major source;

2.	Any source, including an area source, subject to a standard,
limitation, or other requirement under Section 111 of the Clean Air Act
(Act);

3.	Any source, including an area source, subject to a standard or other
requirement under Section 112 of the Act, except that a source is not
required to obtain a permit solely because it is subject to regulations
or requirements under Section 112(r) of the Act;

4.	Any affected source under the Title IV Acid Rain Program;

5.	Any source in a source category designated by the Administrator of
the US Environmental Protection Agency (US EPA) (Administrator) pursuant
to this Section; and

6.	Any source listed in SC Regulation 61-62.70.3(a) that is exempt from
the requirement to obtain a permit under SC Regulation 61-62.70.3(b) may
opt to apply for a permit under this Part 70 program.

The following source categories are exempted from the obligation to
obtain a Part 70 permit, but are not exempted from other SC Department
of Health and Environmental Control (Department) and US EPA requirements
[SC Regulation 61-62.70.3(b)(4)]:

1.	All sources and source categories that would be required to obtain a
permit solely because they are subject to 40 CFR 60, Subpart AAA -
Standards of Performance for New Residential Wood Heaters; and

2.	All sources and source categories that would be required to obtain a
permit solely because they are subject to 40 CFR 61, Subpart M -
National Emission Standard for Hazardous Air Pollutants for Asbestos,
Section 61.145, Standard for Demolition and Renovation.

Any person that operates or proposes to operate a particular source or
installation may submit a request in writing that the Department makes a
determination as to whether a particular source or installation is
subject to the permit requirements of this regulation.  The request must
contain such information as is believed sufficient for the Department to
make the requested determination. [SC Regulation 61-62.70.3(e)]

PART 3.0	GENERAL CONDITIONS

This section describes conditions and provisions applicable to all Part
70 sources.  Specific source category conditions and requirements are
contained in Part 5.0 of this permit.  (Revised 05/21/99)

A.	PERMIT ISSUANCE [SC Regulation 61-62.70.7(a)(1)]

A permit, permit modification, or renewal may be issued only if the
following conditions have been met:

1.	The Department has received a complete application for a permit,
permit modification, or permit renewal;

2.	Except for modifications qualifying for minor permit modification
procedures under SC Regulation 61-62.70.7(e)(2) and (3), the Department
has complied with the requirements for public participation under SC
Regulation 61-62.70.7(h);

3.	The Department has complied with the requirements for notifying and
responding to affected States under SC Regulation 61-62.70.8(b);

4.	The conditions of the permit provide for compliance with all
applicable requirements and the requirements of Part 70; and

5.	The Administrator has received a copy of the proposed permit and any
notices required under SC Regulation 61-62.70.8(a) and (b), and has not
objected to issuance of the permit under SC Regulation 61-62.70.8(c)
within the required time frame.

A Title V operating permit does not excuse any facility from the
preconstruction permitting requirements under SC Regulation 61-62.1.

B.	PERMIT EXPIRATION AND RENEWAL [SC Regulation 61-62.70.7(c)] (Revised
11/13/98)

Permit expiration terminates the source’s right to operate unless a
timely and complete renewal application has been submitted consistent
with SC Regulation 61-62.70.5(a)(1)(iii), 62.70.5(a)(2)(iv), and
62.70.7(b).  In this case, the permit shall not expire until the renewal
permit has been issued or denied.  All terms and conditions of the
permit including any permit shield that may be granted pursuant to SC
Regulation 61-62.70.6(f) shall remain in effect until the renewal permit
has been issued or denied.

Permits being renewed are subject to the same procedural requirements,
including those for public participation, affected State and US EPA
review, that apply to initial permit issuance.

C.	SEVERABILITY [SC Regulation 61-62.70.6(a)(5)]

The provisions of this permit are severable, and if any provision of
this permit, or application of any provision of this permit to any
circumstance is held invalid, the application of such provision to other
circumstances, and the remainder of this permit shall not be affected
thereby.

D.	FEE ASSESSMENT AND PAYMENT [SC Regulation 61-62.70.6(a)(7)]

The owners or operators of Part 70 sources shall pay fees to the
Department consistent with the fee schedule approved pursuant to South
Carolina Regulation 61-62.70.9.

E.	SUBMITTAL OF INFORMATION [SC Regulation 61-62.70.6(a)(6)(v)]

The permittee shall furnish to the Department, within a reasonable time,
any information that the Department may request, in writing, to
determine whether cause exists for modifying, revoking, reissuing, or
terminating the permit or to determine compliance with the permit.  Upon
request, the permittee shall also furnish to the Department copies of
records required to be kept by the permit or, for information claimed to
be confidential, the permittee may furnish such records directly to the
Administrator along with a claim of confidentiality.  The Department may
also request that the permittee furnish such records directly to the
Administrator along with a claim of confidentiality.

F.	PUBLIC PARTICIPATION [SC Regulation 61-62.70.7(h)]

Except for modifications qualifying for minor permit modification
procedures, all permit proceedings, including initial permit issuance,
significant modifications, and renewals, shall provide adequate
procedures for public notice including offering an opportunity for
public comment and hearing on the draft permit.  These procedures shall
meet all requirements of SC Regulation 61-62.70.7(h).

G.	PERMIT REOPENING [SC Regulation 61-62.70.7(f)] (Revised 05/21/99)

This permit shall be reopened and revised under any of the following
circumstances:

1.	Additional applicable requirements under the Act become applicable to
a major Part 70 source for which three or more years remain on the
original term of the permit.  Such revisions shall be made not later
than eighteen (18) months following promulgation of relevant standards
or regulations unless the regulation specifically provides for a longer
compliance period.  No such reopening is required if the effective date
of the requirement is later than the date on which the permit is due to
expire, unless the original permit or any of its terms and conditions
has been extended pursuant to SC Regulation 61-62.70.7(c)(1)(ii).

2.	Additional requirements, including excess emission requirements,
become applicable to an affected source under the acid rain program.
Excess emissions offset plans shall be deemed to be incorporated into
this permit upon approval by the Administrator.

3.	The Department or EPA determines that the permit contains a material
mistake or that inaccurate statements were made in establishing the
emissions standards or other terms or conditions of the permit.

4.	The Administrator or the Department determines that the permit must
be revised or revoked to assure compliance with the applicable
requirements.

In addition, the permit may be modified, revoked, reopened, and
reissued, or terminated for cause by the Department.  The filing of a
request by the permittee for a permit modification, revocation and
reissuance, or termination, or of a notification of planned changes or
anticipated noncompliance does not stay any permit condition. [SC
Regulation 61-62.70.6(a)(6)(iii)]

Proceedings to reopen and issue a permit shall follow the same
procedures as apply to initial permit issuance and shall affect only
those parts of the permit for which cause to reopen exists.  Such
reopenings shall be as expeditious as practicable.  Reopenings shall not
be initiated before a notice of such intent is provided to the Part 70
source by the Department at least thirty (30) days in advance of the
date that the permit is to be reopened, except that the Department may
provide a shorter time period in the case of an emergency.

H.	TEMPORARY SOURCES [SC Regulation 61-62.70.6(e)]

In accordance with SC Regulation 61-62.70.6(e), the Department may issue
a single permit authorizing emissions from similar operations by the
same source owner or operator at multiple temporary locations.  The
operation must be temporary and involve at least one change in location
during the term of the permit.  No sources subject to Title IV of the
Act shall be permitted as a temporary source.

I.	EMERGENCY PROVISIONS [SC Regulation 61-62.70.6(g)(3)]  (Revised
05/21/99)

In the case of an emergency, as defined in SC Regulation 61-62.70.6(g),
the permittee shall verify an affirmative defense of emergency through
properly signed, contemporaneous operating logs, or other relevant
evidence that:

1.	An emergency occurred and that the permittee can identify the
cause(s) of the emergency;

2.	The permitted facility was at the time being properly operated; and

3.	During the period of the emergency the permittee took all reasonable
steps to minimize levels of emissions that exceeded the emission
standards, or other requirements in the permit.

Additionally, the permittee shall submit verbal notification of the
emergency to the Department within twenty-four (24) hours of the time
when emission limitations were exceeded, followed by written
notifications within thirty (30) days.  This notice fulfills the
requirement of SC Regulation 61-62.70.6(a)(3)(iii)(B).  This notice must
contain a description of the emergency, any steps taken to mitigate
emissions, and corrective actions taken.

This provision is in addition to any emergency or upset provision
contained in any applicable requirement.  In any enforcement proceeding,
the permittee seeking to establish the occurrence of an emergency has
the burden of proof.

J.	PROPERTY RIGHTS [SC Regulation 61-62.70.6(a)(6)(iv)]

This permit does not convey any property rights of any sort, or any
exclusive privilege.

K.	ECONOMIC INCENTIVES, MARKETABLE PERMITS, EMISSION TRADING

[SC Regulation 61-62.70.6(a)(8)]

No permit revision shall be required, under any approved economic
incentives, marketable permits, emissions trading and other similar
programs or processes for changes that are provided for in this permit.

L.	TITLE IV SOURCES [SC Regulation 61-62.70.6(a)(4)]

The permittee is prohibited from emissions exceeding any allowances that
the source lawfully holds under Title IV of the Act or the regulations
promulgated thereunder.  No permit revision shall be required for
increases in emissions that are authorized by allowances acquired
pursuant to the acid rain program, provided that such increases do not
require a permit revision under any other applicable requirement.  No
limit shall be placed on the number of allowances held by a source.  The
source may not, however, use allowances as a defense for noncompliance
with any other applicable requirement.  Any such allowances shall be
accounted for according to the procedures established in regulations
promulgated under Title IV of the Act.

Where an applicable requirement of the Act is more stringent than an
applicable requirement of regulations promulgated under Title IV of the
Act, both provisions shall be incorporated into the permit and shall be
enforceable by the Administrator. [SC Regulation 61-62.70.6(a)(1)(ii)]

M.	ADMINISTRATIVE PERMIT AMENDMENTS [SC Regulation 61-62.70.7(d)(3)]

An administrative permit amendment as defined in SC Regulation
61-62.70.7(d) can be made by the Department consistent with the
following:

1.	The Department shall take no more than sixty (60) days from receipt
of a request for an administrative permit amendment to take final action
on such request, and may incorporate such changes without providing
notice to the public or affected States provided that it designates any
such permit revisions as having been made pursuant to this paragraph.

2.	The Department shall submit a copy of the revised permit to the
Administrator.

3.	The source may implement the changes addressed in the request for an
administrative amendment immediately upon submittal of the request,
except transfer/ownership which must comply with SC Regulation 61-62.1,
Section II(E).

N.	MINOR PERMIT MODIFICATIONS [SC Regulation 61-62.70.7(e)(2)]

Minor permit modifications can be made by the Department in accordance
with SC Regulation 61-62.70.7(e)(2)(i).  An application requesting the
use of minor permit modification procedures shall meet the requirements
of SC Regulation 61-62.70.5(c) and shall include items as specified in
SC Regulation 61-62.70.7(e)(2)(ii).

The Department may modify the procedure outlined in SC Regulation
61-62.70.7(e)(2) to process groups of a source’s applications for
certain modifications eligible for minor permit modification processing.
 Group processing of minor permit applications will proceed as outlined
in SC Regulation 61-62.70.7(e)(3).

O.	SIGNIFICANT MODIFICATION PROCEDURES [SC Regulation 61-62.70.7(e)(4)]

Significant permit modification procedures shall be used for
applications requesting permit modifications listed in SC Regulation
61-62.70.7(e)(4)(i).  Significant permit modifications shall meet all
requirements of this Part 70, including those for applications, public
participation, review by affected States, and review by EPA, as they
apply to permit issuance and permit renewal.

P.	DUTY TO COMPLY [SC Regulation 61-62.70.6(a)(6)(i)]

The permittee must comply with all of the conditions of this permit.
Any permit noncompliance constitutes a violation of the SC Pollution
Control Act and/or the Federal Clean Air Act and is grounds for
enforcement action; for permit termination, revocation and reissuance,
or modification; or for denial of permit renewal application.

Q.	INSPECTION AND ENTRY [SC Regulation 61-62.70.6(c)(2)]

Upon presentation of credentials and other documents as may be required
by law, the permittee shall allow the Department or an authorized
representative to perform the following:

1.	Enter upon the permittee’s premises where a Part 70 source is
located or emissions-related activity is conducted, or where records
must be kept under the conditions of the permit.

2.	Have access to and copy, at reasonable times, any records that must
be kept under the conditions of the permit.

3.	Inspect any facilities, equipment (including monitoring and air
pollution control equipment), practices, or operations regulated or
required under this permit.

4.	As authorized by the Act and/or the SC Pollution Control Act, sample
or monitor at reasonable times substances or parameters for the purpose
of assuring compliance with the permit or applicable requirements.

R.	COMPLIANCE REQUIREMENTS [SC Regulation 61-62.70.6(c)(5)]  (Revised
05/21/99)

Consistent with SC Regulation 61-62.70.6(a)(3), this permit contains
compliance certification, testing, monitoring, reporting, and record
keeping requirements sufficient to assure compliance with the terms and
conditions of this permit.  Any document (including reports) shall
contain a certification by a responsible official or designee that meets
the requirements of SC Regulation 61-62.70.5(d).

The responsible official or designee shall certify, annually, compliance
with the conditions of this permit.  The compliance certification shall
include the following:

1.	The identification of each term or condition of the permit that is
the basis of the certification.

2.	The identification of the methods or means used for determining the
compliance status with each term and condition during the certification
period, and whether such methods or means provide continuous or
intermittent data.

3.	The status of compliance with the terms and conditions of the permit
for the period covered by the certification.

4.	Such other facts as the Department may require to determine the
compliance status of the source.

5.	All compliance certifications shall be submitted to the Administrator
as well as to the Department.

The annual compliance certification shall be sent to the Environmental
Protection Agency (EPA) and the South Carolina Department of Health and
Environmental Control - Bureau of Air Quality (SC DHEC - BAQ) at the
following addresses:

US EPA, Region 4			SC DHEC - BAQ

Air Enforcement Branch		Technical Management Section

61 Forsyth Street			2600 Bull Street

Atlanta, GA 30303			Columbia, SC 29201

S.	SCHEDULE OF COMPLIANCE [SC Regulation 61-62.70.5(c)(8)]  (Revised
5/21/99)

The permittee shall submit a compliance schedule that contains the
following for all Part 70 sources that are not in compliance with all
applicable rules:

1.	A description of the source’s compliance status and where
appropriate a compliance schedule with respect to all applicable
requirements as follows:

(a)	For applicable requirements with which the source is in compliance,
a statement that during the permit term the source will continue to
comply with such requirements.

(b)	For applicable requirements that will become effective during the
permit term, a statement that the source will meet such requirements on
a timely basis, unless a more detailed schedule is expressly required by
the applicable requirement.

(c)	A schedule of compliance for sources that are not in compliance with
all applicable requirements at the time of permit issuance.  This
schedule shall include a narrative description of how the source will
achieve compliance, a schedule of remedial measures, including an
enforceable sequence of actions with milestones, leading to compliance
with all applicable requirements.  This compliance schedule shall be at
least as stringent as that contained in any judicial consent decree or
administrative order to which the source is subject.  Any such schedule
of compliance shall be supplemental to, and shall not sanction
noncompliance with, the applicable requirements on which it is based.

2.	A schedule for submission of certified progress reports no less
frequently than every six (6) months for sources required to have a
schedule of compliance to remedy a violation.  Progress reports shall
meet the requirements of SC Regulation 61-62.70.6(c)(4)(i) and (ii).

3.	The compliance plan content requirements specified in this paragraph
shall apply and be included in the acid rain portion of a compliance
plan for an affected source, except as specifically superseded by
regulations promulgated under Title IV of the act with regard to the
schedule and method(s) the source will use to achieve compliance with
acid rain emissions limitations.

T.	NEED TO HALT OR REDUCE ACTIVITY NOT A DEFENSE

[SC Regulation 61-62.70.6(a)(6)(ii)]

It shall not be a defense for a permittee in an enforcement action that
it would have been necessary to halt or reduce the permitted activity in
order to maintain compliance with the conditions of this permit.

U.	OPERATIONAL FLEXIBILITY [SC Regulation 61-62.70.7(e)(5)]

In accordance with SC Regulation 61-62.70.7(e)(5), a permitted facility
is authorized to make changes within their facility without requiring a
permit revision, if the changes are not modifications under Title I of
the Act and the changes do not exceed the emissions allowable under this
permit.  The permitted facility shall provide the Administrator and the
Department written notification as required by SC Regulation
61-62.70.7(e)(5) at least seven (7) days prior to such changes.

PART 4.0	FACILITY WIDE REQUIREMENTS

A.	EMISSIONS LIMITS AND STANDARDS

Table 4.1 contains summaries of facility wide emission limits and
standards.

TABLE 4.1  EMISSION LIMITS AND STANDARDS

Pollutant	Limit/Standard	Regulation	State Only

Requirement	Condition Number

State New Source Review	As Specified in Attachment A	SC Regulation
61-62.1,

Section II (A)	Yes	4.B.2

4.B.3

Toxic Air Pollutants	As Specified in Attachment A	SC Regulation 61-62.5,
Std No. 8	Yes	4.B.3

Hazardous Air Pollution	Comply With Regulation	SC Regulation 61-62.4	No
N/A

Open Burning	Comply With Regulation	SC Regulation 61-62.2	No	N/A

Fugitive Emissions	Comply With Regulation	SC Regulation 61-62.6, Sec III
No	N/A

Ozone Depleting Substances	*	40 CFR Part 82, Subpart F	No	4.B.7

Asbestos	*	40 CFR Part 61.145	No	4.B.8

N/A = Not Applicable

* Specific To Subpart

The maximum allowable emission limits above are derived from the various
Federal and State regulations that govern the operation of this type of
facility.  All applicable facility wide emission limits and
corresponding regulations are listed above.  Additional operating
requirements, which may be more stringent than those above, are
contained in Part 5.0, Part 6.0, and Part 7.0 of this permit.

B.	FACILITY WIDE CONDITIONS  (Revised 11/13/98)

Condition Number	Condition

4.B.1	In accordance with SC Regulation 61-62.1, Section II, the
permittee must comply with all applicable statutes and regulations of
the United States and the State of South Carolina.  This permit does not
relieve the permittee from compliance with applicable local laws,
ordinances, and regulations.

4.B.2	Air dispersion modeling (or other method) has demonstrated that
this facility’s operation will not interfere with the attainment and
maintenance of any state or federal standard.  Any changes in the
parameters used in the air dispersion modeling may require a review by
the facility to determine continuing compliance with these standards.
These potential changes include any decrease in stack height, decrease
in stack velocity, increase in stack diameter, decrease in stack exit
temperature, increase in building height or building additions, increase
in emission rates, decrease in distance between stack and property line,
changes in vertical stack orientation, and installation of a rain cap
that impedes vertical flow.  Parameters that are not required in the
determination will not invalidate the demonstration if they are
modified.  The emission rates used in the determination are listed in
Attachment A of this permit.  Higher emission rates may be
administratively incorporated into Attachment A of this permit provided
a demonstration using these higher emission rates shows the attainment
and maintenance of any state or federal standard or with any other
applicable requirement.  Variations from the input parameters in the
demonstration shall not constitute a violation unless the maximum
allowable ambient concentrations identified in the standard are
exceeded.

4.B.3	The owner/operator shall maintain this facility in compliance with
the pollutant limitations in Part 4, Part 5, Part 6, Part 7, Part 8,
Part 9, Part 10 and/or the emission rates as listed in Attachment A of
this Part 70 operating permit, whichever is more restrictive.  This is a
State Only enforceable requirement.  Should the facility wish to
increase the emission rates listed in Attachment A, it may do so by the
administrative process specified in condition 4.B.2

4.B.4	A list of equipment which are considered insignificant pursuant to
SC Regulation 61-62.70.5(c) has been submitted with your Title V
application and reviewed by our staff.  The list, including source
descriptions and citation for exemption, is summarized in Attachment B
of the permit.  Attachment B excludes those activities identified in
Part A of the insignificant activities list.  Written notification to
the Bureau of Air Quality is required for the addition of any new
equipment which may meet the definition of insignificant or exempt as
described above, excluding those sources listed in Part A of the
insignificant activities list.  (Revised 11/13/98)

4.B.5	In accordance with SC Regulation 61-62.1 Section II, (C)(3), for
all sources not required to have continuous emissions monitors, in the
event of any malfunction of air pollution control equipment or system,
process upset or other equipment failure which results in discharges of
air contaminants lasting for one hour or more and which are greater than
those discharges described for normal operation in the permit
application shall be reported to the local Environmental Quality Control
(EQC) District office within twenty-four (24) hours after the beginning
of the occurrence.  The permittee shall also submit a written report
within thirty (30) days of the occurrence.  This report shall be
submitted to the Manager of the Technical Management Section, Bureau of
Air Quality (BAQ).  The report shall contain as a minimum, the
following:  the identity of the emission unit and associated equipment
where excess emissions occurred, the magnitude of excess emissions, the
time and duration of excess emissions, the steps taken to remedy the
malfunction and to prevent a recurrence, documentation that control
equipment and processes were at all times maintained and operated, to
the maximum extent practicable, in a manner that was consistent with
good practice for minimizing emissions.  Such a report shall in no way
serve to excuse, otherwise justify, or in any manner affect any
potential liability or enforcement action resulting from the occurrence.
This defines the Department’s definition of prompt in its relation to
the degree of reporting as specified by SC Regulation
61-62.70.6(a)(3)(iii)(b).

4.B.6	The owners or operators of Part 70 sources shall complete and
submit emissions inventories as required consistent with the schedule
approved pursuant to SC Regulation 61-62.1, Section III.  This
requirement notwithstanding, an emissions inventory may be required at
any time in order to determine the compliance status of any facility.

4.B.7	The permittee shall comply with the standards for recycling and
emissions reduction pursuant to 40 CFR Part 82, Subpart F, Protection of
Stratospheric Ozone, Recycling and Emissions Reduction, except as
provided for motor vehicle air conditioners (MVACs) in Subpart B.  If
the permittee performs a service on motor (fleet) vehicles that involves
ozone-depleting substance refrigerant in MVACs, the permittee is subject
to all applicable requirements of 40 CFR Part 82, Subpart B, Servicing
of MVACs.

4.B.8	The permittee shall comply with the standards of performance for
asbestos abatement operations pursuant to 40 CFR Part 61.145 and SC
Regulation 61-86.1, including, but not limited to, requirements
governing training, licensing, notification, work practice, cleanup, and
disposal.

(Part 5 updated 5/14/03)

PART 5.0	EMISSION UNIT REQUIREMENTS – NEW FACILITY

A.	EMISSION UNIT DESCRIPTION

Table 5.1 is a description of emission units located at this facility.

TABLE 5.1 EMISSION UNITS

Unit ID	Unit Description	Control Device Description

01	Quarry System	None

02	Raw Mill System	Baghouse

03	Coal Mill System	Baghouse

04	Kiln System	Baghouse

05	Finish Mill System	Baghouses

06	Cement Loadout	Baghouses

07	Tanks	Carbon Adsorption System (T-100, T147 though T-149), None (non
hazardous waste tanks); Industrial furnace (Kiln) and/or Carbon Adsorber
(HWDF only)

B.	CONTROL DEVICE DESCRIPTION

Table 5.2 through 5.7 list descriptions of control devices located at
this facility.

TABLE 5.2 CONTROL DEVICES UNIT ID 02 - RAW MILL SYSTEM EQUIPMENT

Control Device ID	Control Device Description	Installation Date
Pollutant(s)

Controlled

BH99	2,943 acfm Fabric Dust Collector	2003	PM

BH100	5,592 acfm Fabric Dust Collector	2003	PM

BH101	7,946 acfm Fabric Dust Collector	2003	PM

BH102	5,886 acfm Fabric Dust Collector	2003	PM

BH103	4,709 acfm Fabric Dust Collector	2003	PM

BH118	3,532 acfm Fabric Dust Collector	2003	PM

BH123	2,943 acfm Fabric Dust Collector	2003	PM

BH127	5,297 acfm Fabric Dust Collector	2003	PM

TABLE 5.3 CONTROL DEVICES UNIT ID 03- COAL MILL SYSTEM EQUIPMENT

Control Device ID	Control Device Description	Installation Date
Pollutant(s)

Controlled

BH31	2,000 acfm Pulse Jet Dust Collector	1982	PM

BH32	650 acfm Shaker Dust Collector	1980	PM

BH33	2,000 acfm Fabric Dust Collector	1980	PM

BH34	1,500 acfm Fabric Dust Collector	1980	PM

BH95	66,323 acfm Fabric Dust Collector	2003	PM

BH130	3,072 acfm Fabric Dust Collector	2003	PM

BH132	1,001 acfm Fabric Dust Collector	2003	PM

TABLE 5.4 CONTROL DEVICES UNIT ID 04 - KILN EQUIPMENT

Control Device ID	Control Device Description	Installation Date
Pollutant(s)

Controlled

BH83	8,920 acfm Pulse Jet Dust Collector	1997	PM

BH94A	873,842 acfm Fabric Dust Collector	2003	PM

BH94B	103,764 acfm Fabric Dust Collector	2003	PM

BH104	3,826 acfm Fabric Dust Collector	2003	PM

BH105	3,826 acfm Fabric Dust Collector	2003	PM

BH78	3,532 acfm Pulse Jet Dust Collector	1982	PM

BH106	6,475 acfm Fabric Dust Collector	2003	PM

BH107	10,301 acfm Fabric Dust Collector	2003	PM

BH108	4,415 acfm Fabric Dust Collector	2003	PM

BH22	13,000 acfm Pulse Dust Collector	1982	PM

BH23	1,000 acfm Pulse Jet Dust Collector	1997	PM

BH187	12,000 acfm Pulse Jet Baghouse, utilized as a product recovery
unit (PRU).	2005	PM

(page updated 9/23/03)

TABLE 5.5 CONTROL DEVICES UNIT ID 05 - FINISH MILL EQUIPMENT

Control Device ID	Control Device Description	Installation Date
Pollutant(s)

Controlled

BH54	40,000 acfm Pulse Jet Dust Collector	1982	PM

BH55	11,000 acfm Pulse Jet Dust Collector	1982	PM

BH56	3,800 acfm Pulse Jet Dust Collector	1982	PM

BH57	2,943 acfm Pulse Jet Dust Collector	1982	PM

BH96	92,421 acfm Fabric Dust Collector	2003	PM

BH97	92,421 acfm Fabric Dust Collector	2003	PM

BH175	5,886 acfm Fabric Dust Collector	2003	PM

BH115	7,063 acfm Fabric Dust Collector	2003	PM

BH117	10,301 acfm Fabric Dust Collector	2003	PM

BH119	7,063 acfm Fabric Dust Collector	2003	PM

BH120	3,532 acfm Fabric Dust Collector	2003	PM

BH135	6,475 acfm Fabric Dust Collector	2003	PM

BH114	7,063 acfm Fabric Dust Collector	2003	PM

BH116	10,301 acfm Fabric Dust Collector	2003	PM

BH121	3,532 acfm Fabric Dust Collector	2003	PM

BH126	3,532 acfm Fabric Dust Collector	2003	PM

BH136	6,475 acfm Fabric Dust Collector	2003	PM

BH146	92,421 acfm Fabric Dust Collector	2003	PM

BH147	92,421 acfm Fabric Dust Collector	2003	PM

BH174	4,415 acfm Fabric Dust Collector	2003	PM

BH169	5,300 acfm Plenum Pulse Dust Collector	1973	PM

BH170	11,000 acfm Pulse Jet Dust Collector	1982	PM

BH171	5,737 acfm Shaker Dust Collector	1966	PM

BH172	11,000 acfm Plenum Pulse Dust Collector	1970	PM

BH177	4,415 acfm Fabric Dust Collector	2003	PM

BH178	4,415 acfm Fabric Dust Collector	2003	PM

BH180	4,709 acfm Fabric Dust Collector	2003	PM

BH181	1,766 acfm Fabric Dust Collector	2003	PM

BH188	8,000 acfm Fabric Dust Collector	2005	PM/PM10

BH189	8,000 acfm Fabric Dust Collector	2005	PM/PM10

TABLE 5.6 CONTROL DEVICES UNIT ID 06- CEMENT LOADOUT EQUIPMENT

Control Device ID	Control Device Description	Installation Date
Pollutant(s)

Controlled

BH67	16,000 acfm Pulse Jet Dust Collector	1966	PM

BH68	16,000 acfm Pulse Jet Dust Collector	1966	PM

BH63	2,250 acfm Pulse Jet Dust Collector	1966	PM

BH64	1,500 acfm Pulse Jet Dust Collector	Prior to 1971	PM

BH65	2,000 acfm Pulse Jet Dust Collector	Prior to 1971	PM

BH66	1,667 acfm Shaker Dust Collector	Prior to 1971	PM

BH90	1,800 acfm Fabric Dust Collector	2003	PM

BH91	1,800 acfm Fabric Dust Collector	2003	PM

BH122	8,829 acfm Fabric Dust Collector	2003	PM

BH113	8,800 acfm Pulse Jet Baghouse	1996	PM

BH85	12,000 acfm Pulse Jet Dust Collector	1999	PM

BH86	12,000 acfm Pulse Jet Dust Collector	1999	PM

BH87	6,900 acfm Pulse Jet Dust Collector	1999	PM

BH88	4,300 acfm Pulse Jet Dust Collector	1999	PM

BH89	2,000 acfm Pulse Jet Dust Collector	1999	PM

BH144	1,825 acfm Pulse Jet Dust Collector	1999	PM

BH145	1,825 acfm Pulse Jet Dust Collector	1999	PM

BH137	6,475 acfm Fabric Dust Collector	2003	PM

BH138	7,357 acfm Fabric Dust Collector	2003	PM

BH176	2,943 acfm Fabric Dust Collector	2003	PM

BH179	12,949 acfm Fabric Dust Collector	2003	PM

BH183	8,829 acfm Fabric Dust Collector	2003	PM

BH184	2,943 acfm Fabric Dust Collector	2003	PM

TABLE 5.7 CONTROL DEVICES UNIT ID 07 - TANK EQUIPMENT

Control Device ID	Control Device Description	Installation Date
Pollutant(s)

Controlled

VRU111	Backup Carbon Adsorption System	2000	VOC

K300	Industrial Furnace (Kiln)	2003	VOC

VRU112	Backup Carbon Adsorption System	2003	VOC

CC-1	Carbon Adsorption System (Carbon Canister)	2004	VOC

CC-2	Carbon Adsorption System (Carbon Canister)	2004	VOC

C.	EQUIPMENT DESCRIPTION

A description of the equipment located at this facility is provided in
the following tables:

TABLE 5.8 UNIT ID 01 - QUARRY SYSTEM EQUIPMENT (table updated 10/22/03)

Equip ID	Installation Date	Equipment Description	Design Capacity (TPY)
Control Device ID	Exhaust Point ID

R143	2003	Marl Quarrying Equipment #1	17,380,952	None	NP8

R170

R174

R195	2003	Iron Ore Hopper to Conveyor, R170

Conveyor to Iron Ore Bin, R174

Iron Ore Stamler Feeder, R195	202,777 Each	None	NP35

NP39

NP91

R178	2003	Iron Ore Bin to Conveyor, R178	202,777 Each	None	NP43

R171

R175

R204	2003	Wet Fly Ash Hopper to Conveyor, R171

Conveyor to Wet Fly Ash Bin, R175

Fly Ash Conveyor Transfer Point, R204	1,158,730 Each	None	NP36a

NP36b

NP40

NP128

R180	2003	Wet Fly Ash Bin to Conveyor, R180	1,158,730 Each	None	NP45

R139

R140

R141

R142

R190

R191

R193	2003	Clay Hopper, R139

Clay Crusher, R140

Clay Crusher to Conveyor, R141

Clay Conveyors, R142, R190, R191, R193	1,931,230 Each	None	NP4

NP5

NP6

NP7

NP86

NP87

NP88

NP89

NP90

R155

R156

R157

R158	2003	Clay Conveyors, R155-158	1,931,230 Each	None	NP20

NP21

NP22

NP23

R159

R202

R203	2003	Clay Conveyors, R159, R202, R203	1,158,730 Each	None	NP24

NP126

NP127

R160

R161

R196

R197

R198

R199

R200

R201	2003	Marl Conveyors, R160, R161, R196-R199,

Marl Crusher, R200

Marl Crusher to Hopper, R201	17,380,952 Each	None	NP25

NP26

NP80a,NP80b

NP81a,NP81b

NP82

NP83

NP84a,NP84b

NP85

R164

R184

R205	2003	Marl Conveyors, R164, R184, R205	5,986,772 Each	None	NP29

NP49

NP42

R162

R163	2003	Pile #1 Reclaimer to Conveyor, R162

Pile #2 Reclaimer to Conveyor, R163	5,793,688 Each	None	NP27

NP28

TABLE 5.9 UNIT ID 02 - RAW MILL SYSTEM EQUIPMENT (table updated
10/22/03)

Equip ID	Installation Date	Equipment Description	Design Capacity (TPY)
Control Device ID	Exhaust Point ID

R183	2003	Clay Conveyors, R183	1,158,730 Each	None	NP48

R185	2003	Marl Conveyors, R185	5,986,772 Each	None	NP50

R179	2003	Iron Ore Bin to Conveyor, R178

Iron Ore Conveyor, R179	202,777 Each	None	NP44

R181	2003	Wet Fly Ash Bin to Conveyor, R180

Wet Fly Ash Conveyor, R181	1,158,730 Each	None	NP46

R186	2003	Raw Mill Reject Bin	4,906	None	NP51

R126	2003	Raw Mill Cyclone Separator	N/A	BH99	S99

R127	2003	Blending Silo Feed Bucket Elevator – Bottom	N/A	BH100	S100

R128	2003	Blending Silo Top	N/A	BH101	S101

R129	2003	Raw Mill Silo Withdrawal	N/A	BH102	S102

R130	2003	Kiln Feed Elevator – Top	N/A	BH103	S103

R131	2003	Dry Marl Bin	N/A	BH118	S118

R132	2003	Pump Station at Existing Silos (Fly Ash To Bin)	N/A	BH123	S123

R134	2003	Top of Existing Silos (Fly Ash)	N/A	BH127	S127

N/A = Not Applicable

TABLE 5.10 UNIT ID 03 - COAL MILL SYSTEM EQUIPMENT

Equip ID	Installation Date	Equipment Description	Design Capacity (TPY)
Control Device ID	Exhaust Point ID

C400	1980	Coal Unloading Room	N/A	BH32	S32

C401	1980	Coal Unloading Belt	N/A	BH31	S31

C402	1980	Coal Dust Silo	N/A	BH33	S33

C403	1980	Carbon Feeder	N/A	BH34	S34

C412	2003	Coal Mill Vent	N/A	BH95	S95

C413	2003	Carbon Dust Tank	N/A	BH130	S130

C414	2003	Coal Bin System Dedusting	N/A	BH132	S132

C417	2003	Coal Conveyor to Radial Stacker	3,328,800	None	NP57

C418

C419	2003	Radial Stackers to Coal/SVF Pile	1,664,400 Each	None	NP58

NP59

C421

C422

C423

C424

C425	2003	Coal/SVF Conveyors, C421, C422, C424

Coal/SVF Bin, C423

Coal/SVF Hopper, C425	402,347 Each	None	NP93

NP94

NP95

NP96

NP129

N/A = Not Applicable

(page updated 10/22/03)

TABLE 5.11 UNIT ID 04 - KILN SYSTEM EQUIPMENT

Equip ID	Installation Date	Equipment Description	Design Capacity (TPY)
Control Device ID	Exhaust Point ID

K300A	2003	Preheater/Precalciner Kiln Main	2,896,844	BH94A	S94

K300B	2003	Preheater/Precalciner Kiln Bypass	2,896,844	BH94B	S94

K301	2003	Alkali Bypass Dust Loadout	N/A	BH104	S104

K302	2003	Alkali Bypass Dust Loadout	N/A	BH105	S105

C304	1982	Common Conveyor	N/A	BH22	S22

C305	1982	Pan Conveyor North	N/A	BH23	S23

C313	1982	Belt Conveyor North Clinker Silo #4	N/A	BH78	S78

C326	1997	Clinker Reclaim Area	N/A	BH83	S83

C328	2003	Clinker Cooler Transfer Point	N/A	BH106	S106

C329	2003	Top of New Clinker Silo	N/A	BH107	S107

C330	2003	Clinker Transfer Under Existing Silos To Finish Mill #4	N/A
BH108	S108

C501	2005	Sampson Feeder System	300,000	BH187	S187

TABLE 5.12 UNIT ID 05 - FINISH MILL SYSTEM EQUIPMENT

Equip ID	Installation Date	Equipment Description	Design Capacity (TPY)
Control Device ID	Exhaust Point ID

F402	1982	#4 Finish Mill Collecting Belt to Incline Belt	NA	BH57	S57

F403	1982	#4 Finish Mill Main DC	NA	BH54	S54

F403	1982	#4 Finish Mill Classifier DC	NA	BH55	S55

F404	1982	#4 Finish Mill Fines Airslide to Cement Elevator DC	NA	BH56
S56

F726

F727

F728

F709

F710

F711

F712

F713

F714

F729

F730

F731	2003	Conveyor, F726, F727, F728, F709, F710, F711, F729, F730, F731

Pigment Bin to Conveyor, F712

Slag Bin to Conveyor, F713

Synthetic Gypsum Bin to Conveyor, F714	289,681 Each	None	NP97

NP98

NP99

NP100

NP101

NP102

NP103

NP104

NP105

NP106

NP107

NP108

F725	2003	Sugar Silo to #4 Mill Feed	1,927	None	NP74

F405	1982	#4 Finish Mill Dribble Bin	NA	BH175	S175

F700	2003	Clinker Additives Bins - Top (FM5)	NA	BH115	S115

F701	2003	Clinker/Additives Bins - Bottom  (FM5)	NA	BH116	S117

F702	2003	Finish Mill Feed End Dedusting (FM5)	NA	BH120	S120

F703	2003	Finish Mill Discharge End Dedusting (FM5)	NA	BH135	S135

F704

F732

F733	2003	Hopper to Additive Feed Belt, F704

Wet Slag/Synthetic Gypsum Conveyor Transfer Point, F732, F733	270,370
Each	None	NP79

NP109

NP110

F734

F735

F736

F715

F716

F717

F718

F719

F720

F721

F722

F737	2003	Conveyor to Wet Slag Bin, F734, F736

Conveyor to Gypsum Bin, F735, F715

Wet Slag Bin to Conveyor, F716, F720

Gypsum Bin to Conveyor, F717, F721

Conveyor Transfer, F718, F719, F722, F737	270,370	None	NP111

NP112

NP113

NP114

NP115

NP116

NP117

NP118

NP119

NP120

NP121

NP122

F705	2003	#5/#6 Finish Mill Transfer & Storage	NA	BH174	S174

F738

F739	2003	#5/#6 Transition Clinker Silo	482,804	None	NP123

NP124

F800	2003	Clinker /Additives Bins - Top (FM6)	NA	BH114	S114

F801	2003	Clinker/Additives Bins - Bottom  (FM6)	NA	BH117	S116

F802	2003	Finish Mill Feed End Dedusting (FM6)	NA	BH121	S121

F803	2003	Finish Mill Discharge End Dedusting (FM6)	NA	BH136	S136

F500	1966	Top of Finish Mill #1 Cement Silos	NA	BH171	S171

F501	1970	Top of Finish Mill #2 Cement Silos	NA	BH172	S172

F600	1973	Top of Finish Mill #3 Cement Silos	NA	BH169	S169

F601	1982	Top of Finish Mill #4 Cement Silos	NA	BH170	S170

F740	2003	Cement Feed to Cooler – FM#6	NA	BH177	S177

F741	2003	Finish Mill #5 and #6 Dribble Bin Bottom	NA	BH178	S178

F742	2003	Marl/Lime Alleviator	NA	BH180	S180

F743	2003	Dry Marl Transport From 8-Pack	NA	BH181	S181

R123A	2003	Mill Separator – FM5	N/A	BH96	S96

R123B	2003	Ball Mill – FM5	N/A	BH97	S96

R124A	2003	Mill Separator – FM6	N/A	BH146	S97

R124B	2003	Ball Mill – FM6	N/A	BH147	S97

R133	2003	New Additive System – Dry Lime	N/A	BH126	S126

O103	2003	Off-Spec Clinker Silo – Top 	N/A	BH119	S119

C324	2005	Cement Dome Bucket Elevator – Upper	N/A	BH188	S188

C325	2005	Cement Dome Bucket Elevator – Lower	N/A	BH189	S189

N/A = Not Applicable

(page updated 10/22/03)

TABLE 5.13 UNIT ID 06 - CEMENT LOADOUT EQUIPMENT

Equip ID	Installation Date	Equipment Description	Design Capacity (TPY)
Control Device ID	Exhaust Point ID

C319	2003	Cement Dome Conveyor & Collection Box	NA	BH85	S85

C320	2003	Cement Dome Alleviator	NA	BH86	S86

C321	2003	Top of Cement Dome	NA	BH87	S87

C322	2003	Cement Dome Reclaim Tower	NA	BH88	S88

(updated 10/22/03)

C323	2003	Cement Dome Surge Bin	NA	BH89	S89

C337	2003	Rail Loading Bin	NA	BH122	S122

C333	2003	Cement Transport - Post-Cooler & Elevator Bottom	NA	BH137	S137

C334	2003	Cement Transport - Elevator Top	NA	BH138	S138

B100	1988	East Packer	NA	BH67	S67

B101	1988	West Packer	NA	BH68	S68

W101	1966	#1 Truck Scale	NA	BH63	S63

W201	Prior to 1971	#2 Truck/Rail Scale	NA	BH64	S64

W301	Prior to 1971	#3 Truck/Rail Scale	NA	BH65	S65

W401	2003	#4 Truck Scale	NA	BH66	S66

W501	2003	#5 Truck Scale	NA	BH90	S90

W601	2003	#6 Truck Scale	NA	BH91	S91

W701	2003	#7 Truck Scale	NA	BH144	S144

W801	2003	#8 Truck Scale	NA	BH145	S145

W901	2003	#9 Truck Scale	NA	BH176	S176

W902	2004	Truck Load Out Silo	N/A	BH183	S183

W903	2004	Truck Load Out Silo	N/A	BH184	S184

W904	2004	Truck Load Out Silo	N/A	BH185	S185

W905	2004	Truck Load Out Silo	N/A	BH186	S186

RAI1	1996	Rainbow Products	1,314,000	BH113	S113

RAI2	1996	Rainbow Products	438,000	BH113	S113

RAI3, RAI4	1996	Rainbow Raw Material Bins, Hoppers, Weigh Belts, Mixer,
& Bag Spouts	NA	BH113	S113

V112	NA	Haul Trucks Exporting CKD	150,000	NA	NA

V200	NA	Clay Haul Trucks from Quarry to Crusher	437,600	NA	NA

V201	NA	Wet Fly Ash Haul Trucks	170,871	NA	NA

V202	NA	Dry Fly Ash Haul Trucks	151,447	NA	NA

V203	NA	Iron Ore Haul Trucks	51,416	NA	NA

V204	NA	Slag Haul Trucks	132,834	NA	NA

V205	NA	Synthetic Gypsum Haul Trucks	143,299	NA	NA

V207	NA	Lime Haul Trucks	1,659	NA	NA

V208	NA	Pigment Haul Trucks	4,630	NA	NA

V209	NA	Sugar Haul Trucks	995	NA	NA

V210	NA	Carbon Dust Haul Trucks	10,099	NA	NA

V211	NA	Tire Chips Haul Trucks	32,832	NA	NA

V212	NA	High Viscosity Oil Haul Trucks	13,006	NA	NA

V213	NA	HWDF Haul Trucks	50,000	NA	NA

V214	NA	Oxygen Haul Trucks	40,000	NA	NA

V215	NA	Bulk Cement Haul Trucks	932,930	NA	NA

V216	NA	Bagged Cement Haul Trucks	387,114	NA	NA

V217	NA	CKD Haul Trucks from Kiln to Storage	24,687	NA	NA

V218	NA	Fuel Trucks from Quarry to Garage	1,500	NA	NA

V219	NA	Rainbow Products Crushed Marble Haul Trucks	1,268	NA	NA

V220	NA	Rainbow Products Lime Haul Trucks	1,268	NA	NA

V221	NA	Haul Trucks Bringing SVF to Facility	347,250	NA	NA

V222	NA	Calcium Fluoride Haul Trucks	3,473	NA	NA

V223	NA	Mill Scale Haul Trucks	23,150	NA	NA

(page updated 9/23/03and 10/22/03)

N/A = Not Applicable

TABLE 5.14 UNIT ID 07 - TANK EQUIPMENT

Equip ID	Installation Date	Equipment Description	Design Capacity (TPY)
Control Device ID	Exhaust Point ID

T101	1974	HWDF Storage & Supply for Kilns	844,000	VRU111	S111

T102-T106	1988	HWDF Blending & Storage	39,152 (each)	VRU111	S111

T111	2003	HWDF Storage & Supply for Kilns	250,048	VRU112	S94/S128

H100	1988	HWDF Delivery System (pumps, valves, etc.)	N/A	None	N/A

T146	2003	HWDF Storage & Supply for Kilns	150,000	VRU112	S94/S128

T100	1988/modified in 2004	NHWDF

Heated Storage Tank	100,000 gal

(378.5514 m3)	Closed-Vent System and CC-1	S129

T115	1998	No. 2 Diesel Storage	12,000	None	S149

T144	2003	FM #5 & #6 Grinding Aid Tank	12,000	None	S140

T-148	2004	NHWDF

Heated Storage Tank	60,000 gal

(227.1309 m3)	Closed-Vent System and CC-1	N/A

T-147, T-148, T-149	Future	Two (2) NHWDF

Non-Heated

Storage Tanks	60,000 gal

(227.1309 m3)

Each	Closed-Vent System and CC-2	N/A

Boiler	2004	5.0 million Btu/hr natural gas fired Boiler.	--	--	N/A

N/A = Not Applicable

D.	EMISSION LIMITS AND STANDARDS

Tables 5.15 through 5.22 contain summaries of emission unit emission
limits and standards.

TABLE 5.15 EMISSION LIMITS AND STANDARDS - UNIT ID 01 QUARRY SYSTEM
EQUIPMENT

Equipment  ID	Pollutant/

Standard	Limit	Reference Method	Regulation	State Only	Condition Number

R140, R200	Opacity	15%	Method 9	40CFR60.675(4)(i)- Subpart OOO	No
5.E.1(b)

R139, R141, R142, R143, R155, R156, R157, R158, R159, R160, R161, R162,
R163, R164, R170, R171, R174, R175, R178, R180, R184, R190, R191, R193,
R195, R196, R197, R198, R199, R201, R202, R203, R204, R205	Opacity	See
condition	Method 22 Method 9	40CFR60.672(b)- Subpart OOO	No	5.E.1(c)

TABLE 5.16 EMISSION LIMITS AND STANDARDS - UNIT ID 02 RAW MILL EQUIPMENT

Equipment ID	Pollutant/

Standard	Limit	Reference Method	Regulation	State Only	Condition Number

R126, R127, R128, R129, R130, R131, R132, R134, R179, R181, R183, R185,
R186	Opacity	10%	 Method 9	40CFR63.1347, Subpart LLL	No	5.E.2(b)

(page updated 10/22/03)

TABLE 5.17 EMISSION LIMITS AND STANDARDS - UNIT ID 03 COAL MILL SYSTEM
(coal/coke crushing and processing equipment)

Equipment ID	Pollutant/

Standard	Limit	Reference Method	Regulation	State Only	Condition Number

C400, C401, C402, C403, C413, C414, C417, C418, C419, C421, C422, C423,
C424, C425	Opacity	20%	Method 9	40CFR60.252 Subpart Y	No	5.E.3(b)

C412	PM	0.031 gr/dscf	Method 5	40CFR60 Subpart Y	No	5.E.3(c)

C412	NOx 	4.48 lb NOx/ton clinker (first year) 4.33 lb NOx/ton clinker
(after first year) 	CEM	SC 61-62.5, Standard No. 7	No	5.E.3(d)

C412	CO 	8.00 lb CO/ton clinker (first year) 6.8 lb CO/ton clinker
(after first year) 	CEM	SC 61-62.5, Standard No. 7	No	5.E.3(e)

C412	VOC 	0.27 lb VOC/ton clinker 	Bureau Approved	SC 61-62.5, Standard
No. 5.1 & Standard No. 7	No	5.E.3(f)

C412	SO2 	3.26 lb SO2/ton clinker 	CEM	SC 61-62.5, Standard No. 7	No
5.E.3(g)

C412	Opacity	20%	COM or Method 9	40 CFR 60 Subpart Y, 40 CFR
63.1204(a)(7) Subpart EEE	No	5.E.3(h)

C412	Temperature	See Condition	Thermo-couple	40 CFR 60 Subpart Y	No
5.E.3(i)

TABLE 5.18 EMISSION LIMITS AND STANDARDS - UNIT ID 04 KILN SYSTEM
EQUIPMENT

Equipment ID	Pollutant/

Standard	Limit	Reference Method	Regulation	State Only	Condition Number

K300A, K300B	Opacity	20% 	COM or Method 9	40CFR

63.1204(b)(7) Subpart EEE	No	5.E.4(b)

K300A, K300B	Dioxin/Furan	0.20 ng TEQ/dscm Dioxin/Furan limit corrected
to 7% O2, or 0.40 ng TEQ/dscm Dioxin/Furan limit corrected to 7% O2 when
temp <400 (F	Method

0023A

(SW-846)	40CFR

63.1204(b)(1)

Subpart EEE	No	5.E.4(c)

K300A, K300B	PM	0.15 kg/Mg dry feed	Method 5	40CFR

63.1204(b)(7) Subpart EEE	No	5.E.4(d)

K300A, K300B	PM	56.97 lb/hr	Method 5	SC 61-62.5 Standard No. 4	No
5.E.4(e)

K300A, K300B	Ni 	0.006 lb/million BTU total heat input	Method 29	SC Reg.
61-62.5 Standard No. 3	Yes	5.E.4(f)

K300A, K300B	Cd 	1.0 E-4 lb/million BTU total heat input	Method 29	SC
Reg. 61-62.5 Standard No. 3	Yes	5.E.4(g)

K300A, K300B	Cr 	5.0 E-4 lb/million BTU total heat input	Method 29	SC
Reg. 61-62.5 Standard No. 3	Yes	5.E.4(h)

K300A, K300B	As 	2.5 E-4 lb/million BTU total heat input	Method 29	SC
Reg. 61-62.5 Standard No. 3	Yes	5.E.4(i)

K300A, K300B	Pb 	0.005 lb/million BTU total heat input	Method 29	SC Reg.
61-62.5 Standard No. 3	Yes	5.E.4(j)

K300A, K300B	HCl Emissions from the Kiln In-Line Raw Mill System	0.45 lb
HCl/million BTU total heat input	Method 26A

Method 320

Method 321	SC Reg. 61-62.5 Standard No. 3	Yes	5.E.4(k)

K300A, K300B	NOx 	4.48 lb NOx/ton clinker (first 12 months) 4.33 lb
NOx/ton clinker (after first 12 months) 	CEM	SC 61-62.5, Standard No. 7
No	5.E.4(m)

K300A, K300B	CO 	8.00 lb CO/ton clinker (first 12 months) 6.8 lb CO/ton
clinker (after first 12 months) 	CEM	SC 61-62.5, Standard No. 7	No
5.E.4(n)

K300A, K300B	VOC 	0.27 lb VOC/ton clinker 	Bureau

Approved	SC 61-62.5, Standard No. 5.1, Standard No. 7	No	5.E.4(o)

K300A, K300B	SO2 	3.26 lb SO2/ton clinker 	CEM	SC 61-62.5, Standard No.
7	No	5.E.4(p)

K301 K302 	Opacity	10% 	Method 22

Method 9	40 CFR 63.1348 Subpart LLL	No	5.E.4(q)

K300A, K300B	Benzene	(99% Destruction Efficiency	40 CFR 61.355(c)	40 CFR
61.348(a)(1)(iii) Subpart FF	No	5.E.4(s)

K300A, K300B	Clinker production 	2,462,318 short ton/yr of clinker
produced	Record keeping	SC 61-62.5, Standard No. 7	No	5.E.4(u)

K300A, K300B	Kiln Fuel Limitations	See Condition	Record keeping	SC Reg.
61-62.1 and 62.5 Standard No. 3	Yes	5.E.4(v)

K300A, K300B	Ozone	Use of low NOx burners during control period	N/A	SC
Reg. 61-62.99	No	5.E.4(w)

K300A, K300B	THC or CO Emissions	10 ppmv THC (as propane), or 100 ppmv
CO, dry basis, corrected to 7% O2	Method 25,

Method 10, CEM	40CFR

63.1204(b)(5)

 Subpart EEE	No	5.E.4(x)

K300A, K300B	Combined HCl and Cl Emissions	86 ppmv (expressed as HCl
equivalents) on a dry basis corrected to 7% O2	Method 26A, 320,or 321
40CFR

63.1204(b)(6) Subpart EEE	No	5.E.4(y)

K300A, K300B	POHC Emissions	(99.99% destruction efficiency	Method 25	SC
61-62.5, Standard No. 3	No	5.E.4(z)

K300A, K300B	POHC Emissions	(99.99% destruction efficiency	Method 25
40CFR

63.1204(c)(1) Subpart EEE	No	5.E.4(aa)

K300A, K300B	Mercury Emissions	(120 μg/dscm, corrected to 7% O2	Method
29	40CFR

63.1204(b)(1) Subpart EEE	No	5.E.4(bb)

K300A, K300B	Combined Lead & Cadmium emissions 	(180 μg/dscm, corrected
to 7% O2	Method 29	40CFR

63.1204(b)(3) Subpart EEE	No	5.E.4(cc)

K300A, K300B	Combined Arsenic, Beryllium, & Chromium emissions	(54
μg/dscm, corrected to 7% O2	Method 29	40CFR

63.1204(b)(4) Subpart EEE	No	5.E.4(dd)

K300A, K300B	Temperature	Less than Temperature in Performance Test for
APCD	As Approved	40CFR63 Subpart EEE	No	5.E.4(ee)

K300A, K300B	Temperature	>Temperature in performance test for combustion
zone chamber	As Approved	40 CFR Interim Subpart EEE	No	5.E.4(ff)

K300A, K300B	THC Emissions	See condition	CEM	Alternate Method of
Operation	No	5.E.4(gg)

C304, C305, C313, C326, C328, C329, C330, C501	Opacity	10%	Method 22

Method 9	40CFR63.1348 Subpart LLL	No	5.E.4(hh)

C501	PM	61.0 lb/hr	Method 9	SC Regulation 61-62.5, Standard 4, Section
VIII	No	5.E.4(ii)

TABLE 5.19 EMISSION LIMITS AND STANDARDS - UNIT ID 05 FINISH MILL SYSTEM
EQUIPMENT

Equipment  ID	Pollutant/

Standard	Limit	Reference Method	Regulation	State Only	Condition Number

F402, F404, F405, F500, F501, F600, F601, F700, F701, F704, F709, F710,
F711, F712, F713, F714, F715, F716, F717, F718, F719, F720, F721, F722,
F725, F726, F727, F728, F729, F730, F731, F732, F733, F734, F735, F736,
F737, F738, F739, F740, F741, F742, F743, F802, F703, F800, F801, F702,
F803, F705, R123A, R123B, R124A, R124B, R133, O103, C324, C325	Opacity
10%	Method 22

Method 9	40CFR63.1348, Subpart LLL	No	5.E.5(c)

F403	Opacity	10%	Method 22

Method 9	40 CFR 63.1347 Subpart LLL	No	5.E.5(b)

C324, C325	PM	70.1 lb/hr	Method 5	SC Regulation 61-62.5, Standard 4,
Section VIII	No	5.E.5(d)

TABLE 5.20 EMISSION LIMITS AND STANDARDS - UNIT ID 06 CEMENT LOADOUT
EQUIPMENT

Equipment  ID	Pollutant/

Standard	Limit	Reference Method	Regulation	State Only	Condition Number

B100, B101 W101, W201, W301, W401, W501, W601, W701, W801, W901, W902,
W903, W904, W905, C337, RAI1, RAI2, RAI3, RAI4, C319, C320, C321, C322,
C323, C333, C334	Opacity	10%	Method 22

Method 9	40CFR63.1348 Subpart LLL	No	5.E.6(b)

RAI1, RAI2, RAI3, RAI4	PM	0.6 lb/hr	Method 5	SC 61-62.1, II(H)	No
5.E.6(c)

RAI1, RAI2, RAI3, RAI4	Production limits	300,000 ston/yr of cement
throughput; and 100 ston/hr of unloaded raw materials	Record keeping	SC
61-62.1, II(H)	No	5.E.6 (d)

C319, C320, C321, C322, C323	PM	3.05 lb/hr	Method 5	SC 61-62.1, II(H)	No
5.E.6(e)

C319, C320, C321, C322, C323	Production limits	4,440,000 stons/yr
throughput	Record keeping 	SC 61-62.1, II(H)	No	5.E.6(f)

W902, W903, W904, W905	PM	52.8 lb/hr	Method 5	SC 61-62.5 Standard No. 4
No	5.E.6(g)

TABLE 5.21 EMISSION LIMITS AND STANDARDS - UNIT ID 07 TANKS

Equipment  ID	Pollutant/

Standard	Limit	Reference Method	Regulation	State Only	Condition Number

T101, T102, T103, T104, T105, T106, T111, T146	VOC 	95% VOC Removal
Method 21	40CFR61 Subpart FF	No	5.E.7(b)

T101, T102, T103, T104, T105, T106, T111, T146, T100, T115	Opacity	20%
Method 9	SC 61-62.5, Standard No. 4	No	5.E.7(d)

T111	VOC 	1.07 TPY	Method 21	SC 61-62.5, Standard No. 5.1, Standard No.
7	Yes (5.1), No (7)	5.E.7(e)

T101, T102, T103, T104, T105, T106, T111, T146	HWDF Tank VOC Control and
Emission Standards	No detectable VOC emissions (<500 ppmv)	Portable FID
40 CFR 61 Subpart FF	No	5.E.7(f)

T101, T102, T103, T104, T105, T106, T111, T146	Closed Vent System
Standards	No detectable VOC emissions (<500 ppmv)	Portable FID	40 CFR 61
Subpart FF	No	5.E.7(g)

T101, T102, T103, T104, T105, T106, T146	VOC	95% removal	Portable FID	40
CFR 61 Subpart FF	No	5.E.7(h)

Boiler	Opacity	20% Opacity\	Method 9	SC Regulation 61-62.5,

Standard 1, Section I	No	5.E.7(k)

Boiler	PM	0.6 lb/106 Btu Input	Method 5	SC Regulation 61-62.5,

Standard 1, Section II	No	5.E.7(l)

Boiler	SO	3.5 lb/106 Btu Input	Method 6	SC Regulation 61-62.5,

Standard 1, Section III	No	5.E.7(m)

N/A=Not Applicable

The maximum allowable emission limits above are derived from the various
Federal and State regulations that govern the operation of this type of
source.  All applicable facility wide emission limits and corresponding
regulations are listed above.  Additional operating requirements which
may be more stringent than those above are contained in Part 4.0, Part
6.0, and Part 7.0 of this permit.

E.	EMISSION UNIT CONDITIONS

5.E.1 Unit ID 01 – Quarry/Marl Handling Equipment

These sources are subject to New Source Performance Standards (NSPS), 40
CFR 60 subparts A and OOO, Standards Of Performance For Nonmetallic
Mineral Processing Plants.

(40CFR60.11(c) and 40CFR60.672(c), (d)) On and after the sixtieth day
after achieving the maximum production rate at which the affected
facility will be operated, but not later than 180 days after initial
startup as required under 40 CFR60.11, no owner or operator shall cause
to be discharged into the atmosphere from any crusher, at which a
capture system is not used, fugitive emissions which exhibit greater
than 15 percent opacity.

Truck dumping of nonmetallic minerals into any screening operation, feed
hopper, or crusher is exempt from these requirements.

(c)	(40CFR60.11(c) and 40CFR60.672(b), (d), (h)) For non-saturated
materials, on and after the sixtieth day after achieving the maximum
production rate at which the affected facility will be operated, but not
later than 180 days after initial startup as required under 40CFR60.11,
no owner or operator subject to the provisions of this subpart shall
cause to be discharged into the atmosphere from any transfer point on
belt conveyors or from any other affected facility any fugitive
emissions which exhibit greater than 10 percent opacity.

On and after the sixtieth day after achieving the maximum production
rate at which the affected facility will be operated, but not later than
180 days after initial startup, no owner or operator shall cause to be
discharged into the atmosphere any visible emissions from wet screening
operations and subsequent screening operations, bucket elevators, and
belt conveyors that process saturated material in the production line up
to the next crusher, grinding mill or storage bin.

Truck dumping of nonmetallic minerals into any screening operation, feed
hopper, or crusher is exempt from these requirements.

5.E.2 Unit ID 02 - Raw Mill Equipment

(a)	The supplementary raw mill sources are subject to the National
Emission Standards for Hazardous Air Pollutants for Affected Source
Categories, 40 CFR 63 Subparts A and LLL, National Emission Standards
for Hazardous Air Pollutants from the Portland Cement Manufacturing
Industry.  Since the raw mill is part of the in-line kiln/raw mill, the
raw mill is subject to 40 CFR 63 Subparts A and EEE, National Emission
Standards for Hazardous Air Pollutants from Hazardous Waste Combustors,
and emissions limitations for it will be covered under 5.E.4.

(b)	(40CFR63.1347, 40 CFR63.1348) The owner or operator of each new or
existing raw mill or finish mill at a facility which is a major source
subject to the provisions of this subpart shall not cause to be
discharged from the mill sweep or air separator air pollution control
devices of these affected sources any gases which exhibit opacity in
excess of ten percent.

The owner or operator of each new or existing raw material, clinker, or
finished product storage bin; conveying system transfer point; bagging
system; and bulk loading or unloading system; and each existing raw
material dryer, at a facility which is a major source subject to the
provisions of this subpart shall not cause to be discharged any gases
from these affected sources which exhibit opacity in excess of ten
percent.

5.E.3 Emissions Limits from the Coal Mill Equipment

(a)	These sources are subject to New Source Performance Standards
(NSPS), 40 CFR 60 subparts A and Y, Standards Of Performance For Coal
Preparation Plants.  Since the coal mill utilizes part of the kiln
exhaust gases for drying in the vertical roller mill, the coal mill is
subject to the National Emission Standards for Hazardous Air Pollutants
for Affected Source Categories, 40 CFR 63 Subparts A and EEE, National
Emission Standards for Hazardous Air Pollutants from Hazardous Waste
Combustors.

(b)	(40CFR60.252(c)) On and after the date on which the performance test
required to be conducted by 40CFR60.8 is completed, an owner or operator
subject to the provisions of this subpart shall not cause to be
discharged into the atmosphere from any coal processing and conveying
equipment, coal storage system, or coal transfer and loading system
processing coal, gases which exhibit 20 percent opacity or greater.

(40CFR60 Subpart Y) On and after the date on which the performance test
required to be conducted by §60.8 is completed, an owner or operator
subject to the provisions of this subpart shall not cause to be
discharged into the atmosphere from any thermal dryer gases which
contain particulate matter in excess of 0.070 g/dscm (0.031 gr/dscf).

(d)	(SC Regulation 61-62.5, Standard No. 7) NOx emissions from the kiln,
in-line raw mill system and coal mill are limited to 4.48 lb NOx / ton
clinker (first year) and 4.33 lb NOx / ton clinker (after first year) 30
day rolling average - sum of both the main kiln stack and the coal mill
stack.

(SC Regulation 61-62.5, Standard No. 7) CO emissions from the kiln,
in-line raw mill system and coal mill are limited to 8.00 lb CO / ton
clinker (first year) and 6.8 lb CO / ton clinker (after first year) 30
day rolling average - sum of both the main kiln stack and the coal mill
stack.

(SC Regulation 61-62.5, Standard No. 5.1, Standard No. 7) VOC emissions
from the kiln, in-line raw mill system and coal mill are limited to 0.27
lb VOC / ton clinker 3 hr block average - sum of both the main kiln
stack and the coal mill stack.

(SC Regulation 61-62.5, Standard No. 7) SO2 emissions from the kiln,
in-line raw mill system and coal mill are limited to 3.26 lb SO2 / ton
clinker 30 day rolling average - sum of both the main kiln stack and the
coal mill stack.

(40 CFR 60.252(a2), 40CFR63.1204(b)(7)) On and after the date on which
the performance test required to be conducted by 40 CFR60.8 is
completed, an owner or operator subject to the provisions of this
subpart shall not cause to be discharged into the atmosphere from any
thermal dryer gases which exhibit 20 percent opacity or greater.   The
owner or operator must not discharge or cause combustion gases to be
emitted into the atmosphere that contain opacity greater than 20
percent.

(40 CFR 60.253) The owner or operator of any thermal dryer shall
install, calibrate, maintain, and continuously operate a monitoring
device for the measurement of the temperature of the gas stream at the
exit of the thermal dryer on a continuous basis. The monitoring device
is to be certified by the manufacturer to be accurate within ±1.7°C
(±3°F). All monitoring devices of this section are to be recalibrated
annually in accordance with procedures under 40 CFR 60.13(b).

5.E.4 Emissions Limits from the Kiln In-Line Raw Mill System Equipment

(a)	These sources are subject to the National Emission Standards for
Hazardous Air Pollutants for Affected Source Categories, 40 CFR 63
Subparts A and EEE, National Emission Standards for Hazardous Air
Pollutants from Hazardous Waste Combustors.  Per 40 CFR 63.1340(b)(1),
the in-line kiln/raw mill are not subject to 40 CFR 63 Subpart LLL,
National Emission Standards for Hazardous Air Pollutants from the
Portland Cement Manufacturing Industry.  The clinker handling sources
are subject to the National Emission Standards for Hazardous Air
Pollutants for Affected Source Categories, 40 CFR 63 Subparts A and LLL,
National Emission Standards for Hazardous Air Pollutants from the
Portland Cement Manufacturing Industry.

(b)	(40CFR63.1204(b)(7)) The owner or operator must not discharge or
cause combustion gases to be emitted into the atmosphere that contain
opacity greater than 20 percent.

(40CFR63.1204(b)(1)) Dioxin/Furan emissions from the combination of the
kiln stack and the coal mill stack shall not exceed 0.20 ng TEQ/dscm
corrected to 7% oxygen, or dioxin/furan emissions from the kiln shall
not exceed 0.40 ng TEQ/dscm corrected to 7% oxygen provided that the
combustion gas temperature at the inlet to the initial dry particulate
matter control device is less than or equal to 204(C (400 (F) based on
the average of the test run average temperatures.

(40CFR63.1204(b)(7)) Particulate Matter emissions from the combination
of the kiln stack and the coal mill stack shall not exceed 0.15 kg/Mg
dry feed.

These processes are subject to particulate matter emission limitations
from SC Regulation 61-62.5, Standard No. 4.  The emission limitation is
determined as listed below for all process equipment except for the
equipment that is included in the main kiln system and associated stack.

For process weight rates up to 30 tons per hour:

E = (4.10) (P 0.67)

For process weight rates of greater than 30 tons per hour:

E = (55.0) (P0.11) - 40

Where:  E = the allowable emission rate in pounds per hour

  P = process weight rate in tons per hour

For the kiln system the PM emission limitation is 56.97 lb/hr when
operating at full capacity. The averaging time for these emission
limitations is three hours.

(SC Regulation 61-62.5 Standard No. 3) Ni emissions from the kiln
in-line raw mill system shall not exceed 0.006 lb Ni/million BTU total
heat input.

(SC Regulation  61-62.5 Standard No. 3) Cd emissions from the kiln
in-line raw mill system shall not exceed 1.0 E-4 lb Cd/million BTU total
heat input.

(SC Regulation 61-62.5 Standard No. 3) Cr emissions from the kiln
in-line raw mill system shall not exceed 5.0 E-4 lb Cr/million BTU total
heat input.

(SC Regulation 61-62.5 Standard No. 3) As emissions from the kiln
in-line raw mill system shall not exceed 2.5 E-4 lb As/million BTU total
heat input.

(SC Regulation 61-62.5 Standard No. 3) Pb emissions from the kiln
in-line raw mill system shall not exceed 5.0 E-3 lb Pb/million BTU total
heat input.

(SC Regulation 61-62.5 Standard No. 3) HCl emissions from the kiln
in-line raw mill system shall not exceed 0.45 lb HCl/million BTU total
heat input.

These sources are subject to S.C. Reg 61-62.5 Standard No. 5.1, VOC
LAER.  For these sources, VOC LAER is determined to be process
optimization.

(SC Regulation 61-62.5, Standard No. 7) NOx emissions from the kiln
in-line raw mill system shall not exceed 4.48 lb/ton of clinker during
the first 12 months of commercial operation.  After the first 12 months
of commercial operation, 30 day rolling average of NOx emissions from
the kiln in-line raw mill system and coal mill stack shall not exceed
4.33 lb/ton of clinker.

The emission limitation for NOx is based on the site-specific raw
material properties, fuel usage and design of the system.  The Bureau
shall review the raw material testing, Continuous Emission Monitor data,
and any other pertinent information periodically (beginning after the
first two years of commercial operation).  Upon review, the NOx emission
limitation and/or the NOx averaging time may be adjusted downward if
deemed appropriate by the Bureau.  The intent of this condition is not
to remove operational and process flexibility from Holcim, but to show a
realistic permit limit relative to actual operation.

(SC Regulation 61-62.5, Standard No. 7) CO emissions from the kiln
in-line raw mill system shall not exceed 8.00 lb/ton of clinker during
the first 12 months of commercial operation.  After the first 12 months
of commercial operation, 30 day rolling average of CO emissions from the
kiln in-line raw mill system and coal mill stack shall not exceed 6.8
lb/ton of clinker.

The emission limitation for CO is based on the use of bottom and fly ash
as a source of alumina to the cement process.  If in the future, the raw
material changes or the carbon content of the ash substantially
decreases, the emission limitations in this permit for CO may be
reviewed and revised as appropriate.  In no event shall revised CO
emission limitations allow greater emissions than the limitations
listed.

(SC Regulation 61-62.5, Standard No. 5.1, Standard No. 7) 3-hr block
average VOC emissions shall not exceed 0.27 lb/ton of clinker from the
sum of both main the kiln stack and the coal mill stack tested
simultaneously or ratioed appropriately.

(SC Regulation 61-62.5, Standard No. 7) 30-day rolling average SO2
emissions shall not exceed 3.26 lb/ton of clinker from the sum of both
the main kiln stack and the coal mill.

(40CFR63.1348) The owner or operator of each new or existing raw
material, clinker, or finished product storage bin; conveying system
transfer point; bagging system; and bulk loading or unloading system;
and each existing raw material dryer, at a facility which is a major
source subject to the provisions of this subpart shall not cause to be
discharged any gases from these affected sources which exhibit opacity
in excess of ten percent.

The kiln system is used both as the primary control device for the HWDF
burn tank (T111) and the treatment process for the benzene containing
waste received at the facility.

(40 CFR 61.348(a)(1)(iii)) The owner or operator shall design, install,
operate, and maintain a treatment process that destroys benzene from the
waste stream by incinerating the waste in a combustion unit that
achieves a destruction efficiency of 99% or greater for benzene.

This source is subject to SC Regulation 62.5 Standard No. 7.  Upon
review, BACT for this source is determined to be:

NOx- Low NOx burners, Burner Optimization, Kiln Optimization, Multistage
Combustion

CO - Process Optimization

VOC - Process Optimization

Per SC Regulation 61-62.5, Standard No. 7, this source is limited to a
maximum production rate of 2,462,318 short tons per year of clinker.
Holcim must record the actual monthly production rates and maintain
these records on-site for a period of at least five (5) years from the
date generated.  The facility shall also maintain daily clinker
production records for the calculation of the NOx, CO, and SO2
emissions.  These records shall be made available to Department
personnel upon request. Annual reports including all recorded parameters
and calculated values including the annual clinker production rate shall
be submitted to the Manager of the Technical Management Section, Bureau
of Air Quality postmarked no later than 30 calendar days after the end
of the reporting period.  These conditions shall not supersede any State
or Federal requirements such as National Emission Standards for
Hazardous Air Pollutants, unless these conditions would impose a more
restrictive limit.

The kiln will be allowed to burn various types of fuel due to high
temperatures and long residence times including:

(v)(1)	Hazardous waste derived fuel (HWDF) which will be burned at the
burner of the rotary kiln only;

(v)(2)	Tire derived fuel (TDF) which will be burned in the precalciner;

(v)(3)	Non-hazardous liquid fuels which will be burned in the rotary
kiln burner, precalciner burner and 61MW hot gas generator.

(v)(4)	No RCRA coded D/F containing wastes shall be combusted in the
kiln.

(v)(5)	Other types of fuel may also be used as approved by the Bureau.
These requests shall be submitted to the Division of Engineering
Services for review.

Any waste materials as defined by SC Regulation 61-62.1 shall have a
waste analysis performed as required by SC Regulation 61-62.5, Standard
3.

For the control period that begins on May 31, 2004, an owner or operator
of any Portland cement kiln subject to SC Regulation 61-62.99 shall not
operate the kiln during May 31 through September unless the kiln has
installed and operates during May 31 to September 30 with low- NOx
burners, mid-kiln firing, or alternative control techniques, as defined
under section 99.42(a). In all subsequent control periods, an owner or
operator of any Portland cement kiln subject to this rule shall not
operate the kiln during May 1 through September 30 unless the kiln has
installed and operates during May 1 to September 30 with low-NOx
burners, mid-kiln firing, or alternative control techniques, as defined
under section 99.42(a).

(40CFR63.1204(b)(5)) For kilns equipped with a by-pass duct or mid-kiln
gas sampling system, carbon monoxide and hydrocarbon emissions are
limited in both the bypass duct or midkiln gas sampling system and the
main kiln stack as follows.  Emissions in the by-pass or midkiln gas
sampling system are limited to either:

(x)(1)	Carbon monoxide in excess of 100 ppmv, over an hourly rolling
average (monitored continuously with a continuous emissions monitoring
system,) dry basis and corrected to 7 percent oxygen.  If the permittee
elects to comply with this carbon monoxide standard rather than the
hydrocarbon standard under paragraph (aa)(2) of this section, the
permittee also must document that, during the destruction and removal
efficiency (DRE) test runs or their equivalent as provided by 40CFR
63.1206(b)(7), hydrocarbons do not exceed 10 ppmv during those runs,
over an hourly rolling average (monitored continuously with a continuous
emissions monitoring system), dry basis, corrected to 7 percent oxygen,
as reported as propane; or

(x)(2) Hydrocarbons in the by-pass duct or midkiln gas sampling system
in excess of 10 parts per million by volume, over an hourly rolling
average (monitored continuously with a continuous emissions monitoring
system), dry basis, corrected to 7 percent oxygen, and reported as
propane.

(40CFR63.1204(b)(6)) Combined HCl & Cl2, expressed as HCl equivalents,
shall not exceed 86 ppmv on a dry basis corrected to 7% O2 when burning
hazardous waste.  The alternate method of operation listed in Part
7.0(B) of this permit does not impose a limit for HCl & Cl2 emissions
when non-hazardous fuels are being used.

(SC 61-62.5, Standard No. 3(III)(L)(2)) All principal organic hazardous
constituents (POHC) must be destroyed with an efficiency of at least
99.99% when burning hazardous waste.

(40CFR63.1204(c)(1)) The Permittee must achieve a destruction and
removal efficiency (DRE) of 99.99% for each principal organic hazardous
constituent (POHC) designated under the next two paragraphs of this
permit condition.  The Permittee must calculate DRE for each POHC from
the following equation:

DRE = [1-(Wout / Win)] x 100%

Where:

Win  = mass feedrate of one POHC in a waste feedstream; and

Wout = mass emission rate of the same POHC present in exhaust emissions
prior to release to the atmosphere.

The Permittee must treat the POHCs in the waste feed that the permittee
specifies under the next paragraph of this permit condition to the
extent required by the first paragraph of this permit condition.

The Permittee must specify one or more POHCs from the list of hazardous
air pollutants established by 42 U.S.C. 7412(b)(1), excluding
caprolactam (CAS number 105602) as provided by 40CFR63.60, for each
waste to be burned.  The Permittee must base this specification on the
degree of difficulty of incineration of the organic constituents in the
waste and on their concentration or mass in the waste feed, considering
the results of the waste analyses or other data and information.

μg / dscm, corrected to 7% oxygen, when burning hazardous waste.

(40CFR63.1204(b)(3)) The sum of Pb & Cd emissions (semivolatile metals)
from the kiln in-line raw mill system shall not exceed 180 μg/dscm,
corrected to 7% oxygen, when burning hazardous waste.

(40CFR 63.1204(b)(4)) The sum of As, Be, & Cr emissions (low volatile
metals) from the kiln in-line raw mill system shall not exceed 54
μg/dscm, corrected to 7% oxygen, when burning hazardous waste.

(40CFR63.1209(k)(1)) For hazardous waste burning incinerators and cement
kilns, if the combustor is equipped with an electrostatic precipitator,
baghouse (fabric filter), or other dry emissions control device where
particulate matter is suspended in contact with combustion gas, the
permittee must establish a limit on the maximum temperature of the gas
at the inlet to the device on an hourly rolling average. The permittee
must establish the hourly rolling average limit as the average of the
test run averages.

(ff)	(40 CFR 63.1209(k)(2)) The Permittee must measure the temperature
of each combustion chamber at a location that best represents, as
practicable, the bulk gas temperature in the combustion zone. The
Permittee must document the temperature measurement location in the test
plan the permittee submitted under §§63.1207(e) and (f); the permittee
must establish a minimum hourly rolling average limit as the average of
the test run averages. The alternate method of operation listed in Part
7.0(B) of this permit does not impose a limit for combustion zone
chamber temperature when non-hazardous fuel(s) are being used.

(gg)	The Permittee has incorporated an Alternate Method of Operation for
an occasion in which only non-hazardous fuel(s) are being supplied to
the kilns.  The Alternate Method of Operation, located in Part 7.0(B) of
this permit, does not impose a limit for THC when only non-hazardous
fuel(s) are being used.

(hh)	(40CFR63.1348, Subpart LLL) The owner or operator of each new or
existing raw material, clinker, or finished product storage bin;
conveying system transfer point; bagging system; and bulk loading or
unloading system; and each existing raw material dryer, at a facility
which is a major source subject to the provisions of this subpart shall
not cause to be discharged any gases from these affected sources which
exhibit opacity in excess of ten percent.

(ii)	The Sampson Feeder System is subject to particulate matter emission
limitations from SC Regulation 61-62.5, Standard No. 4.  The emission
limitation is determined as listed below.

For process weight rates of greater than 30 tons per hour:

E = (55.0) (P0.11) - 40

Where:  E = the allowable emission rate in pounds per hour

  P = process weight rate in tons per hour

For the Sampson Feeder System the PM emission limitation is 61.0 lb/hr
when operating at full capacity at 250 tons per hour.

5.E.5 Emissions Limits for the Finish Mill System Equipment

(a)	The finish mill sources are subject to the National Emission
Standards for Hazardous Air Pollutants for Affected Source Categories,
40 CFR 63 Subparts A and LLL, National Emission Standards for Hazardous
Air Pollutants from the Portland Cement Manufacturing Industry.

(40CFR63.1347, Subpart LLL) The owner or operator of each new or
existing raw mill or finish mill at a facility which is a major source
subject to the provisions of this subpart shall not cause to be
discharged from the mill sweep or air separator air pollution control
devices of these affected sources any gases which exhibit opacity in
excess of ten percent.

(40CFR63.1348, Subpart LLL) The owner or operator of each new or
existing raw material, clinker, or finished product storage bin;
conveying system transfer point; bagging system; and bulk loading or
unloading system; and each existing raw material dryer, at a facility
which is a major source subject to the provisions of this subpart shall
not cause to be discharged any gases from these affected sources which
exhibit opacity in excess of ten percent.

(d)	These processes are subject to particulate matter emission
limitations from SC Regulation 61-62.5, Standard No. 4.  The emission
limitation is determined as listed below.

For process weight rates of greater than 30 tons per hour:

E = (55.0) (P0.11) - 40

Where:  E = the allowable emission rate in pounds per hour

  P = process weight rate in tons per hour

For the Cement Dome Bucket Elevator the PM emission limitation is 70.1
lb/hr when operating at full capacity at 550 tons per hour.

5.E.6 Emissions Limits for the Cement Loadout Equipment

(a)	The cement loadout sources are subject to the National Emission
Standards for Hazardous Air Pollutants for Affected Source Categories,
40 CFR 63 Subparts A and LLL, National Emission Standards for Hazardous
Air Pollutants from the Portland Cement Manufacturing Industry.

(40CFR63.1348, Subpart LLL) The owner or operator of each new or
existing raw material, clinker, or finished product storage bin;
conveying system transfer point; bagging system; and bulk loading or
unloading system; and each existing raw material dryer, at a facility
which is a major source subject to the provisions of this subpart shall
not cause to be discharged any gases from these affected sources which
exhibit opacity in excess of ten percent.

(SC Regulation 61-62.1, II (H))  PM emissions from the Rainbow products
line shall not exceed 0.6 lb/hr.

(SC Regulation 61-62.1, II (H)) Cement throughput from the Rainbow
Process Line (RAI1, RAI2, RAI3, RAI4) must not exceed 300,000 ston/yr.
Unloaded raw materials must not exceed 100 ston/hr.  The facility shall
maintain daily production records and shall make such records available
to Department personnel upon request.

(SC Regulation 61-62.1, II (H))  PM emissions from the cement dome
sources shall not exceed 3.05 lb/hr.

(SC Regulation 61-62.1, II (H)) Cement throughput from the Cement Dome
(C319, C320, C321, C322, C323) must not exceed 4,440,000 stons/yr. The
facility shall maintain daily throughput records and make such records
available to Department personnel upon request.

These processes are subject to particulate matter emission limitations
from SC Regulation 61-62.5, Standard No. 4.  The emission limitation is
determined as listed below.

For process weight rates of greater than 30 tons per hour:

E = (55.0) (P0.11) - 40

Where:  E = the allowable emission rate in pounds per hour

  P = process weight rate in tons per hour

For the Truck Load Out Silos the PM emission limitation is 52.8 lb/hr
when operating at full capacity at 116.2 tons per hour.

5.E.7 Emissions Limits for the Tanks

(a)	The HWDF tanks and closed vent system, including control devices,
are subject to all applicable provisions of 40 CFR Part 61 Subpart A
(General Provisions), Subpart V (National Emission Standard for
Equipment Leaks (Fugitive Emission Sources)), and Subpart FF (National
Emission Standard for Benzene Waste Operations); and 40 CFR Part 63
Subpart A (General Provisions) and Subpart DD (National Emission
Standards for Hazardous Air Pollutants from Off-Site Waste and Recovery
Operations).

(40CFR61.349(a)(2)(ii)) For each closed-vent system and control device
used to comply with standards in accordance with 40 CFR 61.343 through
40 CFR 61.348, the owner or operator shall properly design, install,
operate, and maintain the control device in accordance with the
following requirements: A vapor recovery system (e.g., a carbon
adsorption system or a condenser) shall recover or control the organic
emissions vented to it with an efficiency of 95 weight percent or
greater, or shall recover or control the benzene emissions vented to it
with an efficiency of 99 weight percent or greater.

(40CFR60 Subpart Kb)  The tanks and closed vent system, including
control devices, are subject to all applicable provisions of 40 CFR Part
60 Subpart A (General Provisions) and Subpart Kb (Standards of
Performance for VOL Storage Vessels).

In accordance with SC Regulation 61-62.5, Standard No. 4 - Emissions
from Process Industries, Section IX - Visible Emissions (Where Not
Specified Elsewhere), where construction or modification began after
December 31, 1985, emissions (including fugitive emissions) shall not
exhibit an opacity greater than 20%.

(SC Regulation 61-62.5, Standard No. 5.1, Standard No. 7) VOC emissions
for the HWDF Tank (T111) shall not exceed 1.07 ton/yr.

The HWDF tanks shall be equipped and controlled as required by 40 CFR
61.343 in regards to the following:

(1)	The tank shall be covered by a fixed roof as defined in
40CFR61.343(a)(1) and vented directly through a closed-vent system to a
control device in accordance with 40CFR61.349.

(2)	The cover and all openings shall be designed to be operated with no
detectable emission as indicated by an instrument reading of less than
500 ppmv above background as determined initially and thereafter at
least once per year by the methods specified in 40CFR61.355(h).

The closed vent system per 40CFR61.349 (a)(1) and shall be designed to
be operated with no detectable emission as indicated by an instrument
reading of less than 500 ppmv above background as determined initially
and thereafter at least once per year by the methods specified in
40CFR61.355(h).

The control device shall be designed and operated in accordance with
40CFR61.349(a)(2). The vapor recovery system (carbon adsorber) shall
control the organic emissions vented to it with an efficiency of 95
weight percent or greater.

These tanks are subject to LAER requirements (SC Regulation 61-62.5,
Standard No. 5.1) and PSD requirements (SC Regulation 61-62.5, Standard
No. 7).  LAER and BACT have been determined to be a vapor balance line
with the emissions vented through a closed vent system to control
devices with at least a 95% efficiency.

(k)	As per SC Regulation 61-62.5 Standard 1 Section I - Visible
emissions from the Boiler shall not exhibit an opacity that exceeds 20%.
This visible emissions limit does not apply during periods of startup,
shutdown and malfunction.

(l)	As per SC Regulation 61-62.5 Standard 1 Section II Particulate
matter emissions from the Boiler shall not exceed 0.6 lb/million Btu
heat input.

(m)	As per SC Regulation 61-62.5 Standard 1 Section III SO2 emissions
from the Boiler shall not exceed 3.5 lb/million Btu heat input.

5.E.8 Facility Wide Emissions Limits

(40CFR63.6(e)(1)(i), Subpart A) Operation and Maintenance (O&M)
Requirements:  At all times, including periods of startup, shutdown, and
malfunction, owners or operators shall operate and maintain any affected
source, including associated air pollution control equipment, in a
manner consistent with good air pollution control practices for
minimizing emissions at least to the levels required by all relevant
standards.

(40CFR63.6(e)(3)(i), Subpart A)  Startup, Shutdown, and Malfunction
(SSM) Plan:  The owner or operator of an affected source shall develop
and implement a written startup, shutdown, and malfunction plan that
describes, in detail, procedures for operating and maintaining the
source during periods of startup, shutdown, and malfunction and a
program of corrective action for malfunctioning process and air
pollution control equipment used to comply with the relevant standard.
As required under Sec. 63.8(c)(1)(i), the plan shall identify all
routine or otherwise predictable CMS malfunctions.  This plan shall be
developed by the owner or operator by the sources( compliance date for
that relevant standard.  The plan shall be incorporated by reference
into the sources( Title V permit.  Also, per 40 CFR 63, Interim Subpart
EEE, (40 CFR 63 (c)(2)(B)) the SSM Plan needs to be submitted to the
Administrator for review and approval.

(SC Regulation 61-62.5, Standard 4, Section IX – Visible Emissions
(Where Not Specified Elsewhere) Where construction or modification began
on or before December 31, 1985, emissions (including fugitive emissions)
shall not exhibit an opacity greater than 40%.  Where construction or
modification began after December 31, 1985, emissions (including
fugitive emissions) shall not exhibit an opacity greater than 20%.

(SC Regulation 61-62.5, Standard 4, Section X – Non-Enclosed
Operations)

All non-enclosed operations shall be conducted in such a manner that a
minimum of particulate matter becomes airborne.  In no case shall
established ambient air quality standards be exceeded at or beyond the
property line.

The owner or operator of all such operations shall maintain dust control
of the premises and any roadway owned or controlled by the owner or
operator by paving or other suitable measures.  Oil treatment is
prohibited.

All crushing, drying, classification and like operations shall employ a
suitable control device acceptable to the Department, and shall
discharge no more particulate matter than that specified in Section VIII
of SC Regulation 61-62.5, Standard 4.

(Part 6 updated 5/14/03)

PART 6.0	MONITORING AND REPORTING REQUIREMENTS – NEW FACILITY

[SC Regulation 61-62.1, Section II]; [SC Regulation
61-62.70.6(a)(3)(i)(B)]

A.	MONITORING AND REPORTING

Table 6.1 contains summaries of the monitoring and reporting required of
this facility.

TABLE 6.1 MONITORING AND REPORTING – UNIT ID 01-07 GENERAL

Unit ID	Pollutant/ Parameter	Limit	Required Monitoring	Monitoring
Frequency	Reporting Frequency	Condition Number

02-06	Initial Notice of Intent to Comply with MACT Standards	N/A
Reporting	N/A	One-time initially	6.B.1(a)

02-06	Notification of Compliance Status with MACT Standards	N/A
Reporting	60 days after compliance demonstration	Every 5 years	6.B.1(b)

02-07	Compliance/Performance Testing Summary Report	N/A	Reporting,
Recordkeeping	Semi-annually	Semi-annually	6.B.1(c)

02-07	SSM Reporting	N/A	Reporting	See Condition	See Condition	6.B.1(d)

02-07	Immediate SSM Reports	N/A	Reporting	See Condition	See Condition
6.B.1(e)

02-07	Operation & Maintenance Plan	N/A	Reporting	N/A	See Condition
6.B.1(f)

02-07	General Reporting Requirements	N/A	Reporting	See Condition	See
Condition	6.B.1(g)

02-07	General Recordkeeping Requirements	N/A	Recordkeeping	See Condition
See Condition	6.B.1(h)

02-07	Air Pollution Control Device Operation & Maintenance Program	N/A
Recordkeeping	As Performed	As Requested by DHEC	6.B.1(i)

02-07	General PC MACT Notification Requirements	N/A	Reporting	N/A	See
Condition	6.B.1(j)

01-07	Submittal of Reports to DHEC	N/A	Reporting	N/A	As Required by DHEC
6.B.1(k)

01-07	Failure to Comply with O&M Plan	N/A	Recordkeeping	N/A	As Required
by DHEC	6.B.1(l)

07	Leak Detection and Repair Program	N/A	Reporting, Recordkeeping	Per
Approved LDAR Program	Per Approved LDAR Program	6.B.1(m)

01-07	Source Test Protocol	N/A	Reporting	N/A	One time	6.B.1(n)

02-07	Exemption From NSPS Requirements	N/A	N/A	N/A	N/A	6.B.1(o)

04	Raw material parameters	N/A	Monitoring, Reporting, Recordkeeping	See
Condition	See Condition	6.B.1(p)

04	Applicability of 40 CFR 63 Interim Subpart EEE (HWC MACT) to Kiln
System	N/A	See Condition	See Condition	See Condition	6.B.1(q)

04	Changes in Design, Operation, or Maintenance of Kiln System	N/A	N/A
N/A	N/A	6.B.1(r)

04	Emergency Safety Vent Operating Plan and Failure Provisions	N/A
Reporting, Recordkeeping	N/A	Within 5 days of ESV opening that results
in emission limit failure	6.B.1(s)

03-04	Certified Operator Training for Waste Fuel Usage	N/A	N/A	N/A	N/A
6.B.1(t)

N/A = Not Applicable

TABLE 6.2 MONITORING AND REPORTING – UNIT ID 01 QUARRY SYSTEM

Unit ID	Pollutant/ Parameter	Limit	Required Monitoring	Monitoring
Frequency	Reporting Frequency	Condition Number

01

Quarry	General Reporting Requirements	N/A	Reporting	See Condition	See
Condition	6.B.2(a)

01

Quarry	Opacity Monitoring of Quarry Equipment	10% Opacity for transfer
points and 15% Opacity for crushers	Method 9	Once within 180 days after
startup of quarry	Once after conclusion of Method 9 testing	6.B.2(b)

TABLE 6.3 MONITORING AND REPORTING – UNIT ID 02 RAW MILL SYSTEM

Stack ID	Unit Description	Pollutant/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

S99	Raw Mill Transfer Point	Visible Emissions Monitoring	No visible
emissions	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.3(a)

S100	Blending Silo Feed Bucket Elevator - Bottom	Visible Emissions
Monitoring	No visible emissions	1-minute Method 22	Monthly; if no
visible emissions for 6 consecutive months, then semi-annually; if no
visible emissions for semi-annual test, then annually	Semi-annually
6.B.3(a)

S101	Blending Silo Top	Visible Emissions Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, then annually	Semi-annually	6.B.3(a)

S102	Raw Mill Silo Withdrawal	Visible Emissions Monitoring	No visible
emissions	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.3(a)

S103	Kiln Feed Elevator Top	Visible Emissions Monitoring	No visible
emissions	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.3(a)

S118	Dry Marl Bin	Visible Emissions Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, then annually	Semi-annually	6.B.3(a)

S123	Fly Ash Receiving Station	Visible Emissions Monitoring	No visible
emissions	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.3(a)

S127	Top of Fly Ash Receiving Silos	Visible Emissions Monitoring	No
visible emissions	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.3(a)

S99	Raw Mill Transfer Point	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-annually 	6.B.3(a)

S100	Blending Silo Feed Bucket Elevator - Bottom	Opacity Monitoring	10%
Opacity	6-minute Method 9	No later than 1 hour after visible emissions
observed during a Method 22 if the equipment continues to operate
Semi-annually 	6.B.3(a)

S101	Blending Silo Top	Opacity Monitoring	10% Opacity	6-minute Method 9
No later than 1 hour after visible emissions observed during a Method 22
if the equipment continues to operate	Semi-annually 	6.B.3(a)

S102	Raw Mill Silo Withdrawal	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-annually 	6.B.3(a)

S103	Kiln Feed Elevator Top	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-annually 	6.B.3(a)

S118	Dry Marl Bin	Opacity Monitoring	10% Opacity	6-minute Method 9	No
later than 1 hour after visible emissions observed during a Method 22 if
the equipment continues to operate	Semi-annually 	6.B.3(a)

S123	Fly Ash Receiving Station	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-annually 	6.B.3(a)

S127	Top of Fly Ash Receiving Silos	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-annually
6.B.3(a)

S94	Roller Mill Emission Limitations	N/A	See Condition 6.B.5	See
Condition 6.B.5	See Condition 6.B.5	See Condition 6.B.5	6.B.3(b)

N/A	Traffic Fugitives	PM	No Fugitive Limit	N/A	N/A	N/A	6.B.3(c)

TABLE 6.4 MONITORING AND REPORTING – ID 03 COAL MILL SYSTEM

Stack ID	Unit Description	Pollutant/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

S31	Coal Unloading Belt	General Monitoring and Reporting Requirements
N/A	Reporting	As indicated by each applicable requirement of 40 CFR 60
Semi-annually	6.B.4(a)

S32	Coal Unloading Room	General Monitoring and Reporting Requirements
N/A	Reporting	As indicated by each applicable requirement of 40 CFR 60
Semi-annually	6.B.4(a)

S33	Carbon Dust Silo	General Monitoring and Reporting Requirements	N/A
Reporting	As indicated by each applicable requirement of 40 CFR 60
Semi-annually	6.B.4(a)

S34	Carbon Feeder	General Monitoring and Reporting Requirements	N/A
Reporting	As indicated by each applicable requirement of 40 CFR 60
Semi-annually	6.B.4(a)

S130	Carbon Dust Unloading	General Monitoring and Reporting Requirements
N/A	Reporting	As indicated by each applicable requirement of 40 CFR 60
Semi-annually	6.B.4(a)

S132	Coal Bin System Dedusting	General Monitoring and Reporting
Requirements	N/A	Reporting	As indicated by each applicable requirement
of 40 CFR 60	Semi-annually	6.B.4(a)

S31	Coal Unloading Belt	Opacity	20%	Visual Inspection	Monthly
Semi-annually	6.B.4(b)

S32	Coal Unloading Room	Opacity	20%	Visual Inspection	Monthly
Semi-annually	6.B.4(b)

S33	Carbon Dust Silo	Opacity	20%	Visual Inspection	Monthly	Semi-annually
6.B.4(b)

S34	Carbon Feeder	Opacity	20%	Visual Inspection	Monthly	Semi-annually
6.B.4(b)

S130	Carbon Dust Unloading	Opacity	20%	Visual Inspection	Monthly
Semi-annually	6.B.4(b)

S132	Coal Bin System Dedusting	Opacity	20%	Visual Inspection	Monthly
Semi-annually	6.B.4(b)

S95	Coal Mill	Opacity Monitoring	20% Opacity	COM or 30-minute Method 9
when COM is offline	Continuous monitoring or daily when COM is offline
See condition	6.B.4(c)

S95	Coal Mill	PM Emission Monitoring	0.031 gr/dscf	Method 5 Reference
Test	Every 2.5 years	Every 2.5 years	6.B.4(d)

S95	Coal Mill	Temperature	N/A	Thermo-couple	Continuously	Semi-annually
6.B.4(e)

S95	Coal Mill	VOC	See 5.E.4(o)	Bureau Approved	Every 2.5 years 	Every
2.5 years	6.B.4(f)

S95	Coal Mill	NOx, SO2, CO	see 5.E.4(m), (n), (p)	CEM	Continuous
Quarterly	6.B.4(g)

S31, S32, S95, S130, S132	Coal Preparation Plant NSPS Applicability	N/A
N/A	N/A	N/A	N/A	6.B.4(h)

S95	Applicability of 40 CFR 63 Interim Subpart EEE (HWC MACT)	N/A	N/A
N/A	N/A	N/A	6.B.4(i)

TABLE 6.5 MONITORING AND REPORTING – ID 04 KILN SYSTEM

Stack ID	Unit Description	Pollutant/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

S22	Clinker Reclaim Stamler	Visible Emissions Monitoring	No visible
emissions	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; 	Semi-annually	6.B.5(a)

S23	Pan Conveyor North	Visible Emissions Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; 	Semi-annually	6.B.5(a)

S78	#4 Clinker Silo	Visible Emissions Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; 	Semi-annually	6.B.5(a)

S83	Clinker Reclaim Area	Visible Emissions Monitoring	No visible
emissions	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; 	Semi-annually	6.B.5(a)

S22	Clinker Reclaim Stamler	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-Annual	6.B.5(a)

S23	Pan Conveyor North	Opacity Monitoring	10% Opacity	6-minute Method 9
No later than 1 hour after visible emissions observed during a Method 22
if the equipment continues to operate	Semi-Annual	6.B.5(a)

S78	#4 Clinker Silo	Opacity Monitoring	10% Opacity	6-minute Method 9	No
later than 1 hour after visible emissions observed during a Method 22 if
the equipment continues to operate	Semi-Annual	6.B.5(a)

S83	Clinker Reclaim Area	Opacity Monitoring	10% Opacity	6-minute Method
9	No later than 1 hour after visible emissions observed during a Method
22 if the equipment continues to operate	Semi-Annual	6.B.5(a)

C501	Sampson Feeder System	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-Annual	6.B.5(a)

S104	Alkali Bypass Dust Loadout - Elevator	Visible Emissions Monitoring
No visible emissions	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; 	Semi-annually	6.B.5(a)

S105	Alkali Bypass Dust Loadout - Tank	Visible Emissions Monitoring	No
visible emissions	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; 	Semi-annually	6.B.5(a)

S106	Clinker Cooler Transfer Point	Visible Emissions Monitoring	No
visible emissions	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; 	Semi-annually	6.B.5(a)

S107	New Clinker Silo Top	Visible Emissions Monitoring	No visible
emissions	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; 	Semi-annually	6.B.5(a)

S108	Clinker Transfer Under Existing Silos	Visible Emissions Monitoring
No visible emissions	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; 	Semi-annually	6.B.5(a)

C501	Sampson Feeder System	Visible Emissions Monitoring	No visible
emissions	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; 	Semi-annually	6.B.5(a)

S104	Alkali Bypass Dust Loadout - Elevator	Opacity Monitoring	10%
Opacity	6-minute Method 9	No later than 1 hour after visible emissions
observed during a Method 22 if the equipment continues to operate
Semi-Annual	6.B.5(a)

S105	Alkali Bypass Dust Loadout - Tank	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.5(a)

S106	Clinker Cooler Transfer Point	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.5(a)

S107	New Clinker Silo Top	Opacity Monitoring	10% Opacity	6-minute Method
9	No later than 1 hour after visible emissions observed during a Method
22 if the equipment continues to operate	Semi-Annual	6.B.5(a)

S108	Clinker Transfer Under Existing Silos	Opacity Monitoring	10%
Opacity	6-minute Method 9	No later than 1 hour after visible emissions
observed during a Method 22 if the equipment continues to operate
Semi-Annual	6.B.5(a)

S94	Preheater/ Precalciner Kiln	Opacity Monitoring	20% Opacity	COM or
30-minute Method 9 when COM is offline	Continuous monitoring or daily
when COM is offline	Quarterly	6.B.5(b)

S94	Preheater/ Precalciner Kiln	Dioxin/Furan Monitoring	0.20 ng TEQ @ 7%
O2 or 0.40 ng TEQ @ 7% O2 if avg. temp  400 F	Method 0023A
(SW-846)	Initially and every 2.5 years thereafter 	Quarterly	6.B.5(c)

S94	Preheater/ Precalciner Kiln	PM Emission Monitoring	0.15 kg/Mg (0.30
lb/ton)

56.97 lb/hr	Method 5	Every 2.5 years	Quarterly	6.B.5(d)

S94	Preheater/ Precalciner Kiln	Inlet APCD Temperature Monitoring
Determine during compliance performance test	Thermo-couple	Continuous
monitoring	Semi-annual	6.B.5(e)

All	Kiln System Sources	General Reporting Requirements	N/A	Reporting	See
condition	See condition	6.B.5(f)

S94	Preheater/ Precalciner Kiln	General Benzene Waste Requirements	N/A
Reporting, Monitoring	See condition	See condition	6.B.5(g)

S94	Preheater/ Precalciner Kiln	Benzene Waste Monitoring	DRE>99%	N/A	N/A
N/A	6.B.5(h)

S94	Preheater/ Precalciner Kiln	Minimum Combustion Zone Temperature
Determine during compliance performance test	Temperature	Continuous	N/A
6.B.5(i)

S94	Preheater/ Precalciner Kiln	Vent stream location changes	N/A
Reporting	N/A	For each occurrence	6.B.5(j)

S94	Preheater/ Precalciner Kiln	Raw material content	See Condition
Reporting	See Condition	Semi-annually	6.B.5(k)

S94	Preheater/ Precalciner Kiln	Quarterly COMs Reporting	N/A	COM
Continuous	Quarterly	6.B.5(l)

S94	Preheater/ Precalciner Kiln	Standard No. 3 Waste Feed Rate	N/A	CMS
Continuous	Exceedances reported quarterly	6.B.5(m)

S94	Preheater/ Precalciner Kiln	Kiln System Plan Reporting	N/A	Reporting
N/A	Prior to operation	6.B.5(n)

S94	Preheater/ Precalciner Kiln	NOx, SO2, CO CEMS	5.E.4(m, n, p)	CEM
Continuous	Quarterly	6.B.5(o)

S94	Preheater/ Precalciner Kiln	Emission Limits and Requirements During
Kiln Venting to Coal Mill	6.B.5	See Condition	See Condition	See
Condition	6.B.5(p)

S94	Preheater/ Precalciner Kiln	 Production rate	2,462,318 ston
clinker/yr	 Record keeping	Daily	Semi-Annual	6.B.5(q)

S94	Preheater/ Precalciner Kiln	Initial Compliance Demonstration	40CFR
63.1349 (b) and 63.7	See Condition	See Condition	See Condition	6.B.5(r)

S94	Preheater/ Precalciner Kiln	Combustion System Inspection	N/A
Monitoring	Annually	Semi-Annually	6.B.5(s)

S94	Preheater/ Precalciner Kiln	HWDF System Control Device Recordkeeping
Requirements	N/A	Record-keeping	N/A	N/A	6.B.5(t)

S94	Preheater/ Precalciner Kiln	Kiln Source Testing – Ni, Cd, Cr, As,
Pb, HCl, POHC, DRE, PM, CO, O2	SC Reg. 61-62.5 Standard No. 3
Monitoring, Reporting	Every 2.5 years 	Every 2.5 years 	6.B.5(u)

S94	Preheater/ Precalciner Kiln	PM Emission Calculations for the Kiln	40
CFR 63.1204 (a) (7)(ii)	N/A	N/A	N/A	6.B.5(v)

S94	Preheater/ Precalciner Kiln	Kiln DRE Standard	at least 99.99% for
each POHC	N/A	Initial	N/A	6.B.5(w)

S94	Preheater/ Precalciner Kiln	Applicability of HWC MACT During SSM
Conditions	N/A	N/A	N/A	N/A	6.B.5(x)

S94	Preheater/ Precalciner Kiln	Hazardous Waste Residence Time
Calculations	N/A	Reporting, Record-keeping	N/A	Each time a notification
of compliance is submitted	6.B.5(y)

S94	Preheater/ Precalciner Kiln	Operating Requirements for Kiln	N/A	N/A
N/A	Record keeping	6.B.5(z)

S94	Preheater/ Precalciner Kiln	SSM Plan for Hazardous Waste Combustor
N/A	Record-keeping	N/A	Record keeping	6.B.5(aa)

S94	Preheater/ Precalciner Kiln	Automatic Waste Feed Cutoff System
Requirements	N/A	Visual Inspection and System Testing	Weekly alarm
checks; monthly cutoff system operability checks	Record keeping
6.B.5(bb)

S94	Preheater/ Precalciner Kiln	Control of Combustion System Leaks	Kiln
Delta P<Ambient P	N/A	N/A	Record keeping	6.B.5(cc)

S94	Preheater/ Precalciner Kiln	O&M Plan for Hazardous Waste Combustor
N/A	Record-keeping	N/A	Record keeping	6.B.5(dd)

S94	Preheater/ Precalciner Kiln	THC Emissions In Alkali Bypass Stack	10
ppm	CEM	Continuous	Quarterly	6.B.5(ee)

S94	Preheater/ Precalciner Kiln	Opacity	20% Opacity	COM or 30-minute
Method 9 when COM is offline	Monitoring daily when COM is offline
Quarterly	6.B.5(ff)

S94	Preheater/ Precalciner Kiln	Kiln Feedstream Analysis	N/A	See
Condition	See Condition	Record keeping	6.B.5(gg)

S94	Preheater/ Precalciner Kiln	DRE, D/F, Hg, PM, Semi-and low volatile
metals, HCl, Cl and max. combustion chamber pressure	40 CFR 63.1209
(EEE)	See Condition	See Condition	Record keeping	6.B.5(hh)

S94	Preheater/ Precalciner Kiln	See Condition	40 CFR 63.1210 (EEE)
Notification	See Condition	N/A	6.B.5(ii)

S94	Preheater/ Precalciner Kiln	See Condition	40 CFR 63.1211

(EEE)	Record-keeping and Reporting	See Condition	See condition	6.B.5(jj)

TABLE 6.6 MONITORING AND REPORTING – ID 05 FINISH MILL SYSTEM

Stack ID	Unit Description	Pollutant/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

All	All Finish Mill Equipment	General PC MACT Requirements	N/A	N/A	N/A
Semi-annually	6.B.6(a)

S55	#4 Finish Mill Classifier	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test	Semi-annually	6.B.6(b)(2)

S56	#4 Finish Mill Fines Classifier	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test	Semi-annually	6.B.6(b)(2)

S57	#4 Finish Mill Collector Belt	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test	Semi-annually	6.B.6(b)(2)

S54	#4 Finish Mill	Visible Emission Monitoring	No visible emissions
6-minute Method 22

If visible emission is observed, perform follow-up Method 22 test within
24 hours	Daily	Semi-annual	6.B.6(b)(3)

S96	#5 Finish Mill Separator and Baghouse	Visible Emission Monitoring	No
visible emissions 	6-minute Method 22

If visible emission is observed, perform follow-up Method 22 test within
24 hours	Daily	Semi-annual	6.B.6(b)(3)

S97	#6 Finish Mill Separator and Baghouse	Visible Emission Monitoring	No
visible emissions 	6-minute Method 22

If visible emission is observed, perform follow-up Method 22 test within
24 hours	Daily	Semi-annual	6.B.6(b)(3)

S55	#4 Finish Mill Classifier	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-Annual	6.B.6(b)(2)

S56	#4 Finish Mill Fines Classifier	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

S57	#4 Finish Mill Collector Belt	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

S54	#4 Finish Mill	Opacity Monitoring	10% Opacity	30-minute Method 9
Initially and every 5 years thereafter	Semi-annually	6.B.6(b)(1)

S96	#5 Finish Mill Separator and Baghouse	Opacity Monitoring	10% Opacity
30-minute Method 9	Initially and every 5 years thereafter	Semi-annually
6.B.6(b)(1)

S97	#6 Finish Mill Separator and Baghouse	Opacity Monitoring	10% Opacity
30-minute Method 9	Initially and every 5 years thereafter	Semi-annually
6.B.6(b)(1)

C324	Cement Dome Bucket Elevator - Upper	Opacity Monitoring	10% Opacity
30-minute Method 9	Initially and every 5 years thereafter	Semi-annually
6.B.6(b)(1)

C325	Cement Dome Bucket Elevator - Lower	Opacity Monitoring	10% Opacity
30-minute Method 9	Initially and every 5 years thereafter	Semi-annually
6.B.6(b)(1)

S114	#6 Finish Mill Clinker/ Additives Bins - Top	Visible Emission
Monitoring	No visible emissions 	1-minute Method 22	Monthly; if no
visible emissions for 6 consecutive months, then semi-annually; if no
visible emissions for semi-annual test, then annually	Semi-annually
6.B.6(b)(2)

S115	#5 Finish Mill Clinker/ Additives Bins - Top	Visible Emission
Monitoring	No visible emissions 	1-minute Method 22	Monthly; if no
visible emissions for 6 consecutive months, then semi-annually; if no
visible emissions for semi-annual test, then annually	Semi-annually
6.B.6(b)(2)

S116	#6 Finish Mill Clinker/ Additives Bins - Bottom	Visible Emission
Monitoring	No visible emissions 	1-minute Method 22	Monthly; if no
visible emissions for 6 consecutive months, then semi-annually; if no
visible emissions for semi-annual test, then annually	Semi-annually
6.B.6(b)(2)

S117	#5 Finish Mill Clinker/ Additives Bins - Bottom	Visible Emission
Monitoring	No visible emissions 	1-minute Method 22	Monthly; if no
visible emissions for 6 consecutive months, then semi-annually; if no
visible emissions for semi-annual test, then annually	Semi-annually
6.B.6(b)(2)

S120	#5 Finish Mill Feed End Dedusting	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S121	#6 Finish Mill Feed End Dedusting	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S135	#5 Finish Mill Discharge End Dedusting	Visible Emission Monitoring
No visible emissions 	1-minute Method 22	Monthly; if no visible
emissions for 6 consecutive months, then semi-annually; if no visible
emissions for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S136	#6 Finish Mill Discharge End Dedusting	Visible Emission Monitoring
No visible emissions 	1-minute Method 22	Monthly; if no visible
emissions for 6 consecutive months, then semi-annually; if no visible
emissions for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S169	Top of Finish Mill #3 Silos	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S170	Top of Finish Mill #4 Silos	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S171	Top of Finish Mill #1 Silos	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S172	Top of Finish Mill #2 Silos	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S174	#5 & #6 Finish Mill Hopper Dedusting	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S175	#4 Finish Mill Dribble Bin	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S180	Marl/Lime Alleviator	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S119	Off Spec Clinker Silo – Top 	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S126	New Additive System – Dry Lime	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S177	Cement Feed to Cooler – FM#6	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S178	Finish Mill #5/#6 Dribble Bin	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S181	Dry Marl Transport from 8-pack	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

C324	Cement Dome Bucket Elevator - Upper	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

C325	Cement Dome Bucket Elevator - Lower	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, then annually	Semi-annually	6.B.6(b)(2)

S114	#6 Finish Mill Clinker/ Additives Bins - Top	Opacity Monitoring	10%
Opacity	6-minute Method 9	No later than 1 hour after visible emissions
observed during a Method 22 if the equipment continues to operate
Semi-Annual	6.B.6(b)(2)

S115	#5 Finish Mill Clinker/ Additives Bins - Top	Opacity Monitoring	10%
Opacity	6-minute Method 9	No later than 1 hour after visible emissions
observed during a Method 22 if the equipment continues to operate
Semi-Annual	6.B.6(b)(2)

S116	#6 Finish Mill Clinker/ Additives Bins - Bottom	Opacity Monitoring
10% Opacity	6-minute Method 9	No later than 1 hour after visible
emissions observed during a Method 22 if the equipment continues to
operate	Semi-Annual	6.B.6(b)(2)

S117	#5 Finish Mill Clinker/ Additives Bins - Bottom	Opacity Monitoring
10% Opacity	6-minute Method 9	No later than 1 hour after visible
emissions observed during a Method 22 if the equipment continues to
operate	Semi-Annual	6.B.6(b)(2)

S120	#5 Finish Mill Feed End Dedusting	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

S121	#6 Finish Mill Feed End Dedusting	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

S135	#5 Finish Mill Discharge End Dedusting	Opacity Monitoring	10%
Opacity	6-minute Method 9	No later than 1 hour after visible emissions
observed during a Method 22 if the equipment continues to operate
Semi-Annual	6.B.6(b)(2)

S136	#6 Finish Mill Discharge End Dedusting	Opacity Monitoring	10%
Opacity	6-minute Method 9	No later than 1 hour after visible emissions
observed during a Method 22 if the equipment continues to operate
Semi-Annual	6.B.6(b)(2)

S169	Top of Finish Mill #3 Silos	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-Annual	6.B.6(b)(2)

S170	Top of Finish Mill #4 Silos	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-Annual	6.B.6(b)(2)

S171	Top of Finish Mill #1 Silos	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-Annual	6.B.6(b)(2)

S172	Top of Finish Mill #2 Silos	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-Annual	6.B.6(b)(2)

S174	#5 & #6 Finish Mill Hopper Dedusting	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

S175	#4 Finish Mill Dribble Bin	Opacity Monitoring	10% Opacity	6-minute
Method 9	No later than 1 hour after visible emissions observed during a
Method 22 if the equipment continues to operate	Semi-Annual	6.B.6(b)(2)

S180	Marl/Lime Alleviator	Opacity Monitoring	10% Opacity	6-minute Method
9	No later than 1 hour after visible emissions observed during a Method
22 if the equipment continues to operate	Semi-Annual	6.B.6(b)(2)

S119	Off Spec Clinker Silo – Top 	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

S126	New Additive System – Dry Lime	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

S177	Cement Feed to Cooler – FM#6	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

S178	Finish Mill #5/#6 Dribble Bin	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

S181	Dry Marl Transport from 8-pack	Opacity Monitoring	10% Opacity
6-minute Method 9	No later than 1 hour after visible emissions observed
during a Method 22 if the equipment continues to operate	Semi-Annual
6.B.6(b)(2)

TABLE 6.7 MONITORING AND REPORTING – ID 06 CEMENT LOADOUT SYSTEM

Stack ID	Unit Description	Pollutant/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

S63	#1 Truck Scale	Visible Emission Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S64	#2 Truck/Rail Scale	Visible Emission Monitoring	No visible emissions
	1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S65	#3 Truck/Rail Scale	Visible Emission Monitoring	No visible emissions
	1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S66	#4 Truck Scale	Visible Emission Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S67	East Packer	Visible Emission Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S68	West Packer	Visible Emission Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S85	Cement Dome Conveyor and Collection Box	Visible Emission Monitoring
No visible emissions 	1-minute Method 22	Monthly; if no visible
emissions for 6 consecutive months, then semi-annually; if no visible
emissions for semi-annual test, 	Semi-annually	6.B.7(a)

S86	Cement Dome Alleviator	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, 	Semi-annually	6.B.7(a)

S87	Cement Dome Top	Visible Emission Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S88	Cement Dome Reclaim Tower	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, 	Semi-annually	6.B.7(a)

S89	Cement Dome Surge Bin	Visible Emission Monitoring	No visible
emissions 	1-minute Method 22	Monthly; if no visible emissions for 6
consecutive months, then semi-annually; if no visible emissions for
semi-annual test, 	Semi-annually	6.B.7(a)

S90	#5 Truck Scale	Visible Emission Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S91	#6 Truck Scale	Visible Emission Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S113	Rainbow Products	Visible Emission Monitoring	No visible emissions
1-minute Method 22	Monthly; if no visible emissions for 6 consecutive
months, then semi-annually; if no visible emissions for semi-annual
test, 	Semi-annually	6.B.7(a)

S122	Cement Transport to Rail Loading Bin	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, 	Semi-annually	6.B.7(a)

S137	Cement Transport Elevator Bottom	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, 	Semi-annually	6.B.7(a)

S138	Cement Transport Elevator Top	Visible Emission Monitoring	No
visible emissions 	1-minute Method 22	Monthly; if no visible emissions
for 6 consecutive months, then semi-annually; if no visible emissions
for semi-annual test, 	Semi-annually	6.B.7(a)

S144	#7 Rail Scale	Visible Emission Monitoring	No visible emissions