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## ) Startup, Shutdown andMalfunction Plan InAccordancewith Brick and StructuralClay NationalEmission Standardfor Hazardous AirPollutants

BillTudor For
BORALBRICKS TERRE HAUTE FACILITY TERREHAUTE, INDIANA

LAST REVISED

February2008



# • Responsible Official Signature
Regional Production Manager Date 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1

- 1 1 1 1 1 1 1 1 1Revision to SSMP: 

# ) Original SMMP Date ofRevision Reason for Revision February2008



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### SECTION 1.0- INTRODUCTION Boral Bricks Terre Haute Plant

This Startup, Shutdown, and Malfunction Plan (SSMP) has been developed to meet the requirements found in the National Emission Standard for Hazardous Air Pollutants (NESHAP) codified in 40 CFR Part 63, Subpart A {§63.6(e)}, Subpart JJJJJ {§63.8420(c)}and Section D.3.13 ofthe current permit, T 167-23205-00139. This SSMP covers the tunnel kiln (EU02), which is the affected source in the Subpart JJJJJ, and the Hellmich dry hydrated lime injection baghouse system CDOl (DIFF). At all times, including periods ofstartup, shutdown, and malfunction, Boral Bricks Terre Haute (Boral Bricks) will operate and maintain any air pollution control equipment and monitoring equipment that is used to meet the standard in a manner consistent with safety and good air pollution control practices for minimizing emissions to the levels required by the relevant standards (i.e., meet the emission standard or complywith the SSMP). Determination ofwhether such operation and maintenanceprocedures are being used will bebased on information thatmay include, but is not limited to, monitoring results, review of operation and maintenance procedures (e.g. the SSMP), review ofoperation and maintenance records, and inspection ofthe source. Malfunctions will be corrected as soon as practicable after their occurrence in accordance with this SSMP. To the extent that an unexpected event arises during a startup, shutdown, or malfunction, Boral Bricks will comply by minimizing emissions during such a startup, shutdown, and malfunction event consistent with safety and good air pollution control practices. Theremainder ofthis document summarizes the procedures that will be followed during periods when the kiln and control device are being started, shutdown, and during malfunctions. Boral Bricks must record each start-up, shutdown, or malfunction period and document any additional information required by the regulation. Examples offorms that can be used for these instances havebeen included in this SSMP.

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### SECTION 2.0- PURPOSE Boral Bricks Terre Haute Plant

Under 40 CFR 63.6(e), Boral Bricks is required to develop and implement for the Terre Haute kiln and control device a written SSMP that describes, in detail: (1) procedures for operating and maintaining the source during periods of startup, shutdown, and malfunction; (2) a program of corrective action for malfunctioning process; and (3) the air pollution control and monitoring equipmentused to comply with the relevant standard. The purpose ofthe SSMP is to: (A) Ensure that, at all times, Boral Bricks operates and maintains air pollution control and monitoring equipment in a manner consistent with safety and good air pollution control practices for minimizing emissions to the levels requiredbythe relevant standards; (B) Ensure that Boral Bricks is prepared to correct malfunctions as soon as practicable after their occurrence in orderto minimize excess emissions ofhazardous air pollutants; and (C) Reduce the reporting burden associated with periods ofstartup, shutdown, and malfunction (including corrective action taken to restore malfunctioning process and air pollution control equipmentto its normal orusual manner ofoperation).

Page 2 of47 BoralTerre Haute SSMP Feb 2008 Revision 0- Feb. 2008Startup, Shutdown andMalfunction Plan Boral Bricks Terre Haute Plant 

### ) SECTION 3.0- REGULATORY ANALYSIS



## )
_/ The general regulatoryrequirements citedbelow are addressed inthis plan:

3.1 e: §§63.6(e)(3) of Subpart A, General Provisions and 63.8420(c) of Subpart JJJJJ requires that Boral Bricks develop and implement a SSMP for operations used to comply with the Brick and Structural Clay NESHAP. This SSMP is intended to meet the requirements for Boral Bricks Terre Haute kiln operations.

i'l §63.6(e)(3) of Subpart A, General Provisions, requires Boral Bricks to describe the corrective action that will be taken if a malfunction occurs at an affected process, air pollution control device or monitoring equipment.

i'l In addition to the requirements to develop and implement a written SSMP, Boral Bricks is also required under §63.6(e)(3)(vii) to perform the following activities or functions: Keep records ofany malfunction event that occurs and keep records ofthe actions taken to minimize emissions during the event. Submit reports ifprocedures taken during the event are not consistent with the procedures that are included inthe SSMP and excess emissions occurred. Revise the SSMP ifa malfunction occurs that has not been described within this SSMP orprocedures for corrective actionhave notbeen adequately described. Update the plan if requested by EPA or the appropriate State or Local Air Pollution Control Authority.
Definition of"Malfunction" During the course of normal operations, Boral Bricks may experience malfunction events. Please be aware that facilities may use a different definition ofthe term "malfunction" than the regulatory definition. The General Provisions define a "malfunction" as: Any sudden, infrequent, and not reasonably preventable failure of air pollution control and monitoring equipment, process equipment, or a process to operate in a normal or usual manner which causes, or has the potential to cause, the emission limitations in an applicable standard to be exceeded. (§63.2). As stated above, a malfunction, as defined under Part 63, must have the potential to cause an exceedance in the emission limitations of the standard. This plan, however, is designed to document all upsets and to determine whether or not theymeet the definition ofa "malfunction" under the rule.

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Boral Bricks also has a separate plan for routine maintenance ofthe Terre Haute kiln process equipment and control device covered under the Brick and Structural Clay NESHAP that is called our Operating, Monitoring, and Maintenance Plan (OMMP). According to our OMMP, routine maintenance operations must be performed in accordance with the equipment manufacturer's specifications and recommendations, as well as the procedures specific to Boral Bricks that are detailed in our OMMP.

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# ) Startup, Shutdown and Malfunction Plan BoralBricks Terre Haute Plant

SECTION 4.0- AFFECTED SOURCES AND CONTROL DEVICES This plan covers the following devices: General Description: Affected Source: Capture/Control/Monitoring Device ID: BriefDescription ofSystem: Terre Haute Tunnel Kiln Controlled by Dry Hydrated Lime Injection Baghouse TerreHaute Tunnel Kiln (EU02) Dry Hydrated Lime Injection Baghouse System CDOI (DIFF)
The Terre Haute tunnel kiln is a landfill gas with natural gas backup kiln designed to produce 26 tons offired brick perhour. Due to the site-wide potential emissions ofHF, HCl and total HAP, the Boral Bricks complex is a major source ofHAP. The Terre Haute tunnel kiln was constructed after the promulgation date ofJuly 22, 2002, and thus the kiln must comply with the "new source MACT requirements" that are contained in 40 CFR Part 63, Subpart JJJJJ. The existing source MACT requirements require the kiln to meet the following limits: HF- 90% control or 0.057lb/ton (0.029 kg/Mg) HCl

- 85% control or 0.056 lb/ton (0.028 kg/Mg) PM- 0.12 lb/ton (O.XXkg/Mg) (Method 5 filterable PM) VE: No Visible Emissions per Method 22
Boral Bricks Terre Haute elected to add a Hellmich dry injection baghouse system (DIFF) in order to complywith the above limits
.

Page 5 of47 BoralTerre Haute SSMP Feb 2008 Revision 0- Feb. 2008Startup, Shutdown and Malfunction Plan Boral Bricks Terre Haute

5.0 PROCEDURES FOR STARTUP, SHUTDOWNS, & MALFUNCTIONS
This section includes a description of Boral Terre Haute standard procedures for starting the tunnel kiln (EU02), and reagent injection baghouse system, shutting down the kiln and reagent injection baghouse system, and for dealing with malfunctions that occur. For the purposes of this plan, the malfunctions include only those incidents that have the potential to cause an exceedance ofthe emission or operatinglimits. These situations would include: o A situation that causes the emissions from Kiln 1 (EU02) to bypass the control device (DIFF) bevented directlyto the atmosphere; and o A situation that causes the reagent injection baghouse system to fail, thus increasing emissions above the NESHAP limits. o Anoccurrence that causes the operating limits to be exceeded. o Failure ofthe electronic monitoring system. In general, the focus ofourprocedures is to protectboththe integrityofthe control system and reduce the emissions to the atmosphere. Boralbelieves that both are critical to ensuringthe long-term emissionreduction ability ofthe system. In addition, the safetyofplantpersonnel and visitors is always the first priority. ) To balancethese, Boral follows the following general principles:
• The exhaust from the kiln is vented through the control device whenthe stack temperature is within the acceptablerange. Venting at too low a temperature could cause moisture to enter the system and causethe lime to solidify. Venting at too high a temperature could damage thebagswhich would lead to visible and gaseous emissions. [It shouldbe noted that Boral usesbags appropriate for the expected temperatureranges to be encountered].
• There mustbe a clearpaththoughthe system for the exhaust to bevented through the control. Exhausting whenthere is no clearpath (e.g., dampers closed to all cleaning modules) would damage the control, creatingpotential safetyissues and potentially damagingthe integrity ofthe cleaningprocess.
• Thelimefeed into the control is continuous, unless feeding additional lime could damage the system. For example, the lime flow wouldbehalted ifthere is not sufficient flow sincethe lime needs sufficient air flow to keep the particles suspended and to avoid blockages. All ofthese principles were considered when the procedures were developed. This plan includes three procedure for start-up, a regular shutdown procedure, an emergency shutdownprocedure (i.e., "hard shutdown") and numerous malfunction scenarios. Page 6 of47 BoralTerre Haute SSMP Feb 2008 Revision 0- Feb. 2008

## ) BORAL BRICKS Terre Haute

SECTION 5.1- STARTUP PROCEDURES This section describes the start-up procedures for the Lingl kiln and the Hellmich DIFF. The kiln is due to startup in February 2008. The Hellmich DIFF will bebrought online initiallywhile thekilnwas in operation (when the temperature ofthe flue gas is intheright temperaturerange). The standard start-up procedure for the kiln and control device is described onthe following page. This same general procedure is followed for each start-up ofthe control/kiln. However, some steps are skipped ifpreviously completed. In general, there are three possible start-up scenarios that could occur: • Cold kiln, cold control. As stated above, this scenario has yet to occur since the control was started while thekiln was "hot." Theprocedure onthe nextpage is based on a "cold kiln/cold control" start. • Hotkiln, cold control. Theprocedure onthe nextpage was followed, except that the exhaust air was immediately "up to temperature." (Initial System Start) • Hotkiln, hot control. This would be a re-start after some event caused the control to switchto bypass. Otherthanbypasses that occur for routine maintenance, an example of these events would be a briefpower outagethat causes the system dampers to close. In this event, therestart procedure would still runthrough the system checks, butmost steps wouldbe shortened sinceboththebaghouse and the exhaust wouldbeup to the correct temperature.

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## II STARTUP- NORMAL 

## II

Thehot and cold startup procedures for the kiln and lime injectionbaghouse system are outlined below. Boral Bricks will document eachtime the system undergoes startup. Steps for Hot Startup Notes 1. Reset the main gas valve and restart air compressor ifnecessary. 2. Start signal is initiated from thekiln controls. 3. Thekiln exhaust fan at the DIFF starts in bypass mode and goes through apurge cycle ofthe kiln for safety. 4. Theburners are ignited and the DIFF System mustbe at a constant switches immediatelyto the full automatic temperature of284°F before the DIFF mode (full operation). The DIFF runs for one canbe started. hourwhile checkingto see thatthe exhaust In the eventthat the minimum temperature is above the minimum for proper temperature is notreached, thekiln operation. Whenthe propertemperature is will normallynotbehot enough for reached, theDIFF will beplaced backinto the normal resumption ofprocessing automatic operation and production will ofbrick. No new product will be resume. introduced to thekiln and thus emissions will beminimized during this time. 5. Heat kiln up until the temperature is sufficient to beginprocessingbrick and start thepusherprocess. 6. Check DIFF operation and insure that all controls areproperly operating.

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Steps for Cold Startup 1. Reset the main gas valve and restart air compressor ifnecessary. 2. Start signal is initiated from the kiln controls. 3. Thekiln exhaust fan at the DIFF starts inbypass mode and goes through a purge cycle ofthe kiln for safety. 4. Theburners are ignited. When the proper temperature is reached, the DIFF will beplaced into automatic operation and production will commence. 5. Heatkiln up until the temperature is sufficient to beginprocessingbrick and start the pusher process. 6. Check DIFF operation and insure that all controls are properly operating.
Steps Taken to Minimize Emissions: Notes

No new product will beintroduced to the kiln until propertemperatures are reached and thus emissions will be minimized during this time.

1. When there is any type ofmalfunction ofthe kiln that results in the kiln stoppage such as interruption ofnatural gas supply or electrical power, no newproduct is placed into or comes out ofthekiln. 2. No new product is processed in the kiln until a proper operational temperature is reached for pushing new product into the kiln. The minimum temperature required for the DIFF operation will be reached before the kiln is at a proper temperature for introduction of new product. With no new product being introduced to the kiln, the level of emissions will be continually decreasing until the pushing of new productionresumes. 3. In orderto minimize emissions, the fresh lime metering screw shouldbe set to the maximummeteringperformance so that thebaghouses fill with lime as quickly as possible. Once thereactionproduct cellularwheel sluice is removing material, you can assume that there is enoughrecirculated material in the process. The fresh lime meter can nowbe set to the normal flowrate setting (level established during the performance test).

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SECTION 5.2- SHUTDOWN PROCEDURES 

## II SHUTDOWN- NORMAL

Thereis generallyminimal need for shutting down the control and/orthekiln. Thekiln tends to remain in operation. Ifthe control and/orthekiln need to be stopped, the following general principles impacttheprocedures
• Unless a safetyissue or control device integrityissue occurs, the kiln will continue to vent through the control device until the exhaust reaches the low temperature setpoint (284 °F).
• Unless safetyto Boralpersonnel and visitors orongoingintegrityofthe control is threatened, all procedures will be aimed at minimizing avoidable emissions ofHAP to the atmosphere. Ifthe control mustbetaken offline for routine maintenance, the time willbe documented as beingpart ofthe time allowed underthe Routine Maintenance Bypass Allowance in Boral's permit.
5.2.1 Normal Shutdown Procedures The normal shutdown procedures for the kiln and lime injection baghouse system are listed below. Boral Bricks will document eachtime the system is shutdown. Steps for Kiln Shutdown 1. Initiate shutdownthrough thekiln controls. 2. Theburners are stopped at thekiln and the pushing ofnew product into thekiln is immediately stopped. Steps for DIFF Shutdown Notes 1. Initiate shutdown through the kiln controls. 2. TheDIFF damper goes to thebypass position and the fan stops immediately.

Page 10 of47 Notes

Bora! Terre Haute SSMP Feb 2008 Revision 0- Feb. 2008 

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Steps for Long Term DIFF Shut Down Followingis theprocedure for shutting the system down for a long period oftime or ifentrance inside the system is required. 1. The fuel sources to the kiln will be stopped. Unless a safetyissue or control device integrity issue occurs, the kiln will continue to vent through the control device until the exhaustreaches the low temperature setpoint (284 °F) 2. Whenkiln exhaust temperature is below lowtemperature setpoint, the control will beplaced in bypass mode. 3. The filter bags will be cleaned to

remove excess lime 4. Ifthe control is to sit for an extended period, the hoppers inthebottom ofthe baghouse will be emptied to the waste silo and the waste lime will be disposed. At this point the control canbe shut down completely for maintenance.
Steps Taken to Minimize Emissions: Notes

1. The introduction ofnew product into the kiln is stopped at the same time that theburners are stopped. 2. Thekiln will continue to vent through the control device until the exhaustreaches the low temperature setpoint (284 °F). This insures that the exhaust will be cleaned as long as theraw gas may containharmful emissions.

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## ) BORAL BRICKS Terre Haute

5.2.2 Emergency Shutdown Procedures 

## II SHUTDOWN- EMERGENCY 

## II

The emergency shutdown procedures for the kiln and reagent injection baghouse system are listed below. Boral Terre Haute will document each time there is an emergency shutdown. Emergency shutdown is triggered automaticallybythe system when it senses conditions that can lead to imminent danger or damage to equipment. Emergency stops buttons are also located in several areas ofthe plant. Emergency shutdown is exactly the same as is listed previously in section 5.2.1. Steps Taken to Minimize Emissions:
• In an emergency shutdown, safety is the primary issue. Boral Terre Haute will work to minimize emissions to the extent practicable. • Maintenance will determine whether the shutdown was due to true malfunction of the system or due to a malfunction ofa sensor. The kiln will be stopped ifthe shutdown is due to a baghouse malfunction that stops the exhaust fan or ifthe malfunction is a part of the kiln control system. If the emergency pertains to only the baghouse, only the baghouse will cease operation and the system will operate in bypass until the situation is controlled.

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SECTION5.3- MALFUNCTION PROCEDURES 

## II MALFUNCTIONS- OVERVIEW 

## II

This section describes the overall approach to identifying the cause of a malfunction and correcting it. It should be noted that Boral-Terre Haute has a responsibility to assure worker safety and to comply with all NFPA safetyrequirements. This will often affect the approach that must be taken to rectify a malfunction situation. Boral-Terre Haute will work to minimize emissions at all times, while ensuring all otherhealth and safetyrequirements are also met. Anymalfunction ofthebaghouse initiates an alarm: Hellmich DIFF has 2 categories ofalarms: 1. WARNINGALARM: This is an audible alarm and a light will flash. The alarm devices are locatedboth at thebaghouse and inside the mainplant facility to ensure that prompt attention can be given. There are a number ofmalfunctions that can trigger a fault within the system and trigger an alarm. Depending on the nature ofthe malfunction, the baghouse may or may not go to bypass immediately. Most ofthe faults begin as warnings ofa minor malfunction that if not given attention will lead to a bypass of the system after a predetermined time period. The onlymalfunctions that lead to an immediate switch to bypass are loss ofl.D. fan, loss ofcompressed air or loss ofpower. Too high or too low temperature to the baghouse will also lead to a bypass ifthey are not corrected. The graphic display will show the nature ofthe malfunction and indicate the part ofthe device that needs attention. 2. CRITICAL ALARM: An alarm that is triggered by an event that puts personnel safety or equipment integrity in danger. A critical alarm will immediately cause the system to go into bypass and shutdown. This alarm is only triggered when either personnel are in danger or the integrity ofthe system could be compromised. Protecting the integrity ofthe system will ensure amore rapid return to normal operation ofthe control. In general, there is at least one system or indication alarm that would indicate problems before they would rise to the level ofa critical alarm.
Boral's approach for minimizing emissions during any malfunctions are based on the following concepts: 1. 

### Minimize the amount of time the system is shutdown. To minimize the amount oftime the kilns and the DIFF systems are shutdown, Boral will: a. Respond as quickly as possible to each WARNING ALARM. b. Maintain spare parts on hand for all components that have or are known to have the potential for failure, as well as any parts recommended by the Kiln manufacturer and Reagent Injection Fabric Filter System manufacturer.

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Description ofEquipment: Type ofMalfunction: Possible Causes (not complete): Alarm Type:
Steps Taken to Correct Problem: DIFF MALFUNCTION 21

Failure ofequipmentto reset itselfto correct operation after a power outage. Failure ofAutomatic Resets following a power outage Powerfailure ObservationbyBoral Staff

1. Maintenance is contacted due to visual observation and responds immediately. 2. KeyBoralpersonnel will identifythe cause ofthe problem. 3. Boral staffand maintenance will work and trouble shootthe system until repaired. 4. Upon resetting the equipment, the DIFF silo will bere-filled (ifrequired) to normal levels withreagent. Steps Taken to Minimize Emissions: 1. After a power failure, Boral personnel will confirm that all default settings have been reset to the correct operating order as quickly as possible. 2. In most cases, the DIFF will continue to operate and since there is reagent in the system during much ofthe malfunction HF will continueto beremoved.

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Type ofMalfunction: Acts ofGod 

## II ACTS OF GOD

General Steps Taken to CorrectMalfunction and Reduce Emissions
• Ensure that the situation has become stable and the hazards have been cleared before proceeding further.
• Confirm the system status and note which equipment is off-line or otherwise impaired.
• Notify appropriate maintenance or otherresponsiblepersonnel (see Section 6.1).
• Respond to correct or repair the malfunction in a safe, efficient and timely manner as soon as it is practicable, for example: o Right overturned equipment and attempt to reinstall/restart; and o Ensure all power and gas lines are functioning correctly and are free from defect
• Suspend operations as soon as practicable until compliance can be assured if failure cannotberepaired in a timelymanner.

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## IIBORAL BRICKS Terre Haute 

## II LOSS OF POWER/GAS 

## II
Type ofMalfunction: Loss ofPower or Gas

General Steps Taken to Correct Malfunction and Reduce Emissions

• Ensure that the situation has become stable and the hazards have been cleared before proceeding further.
• Confirm the system status and note which equipment is off-line or otherwise impaired.
• Notify appropriate maintenance or otherresponsible personnel.
• Respond to correct or repair the malfunction in a safe, efficient and timely manner as soon as it is practicable, for example: 

## •

• Call power company ifpower failure seems plant-wide; if not, trace power failure from equipment to power source; o Check source ofgas; o Trace gas line from equipment to the source and determine whether any leaks orbreaks in line exist; and o Repair anybreaks or leaks that are found intheutility system at the facility. A loss ofgas pressure or a general loss ofpower will result in an automatic stoppage ofthe kiln operation and thus emissions will be minimized until power and or gas is restored to allow normal operations. Ifthe power loss is only at the baghouse unit, there will be no exhaust from thekiln and the kiln will automatically stop and will not operateuntil the situation is corrected.

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### SECTION 6.0- RESPONSffiiLITIES AND POINTS OF CONTACT SECTION 6.1- ORGANIZATIONAL CHART Table ofkey individuals (by name or position), their contact information (phone, pager, cell, email), theirresponsibilities, backup personnel.
PlantManager Greg Camp Direct Phone: 706-421-3898 Regional Production Manager Bill Tudor Direct Phone: 205-908-0593 Environmental Manager: Neil Klein Cell Phone: 812-221-6421 SECTION 6.2- RECORDKEEPING PLAN All data and reports demonstrating compliance with a MACT standard, as well as previous versions ofthe SSMP, mustbemaintained for five years. Location of Electronic File: All records will be kept at the plant premises for inspection on demand.
SECTION 6.3- TRAINING REQUIREMENTS To be completed
SECTION 6.4- SSMP VERSION CONTROL PROCEDURES Protocol for identifying when to update the plan, managing previous versions ofthe plan and document control procedures is included in Section 7.0.

Page 44 of47 Bora! Terre Haute SSMP Feb 2008 Revision 0- Feb. 2008Boral Bricks, Inc. Terre Haute Plant


### SECTION 7.0- RECORDKEEPING AND REPORTING REQUIREMENTS
SECTION 7.1- OVERVIEW OF REQUIREMENTS The type ofrecords that will be retained byBoral-Terre Haute meet the requirements ofPart 63. These records include: • Log ofall startups and shutdowns ofthe machines • Record ofeach malfunction, and whether the actions taken to correct the malfunction were the same as the SSMP. (Itmaybepossible that some events are not malfunctions. Ifit canbe determined that an event was not a malfunction, such an event will bedocumented). The types ofreports that are required to be submitted by Boral-Terre Haute vary considerably, depending on whether the actions taken were consistent with the SSMP. 

## •



# • If the actions taken during the malfunction were consistent with this SSMP, Boral-Terre Haute will state this fact in our semiannual excess emissions report (due within 30 days following the end of each 6-month period) with the following information included (§63.10(d)(S)(i)):
o Certifying signature ofthe**owner/open~tor** or otherresponsible official; o Statement that the actions taken during the malfunction were consistent with the Malfunction Plan; o The number, duration, and a briefdescription ofmalfunction that occurred during the reporting period (§63.10(d)(5)(i)) or a copy of a malfunction report form that includes this information (see Section 7.2.1 for an example form); o Whether any excess emissions and/or parametermonitoring exceedances arebelieved to have occurred during themalfunction (§63.10(d)(S)(ii)); and o Any additional information requiredby our State orpermitting authority. Ifthe actions taken during a malfunction were not consistent with this SSMP, because the plan did not address the type ofmalfunction that occurred and/or the actions taken were not included in the current SSMP, and excess emissions occurred, the Environmental Supervisor should report the actions taken bytelephone or facsimile (FAX) transmission within two (2) working days after the malfunction. A lettermust thenbe sent within seven (7) working days after the malfunction. The letter should include the following information (§63.10(d)(5)(ii)):
o Name, title, and certifying signature ofresponsible official; o Explanation ofthe circumstances ofthe malfunction; o Thereasons for not following the current SSMP; and o Any additional informationrequiredby our State orpermitting authority.
• Ifactions taken during the malfunction were not consistent with the SSMP or did not address the particular type ofmalfunction that occurred, and the Boral-Terre Haute's SSMP should Page 45 of47 BoralTerre Haute SSMP Feb 2008 Revision 0- Feb. 2008

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include these events or actions for future events. Then General Provisions also require ((§63.6(e )(3)(viii)):
o Revise the SSMP within 45 days after the malfunction to include procedures for operating and maintaining the source during similar malfunction events, with a program ofcorrective action to address the malfunctions; and o Report the revisions ofyour SSMP inthe semi annual excess emissions report (within 30 days following the end ofeach 6-monthperiod).

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SECTION 7.2- EXAMPLE REPORT FORMS i. Malfunction reports (internal)

Forms to be completed for each malfunction that occurs - must include determination ofwhether SSMP was followed. ii. Malfunction Log

Table listing each malfunction and whether it was included in plan or, ifnot, whether required notifications were provided iii. Example Notifications

iv.Provide examples of: verbal/written notification required within 2 days of malfunction not included in SSMP; written notification required within 7 days ofthe end ofa malfunction not included in SSMP; language to include in semiannual reports. Addresses
INDIANA DEPARTMENT OF ENVIRONMENTAL MANAGEMENT Indiana Department ofEnvironmental Management· ComplianceData Section, Office ofAir Quality 100 North Senate Avenue MC61-53IGCN1003 Indianapolis, Indiana 46204-2251 And Vigo CountyAirPollution Control 103 South Third Street Terre Haute, Indiana 47807 US EnvironmentalProtection Agency EPARegion 5 Regional Office 77 W. Jackson Blvd. Chicago, IL 60604

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