Presented to:
Chemical Destruction Community Advisory Board’s Explosive Destruction Technology Working Group
Presented by:
Jeff Brubaker, ACWA Site Manager
John McArthur, Systems Contractor Environmental Manager
Heat Tracing Solutions for LNG facilities in Arctic ConditionsDillen Valerie
Pentair attended the LNG Congress in Rusia 2017. This presentation focusses on the advantages of heat-tracing and control and monitoring for LNG facilities in Arctic Environment- Take the Chill out of Projects and personnel!
Trac-Loc Tank Insulation for increased Safety and Guaranteed Financial & Oper...Dillen Valerie
Trac-Loc® is a standing seam insulation system that offers tank owners a
superior system compared to conventional insulation methods. Find out how with this slide deck
This document discusses KLM Technology Group, which provides training and consulting services related to process plant equipment and operations. It focuses on training courses for process flares, including an introduction to process flares, advanced flare design/operation/troubleshooting courses, and a syllabus for an advanced flare systems course. The document provides information on flare types (elevated and ground), system components, design factors and considerations, and safety, environmental, and social requirements related to flare system design.
Refrigeration and its Terminologies;
(i) Capacity or Units of refrigeration,
(ii) COP,
(iii) Types of Refrigerants
(iv) Refrigerants and their desirable properties,
Refrigeration Cycles:
(i) Vapor compression refrigeration system; description, analysis, refrigerating effect.
(ii) Vapor compression refrigeration system Special Case 1,2,3;
(iii) Deviation of the Actual Vapor Compression Refrigeration Cycle from the Ideal Cycle
Air cycle refrigeration;
a) reversed Carnot cycle,
b) reversed Brayton cycle,
c) Vapor absorption refrigeration system.
Previous Year Problems with Solution
This document provides a nitrogen purging procedure for repairing a 16" gas pipeline between UTUE KP and UBIT PP in Nigeria. It outlines the objectives, scope of work, safety considerations, equipment needs, and step-by-step work procedures. The key steps include isolating and depressurizing the pipeline, installing nitrogen tie-in points, purging the line with nitrogen in cycles until gas concentration drops below 5% LEL, recording purge results, and demobilizing equipment. The procedure is intended to remove combustible gases and oxygen from the pipeline to allow for safe repair work.
Thermon Industrial Hazardous Area Trace Heating - General InformationThorne & Derrick UK
This document provides an overview comparison of three common types of heat tracing systems: thermal fluid, electric, and steam. It discusses the history and evolution of each system type and highlights some of their key merits and limitations. The document emphasizes that no single system is definitively best for every application and that factors like specific process requirements, energy efficiency, installation costs, and maintenance should all be considered when selecting a heat tracing solution.
Heat Tracing Solutions for LNG facilities in Arctic ConditionsDillen Valerie
Pentair attended the LNG Congress in Rusia 2017. This presentation focusses on the advantages of heat-tracing and control and monitoring for LNG facilities in Arctic Environment- Take the Chill out of Projects and personnel!
Trac-Loc Tank Insulation for increased Safety and Guaranteed Financial & Oper...Dillen Valerie
Trac-Loc® is a standing seam insulation system that offers tank owners a
superior system compared to conventional insulation methods. Find out how with this slide deck
This document discusses KLM Technology Group, which provides training and consulting services related to process plant equipment and operations. It focuses on training courses for process flares, including an introduction to process flares, advanced flare design/operation/troubleshooting courses, and a syllabus for an advanced flare systems course. The document provides information on flare types (elevated and ground), system components, design factors and considerations, and safety, environmental, and social requirements related to flare system design.
Refrigeration and its Terminologies;
(i) Capacity or Units of refrigeration,
(ii) COP,
(iii) Types of Refrigerants
(iv) Refrigerants and their desirable properties,
Refrigeration Cycles:
(i) Vapor compression refrigeration system; description, analysis, refrigerating effect.
(ii) Vapor compression refrigeration system Special Case 1,2,3;
(iii) Deviation of the Actual Vapor Compression Refrigeration Cycle from the Ideal Cycle
Air cycle refrigeration;
a) reversed Carnot cycle,
b) reversed Brayton cycle,
c) Vapor absorption refrigeration system.
Previous Year Problems with Solution
This document provides a nitrogen purging procedure for repairing a 16" gas pipeline between UTUE KP and UBIT PP in Nigeria. It outlines the objectives, scope of work, safety considerations, equipment needs, and step-by-step work procedures. The key steps include isolating and depressurizing the pipeline, installing nitrogen tie-in points, purging the line with nitrogen in cycles until gas concentration drops below 5% LEL, recording purge results, and demobilizing equipment. The procedure is intended to remove combustible gases and oxygen from the pipeline to allow for safe repair work.
Thermon Industrial Hazardous Area Trace Heating - General InformationThorne & Derrick UK
This document provides an overview comparison of three common types of heat tracing systems: thermal fluid, electric, and steam. It discusses the history and evolution of each system type and highlights some of their key merits and limitations. The document emphasizes that no single system is definitively best for every application and that factors like specific process requirements, energy efficiency, installation costs, and maintenance should all be considered when selecting a heat tracing solution.
Chemical engineering apparatus can be divided into proprietary equipment like pumps and filters, which are designed by manufacturers, and non-proprietary custom equipment like reactors and distillation columns. While chemical engineers are not normally involved in the detailed design of proprietary equipment, they are involved in selecting, sizing, and providing specifications for custom equipment. Chemical engineers work with mechanical designers to transmit information like vessel dimensions, but leave detailed mechanical design to specialists. All chemical engineering apparatus must be designed according to relevant codes and standards for safety.
Graded Unit Project Fuel Purification Final Report Online Submission (1)Steven Brady
This document provides the final design for a fuel purification system for a new marine vessel called the MAERSK Braveheart. The design includes purification systems for heavy fuel oil, lube oil, and diesel oil. Alfa Laval, Westfalia, and Mitsubishi purification units were considered, with Alfa Laval selected as the preferred option based on an evaluation. The design includes system diagrams, component selections, layouts of the purification room including ventilation and maintenance facilities, safety features like fire protection, and cost estimates. Deliverables such as calculations, drawings, and documentation are provided to fully specify the purification system design for the client.
This document discusses removing sulfur from petroleum refining using a Distributed Control System (DCS). It begins with an introduction to hydrodesulfurization, the catalytic process used to remove sulfur from fuels to reduce emissions. The objective is to automate the sulfur removal process using a DCS. It describes the sulfur removal process and hydrogen sulfide capture. It then provides an overview of DCS and its advantages over centralized control systems. The document details implementing control logic like temperature, pressure, and flow controls into the DCS. It discusses results like improved continuity and flexibility compared to a PLC system. In conclusion, the DCS provides improved plant control, efficiency, and crude oil quality for the desulfurization process.
This document outlines the design of the HVAC system for the first floor of a science and technology hospital in Sana'a, Yemen. It discusses the building description, cooling load calculations using both manual and technical methods, duct design including duct sizing and selection of fans and accessories, and pipe design for the chilled water system. The technical method of load calculation in the REVIT program was found to be more accurate than the manual method. Ductwork was designed and fans were selected to meet the required air flows. A closed two-pipe direct return chilled water system was chosen for temperature control.
False air or excess air in sealed systems like boiler flue gas paths or ACC vacuum systems can cause issues like heat loss, fan inefficiency, and increased downtime. It is important to identify sources of false air, measure levels periodically, and implement remedial actions like sealing leaks. Key steps include dedicating teams to identify leak areas, take measurements, and make repairs during outages in a timely manner, as well as implementing design and fabrication best practices, online monitoring instruments, and preventative maintenance programs.
5 Steps to Achieve More CostEffective Aminebased Carbon Capture Processes at ...NazrulIslam657555
The document outlines 5 steps to develop a cost baseline for a commercial-scale amine-based carbon capture process at a 555 MWe natural gas power plant. The steps include: (1) developing and validating an Aspen Plus process model, (2) simulating the full plant design, (3) sizing major equipment, (4) estimating capital and operating costs using Aspen Capital Cost Estimator, and (5) analyzing costs and comparing to industry benchmarks. The analysis estimated a total capital cost of $326.6 million and annual operating cost of $47 million for the reference case of a 30 wt% MEA solvent system capturing 1.475 million tons per year of CO2.
The document outlines the requirements and expectations for a chemical plant design project. It includes sections on the project scope, required deliverables, evaluation criteria, and technical considerations. Students will work in groups of up to 4 people to develop a complete design package for a chemical process. The project is due on December 1st and must include items such as a technology review, heat and material balances, process flow diagrams, equipment specifications, and a cost analysis. Updates on progress must be submitted every two weeks.
CHARMED Upgrading the UT Pickle Separations to DeltaV v11Emerson Exchange
This presentation was given at Emerson Exchange 2010 and shows how the control system at the UT Pickle Separations unit was upgraded to DeltaV v11. Before and after pictures are included that show the new controllers, IO, and major changes made in the control room.
The document provides design details for an acetic acid process plant with a capacity of 400,000 tonnes per year. It evaluates various process technologies for producing acetic acid and selects the methanol carbonylation process. The design includes piping and instrumentation diagrams and specifications for the main unit operations - reactor, flash tank, drying distillation column, heavy ends distillation column, absorption column, and storage tank. It also covers process control and instrumentation, safety, environmental, and economic aspects of the plant design.
This document provides an overview of safety practices for oil movement and storage operations at Reliance Jamnagar Refinery. It discusses the refinery's tank farm and pipeline facilities, security measures, and key safety features of the storage tanks, pump houses, and automation systems. Process Safety Management is a core part of the refinery's approach to identify and control process hazards to prevent incidents and injuries.
The document summarizes the mechanical ventilation and air conditioning system of the Pinnacle Sunway building. It describes the centralized chilled water system which uses water chillers to produce chilled water that is circulated through the building to fan coil units. Key components discussed include the chiller plant in the basement, cooling towers on the roof, and the chilled water piping distribution system. Diagrams show the layout and location of major mechanical equipment.
Practical Implementation Of Renewable Hydrogen & Fuel Cell Installations in t...guest083950
Paper presented at the conference Detail Design in Architecture 8 at University of Wales Institute Cardiff, on the 4th September 2009.
Authors: Gavin D. J. Harper & Ross Gazey
The document provides details about ADCO's CO2 injection pilot project in the Bab Far North Field. The objectives are to collect technical data to assess CO2 injection effectiveness for enhanced oil recovery and to reduce CO2 emissions. The project involves injecting CO2 alternately with water into wells via a CO2 pipeline. It describes the design basis including capacities, fluid properties, and the process design for CO2 and water injection and production systems. It also outlines operating, control, startup, and changeover philosophies for injection well and pipeline operations.
remove from plant critical systems steam piping prior to start-up:
Construction Debris
Scales
Rust
Loose Material
Construction Leftovers
Oil
Weld Spatter…etc.
Remove debris to meet equipment (Turbine) OEM criteria for accepting steam.
Failure to remove debris may cause damage to turbine blades, valve internals
FIRE ENGINEERING - Brief introduction (ATNS)Laura Steyn
This document provides an introduction to fire engineering services offered by DTM, including architectural services, engineering services, and fire protection plans. It discusses hazards and risks such as continued operations and health of occupants. It then compares hypoxic fire prevention systems to conventional gas suppression systems, noting advantages of hypoxic systems like preventing fire development and less potential for equipment damage or downtime. Background information on hypoxic air systems is also provided. Budgets are given for hypoxic systems at two airport locations.
The document discusses various topics related to process plant safety including material handling safety, chemical plant design, piping and instrumentation diagrams, control systems, alarms, equipment and piping design, passive and active protections, emergency shutdown systems, and inherent safety techniques. It provides details on factors to consider for safe material handling, guidelines for chemical plant layout and design, symbols used in P&IDs, designing alarm and control systems, and methods to build safety into chemical plant design.
Thermo Fisher Scientific is the world leader in analytical instruments, equipment, reagents, and services for research, analysis, discovery, and diagnostics. Its Environmental Instruments Division is committed to being the global leader in environmental monitoring applications to help customers make the world healthier, cleaner, and safer. It provides air quality monitoring solutions including ambient air and emissions monitoring systems using proven technologies like gas analyzers and particulate monitors. The division has global integration centers and offers complete turnkey project solutions.
The document provides an overview of technical information for specifying flexible conduit for use in hazardous areas. It discusses explosive atmospheres and what is needed for an explosion to occur. It also outlines various standards for hazardous areas including ATEX, IECEx, UL/CSA. The document explains equipment classification systems and provides guidance on choosing the proper conduit or cable for an application. It aims to help readers understand hazardous area installations and product marking requirements.
The document provides an overview of technical information for specifying flexible conduit for use in hazardous areas. It discusses explosive atmospheres and what is needed for an explosion to occur. It also outlines various standards for hazardous areas including ATEX, IECEx, UL/CSA. The document explains equipment classification systems and provides guidance on choosing the proper conduit or cable for an application. It aims to help readers understand hazardous area installations and product marking requirements.
The Kentucky Chemical Demilitarization Citizens Advisory Commission and Chemical Destruction Citizens Advisory Board wrote to the commander of the Blue Grass Chemical Activity to acknowledge efforts to provide information about mold mitigation at the site and to provide observations and recommendations. The advisory boards noted contradictions between current empirical evidence of mold in some igloos and previous studies. They recommended keeping vents open on all igloos except three with mold growth and continuing mitigation efforts in those three igloos, as well as any increased inspections needed due to closed vents.
The Pentagon has directed ACWA to develop an alternative approach for hydrolysate treatment at Pueblo and Blue Grass in case the on-site methods become incapable. ACWA wants to develop criteria with input from the CACs and NRC for evaluating any alternative treatment approaches. ACWA will have the CACs review a statement of task for the NRC before submitting. The NRC is expected to deliver a letter report for Pueblo in 10-12 months and a full report for Blue Grass in 18 months. Developing contingency criteria does not imply changes to current on-site hydrolysate treatment and allows for community input. The SWWG should review the statement of task and engage in developing the criteria.
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Similar to Explosive Destruction Technology30 Percent Design Update May 6, 2014
Chemical engineering apparatus can be divided into proprietary equipment like pumps and filters, which are designed by manufacturers, and non-proprietary custom equipment like reactors and distillation columns. While chemical engineers are not normally involved in the detailed design of proprietary equipment, they are involved in selecting, sizing, and providing specifications for custom equipment. Chemical engineers work with mechanical designers to transmit information like vessel dimensions, but leave detailed mechanical design to specialists. All chemical engineering apparatus must be designed according to relevant codes and standards for safety.
Graded Unit Project Fuel Purification Final Report Online Submission (1)Steven Brady
This document provides the final design for a fuel purification system for a new marine vessel called the MAERSK Braveheart. The design includes purification systems for heavy fuel oil, lube oil, and diesel oil. Alfa Laval, Westfalia, and Mitsubishi purification units were considered, with Alfa Laval selected as the preferred option based on an evaluation. The design includes system diagrams, component selections, layouts of the purification room including ventilation and maintenance facilities, safety features like fire protection, and cost estimates. Deliverables such as calculations, drawings, and documentation are provided to fully specify the purification system design for the client.
This document discusses removing sulfur from petroleum refining using a Distributed Control System (DCS). It begins with an introduction to hydrodesulfurization, the catalytic process used to remove sulfur from fuels to reduce emissions. The objective is to automate the sulfur removal process using a DCS. It describes the sulfur removal process and hydrogen sulfide capture. It then provides an overview of DCS and its advantages over centralized control systems. The document details implementing control logic like temperature, pressure, and flow controls into the DCS. It discusses results like improved continuity and flexibility compared to a PLC system. In conclusion, the DCS provides improved plant control, efficiency, and crude oil quality for the desulfurization process.
This document outlines the design of the HVAC system for the first floor of a science and technology hospital in Sana'a, Yemen. It discusses the building description, cooling load calculations using both manual and technical methods, duct design including duct sizing and selection of fans and accessories, and pipe design for the chilled water system. The technical method of load calculation in the REVIT program was found to be more accurate than the manual method. Ductwork was designed and fans were selected to meet the required air flows. A closed two-pipe direct return chilled water system was chosen for temperature control.
False air or excess air in sealed systems like boiler flue gas paths or ACC vacuum systems can cause issues like heat loss, fan inefficiency, and increased downtime. It is important to identify sources of false air, measure levels periodically, and implement remedial actions like sealing leaks. Key steps include dedicating teams to identify leak areas, take measurements, and make repairs during outages in a timely manner, as well as implementing design and fabrication best practices, online monitoring instruments, and preventative maintenance programs.
5 Steps to Achieve More CostEffective Aminebased Carbon Capture Processes at ...NazrulIslam657555
The document outlines 5 steps to develop a cost baseline for a commercial-scale amine-based carbon capture process at a 555 MWe natural gas power plant. The steps include: (1) developing and validating an Aspen Plus process model, (2) simulating the full plant design, (3) sizing major equipment, (4) estimating capital and operating costs using Aspen Capital Cost Estimator, and (5) analyzing costs and comparing to industry benchmarks. The analysis estimated a total capital cost of $326.6 million and annual operating cost of $47 million for the reference case of a 30 wt% MEA solvent system capturing 1.475 million tons per year of CO2.
The document outlines the requirements and expectations for a chemical plant design project. It includes sections on the project scope, required deliverables, evaluation criteria, and technical considerations. Students will work in groups of up to 4 people to develop a complete design package for a chemical process. The project is due on December 1st and must include items such as a technology review, heat and material balances, process flow diagrams, equipment specifications, and a cost analysis. Updates on progress must be submitted every two weeks.
CHARMED Upgrading the UT Pickle Separations to DeltaV v11Emerson Exchange
This presentation was given at Emerson Exchange 2010 and shows how the control system at the UT Pickle Separations unit was upgraded to DeltaV v11. Before and after pictures are included that show the new controllers, IO, and major changes made in the control room.
The document provides design details for an acetic acid process plant with a capacity of 400,000 tonnes per year. It evaluates various process technologies for producing acetic acid and selects the methanol carbonylation process. The design includes piping and instrumentation diagrams and specifications for the main unit operations - reactor, flash tank, drying distillation column, heavy ends distillation column, absorption column, and storage tank. It also covers process control and instrumentation, safety, environmental, and economic aspects of the plant design.
This document provides an overview of safety practices for oil movement and storage operations at Reliance Jamnagar Refinery. It discusses the refinery's tank farm and pipeline facilities, security measures, and key safety features of the storage tanks, pump houses, and automation systems. Process Safety Management is a core part of the refinery's approach to identify and control process hazards to prevent incidents and injuries.
The document summarizes the mechanical ventilation and air conditioning system of the Pinnacle Sunway building. It describes the centralized chilled water system which uses water chillers to produce chilled water that is circulated through the building to fan coil units. Key components discussed include the chiller plant in the basement, cooling towers on the roof, and the chilled water piping distribution system. Diagrams show the layout and location of major mechanical equipment.
Practical Implementation Of Renewable Hydrogen & Fuel Cell Installations in t...guest083950
Paper presented at the conference Detail Design in Architecture 8 at University of Wales Institute Cardiff, on the 4th September 2009.
Authors: Gavin D. J. Harper & Ross Gazey
The document provides details about ADCO's CO2 injection pilot project in the Bab Far North Field. The objectives are to collect technical data to assess CO2 injection effectiveness for enhanced oil recovery and to reduce CO2 emissions. The project involves injecting CO2 alternately with water into wells via a CO2 pipeline. It describes the design basis including capacities, fluid properties, and the process design for CO2 and water injection and production systems. It also outlines operating, control, startup, and changeover philosophies for injection well and pipeline operations.
remove from plant critical systems steam piping prior to start-up:
Construction Debris
Scales
Rust
Loose Material
Construction Leftovers
Oil
Weld Spatter…etc.
Remove debris to meet equipment (Turbine) OEM criteria for accepting steam.
Failure to remove debris may cause damage to turbine blades, valve internals
FIRE ENGINEERING - Brief introduction (ATNS)Laura Steyn
This document provides an introduction to fire engineering services offered by DTM, including architectural services, engineering services, and fire protection plans. It discusses hazards and risks such as continued operations and health of occupants. It then compares hypoxic fire prevention systems to conventional gas suppression systems, noting advantages of hypoxic systems like preventing fire development and less potential for equipment damage or downtime. Background information on hypoxic air systems is also provided. Budgets are given for hypoxic systems at two airport locations.
The document discusses various topics related to process plant safety including material handling safety, chemical plant design, piping and instrumentation diagrams, control systems, alarms, equipment and piping design, passive and active protections, emergency shutdown systems, and inherent safety techniques. It provides details on factors to consider for safe material handling, guidelines for chemical plant layout and design, symbols used in P&IDs, designing alarm and control systems, and methods to build safety into chemical plant design.
Thermo Fisher Scientific is the world leader in analytical instruments, equipment, reagents, and services for research, analysis, discovery, and diagnostics. Its Environmental Instruments Division is committed to being the global leader in environmental monitoring applications to help customers make the world healthier, cleaner, and safer. It provides air quality monitoring solutions including ambient air and emissions monitoring systems using proven technologies like gas analyzers and particulate monitors. The division has global integration centers and offers complete turnkey project solutions.
The document provides an overview of technical information for specifying flexible conduit for use in hazardous areas. It discusses explosive atmospheres and what is needed for an explosion to occur. It also outlines various standards for hazardous areas including ATEX, IECEx, UL/CSA. The document explains equipment classification systems and provides guidance on choosing the proper conduit or cable for an application. It aims to help readers understand hazardous area installations and product marking requirements.
The document provides an overview of technical information for specifying flexible conduit for use in hazardous areas. It discusses explosive atmospheres and what is needed for an explosion to occur. It also outlines various standards for hazardous areas including ATEX, IECEx, UL/CSA. The document explains equipment classification systems and provides guidance on choosing the proper conduit or cable for an application. It aims to help readers understand hazardous area installations and product marking requirements.
Similar to Explosive Destruction Technology30 Percent Design Update May 6, 2014 (20)
The Kentucky Chemical Demilitarization Citizens Advisory Commission and Chemical Destruction Citizens Advisory Board wrote to the commander of the Blue Grass Chemical Activity to acknowledge efforts to provide information about mold mitigation at the site and to provide observations and recommendations. The advisory boards noted contradictions between current empirical evidence of mold in some igloos and previous studies. They recommended keeping vents open on all igloos except three with mold growth and continuing mitigation efforts in those three igloos, as well as any increased inspections needed due to closed vents.
The Pentagon has directed ACWA to develop an alternative approach for hydrolysate treatment at Pueblo and Blue Grass in case the on-site methods become incapable. ACWA wants to develop criteria with input from the CACs and NRC for evaluating any alternative treatment approaches. ACWA will have the CACs review a statement of task for the NRC before submitting. The NRC is expected to deliver a letter report for Pueblo in 10-12 months and a full report for Blue Grass in 18 months. Developing contingency criteria does not imply changes to current on-site hydrolysate treatment and allows for community input. The SWWG should review the statement of task and engage in developing the criteria.
Presented to:
Kentucky Chemical Demilitarization Citizens’ Advisory Commission and
Chemical Destruction Community Advisory Board
Presented by:
Jeff Brubaker Doug Omichinski
Site Project Manager Project Manager
The document provides updates from various working groups of the Chemical Destruction Citizens Advisory Board (CDCAB). The Economic Development Working Group is conducting a three-phase economic impact study of the chemical destruction process. The Secondary Waste Working Group is focusing on a planned rocket separation operation and submitted comments on its required permits. The Monitoring Working Group developed and circulated a recommendation regarding mold mitigation efforts at the Blue Grass Chemical Activity, advising that vents remain open on most igloos containing chemical agents.
LTC Christopher Grice provided an update on the rocket separation operation at Blue Grass Chemical Activity to the Kentucky Chemical Demilitarization Citizens’ Advisory Commission and Kentucky Chemical Destruction Community Advisory Board. The rocket separation was completed on May 13, 2014, with 42 of 44 planned rockets separated. Samples from each of the 19 unique propellant lots were taken, with 23 samples shipped to ARDEC for testing in June and the remaining 19 stored for future testing by BGCAPP. All rocket motor samples were monitored and found to be free of chemical agents according to DA PAM 385-61.
The document provides a quarterly update on the Blue Grass Chemical Agent-Destruction Pilot Plant project. Construction is over 82% complete and systemization activities are over 18% complete. Upcoming work includes starting construction of the Container Handling Building, Medical Facility, and Personnel Maintenance Building. Laboratory testing of dilute mustard agent will begin this summer. Safety performance remains high, with recordable and lost-time injury rates well below industry averages. Community involvement efforts have raised over $100,000 for local charities.
The document provides an update from the Economic Development Working Group co-chair Craig Williams. It summarizes work analyzing the existing workforce and economic environment in Madison and Rockcastle counties in Kentucky, known as the Richmond-Berea micropolitan statistical area. The analysis includes educational attainment levels and age structure of the population based on US Census data to understand how to potentially mitigate effects of anticipated economic events. Future meetings and a final report are planned.
Presented to:
Kentucky Chemical Demilitarization Citizens’ Advisory Commission and Kentucky Chemical Destruction Community Advisory Board
Presented by:
LTC Christopher Grice
Commander, Blue Grass Chemical Activity
The document discusses ACWA funding for fiscal year 2015. It states that ACWA is fully funded for 2015 with $575.9 million allocated for research, development, testing and evaluation split between ACWA sites and $38.7 million allocated for military construction for the BGCAPP program, bringing BGCAPP's funding level to approximately $326.65 million. The document was presented by Craig Williams on June 11, 2014 and includes a section for questions and discussion.
The document summarizes plans to implement an explosive destruction technology (EDT) to destroy over 15,000 mustard projectiles at the Blue Grass Chemical Agent-Destruction Pilot Plant (BGCAPP). BGCAPP awarded a contract to UXB International in November 2013 to provide a static detonation chamber (SDC) for this purpose. Regulatory permitting processes are underway, including a RCRA Part B permit modification and Title V air permit revision. Key engineering documents like process flow diagrams, piping and instrumentation diagrams, and mass and energy balances will be included to support permit applications. Operations are scheduled to begin in winter 2016/early 2017 once the SDC system has been designed, constructed, tested, and permitted.
The document discusses plans to implement explosive destruction technology (EDT) to destroy over 15,000 mustard projectiles at the Blue Grass Chemical Agent-Destruction Pilot Plant (BGCAPP) in Kentucky. Bechtel Parsons Blue Grass (BPBG) awarded a contract to UXB International to use a static detonation chamber (SDC) system. The SDC design is underway and regulatory permitting processes have begun. Construction of the SDC facility is scheduled from fall 2014 to fall 2016 with operations starting in winter 2016/early 2017. Public meetings will provide information and get input on the EDT plans and permits.
The document summarizes the history and work of the Explosive Destruction Technology Working Group, which consists of members from various government and private organizations involved in the chemical weapons disposal process. It describes several key meetings where the group discussed using explosive destruction technology (EDT) to dispose of mustard munitions at Blue Grass Army Depot that were difficult to process through incineration. While the group did not endorse a specific EDT, they provided recommendations to consider EDTs if regulatory requirements and public involvement were met.
The document provides an update from the Explosive Destruction Technology (EDT) Working Group meeting on June 11, 2014. It includes information about a tour of the Anniston, Alabama EDT facility by working group members and details presented at the 30% design meeting, such as the EDT process equipment layout and schedule. It also notes differences between the Anniston and Blue Grass Army Depot EDT units and discusses the permit modification process.
Presented to:
Kentucky Chemical Demilitarization Citizens’ Advisory Commission/ Chemical Destruction Community Advisory Board Meeting
Presented by:
Jeff Brubaker
Site Project Manager
Presented to:
Kentucky Chemical Demilitarization Citizens’ Advisory Commission/ Chemical Destruction Community Advisory Board Meeting
Presented by:
Jeff Brubaker Tom McKinney
Site Project Manager Project Manager
The Economic Development Working Group met on September 11th to discuss action items from a previous meeting. They planned to expand distribution of an economic study and schedule a meeting to refine proposals for further phases of the study to seek funding. A separate Depot Development Coalition met on November 18th to discuss the economic study and pursue public-private partnership opportunities at the Blue Grass Army Depot. They assigned subcommittees to pursue further study funding and research partnership opportunities. The Working Group then met to distribute documents from the Office of Economic Adjustment and draft an application for funding to develop further phases of the economic study.
The document summarizes updates on several countries' progress toward destroying their chemical weapon stockpiles in accordance with the Chemical Weapons Convention. The United States, Russia, and Libya were unable to meet the 2012 deadline and submitted new plans to complete destruction by 2023, a classified date for Russia, and 2016 for Libya. The document also provides details on chemical weapons destruction facilities planned and operated by the United States and Libya.
The document summarizes Syria's chemical weapons disarmament schedule and process as agreed upon when Syria joined the Chemical Weapons Convention in September 2013, following allegations of chemical weapons attacks. Key points include: Syria's schedule for removing and destroying chemical weapons by mid-2014; plans to neutralize mustard agents and precursors aboard the MV Cape Ray using a field deployable hydrolysis system, as was successfully used in the US; outstanding issues regarding transport through Syria's conflict and risks of on-board work; and Kentucky's potential contributions based on its experience with chemical weapons destruction projects.
The document provides updates from four working groups of the Chemical Destruction Citizens Advisory Board:
1. The Economic Development Working Group met with state agencies to integrate support for a job loss study and brief congressional delegations.
2. The Secondary Waste Working Group discussed a proposed rocket separation operation and will make a recommendation to the full board.
3. The EDT Working Group notes Colorado's environmental assessment is complete and Kentucky's draft will be released after comments.
4. The Monitoring Working Group expects a decision soon on storage modifications based on previous recommendations.
The Power of Community Newsletters: A Case Study from Wolverton and Greenleys...Scribe
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Dive into the success story of Wolverton and Greenleys Town Council's newsletter in this insightful webinar. Hear from Mandy Shipp and Jemma English about the newsletter's journey from its inception to becoming a vital part of their community's communication, including its history, production process, and revenue generation through advertising. Discover the reasons behind outsourcing its design and the benefits this brought. Ideal for anyone involved in community engagement or interested in starting their own newsletter.
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Explosive Destruction Technology30 Percent Design Update May 6, 2014
1. Explosive Destruction Technology
30 Percent Design Update
May 6, 2014
Presented to:
Chemical Destruction Community
Advisory Board’s Explosive Destruction
Technology Working Group
Presented by:
Jeff Brubaker, ACWA Site Manager
John McArthur, Systems Contractor
Environmental Manager
2. A Partnership for Safe Chemical Weapons Destruction
Bechtel Parsons Joint Venture team
3. A Partnership for Safe Chemical Weapons Destruction
3
Agenda
EDT Facility Layout
Munitions Processing Steps
Equipment Layout
Other Materials
Questions/Discussion
4. A Partnership for Safe Chemical Weapons Destruction
EDT Facility Layout
4
5. A Partnership for Safe Chemical Weapons Destruction
O2SF Outside Operations Support Facility
ESB EDT Support Building
MH Monitoring House
ESM EDT Service Magazine
EEB EDT Enclosure Building
CON Control Room
TOF Treaty Office Facility
5
EDT and OPS Facilities
6. A Partnership for Safe Chemical Weapons Destruction
6
ESM
ESB
EEB
MH
O2
SF
O2SF
BGCAPP Site Plan / EDT Site Location
7. A Partnership for Safe Chemical Weapons Destruction
7
TOF
BGCAPP Site Plan / EDT Site Facility
ESM
ESBEEB
MH
8. A Partnership for Safe Chemical Weapons Destruction
Function: The purpose of the O2SF will be a primary location for
support functions related to the start and end of daily and shift
activities and routine facility support
O2SF will consist of the following areas to support the Project:
7 offices and 12 cubicles
A Mask Issue, fit and test area
First Aid Area (with a blood draw area and a small Laboratory for Medical personnel)
Hazmat/decon Storage Area
Toxicological Area Protective (TAP) gear storage
Lunch Room
Restrooms and Showers
Locker Areas (with approximately 150 lockers)
A Cotton Goods Issue Room
An IT Help Desk and a small Communication Equipment Room
8
O2SF – Facility Design Description
9. A Partnership for Safe Chemical Weapons Destruction
Function: The purpose of the ESB is the primary support functions
directly related to the operation of the EDT to support the disposal of
the Mustard agent inventory at Blue Grass Army Depot (BGAD)
The ESB houses and supports the EDT operational crews and the
direct support crew functions
ESB will have 6 offices, 10 cubicles, a Conference Room, a TAP
Gear / Tool / Parts Storage Area, a Lunch Room / Crew
briefing/training area, Restrooms, an Electrical Room, a
Communications Room, and a small Custodial Utility Room
The offices are for general purpose and direct support services use,
and planned to accommodate Plant Management, Engineering,
Automation and personnel that directly support the EDT operations
It will support approximately 20 people on Day Shift and
approximately 90 people on rotating shift that are part of the
operational crews that work within the EDT Complex
ESB – Facility Design Description
10. A Partnership for Safe Chemical Weapons Destruction
A Conference Room will provide space for crew training, turn-
overs, and meetings
The Lunch Room/Crew Room contains approximately 40
lockers. This area will have a seating area for approximately
27 personnel. This area also serves as a meeting area to be
used for shift turn-over, crew training, meetings and
presentations. It will also contain several computer
workstations for general crew use (e.g. timekeeping, complete
computer based training, complete Read and Sign
requirement, etc.)
The building’s HVAC system can be shut down to utilize the
ESB as a shelter-in-place facility
The ESB will not house any Chemical Weapons Convention
(CWC) Treaty personnel
Adjacent to the ESB is the EDT Control Room (CON)
ESB – Facility Design Description
11. A Partnership for Safe Chemical Weapons Destruction
Function: The purpose of the EDT Process Monitoring House
(MH) is a centralized area which contains the air monitoring
equipment and some process monitoring equipment to
support operator safety and verify environmental compliance
during 24/7 processing operations of the EDT Facility.
The MH consist of a 16 by 36 foot raised structure,
MiniCAMS, DAAMS, CEMS, and other air monitoring
equipment.
11
MH – Facility Design Description
12. A Partnership for Safe Chemical Weapons Destruction
Function: The purpose of the ESM will be to hold a reserve of
Mustard munitions to support 24/7 processing operations of the EDT
Facility
The ESB consist of a 30 by 30 foot Non-Standard Storage Structure
(NSS) with an HVAC unit, a Monitoring Shack, a Bottle Storage Area
with overhead cover, and a 1,000 CFM Filter Unit mounted on a
trailer.
ESM Capability:
– Maximum explosive capability = 500 pound Net Explosive Weight (NEW) (1,206
projectiles)
– Site Plan Safety Submittal (SPSS) Limit = 1,128 projectiles
Pallet stacking within the ESM is limited to two high
The floor is designed with secondary containment and water stops
The Monitoring Shack contains MiniCAMS and DAAMS to support air
monitoring of the ESM, EONCs, and the 1,000 CFM Filter Unit
12
ESM – Facility Design Description
13. A Partnership for Safe Chemical Weapons Destruction
13
EONC Transport of Chemical Weapons
14. A Partnership for Safe Chemical Weapons Destruction
Function: The purpose of the EEB is to house the SDC and OTS
process equipment
The EEB consist of a 77 by 120 foot building (approx.)
The building has an A, B, C, D Agent Areas with a Cascading
Ventilation System and a Munitions Delivery Airlock
The SDC consist of a:
– Loading Conveyor and Elevator Lift
– Loading Chamber #1 and #2
– The Detonation Chamber (DC)
– A Buffer Tank
– A Scrap Chute, Scrap Cooling Conveyor, Belt Conveyor, and a Scrap
Bin
14
EEB – Facility Design Description
15. A Partnership for Safe Chemical Weapons Destruction
The Off-Gas Treatment System (OTS) consist of a:
– Thermal Oxidizer
– Spray Dryer
– Bag House Filter
– Quench
– Acid & Neutral Scrubber
– ID Fans
– Heat Exchanger and Cooler
– A Re-Heater
The building has a 16,000 CFM IONEX Carbon Filter Unit
And the OTS has a 4,000 CFM IONEX Carbon Filter Unit
15
EEB – Facility Design Description
16. A Partnership for Safe Chemical Weapons Destruction
16
EDT Enclosure Building (EEB)
Layout is based
on the Vendor’s
Preliminary
Design and Equipment
Layout Drawings
17. A Partnership for Safe Chemical Weapons Destruction
17
Airlock
OTS
Gears
Switch
Monitoring
House
4000
IONEX
16000
DC
ChillerScrap
Conveyor
Lift
Feed
Conveyor
THO
Air Tank
Air
Compressors
Layout is based
on the Vendor’s
Preliminary
Design and Equipment
Layout Drawings
BT
EDT Enclosure Building (EEB) Layout
18. A Partnership for Safe Chemical Weapons Destruction
18
EDT Enclosure Building (EEB)
SDC
OTS
Monitoring
House
Airlock
IONEX
4000
Layout is based
on the Vendor’s
Preliminary
Design and Equipment
Layout Drawings
19. A Partnership for Safe Chemical Weapons Destruction
Agent
Area
Category
Color
Code
Purpose Areas Included Remarks
A Red Primary Containment of liquid and
vapor agent
Detonation Chamber (DC) and off-gas
piping to the Thermal Oxidizer (THO)
Most negative pressure
B Orange Secondary Containment of vapor
agent
Around the DC, off-gas piping to the
THO, and the THO itself
More negative pressure
C Yellow Tertiary Containment providing an
area under ventilated engineering
controls
Munition Handling and loading areas
within the building and around the
Secondary Containment areas
Slight negative pressure. Will
require both MHE and personnel
air lock(s) from the D area
D Green No containment. Provides weather
protection to EDT equipment and
crew
The outer building No negative pressure on this
structure
THO OTSDCLoading Area
Category D area
Category C area
Filter / Stack
4,000
Vestibule
No Scale is given to any component of this concept drawing
19
Category B area
EEB – Agent Containment Areas
Carbon Filter
16,000
Air is pulled from atmosphere pressure through process areas with progressing decreasing (negative) pressure as
an engineering control measure
20. A Partnership for Safe Chemical Weapons Destruction
Function: The purpose of the CON is to serve as the Commend and
Control (C2), and the operational center for EDT Facility.
The CON consist of a 16 by 20 foot structure.
Process Equipment include:
– DC HMI stations 1 and 2
– OTS MHI stations 1 and 2
– Dynamic Pressure Sensing Station
– CCTV HMI station with multiple monitors
The CON will be staffed by:
– Shift Plant Manager (SPM)
– Control Room Operators (CRO) (2 each)
– Operations Support Tech
– Automation Specialist (Day Shift only) 20
EDT CON – Facility Design Description
21. A Partnership for Safe Chemical Weapons Destruction
EDT Enclosure Building (EEB)
– On a concrete pad
– Personnel Entry/Exit
– Emergency Exits
– Munition Delivery Airlock
– Scrap Handling Area
SDC System
– Feed Conveyor
– Lift
– Loading Chamber 1
– Loading Chamber 2
– Detonation Chamber (DC)
– Scrap Conveyor
– Inspection Conveyor
– Belt Conveyor
– Scrap Bin
– Buffer Tank
– Dust Handling System
• Off-Gas Treatment System (OTS)
– Thermal Oxidizer
– Spray Dryer
– Bag House Filter
– Quench
– Acid & Neutral Scrubber
– ID Fans
• IONEX Carbon Filter Units (two)
– OTS Filter Unit
– Building Filter Unit
• Utilities
– Natural Gas
– Electrical
– Water
– Emergency Generator
– Air Compressor
– Hydraulics 21
EDT Equipment Components
22. A Partnership for Safe Chemical Weapons Destruction
Munitions Processing Steps
22
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23
EDT Munitions Processing Steps
(Based on the Preliminary 30% Design)
BGCA CW
Storage Igloo
Wooden Pallets
Steel Banding
CW Munitions
are un-banded
CW placed in
Staging Area
EDT CW
Service
Magazine
CW placed in
Feed Tray
SDC
CW enters the
Detonation
Chamber
CW moved via
Conveyor /
Elevator
CW moved
through
Air-Locks
SDC
LC1 - 112
LC2 - 114
LFT
104
COV
101
Information Sources: Updated Vendor PFD and P&ID drawings received 18 February 2014.
Disclaimer: The above illustrated Process Steps are based on the general preliminary design information provided.
Equipment abbreviation code and ID number that
relates to those on the PFDs and Mass Balance
24. A Partnership for Safe Chemical Weapons Destruction
24
EDT Munitions Processing Steps
(Based on the Preliminary 30% Design)
Page 2 of 4
Dust
Metal - Oxide
Volatile / Semi-Volatile
Heavy Metals (Pb, Be, Cr)
Dosing
Station
Dry Salts &
Particulates
Ash
Large Particulates
Spray
Dryer
Bag
House
Filter
Sodium
Bicarbonate
Detonation
Chamber
Buffer
Tank /
Cyclone
Separator
Scrap Metal Recycled to DC
(for 5X treatment)
THO
310
BHF
330
SPD
320
BT
160
Process
Water Tank
Air
Nature Gas
Air
Water
IBC
Air
DC
120
PWT
424
ADS
470 (NaOH)
NAS
480
Bleed Water
Information Sources: Updated Vendor PFD and P&ID drawings received 18 February 2014.
Disclaimer: The above illustrated Process Steps are based on the general information provided.
Scrap Conveyor 2
5X
Scrap Metal
for Recycle
Air
Heater
Emergency Water
Water
Process
Vent
Filter
Dust
Thermal
Oxidizer
Air
PVF
171
PVC
170
Cyclone
25. A Partnership for Safe Chemical Weapons Destruction
25
EDT Munitions Processing Steps
(Based on the Preliminary 30% Design)
Information Sources: Updated Vendor PFD and P&ID drawings received 18 February 2014.
Disclaimer: The above illustrated Process Steps are based on the general preliminary design information provided.
Quench
Tower
Acid
Scrubber
Neutral
Scrubber
Water
Feed/Recycle loops
Heat
Exchanger
NaOH
AC
366
SEP
367
QUE
340
HX
362
NSC
360
ASC
350
Emergency Water
Tank
Separ
ator
Air
Cooler
EWT
322
BWT
430
Bleed
Water Tank
Condensate
Tank
COT
363
NaOH
Bleed Water
Emergency Water
Dust
Chlorine, Hydrogen chloride
SOx
SOx
Chlorine
Heavy Metals
Heater
AH
370
Air
26. A Partnership for Safe Chemical Weapons Destruction
26
EDT Munitions Processing Steps
(Based on the Preliminary 30% Design)
Information Sources: Updated Vendor PFD and P&ID drawings received 18 February 2014.
Disclaimer: The above illustrated Process Steps are based on the general preliminary design information provided.
ID Fan
1
ID Fan
2
Pre
Filter
HEPA
Filter
HEPA
Filter
Carbon
Filter
SIC
Carbon
Filter
Filter Bank
(five filter element)
Carbon Filter
Elements
STACK
Monitoring
House
ION
400
IDF1
370
IDF2
371
Exhaust Stack
Laboratory
Monitoring
House
Water Vapor
MiniCAMS
DAAMS
CEMS
CO
O2
ID Fan
Sample
Ports
27. A Partnership for Safe Chemical Weapons Destruction
Equipment Layout
27
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28
Note: Our Scrap Conveyor
is turned 90 degrees from
the Cool Down Conveyor
Feed
Conveyor
Munitions
Lift
Dust
Collection
Scrap
Bin
Belt
Conveyor
Secondary
Containment
Buffer Tank
EDT Process Equipment Layout
29. A Partnership for Safe Chemical Weapons Destruction
29
Tilting Cradle
Fragment
Shield
Loading
Chamber 1
Gate 2
Secondary
Containment
Loading
Chamber 2
Gate 1
EDT Process Equipment
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30
Fragment
Liner
Destruction
Chamber
Heating
Elements
DC Empting
Arrangement
Locking RingInsulation
EDT Process Equipment
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31
1
4
3
2
EDT Feeding Cycle
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Air
Heater
32
DC Empting Cycle / Scrap Removal &
Cooling
33. A Partnership for Safe Chemical Weapons Destruction
33THO QUE ASC
NSC
BHFSPD HXIDF1
IDF2
Upgraded / Larger THO & OTS
– Limiting Throughput (Pacing Station) for the Anniston unit
The THO is 98% larger:
– Anniston unit is: 162 ft3
– BGCAPP unit will be: 321 ft3
The OTS is 75% larger
Closed Loop Process Water System
OTS - Key Design Elements
34. A Partnership for Safe Chemical Weapons Destruction
Reverse angle
Spray Dryer Dosing Station
Spray Dryer Waste Drum
Quench Venturi
Bag House Waste Drum
Emergency
Water Tank
Bag House Filter
Spray Dryer
Thermal
Oxidizer
Scrubbers
34
OTS Process Equipment Layout
35. A Partnership for Safe Chemical Weapons Destruction
35 15B
1S
3 4
2
5 6
15A
98
7 12 13
10
14
11
C/N Host
SP
SP
P
1
P
2
1 EONC Unload
2 Service Magazine
3 Carbon Midbed
4 Fixed Perimeter
5 Perimeter Trailer
6 Perimeter Trailer
7 Air Lock
8 Loading Area
9 Buffer Tank
Enclosure
10 D/C Enclosure
11 Scrap Exit Area
12 HVAC Midbed
13 HVAC Stack
14 OGT Carbon
Midbed
15 OGT Stack A/B
EDT Personnel Safety Monitoring
Locations
36. A Partnership for Safe Chemical Weapons Destruction
Other Materials
36
37. A Partnership for Safe Chemical Weapons Destruction
37
• Processing Rates - without Overpack
– M110 155mm H Projectiles
– At Peak and Normal Processing Rates:
• Peak Rate estimated: 6.1 projectiles per hour
• Peak Rate actual: To be determined during the
Factory Acceptance Test (FAT)
• Normal Rate estimated: 4.8 projectiles per hour (81%
availability)
Processing Rates
38. A Partnership for Safe Chemical Weapons Destruction
Activity Date
EDT CW Operations Jan – Oct 2017
Ramp-Up Period
Full Rate Period
Regulatory Testing
Over-Pack Processing
EDT Closure and Turn-Over Nov 2017 – May 2018
Decontamination
Restoration
De-staffing
System / Facility Turn Over
Main Plant CW Operations (forecasted Start date) Jan 2018
38
EDT Schedule and Key Milestones
39. A Partnership for Safe Chemical Weapons Destruction
39
• Day Crew arrive at O2SF – Change Out / Draw Mask / Transport to the EDT Complex
• Crew Turn-Over / POD Briefing
• Daily RCRA inspections (AM)
• Verify FPIs and LCOs are completion and approval
• Routine Activities:
Open, complete, and print Feed Sheets
Establish TCEAs – as required (EONC delivery / Munition transfer / EEB processing)
Conduct munitions transfer from the ESM to the EEB Loading Area (twice per shift)
Load Munitions in Feed Trays (twice per shift)
Begin CW Processing - Feed Trays to the SDC
Scrap inspection and removal – as required
Dump Scrap Bin – as required
Daily Operational Report
• Night Crew arrive at O2SF / – Change Out / Draw Mask / Transport to the EDT Complex
• Crew Turn-Over
• Repeat the above Routine Activities
• Munitions Accountability paperwork
• Midnight – Perform a Daily Munition Inventory – develop the COD packet for the prior 24 hrs
• Equipment PM Checks are performed
• Lab Perform equipment challenges (AM)
• Resume CW Processing
Typical EDT Operational Day
40. A Partnership for Safe Chemical Weapons Destruction
Location: Anniston BGCAPP
Description SDC 1200 CM (Chemical Mobile) SDC 1200 C (Chemical)
Transportable unit Fix Facility unit
CW Net Explosive Wt. (NEW) 2.2 lb HE / 6.61 Propellant TBD (min, 2.2 lb HE / 6.61 Propellant)
Fragment Shield: Tube Shaped (sides only) Bowl Shaped (sides with a bottom)
DC Heater: 3 on the bottom of the DC 3 on the bottom plus additional on sides
Cooling Fan for Locking Ring: None Yes (added to minimize binding at high temps.)
LC1 and LC2 Vents to THO: No Yes
(to minimize/prevent agent migration to the Process Ventilation)
Bypass valve around off-gas No Yes
orifice: (to minimize press in the chamber to minimize agent migration to LC2)
Off-Gas Treatment System (OTS): Has a SDC 1200 sized OTS Has a larger SDC 2000 OTS (75% larger)
Thermal Oxidizer (THO): 162 ft3 321 ft3 (98% larger)
Bleed Water Tank: No Yes (added to support 24/7 operations)
Chiller to remove Condensate: No (collection pump to recycle H2O) Yes (added after the Neutral Scrubber)
Re-Heater after Chiller: None initially – installed later Included
Carbon Filter System: IONEX CD2000 IONEX CD4000
Building Type: Sprung Structure Steel Building
Building HVAC: No - Portable AC unit added Yes
Cascading Ventilation System: Vapor containment only Yes (with Category A, B, C, and D areas)
Number of Mustard Projectiles: 2,737 CW munitions processed Approx. 16,000 munitions to be processed
Agent Types: HD and HT Mustard H Mustard (with solids and heels)
DOT Bottles: None processed Two (2) are planned
40
EDT Unit Differences
(Anniston vs. BGCAPP)
41. A Partnership for Safe Chemical Weapons Destruction
Questions/Discussion
41