Michael A. Grabowski

Principal Process / Specialty Engineer

Education:

Certifications/Licenses:

Contact information:

Summary: Thirty five years experience in specialty chemicals, carbon fiber, refrigerants, electro chemicals, polymer process engineering, petrochemical process engineering, natural gas energy development, and biomedical engineering. Project execution experience in conceptual, front- end, and detailed process engineering involving estimating/economics, energy/material balances, viscous fluid flow, gas-liquid separation, material handling, film technology, process troubleshooting, both centrifugal and reciprocating compressors, steam turbine drives, and start-to-finish equipment installations. Considerable experience exists with Aspen/Hysys process simulations as well as computer applications of numerical methods.

Master's Degree, Petroleum Engineering, University of Houston Bachelor's Degree, Chemical Engineering, Northwestern University Bachelor's Degree, Applied Mathematics, Northwestern University Registered Professional Engineer (13917, South Carolina) 205 Chateau Drive

Greenville SC 29615 USA

864-***-**** home’

864-***-**** cell

acrim2@r.postjobfree.com

The following is a list of projects / clients worked on while employed by Jacobs Inc from September 2012 to present:

Representative assignments include:

Process Engineer, Infineum, Bayway Plant New Jersey. Design engineer for a facility to produce a lubrication oil additive. This is a batch – continuous process. Responsibilities include heat exchanger – pump – vessel design, hydraulics, instrumentation, safety relief valve design, and system design (P&ID’s). Process Engineer, ExxonMobil, Baton Rouge Plant, Louisiana. HCLA Amine Scrubber Project. Performed hydraulic calculations and heat exchanger design employing HTRI software for retrofit applications. . Quality checker for hydraulics calculations, safety relief design, and vendor submittals for instruments, safety relief valves, and heat transfer equipment. Process Engineer, Motiva, Geismar Plant, Louisiana. Quality checker for hydraulics calculations and safety relief design.

Process Engineer, BP America, Cooper River Plant, South Carolina. FEL3 engineering for a PTA unit upgrade project. Quality checker for PSV (Pressure Safety Relief Valves). Area Lead Engineer Jacobs Zate for South Harad section of Gas Gathering Manifolds (GGM) Project. This is a front end effort to update existing GGM facilities to include new pipe line scraper receivers and various piping modifications such as double block and bleed valve configurations, updates to lower explosive level (LEL) and hydrogen sulfide (H2S) safety instrumentation. This work required use of client IPlant data base to research existing P&ID’s as well as site visits to confirm current layout configuration.

Process engineer to prepare an estimate for Abqaiq Closed Drain Systems. This is an effort to prepare a detailed estimate to update an existing facility to include a number of closed drain vessel systems.

Process engineer to prepare an estimate Waste Water Treatment Facilities at RTR. This is an effort to prepare a detailed estimate to update an existing facility to bring the existing system into compliance. The systems included an MBR (Membrane Bio-Reactor system), GAC (granulated activated carbon system) and a WAO (wet air oxidation system ) to treat spent caustic. Lead Engineer Jacobs Zate for Loading Rack Facility at RT Distribution Project. The client was Dragados Gulf Construction Co. LTD. The project is located at Saudi Aramco’s Ras Tanura Refinery. This is a detailed engineering effort to design and construct a truck loading facility for diesel to be shipped to the Wasit Gas Plant for sulfur mitigation. This project includes API storage tanks, transfer pumps, truck loading facilities, closed drain system, oily water sump and transfer pumps, foam generation system for fire suppression, and fire water design. Principal Process / Specialty Engineer, Ma’aden Inc., Ras Al Khair, Saudi Arabia. Preparation of work packages to de-bug, de-bottleneck, and troubleshoot a phosphate fertilizer production facility with particular emphasis on the selection materials of construction to address corrosion issues.

Principal Process / Specialty Engineer, Evonik Inc., Mobile, Alabama. Front end package (FEED) for a (MMA), Methyl Methacrylate production facility. The following is a list of projects / clients list worked on while employed by Fluor Inc from June 1988 through September 2012.

Principal Process / Specialty Engineer

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KIMERA

Fluor

04/ 2012 – 09/2012

Feed effort for a DPAM ( Dried Polyacrylamide ) manufacturing facility. USEC Inc.

Fluor American Centrifuge Plant (ACP)

08/ 2010 – 04 / 2012 Piketon, Ohio, United States

Fluor is providing the engineering, procurement, and construction (EPC) for the ACP Project, a uranium enrichment facility incorporating next-generation technology to produce 3.8 MM SWU/year of fuel for nuclear powered plants. This work required a DOE Q – level security clearance.

Yangpu

Fluor Hainan Pan-Asia Petrochemical Co., Ltd

05/2010 – 08/2010 2,600 kt/a Olefins and Petrochemicals Project in Hainan, China

Feasibility study for a petrochemical complex to be located in China. This project includes 17 main production units with the 500 kt/a propane dehydrogenation unit and 1,300 kt/a ethylene cracking unit as well as associated utilities and auxiliary faciliti . SIPChem

Fluor Jubail Acetyls Complex - AA, VAM & Utilities 02/2009 – 03/2010 Al Jubail, Saudi Arabia

A 300,000-TPA Dupont-technology vinyl acetate monomer plant and 400,000-TPA Eastman- technology acetic acid plant

Operations support specialist for the Jubail Acetyls C lex. Provide engineering to support the pre-commissioning, commissioning, and start-up efforts. Conduct hydraulic analysis, safety reviews, trouble shoot, and debug vendor packaged systems. Tasnee / Rohm and Haas

Fluor SAMCo Project

10 / 2008 – 2 / 2009 Deer Park, Texas, United States Process Manager for the Oxidation – Separations – TGAA/ FAA – and Melt Crystallization design areas for a facility to produce Acrylic Acid. Assignment required technology development to produce a PDP (Process Design Package) which would trigger a FEED (Front End Design effort). This project is a joint venture between Tasnee and Rohm & Haas with R & H providing the process technology. Objective is to produce 160 mt/yr of NBA (N-Butyl Acrylate), 30 kt/yr of FGAA (Flocculent Grade Acrylic Acid), and 50 kt/yr of 2EHA. Facility to be located in Jubail, Saudi Arabia.

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Eastman Chemical

Fluor A-Wood Project

06/2008 – 10/ 2008 Kingsport, Tennessee, United States Lead process engineer for a facility to produce 100 million board feet per year of acetylated wood product using EverlokTM technology. Facility is a combination of manufacturing and chemical processing steps. Wood is kiln dried and chemically treated with a mixture of acetic acid and acetic anhydride in a jacketed reactor. After reaction, the wood is transferred to another jacketed vessel and dried using microwave energy. Solvents removed from wood processing are reclaimed and processed for reuse.

TX Energy

Fluor Texas Gasification Project

01/2008 - 06/2008 Beaumont, Texas, United States

Front-end engineering and design (FEED) and EPC for a gasification project Design specialist for a coke / coal gasification process. Project objective is to produce hydrogen, carbon dioxide for enhanced oil recovery, and synthetic natural gas. Specific responsibilities include design of 80,000 hp centrifugal compression for CO2 export, 20,000 hp reciprocating compressors for hydrogen service, 45,000 hp centrifugal compression system for propylene refrigerant system. Coordinated design efforts for a Rectisol process unit used for acid gas purification.

Eastman Chemical

Fluor Integrated Chemicals Project V- FEED

06 / 2007 – 12 / 2007 Corpus Christi, Texas, United States Fluor is providing FEED services for a grassroots integrated Terephthalic Acid (PTA) and Polyethylene Terephthalate (PET) chemical complex to be located in the US Gulf Coast. U & O area process lead for a facility producing Polyethylene Terephthalate (PET). Facilities include steam generation, boiler water treatment, cooling water system, cooling water treatment, process demineralized water, waste water treatment, compressed air, nitrogen, railcar management, marine unloading, tank farm, and fire water systems. Usolye-Siberian Silicon, LLC

Fluor Polycrystalline Silicon Plant (Nitol)

03 / 2007 - 06 / 2007 Usolye-Sibirskoye, Russia

The FEED package for a grassroots 1500 t/yr photo-voltaic grade polycrystalline silicon plant used Siemens' vapor deposition technology to produce photo-voltaic grade silicon for the high- growth solar cell industry.

General process engineering support for a facility that is to produce silicon. Responsibilities include project procedures, CAD coordination, standards and specifications. Facility located in Siberia.

Principal Process / Specialty Engineer

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Principal Process / Specialty Engineer

SIPChem Jubail Acetyls Complex

Fluor AA, VAM & Utilities

03 /2006 – 03 / 2007 Al Jubail, Saudi Arabia

A 300,000-TPA Dupont-technology vinyl acetate monomer plant and 400,000-TPA Eastman- technology acetic acid plant

Lead process engineer for a 300,000 mt/yr Vinyl Acetate Monomer production facility to be constructed in Jubail, Saudi Arabia. This design was heavily dependent on work sharing with the Greenville SC and New Delhi, India offices. Design effort consisted of maintenance of P&ID’s, preparation and maintenance of equipment data sheets, hydraulic calculations, preparation of instrument data sheets, preparation of Pressure Safety Relief Valve data sheets, and review of vendor information / vendor bid tab evaluation.

Saudi Kayan Petrochemical Company

Fluor SK Petrochemical Complex - PMC

Services

2005 - 2006 Al-Jubail, Saudi Arabia

Olefins cracker and downstream petrochemical units, including amine derivatives and port facility. Assist in the front end coordination and process management for an amines production c lex to be located in Al-Jubail, Saudi Arabia. The products mix includes Choline Chloride, DMF, Ethanolamines, and Ethoxylates. Design effort involves oordination of the design of the different production facilities and integration of that work into the overall production complex. USEC Inc.

Fluor American Centrifuge Plant (ACP)

2005 - 2005 Piketon, Ohio, United States

Fluor is providing the engineering, procurement, and construction (EPC) for the ACP Project, a uranium enrichment facility incorporating next-generation technology to produce 3.8 MM SWU/year of fuel.

Front End Engineering support for a nuclear fuel proce ing complex. BCI Due Diligence

Fluor BCI Bagess to Ethanol Project

2005 - 2005 Jennings, Louisiana, United States

Process engineer on a team to evaluate the commercial feasibility (Due Diligence) of a proprietary process to convert bagasse to ethanol. Area of responsibility involved process unit operations. Key aspect of the process is a recently developed bacterium, Escherichia Coli K011 which has the ability to ferment C5 sugars resulting from the hydrolysis of hemicellulose thereby increasing the yield of ethanol from bagasse.

Aspen Aerogels

Fluor Aspen Aerogels

2005 - 2005 Rumford, Rhode Island, United States

Process lead on a proposal team to design and construct a facility to produce proprietary nanoporous aerogel insulation.

Shanghai Isocyanates JV

Fluor Integrated Isocyanates Project (IIP)

2004 - 2005 Caojing, Shanghai, China

Managing partner of consortium project with process units for DNT, nitric acid, nitrobenzene, aniline, toluenediisocyanate, and MDI.

Design engineer for an HCl liquefaction – storage – vaporization system. Primary emphasis to identify low differential pressure compressor to enable utility refrigerant F-134a return flow. This required the identification of appropriate technology and vendor coordination. Johns Manville

Fluor Sequoia Pipe Insulation

2004 - 2004 Defiance, Ohio, United States

Design engineer for the Pre-React and Binder Mix/ Delivery Systems for a fiberglass manufacturing facility. Prepare design basis, material balance, PFD’s, equipment data sheets, P&ID’s, and support project estimate.

GE Plastics

Fluor HPP Global Expansion Project

2003 - 2005 Cartagena, Spain

Fluor performed Conceptual and Basic Engineering for the GE Plastics HPP Global Expansion Project, which consisted of an oxidation unit and a 5,000 Mt/yr polymer production facility. Design engineer for a portion of a continuous process to purify Chlorophthalic Anhydride (ClPA). Process involves reactive distillation, heat transfer, and hydraulics. Duties include process administrative support to maintain quality, schedule, and project communications. Design engineer for a batch process to produce a monomer intermediate 4, 4 Oxydiphthalic Anhydride (ODPA). Process scale up from laboratory and pilot plant testing. Prepared Material Balance, conceptual design of process equipment to support estimate, materials selection criteria, and prepared project process design criteria. Amgen

Fluor Amgen Bio-Now

2002 - 2003 Rhode Island, United States

Manager of equipment expediting for a pharmaceutical facility located in West Greenwich, Rhode Island.

Responsibilities included management and supervision of a team of eight engineers to expedite process equipment and instrumentation for a $200 MM production facility. Bio-processing equipment designed to ASME BPE standards, status using Material Manager Software, address quality issues, overcome technical hurdles, participat ment of change process, and motivate vendors to adhere to project construction schedule. Principal Process / Specialty Engineer

Principal Process / Specialty Engineer

Principal Process / Specialty Engineer

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Principal Process / Specilaty Engineer

Principal Process / Specialty Engineer

Georgia Pacific Inc.

Fluor Steam Reformer Project

2002 - 2002 Virginia, United States

Area design engineer for a new steam reformer technology to convert black liquor into a fuel gas for steam production. Project responsibilities involved the revision of equipment and instrumentation specifications to incorporate changes resulting from design reviews and vendor information. These revisions required hydraulic calculations to be updated using Fathom\Arrow software. InTools used for instrumentation. This was a FrontRunner project. Conoco, Inc.

Fluor Carbon Fiber Production Facility

1999 - 2002 Ponca City, Oklahoma, United States

Lead engineer for an 8.3 million lbs/yr carbon fiber production facility. This is a unique facility employing new technology. Proving the operation of this plant will allow a low cost pathway for carbon fiber production.

The project involves the scale-up of a pilot plant facility. The design process was able to successfully adapt to take advantage of a continuing R & D effort. Moreover, as a result of our participation in the design, we have commissioned a longer term research effort to allow for further significant design enhancements. The results of this research will be incorporated into a 50 million lbs/yr facility scheduled for design in 2004. The process group drove a Value Awareness program which resulted in capital savings of 5.1 million dollars for a 180 million dollar facility.

The process involves the recovery of a heart-cut (Decant Oil Distillate) from No. 5 FCC Slurry Oil. An isotropic pitch is produced by thermal polymerization of the Decant Oil Distillate in a furnace. This stream is then processed to separate natural spin solvent from the heavier isotropic pitch

(Thermal Tar).

A mesophase pitch is extracted from the thermal tar, its melt point is increased by heat soaking, and it is then solvated with natural spin solvent and xylene prior to flaking. The melt point is further increased and dimer (the lower end of the mesophase range) is reduced in a two-stage mixer/settler extraction system. The resultant mesophase pitch is then flaked and stored. The xylene solvent is purified and reused.

The flaked mesophase pitch is heated. Melted and pumped to the spinning section. The carbon fibers are laid on a series of conveyors where the temperature is ramped up, solvent is removed and the fibers are heat treated. The fiber mat is wound up and transferred to warehouse. The fiber mat can be chopped or milled for specific applications. Technology of this process consists of heating viscous pitch, high temperature / high viscosity / high pressure pumping applications, spinning carbon fibers, heat treating carbon fibers, graphitization of carbon fibers, chopping / milling carbon fibers. Unique aspects of this project:

A facility of this type does not currently exist anywhere in the world today. We have pushed the envelope with regards to pumping systems (high pressure, high temperature, high viscosity), heat transfer systems (we are currently exceeding recommended temperature constraints for heat transfer fluids), and piping duct systems (our applications have no precedence in the current codes ASME B31.3 or SMACNA.

We had technology partners in the Spinning and Fiber Furnace sections of this facility. It has been a very involved process to earn our partners trust and develop the procedural and communication systems required to maintain progress on this project. Principal Process / Specialty Engineer

Principal Process / Specialty Engineer

Senior Process / Specialty Engineer

Solutia, Inc.

Fluor Specialty Gas Purification Facility

1998 - 1998 Pensacola, Florida, United States

Area lead for the ALPHOX (Benzene to Phenol) Project. The project objective is the commercialization of a pilot plant design to a 300 mil uction facility. Specific responsibility involves the conceptual process design and economic analysis of a Nitrous Oxide purification facility. The Nitrous Oxide is a waste gas which, when purified, is used as a feed stock in the ALPHOX process. The process includes gas compression, SCR (specific catalytic reduction) reactor, and DEOX (Oxygen removing catalytic reactors). The design effort required the commissioning, interpretation, and scale up of laboratory experiments in order to develop comparative economics used to guide the selection of technology. It is anticipated that the technology will be licensable and provide the most economic route to Phenol production. This plant will be located in Pensacola, Florida. Monsanto (Agricultural Products Division)

Fluor Herbicide Production Facility

1997 - 1997 St. Louis, Missouri, United States

Lead process engineer for a front-end design package for a facility to produce PIA, an intermediate for Glyphosate Herbicide. The process primarily consists of batch operations involving hazardous / corrosive slurries. Solid - liquid separations accomplished using filtration and centrifuges. Zirconium, Titanium, and Hastelloy construction employed. Areas of the process required scale up of laboratory experiments. This work involved preparation of test protocols, supervision of experiments, and analysis of test results. The plant will be located in Belgium which required the translation of technology from U.S. to European standards. The process team peaked at 21 individuals. Total estimated cost is $186 M. Amoco Performance Products

Fluor Polysulfone Production Facility

1996 - 1996 Augusta, Georgia, United States

Area lead for a Front- end loaded design effort. Design of a retrofit Polysulfone Polymer production facility to be located in Augusta, Georgia. This particular technology consists of a liquid phase batch reactor in which product quality is directly related to the accuracy of the individual feed charges while project economics dictat actor cycle time be minimized. Therefore, reactor charges had to be accomplished as quickly and accurately as technology would allow.

The polymerization is accomplished by reacting Bis-Phenyl A, Sulfone Monomer, and caustic in a solution of MonochloroBenzene and DimethylSulfoxide. Solvent was reclaimed and purified using both batch and continuous distillation columns.

Senior Process / Specialty Engineer

Senior Process / Specialty Engineer

Senior Process / Specialty Engineer

Process / Specialty Engineer

Hoechst

Fluor Chemical Processing Facility

1995 - 1996 Palau Sakra, Singapore

EPCM for grassroots chemical processing facility

Area lead for the detailed design of a petrochemical process facility to produce 170,000 metric tons per year Vinyl Acetate Monomer (VAM). VAM is produced in a fixed bed catalytic reactor by the exothermic vapor phase reaction of ethylene, oxygen, and acetic acid to produce vinyl acetate and water. The main secondary reaction produces carbon dioxide and water. Purified product is obtained in a series of nine distillation columns which also serve to recover and purify ethylene and acetic acid. Scope included preparation of Front End Engineering Package by adapting the technologies practiced in client’s operating units at different locations for different sections of the Unit integrating the whole facility. The scope also included subsequent detailed engineering for the facility. Responsible for design of reactor, main centrifugal compressor (API 618), reciprocal compressor (API 617), preparation of equipment data sheets for pumps - vessels – heat exchangers, hydraulic – pneumatic calculations, design of instrumentation, Aspen Process Simulation, preparation of Material Balance and Proces iagrams, preparation of Piping and Instrument Diagrams, review of vendor design, design of Pressure Safety Relief Systems, design of Safety Interlock Systems, chair process design reviews, participate in Process Safety Reviews, contribute to Value Engineering effort, prepare process description, prepare – maintain

– status process design schedule, prepare – maintain - status process man hour budget. Ciba

Fluor Multipurpose Herbicide Production

Facility

1994 - 1995 St. Gabriel, Louisiana, United States

Design of a multi-purpose, batch production facility used to produce CGA 152005, a broad leaf weed herbicide. Seventeen chemical processing steps were involved with batch distillation used in purification steps. Discrete Simulation techniques were employed to verify plant capacity. The design of the facility was modular (highly standardized) and multi-purpose. Equipment required for future products was identified and the facility and pipe was designed to allow for future installations. Design documents (P&IDs) were developed in a modular style to allow for minimum rework for other alternative products and production schemes. Elf Atochem

Fluor Refrigerant Fluorocarbon Facility

1993 - 1994 Calvert City, Kentucky, United States

Design of a facility to produce an environmentally saf frigerant fluorocarbon (F-134a) with no ozone depletion potential. Process involves the production of an intermediate compound (F-133a) in a liquid phase catalytic reactor by reacting trichloroethylene with hydrogen fluoride in the presence of a liquid catalyst. Final reaction to product occurs in a gas phase fixed bed reactor. By- product hydrogen chloride vapor is used to produce a food grade hydrochloric acid. Confidential Client

Fluor Synthetic Gas Plant

1993 - 1993 Greenville, South Carolina, United States Member of a team for the conceptual design effort for a Syn Gas production facility. Project involved the production of carbon monoxide by steam reforming a refinery off gas and the evaluation of licensable technology for product purification. Participated in the preliminary engineering and process development. The facility will produce 112,000 tpy of carbon monoxide which will serve as feedstock for an acetic acid plant. The project includes a steam reformer, amine absorption unit, molecular sieve, and cryogenic unit. Investigated the use of Cosorb, Sulfinol, and membrane systems for gas purification. Tennessee Eastman

Fluor Cellulose Acetate Production Facility

1992 - 1993 Kingsport, Tennessee, United States

Design of a 60,000 mt/yr facility utilizing Rhone Poulenc and Tennessee Eastman technology. Area lead for the acetic acid recovery, solvent recovery, and waste solids minimization production areas.

Glacial acetic acid recovered from process via a liquid-liquid extraction of weak acid with organic solvent and concentrated with azeotropic distillation. Reactive distillation employed to produce isopropyl acetate via the esterification of isopropyl alcohol and acetic acid. Olin Chemicals

Fluor Aliphatic Di-Isocyanates Plant

1991 - 1992 Lake Charles, Louisiana, United States To enter the ADI market, development of new technology and construction of new facility Design Engineer for an aliphatic di-isocyanates production facility. Responsibilities include refrigeration unit, secondary containment for lethal gaseous missions, material selection for secondary containment of liquid hazardous wastes, cooling tower specification, coalescer design, design of carbon bed-molecular sieve liquid absorption systems. Amoco Performance Products, Inc.

Fluor Utilities upgrade

1990 - 1991 Augusta, Georgia, United States

Supported product expansion Upgrade to include 60,000 pound/hour steam generator, cooling tower, DI water system, and increased fuel oil and natural gas deliverability. Sun Chemical Corporation

Fluor Heatset Printing Ink Facility

1990 - 1990 Germany

Design of 30,000 metric tons per year grass-roots heatset printing ink facility to be constructed in West Germany. This required technology for viscous flow and agitation for a batch blending procedure. DIN standards used.

Amoco Performance Products, Inc

Fluor Waste Treatment Facility

1989 - 1990 Marietta, Ohio, United States

Design of a batch process liquid waste treatment facility utilizing Fenton's reaction to catalytically oxidize Monochloro Benzene using Hydrogen Peroxide. Process upgrade and debugging of aromatic polysulfone polymer facility.

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Process / Specialty Engineer

DuPont

Fluor Dupont Lycra

1988 - 1989 Waynesville,, Virginia, United States

Production increase of elastomeric urethane polymer (Lycra-Spandex fiber). Responsibilities included preparation of Process Flow Diagrams, Process detailed engineering for proprietary polymers. Process calculations prepared concerning fluid flow, heat transfer, solid liquid contacting, gas-liquid separations, agitation design for polymer batch reactors, molecular sieve technology and design of act ated carbon systems. Employer : Department Of Energy, Morgantown, WV

1985 - 1988

Conducted reservoir engineering study of natural gas production potential for Devonian Shale reservoirs. Technology required use of pressure transient analysis for dual-porosity, naturally fractured reservoirs. Reservoir simulation accomplished via use of SUGAR, G3DFR, and BOAST numerical simulation packages. Analysis conducted in W t Virginia, Pennsylvania, New York, Ohio, Kentucky, Michigan and Illinois. Conducted production field test and analysis of a horizontally drilled wellbore in Wayne County, West Virginia. Responsibilities included selection and installation of all hardware and instrumentation, production test design, training of field personnel, analysis of test results via pressure transient analysis methods, and numerical computer simulation of gas reservoirs to characterize production potential. Conducted in-house seminar to educate staff as to the basics of reservoir engineering in the natural gas industry.

Employer: Baxter-Travenol, Deerfield, IL

1980 - 1983

Engineering support for capacity expansion and increased production efficiency for bio-medical products and parenteral solutions. Facilities located in Cleveland, Mississippi, North Cove, North Carolina and Morton Grove, Illinois. Involved in many diverse projects in the medical products industry of both the staff and plant level. Prepared the equipment requirements and procurement for a facility in Brazil to produce blood packs for blood donation. Completed miscellaneous process fluid and air requirements involving sanitary conditions and GMP. Involved in the installation and debugging or European equipment (KIEFFEL) to automate the production of flexible containers for intravenous solutions. Process involved the use of microwave energy to seal PVC film.

Employer: Koppers, Cicero, IL

1979 - 1980

Process engineering support for a petrochemical facility, phthalic anhydride produced from ortho- xylene in a fixed-bed catalytic reactor licensing BASF technology. Maleic anhydride isolated from waste stream. Process engineering support for the production of anthracene, cresylic acid, napthalene and pitch from coal tar of some location. Process / Specialty Engineer

Languages:

Reading Proficiency Speaking Proficiency Writing Proficiency Professional Associations:

Employer: GOULD, INC., Rolling Meadows, IL

1978 - 1979

Engineering design and pilot plant production support for a rechargeable battery system for an electric vehicle.

Conducted research and development activities for a Nickel-Zinc Battery System. Performed battery testing to verify capacity and longevity. Conducted and managed field tests

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