Resume - HYSYS/PROII/NGL/LPG/LNG/SYN GAS - CONCEPTUAL, FEED AND DETAIL

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Resume #78709

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SUMMARY OF EXPERIENCE:

Key Responsibilities

To provide support to energy project developers including:

o Feasibility studies, Technology reviews, & economic appraisals o Project management of planning & consenting processes o Project concept design and specifications o Technology selection o EPC negotiation support

Project development, Define and develop scope of work (SOW) and schedule and signed agreement on SOW with client. Project meeting notes execute. SOW includes process estimate, process development, and process document and process communication.
Simulation model - Gas Process(LTS, DewPoint Control, Depropanizer)(HYSYS/PROII), Crude Atm Distillation(Pump around, Side Stripper with Kerosene, Diesel and AGO(HYSYS). Amine Unit(HYSYS), CSTR reactor propylene oxide react with water to product glycol(HYSYS).

(1) Conceptual basic design/Front End design. Gasification (included pyrolysis) technology on BTL, CTL and GTL. Gas treating (Rectisol/Selexol/Amine) and processing experience (SYNTHESIS GAS and METHANE). Cryogenic separation(N2,ASU), PSA, Sour gas removal, Sulfur recovery, Steam methane reforming, Oxygen blown gasification, Air separation, Multi-stage Molecular sieve; Steam reforming, syngas clean, water gas shift, FT process, and utility requirement. Coorindinate with other process license on Haldor Topsoe, Sofregaz, Sofresid and Axens

(2) Conceptual basic design/Front End design/detail design/construction. Upstream/downstream and onshore/offshore (included FPSO) in gas process and process separation sequence. Slug catcher, Crude oil/water/gas separation, Desalter, dehydration, dew point control, gas compression, NGL/LPG, sour gas removal, advanced process control (APC) in gas process optimal. Cryogenic process (N2, Air separation unit (ASU)) and PSA. Familiar with ConocoPhillip LNG 3 streams refrigerate loop that is similar to what I developed the mixed refrigerates.
Projects are steam methane refroming, biomass to liquid (BtL) gasification ( pyrolysis) syngas cleaning, cryogenic process (N2), air separation unit (ASU), natural gas process (NGL/LPG) with onshore and offshore, sour gas removal, pipeline (sub sea/ground)
Special technology: mixed refrigerate process [1], advanced process control in gas process [2]. Process skill is process technology evaluation (license/non license), economic analysis, process development, design basis, process description and oversee EPC. Detail skill is process simulation, material & energy balance, PFD/PID, metallurgy, relief load, equipment specification (vendor package[3], pump, distillation column, API vessel and tank, heat exchanger rating/design, and line size) and process instrument specification (control valve, relief valve and associate). Operation procedure (normal, start up and emergency shutdown).
Notes:
[1] In the refrigeration system, small molecular refrigerate is to use less energy to cool down but use more energy to compress. The converse applies in the large molecular refrigerate. Cryogenic process required the different level cooling power by using the mixed refrigerates that can meet the different level cryogenic process need. And will save compressor and condenser horse power in refrigeration system.
[2]Provide model base control for natural gas process plant. Simulation, statistical regression and nonlinear multivariable control to build model base control. Calibrating the real time data from natural gas process (NGL/LPG), amine process (sour gas removal process) and sulfur recovery unit are for building simulation. The model base control can gain process operation flexible and profitable for the plant. The method is very successful. Perform well successful on 3-amine unit at Texaco in New Mexico, NGL/LPG unit in South American client and sulfur recovery unit for another client. HYSYS, PRO-II and TSWEET are used for simulation. Coordinate and integrate model with instrument engineer and programmer.
[3] Vendor package: plate heat exchanger, slug catcher, dehydration, and compressor
DETAIL EXPERIENCE
CHOREN USA
CHOREN Carbon V technology is the first license on pre commercial for Biomass to liquid (BtL) (40MW/160MW) gasification technology. Define, develop and schedule scope of work with client. Develop and modify on design basis, process option, process description, PFD, stream list/equipment list, utility requirement and operation procedure (normal, start up and emergency shutdown). Attend gasification technology and BtL process facility (40MW) training in Freiberg, Germany. Working on CEA Project (40MW) Pre FEED study to produce BtL and For Energy (160MW) Pre FEED study to produce H2. Special study on syn gas cleaning process (Rectisol/Selexol/Amine), Fischer-Tropsch process, IGCC, water gas shift process (convert CO to H2), steam reforming process, cryogenic process, air separation, methanol process(ICI and Lurgi), methanol cracking process, ethanol water separation. Coorindinate with other process license on Haldor Topsoe, Sofregaz, Sofresid and Axens. Coal to liquid (CtL) has under construction in China. (License)
BECHTEL
Develop refinery pilot plant for Chevron, Pascagoula, Mississippi. Responsibility for develop, review and modify the new process for Hydrotreating and sour gas removal process. (EPC).
NASA/JSC (LOCKHEED MARTIN)
Minus Eighty degree Celsius (-80C) Laboratory Freezer (MELFI) for International Space Station (ISS) - As NASA technical monitor for MELFI from review cryogenics process design, test, operation, emergency application, safety assurance and flight hardware integrate into ISS US module. Coordinate subcontractors. One of the core Tiger team members to provide solution for any emergency issue and issue solution presentation. (License/Operation)
GE CONTENTIAL CONTROL
Developing model base control for Gas plant (South American client), Amine Plant (TEAXCO), Sour gas recovery Plant (TEXACO). Provide model base control for natural gas process plant. Simulation, statistical regression and nonlinear multivariable control to build model base control. Calibrating the real time data from natural gas process (NGL/LPG), amine process (sour gas removal process) and sulfur recovery unit are for building simulation. The model base control can gain process operation flexible and profitable for the plant. The method is very successful. Perform well successful on 3-amine unit at Texaco in New Mexico, NGL/LPG unit in South American client and sulfur recovery unit for another client. HYSIM, PRO-II and TSWEET are used for simulation. Coordinate and integrate model with instrument engineer and programmer. (License)
KBR
British Petroleum (BP) NGL/LPG projects - Process study for is in north Alaska (North Star). Hysim is to develop and analysis process by changing composition and equation of state. (E)
Qatar General Petroleum Company (QGPC) NGL/LPG lump sum project - Process study for NGL/LPG in Brown & Root London office. Joule Thomson valve, turbo expander and C2 recovery split column are developed for NGL/LPG/Condensate recovery curve from year 1 to year 26 that is based on C2 recovery. Equipment is chosen for the different process model in the operation. Equipment size is prepared to analysis cost estimation and financial plan. Hysim is developed to study process. (EPC)
BP in Colombia Exploration - Front-end design is for BP in Colombia Exploration. Project scope covers to develop process to meet the different NGL/LPG specification. Process are included low temperature separator (LTS), fractionation, propane refrigeration system and hot oil system. Hysim is developed to study process (E)
United Arab of Emirates (ANDOC) onshore gas process / pipeline gathering project - Front-end design is for is the onshore gas development project. Project scope is covered to design the supply gas for the nationwide distribution of fuel gas, to recovery NGL, to export NGL/gasoline and to reinject gas to reservoir. Process design is included LTS, fractionation and refrigeration system. Hysim is to developed process model. (E)
Arco Chemical Co. and China Petroleum Co. (Arco/China) onshore/ offshore process and sub sea pipeline - Front-end onshore and offshore process design project is for the Arco Chemical Co. and China Petroleum Co. (Arco/China). Gas well is located on the south of China Sea. Project scope is covered that condensate is separated from raw gas on the offshore platform, then dehydrate and compress gas to Hong Kong. Condensate is pumped to Hainan Island from the offshore platform. Process design is included wellhead design, LTS, dehydration and fractionation on the offshore. Wax handling, receiving/pumping station and pipeline design at Hainan Island. Hysim is developed to study process. (EPC)
United Arab of Emirates (ADOC) onshore gas gathering development -Front end design is for the onshore gas gathering development in the United Arab of Emirates (ADOC). Project scope covers to design the gathering oil and gas pipeline from wellhead to the central plant. Pipephase is to study pipeline simulation. (E)
STONE & WEBSTER
Development Ethylene Process front end project for Han Yang Company (Korea). PFD/PID, Process simulation, equipment spec (pump(min flow)/compressor/heat exchanger/separator/distillation column), line sizing, instrument spec(control valve, relief valve, on/off valve, ESD valve),utility (flare header, KO drum, steam system)
FLUOR DANIEL
Chinese Petroleum Co. diesel/gasoline pipeline - Detail engineering design is for diesel/gasoline pipeline for Chinese Petroleum Co. (CPC). Project scope covers to design pumping/receiving station, pipeline, and storage tank facilities and to write operation manual. (E)
Detail engineering design BTX (UOP) unit is for Chinese Petroleum Co. (CPC) - Project scope covers to check material & energy balance, PFDs, PIDs, design equipment, heat exchanger rating/design, line size,
And process instrument data., Utility design is included steam/condensate, cooling water, flare system, plant air, drain system, storage tank and wastewater treatment. (E)
Engineering design for sprinkle system of LPG storage tank is for CPC - Process design is included pump calculation and selection, line size, sprinkle distribution system and safety issue. (E)
Front end design extractive distillation C4/C5 is for CPC - Project scope covers from process simulation, material & energy balance, PFDs, PIDs, design equipment, heat exchanger rating/design, line size and process instrument data. (E)
EXXON MOBIL

Plant process engineer is in ammonia/urea unit. Process study and troubleshooting are the major work in the unit. (Operation)

9/2008 - now Choren USA, Houston, TX, Sr. Process Engineer
5/2008 - 9/2008 Bechtel, Houston, TX, Sr. Process Engineer
2/2002 - 5/2008 Gas process consultant Sr. Process Engineer
9/1996 - 2/2002 Lockheed Martin Houston, TX, Project Engineer
2/1996 - 6/1996 GE Continental Control Houston, TX, Staff/Simulation Engineer
3/1991 - 2/1996 Brown Root Houston, TX, Process Engineer
9/1989 - 3/1991 Stone & Webster Houston, TX Process Engineer
9/1985 - 12/1988 Fluor Daniel Taipei/Taiwan, Process Engineer
6/1980 - 9/1983 Taiwan Fertilization Co. (Exxon Mobil) Malio / Taiwan, Process Engineer

References: Available upon request

1. Steady State or dynamic process simulation using PROII, HYSYS or ASPEN
2. Preparation of PFDs, P&IDs and datasheets
3. Equipment sizing & rating and hydraulics
4. Safety relief sizing and HAZOP analysis

Knowledge of API methods
Major Responsibilities/ Functions:
1. Evaluate chemical processes and unit operations to improve operating efficiency and rate, product quality, on-stream factor and economy.
2. Process improvement, plant optimization, plant debottlenecking, and energy and material balances.
3. Designing, installing and commissioning new product units, monitoring development (that is modifications and upgrades) and troubleshooting existing processes.
4. Using computer modeling and simulations to design and evaluate processes and operating systems for the manufacture of products.
5. Preparing reports, PFDs and P&IDs and ensuring the process works at the optimum level, to the right rate and quality of output, in order to meet supply needs
6. Making observations and taking measurements directly, as well as collecting and interpreting data from the other technical and operating staff involved.
7. Review all process designs and modifications for safety implications/requirements. Preparing Line Design Tables and updating equipment lists.
8. Chemical process engineering work involving simulation and design of chemical plants, equipment sizing and preparing engineering drawings.
9. Development of steady state and dynamic simulation applications of refineries, petrochemical plants, and gas plants

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