cv_eugene_engels 2015 attachment

Summary: Having worked on multiple grassroots and revamp refinery projects in FEED and EPC phases Eugene
gained broad knowledge in many fields of the Oil & Gas and Petrochemical industry. His practical refinery
experience was expanded by multiple construction/commissioning/startup assignments to the
construction site, following the home office EPC phase. In doing so, Eugene gained direct and practical
work experience in the following process fields:
- Refinery: Hydrotreating, Hydrocracking, Gas Plants, Fractionation, Sulphur/Sour block, Visbreaker,
Crude/Vacuum Distillation, Hydrogen Production, PSA; participated in feasibility/FEED/EPC phases.
- (Petro-)Chemical: Steam cracker and auxiliary units, Pygas, MTBE, Polysilicon in feasibility and FEED
phases.
Further expertise was obtained in the Utilities & Off-sites (Storage and Logistics) area for these projects.
In the Rotterdam area, having worked for various local clients, experience was gained in the field of fire
fighting, terminal expansions and water hammer issues.
During these projects substantial amount of project engineering capabilities were developed, dealing
with many clients, downstream disciplines and the requirement of designing and engineering co-
currently in tight-schedule projects. On top of that extensive lead experience has been obtained with
multi-office project execution.
Strong points of Eugene are the ability to focus on deliverables during tight-schedule projects, and his
practical approach to the design of process units. His specialty is being project-minded, keeping
momentum in a multidisciplinary team and working in multi-project environments.
For more information, see end of document.
Specific Experience:
CB&I Senior Process Engineer
Area Lead engineer Orpic, LIWA Plastics Project
07/2014 - current Sultanate of Oman
This project comprises a complete grass-roots petrochemical steam cracker complex, including U&O. Area Lead engineer in
PDP and FEED phase of the MTBE unit, Butene-1 unit and Pygas unit. Leading team of 3 in-house engineers, and 6 engineers
at MOPEX location for schedule driven project.
Lead engineer Shell Deutschland Öl, Staircase Project
02/2013 - 07/2014 Wesseling, Germany
Capacity increase and safety upgrade of steam cracker unit. Complex revamp project in schedule/turnaround driven project
with >1500 tie-ins, new heat integration equipment and 750 new instruments.
- Lead engineer in Basic Engineering phase with supervision of 2 process engineers.
- Assignment at Shell, Wesseling, Germany: Lead process engineer in Detailed Engineering and EPC phase. Supervision of 6
process engineers.
Contractor for Steven Parc technical specialists Senior Process engineer
Assigned at Spie Controlec Engineering Multiple projects, Schiedam
Clients Shell Europoort, Argos Terminals, Rubis Terminal, VTTI,
Rijkswaterstaat, Shell Global Solutions, Cabot, Nufarm.

06/2012 – 02/2013 Rubis Terminal, Botlek
Lead engineer for various terminal expansion projects; New tanks, pump stations, jetty’s, pig stations. Performed product
routing studies and relief valve studies. Due to the active expansion program several projects were run in concurrent
engineering mode. This required a strong focus on progress and schedule, while maintaining the overview on all running
projects. Worked closely with piping department in order to secure client requirements and deliver according schedule.
07/2012 – 10/2012 Argos Terminals, Pernis
Lead engineer for firewater expansion project; Study lead of fire water screening study for a multitude of terminal expansion
options, developing into basic engineering. Supervision of 2 process engineers.
06/2012 – 10/2012 Miscellaneous projects
Provided consultancy for several other projects:
- Safeguarding Memorandum for complete Olefins pilot plant for major Dutch oil & gas client (confidential)
- Water hammer study for several Rijkswaterstaat tunnel projects
- Water hammer study VTTI/Vitol tank terminal
Focus was on keeping strong focus on quality of the deliverables of engineers, while delivering according client schedule,
thereby accommodating smooth transition to next phases.
FLUOR Senior Process Engineer
Process engineer / Process Area Lead engineer Ruhr Oel GmbH/ BP Gelsenkirchen
Margin Improvement Program
06/2010 – 05/2012 Gelsenkirchen, Germany
The overall objective of MIP is to improve refinery margins by a number of modifications in the equipment and operation of
the refineries in Horst and Scholven.
Process engineer (06/2010 – 08/2011):
- Assigned as process engineer on the revamp of the Scholven hydrocracker unit to investigate the implications of using a
new middle distillates selective catalyst, selectively producing kerosene and vacuum gas oil (Diesel or Light Heating Oil. The
units under investigation were the hydrocracker unit, fractionation unit and gas/amine plant.
The "Appraise" phase consisted of building simulations for these three units based on Licensor yield estimates and
subsequently establishing the expected hydraulic and equipment bottle-necks.
During the "Select" phase defined the scope for mentioned units, prepared equipment datasheets, developed PFDs and
P&IDs, prepared input to line list and developed control and safeguarding narratives. Attended HAZOP for these units.
Performed process design for internals for the extensive fractionation section revamp.
- Assigned as process engineer on the revamp of the Scholven crude and vacuum unit to improve cuts between middle
distillates and as a result improve overall refinery profitability.
During “Appraise” and “Select” phase developed heat & mass balances based on simulations, identified scope, attended
HAZOP. Focus was also put on constructability in congested areas. During all phases of these projects performed checks of
deliverables of co-workers and discussed results with client.
Process Area Lead engineer (08/2011 – 05/2012):
During “Define” phase assigned as area lead engineer for the hydrocracker unit and the crude/vacuum unit. During this phase
acting as direct contact person for counterpart at client side. Actively participated in vendor clarification meetings.

Maintained short communication lines with all departments in order to define scope during tight schedule. Hosted internal
and external P&ID reviews. Performed process design for internals for the extensive fractionation section revamp.
Process Engineer OMV Refining & Marketing GmbH
Fluor Development of General Process Design Criteria
03/2010 - 06/2010 Vienna, Austria
Engineering study for the development of General Process Design Criteria.
Co-developed Process Design Criteria document. Coordinated development in mutual effort between Process and
Mechanical department. Participated in review and progress meetings with the client, both in-house by telecon and at OMV
headquarters.
Process Engineer Shell Refining Company (Fed. of Malaya) Bhd.
Fluor Hijau Gasoil FEED Project
12/2009 - 01/2010 Port Dickson, Malaysia
The project basic design and engineering package is being produced for an HDS to process 6300 tpd diesel to Euro II quality
and the possibility, with limited additional equipment, to produce Euro IV (M).
Prepared Control and Safeguarding Narratives and Shell standard Safeguarding Memoranda for SWS and LP ADIP unit.
Checked work of co-engineers in same field. Acted as Fluor's focal point for Shell's Flawless Project Delivery (FDP) program in
the field of Commissioning and Startup.
Process Area Lead Engineer Confidential
Fluor Confidential
04/2009 - 12/2009 Jubail 2, Saudi Arabia
FEED services for the 3,000 ton per year polysilicon plant with TCS (hydrochlorination), polysilicon, off-gas recovery and
associated U&O were completed in 5.5 months.
Assigned to Utility & Off-sites area of Demin/De-ionized Water, BFW, Steam & Condensate, Caustic and HCl Acid system.
Responsible for developing system Basis of Designs, issuing datasheets/duty specs, PFD's/UFD's, P&ID's, Utility Distribution
Diagrams, and Control Descriptions + Cause & Effect diagrams. Coordinated integration of TKHP steam system with Fluor
steam system. Developed overall Basis of Design for all Utilities used on the project. Participated in Value Engineering
workshop.
Process Engineer Confidential Client
Fluor Integrated Solar Complex Feasibility Study
08/2008 - 10/2008 Saudi Arabia
The scope of the feasibility study involved a Silicon Smelter, a solar-grade Polysilicon Plant and a Photovoltaic Panel
Manufacturing Facility including centralized auxiliary, infrastructure and utility systems. The feasibility study was concluded
with the delivery of a Class 5 capital cost estimate.
Participated in identifying and developing all utility and infrastructure scope for this grass-roots project and provided input
for the cost estimate on all utility systems and the study report.
Process Area Lead Engineer The Silicon Mine
Fluor Solar-Grade Polysilicon Plant

03/2008 - 08/2008 Geleen, Netherlands
The purpose of the grassroots project was to produce solar grade polysilicon for the production of solar cells; Fluor
performed conceptual, basic engineering and transition to the EPC phase.
Assigned as a Process area lead engineer on utilities and interfaces, supervising a team of three Process Engineers with
different levels of experience. The utility scope comprised of Plant/Potable/Demin/Cooling Water storage and distribution,
Plant and Instrument Air distribution, Nitrogen purification and distribution, Refrigeration package, Hydrogen generation
unit, Steam/Condensate collection, Caustic storage and distribution and Waste Water pretreatment. Activities on the project
included development of P&ID's, issuing of equipment datasheets, participating in interface meetings with client and third
parties. Worked in a worksharing environment with a Global Execution Center based in Asia.
Process Engineer Bayernoil
Fluor ISAR Project
10/2005 - 03/2009 Neustadt and Vohburg, Germany
Fluor performed the study, FEED, and EPCM of a large program consolidating three refineries into two sites.
Assigned as a Process Engineer in the basic and detailed engineering phase of a new Mild Hydrocracker. Main responsibilities
were hydraulic analysis of the high pressure loop; establishing design conditions; generation of equipment datasheets
(process data); relief valve/flare load calculations, control valve specifications; HAZOP participation; ISBL utilities.
Also worked as a site engineer on the Logistics part of the project during a 6 months assignment. Revamped various parts of
the tankage area (piping, pumps, tanks, instrumentation, etc) in close operation with the client based on the new flow data
from the revamped processing units. The work included getting all OSBL P&ID's Released for Design, specify pump
datasheets, perform a HAZOP.
Back in the office worked on the basic engineering of a revamp of a Visbreaker including a Vacuum Unit. The work included
making the P&ID's Released for Design, perform a HAZOP, specify Process Datasheets for equipment and instrumentation,
etc.
Assigned to site as a Process site engineer again for a period of 5 months to assist the construction workforce. Process units
included Mild Hydrocracker and revamped Fractionation Unit, Visbreaker and Vacuum Unit, Hydrogen Generation Unit (SMR)
and the Sulphur Block. Also assisted during commissioning and startup of these units.
Process Engineer Petrom
Fluor Gas Oil Hydrotreating Unit Modernization
03/2005 - 09/2005 Petrobrazi, Romania
The objectives of the project were to increase the gasoil capacity to 1,250,000 t/y and to reduce the product sulphur content
to 10 ppm; equipment included a reactor, feed heater, recycle gas compressor, and make-up gas compressor.
Main responsibilities in the FEED-phase of the project were issuing equipment datasheets, establishing utilities consumption,
development of utilities drawings, hydraulic check of low pressure loop, issuing instrument datasheets of low pressure loop,
defining Turnover Systems and commissioning plan.
In the final phase of the project worked on site as a Commissioning and Startup engineer. This included (pre)commissioning
of the Hydrotreating Unit and PSA unit and startup of both units.
Process Engineer BAM
Fluor Balgzand Bacton Line
09/2004 - 03/2005 Anna Paulowna, Netherlands
The scope of Fluor is detailed engineering and design services required for the construction of the Compressor Station
Noord-Holland by others. The Compressor Station NOORD-HOLLAND will play an important role in the distribution of natural

gas from the Netherlands to the United Kingdom. The Compressor Station will be designed to mix, measure and transport
natural gas from the gas fields of the Dutch part of the "Continental Plat" via a transport line to Bacton in England.
Main responsibilities on the project were: issuing datasheets for equipment and instruments, generating heat & material
balances, writing the operating manual and designing the vent philosophy.
Languages:
Reading Proficiency Speaking Proficiency Writing Proficiency
Dutch Fluent Fluent Fluent
English Fluent Fluent Fluent
French Average Below Average Below Average
German Fluent Fluent Fluent
Russian Beginner Beginner Beginner
Training:
VCA for Managers, PBNA (2013)
Distillation Design & Operation by H. Kister (2007)
Lead Engineer Course, Fluor (2010-2011)
Lead Engineer Course, CB&I (2014-2015)
Salary indication of job offerings:
The following is an indication of minimum gross salary requirements for a new position. This indication is
added to set the correct basis for recruiters offering any a new position. However, this is just part of
package deal.
Netherlands Europe / World
- Lead function fixed contract: € 85,000.- - To be discussed
- Lead function agency contract: € 95,000.-
- Non-lead function fixed contract: € 95,000.-
- Non-lead function agency contract: € 105,000.-

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