Engineer Process

CURRICULUM VITAE

Senior Process Engineer

Zaman Azimi

*.*.*****@*****.*** Tel:+628**********

PERSONAL INFORMATION

Date of Birth: Aug-1977

Nationality: Iranian

Gender: Male

EDUCATION

March 2005 Iran University of Science and Technology, Tehran, Iran

M.Sc. in Chemical Engineering, Direction of Simulation & Control of Processes

Sep. 2000 University of Tehran, Tehran, Iran

B.Sc. In Chemical Engineering, Direction of Natural Gas Industries Engineering

LANGUAGES

English: Good command of writing and speaking

France: Get started

Farsi: Native

SOFTWARES

Professional softwares:

HYSYS, FLARENET, FLARESIM, PIPESYS , PIPEPHASE, PIPESIM,

PROVISION, BJAC

General softwares:

Office (Word, Excel, Power point), Microsoft Windows, MATLAB and AutoCAD

HIGHLIGHTS OF QUALIFICATION

• Experience in Process (Chemical) engineering (Pre FEED,FEED preparation, Detailed engineering, Procurement, Development, Review and Endorsement)

• Acquainted with relevant international standards like DEP, GS, ETP, API, ASME, NFPA, IPS

• Expert in Emergency Depressurisation (EDP) calculations with HYSYS Software.

• Extensive expert in preparing and development of Process Flow diagrams (PFD’s), Utility Flow diagrams (UFD’s) and Piping and Instruments diagrams(P&ID’s).

• Extensive expert in preparing HEAT AND MASS BALANCE TABLES for process and utility and UTILITY CONSUMPTION calculation note

• Extensive expert in sizing of one, two and three phase fluids lines and polymer (non newtonian fluids) lines and CAUSE AND EFFECT charts,

• Expert in Pressure safety valves (PSV’s), RUPTURE DISK and VACUUM RELIEF VALVES sizings,

• With strong skills in equipment sizing and preparation of all calculation sheets and/or process data sheets for vessels (Two and Three phase), Tanks, Silos, Heat exchangers (Shell and tube, Air cooler, Plate type), Filters, Pumps (Centrifugal, Gear, Reciprocate) and Control valves,

• Providing technical assistance to other groups for preparation of their documents (answering to IDC’s),

• With skills in preparation of Process Specifications documents: Process design basis, Process design criteria and Process and utility description,

• Experience in a whole HAZOP study of a Plant.

• Vendor drawings /documents checking of equipment or package from process point of view,

• Specifying process requirements associated with package units, attending packages/equipments kick-off meetings and checking vendor documents,

• Experience of tender documents endorsement and preparing the report of major slippages, their causes and proposed corrective actions,

• Highly motivated, creative, versatile and having demonstrated ability to work in a multidisciplinary team environment.

PROFESSIONAL EXPRIENCE

1) PT. Nippon Steel Construction Indonesia (NISCONI), Jakarta, Indonesia

Jan 2010-Onward

1-1)South Mahakam development project- EPC project

Client: Total E&P Inonesie

Jan. 10-Onward

Position: Senior Process Engineer/Lead process engineer

South Mahakam is a gas condensate field located in East Kalimantan, Indonesia, approximately

some 25 kilometres from the Balikpapan shore. The principal areas comprising the South Mahakam Field include Stupa, East Mandu, Jumelai and Jempang-Metulang. The current Phase 1 development includes the 2 platforms in Stupa field (one in Main Stupa and one in West Stupa) and one plarform in East Mandu field.

Platforms are unmanned, as well as the other South Mahakam Wellhead platforms. Facilities shall be controlled & monitored through the existing SENIPAH BSP Control Building,which controls and monitors the Peciko field as well. The Stupa field production will be routed through Main Stupa directly to Senipah through a 24” gas line. The production of East Mandu shall utilize a tie-in to the 24” line utilized to route the Stupa field production to Senipah.

Reporting to Lead Engineer/Project Manager, I was responsible for:

• Preparing Process document register and participating in preparing the project schedule and resource management plan, Supervision/preparation process documents (Including PFD, P&ID’s, calculation notes,Safe chart, ESD logic Diagram ….

• Reviewing basic design dossier for any errors, omissions, deficiencies, inaccuracies, contradictions and/or discrepancies; and preparing endorsement report,

• Providing technical assistance to third parties( providing scope of work for Pipeline network hydraulic calculation)

• Liaise with Client/other disciplines on technical matters.

• Contribution to a whole HAZOP study of the South Mahakam project(Including Offshore and Onshore).

1-2) Project: Yetagun Phase 4 Project (Brown field Project)-Design review

Jan. 10-March 10

Position: Senior Process Engineer

PCML is operates the offshore Yetagun gas field located approximately 200 km southwest of Dawei in the Andaman Sea offshore of Myanmar. Produced gas and condensate are being separated and dehydrated in an offshore production platform. Clean dry gas is exported Clean dry gas is exported to PTT in Thailand via 24” pipeline but condensate is being delivered to FSO (Floating, storage and Offloading) via 6” subsea pipeline.

PCML has drilled 4 wells in 2008 to increase the sales gas reservers and prolong the plateau to meet Gas Sales Agreement and will install a booster compression platform under the current project (Phase 4).

Reporting to Lead Engineer, I was responsible for:

• Reviewing basic design dossier/Rev. A Detail engineering documents for any errors, omissions, deficiencies, inaccuracies, contradictions and/or discrepancies,and preparing report. Following documents checked:

Design basis/Criteria

PFD’s/P&ID’s (Demoltion/Modification)

Adequacy check of equipment, lines , packages and instruments(For existing facilities)

Calculation note of Equipment, lines and Instruments(for new facilities)

Simulation report

Flare and blowdown study

• Attending in design review meetings

2) Sadra Co., Tehran, Iran

May 09-Dec 09

2-1) SADRA company, Tehran, Iran

May 09-Dec 09

Position: Senior Process Engineer-Part time

The Reshadat oil field is located in the Persian Gulf, 110 km south-west of Lavan Island. The project comprises one satellite wellhead platform and a central complex including production, living quarters, wellhead and flare platforms. Produced oil from the facilities will be exported via a 16" pipeline to Lavan Island. The produced gas will be compressed for export and also for injection into the gas injection well. Because of the changes in composition of feed and other changes, this project was Rebided.

Reporting to Process lead/Process head, I was responsible for:

• Reviewing basic design/detail design documents done by subcontractor for any errors, omissions,

Attending in meetings with vendors of equipment and packages and Evaluation of vendors from process point of view and Supervision on applying engineering procedures to insure compliance with the quality program

3) PT Technip, Jakarta, Indonesia

March 08-March 09

3-1) Project: Block-A gas development Project-Feed Phase

Nov 08-March 09

Client: Medco Energy

Position: Senior Process Engineer

PT MEDCO E & P MALAKA, as operator, plans to develop the Block-A gas reserves for sales gas export to PLN power station and PT PIM. The Block-A gas field is located in Aceh (Nanggroe Aceh Darussalam), Indonesia. The project envisages development of two production stations, namely, Alur Rambong Station and Alur Siwah Central Processing Plant (CPP) located either in the onshore or the offshore of North Aceh or East Aceh Region. Alur Siwah CPP will be located 10.5km south of Alur Rambong Station.

Alur Siwah CPP production facilities will be designed for producing sales gas equivalent to heat value of 110 BBTU/D. The wet gas will be sweetened (H2S & CO2 removal), dehydrated, dew point controlled and exported to PT PIM. Sales gas from Alur Siwah CPP will be exported to Exxon Mobil SLS A which is 20km away from Alur Siwah CPP.

Reporting to Lead Engineer, I was responsible for:

• P&ID’s development and providing operating and control philosophy

• Supervision on providing Shutdown hierarchy diagram, process equipment sizing calculation, equipment process datasheet and instrument process datasheet

3-2) Project: Java Rehabilitation Project-Phase 3+(Pre-FEED)

Jul 08-Sep 08

Client: BP West Java Ltd.

Position: Lead Process Engineer & Echo/Papa Flow Stations Lead engineer

BP West Java Ltd. intends to rehabilitate the production facilities at Offshore North West Java. The risk reduction is focused on the MAR and MAHAR/HAZOP reports,Texas City Follow Up,Integrity/Defects findings and ETP Conformance.

Phase 1 consists of Mike Mike flow station, phase 2 KLA and Lima and phase 3+ is for other flow stations (Echo, Uniform, Foxtrot, NGL,NUI, Papa, AA, Zulu, ORF and Bravo ).

As a lead engineer for Echo and Papa F/S and lead process engineer, reporting to project manager , I was responsible for:

• Reviewing PFD and P&ID, Hazardous area classifications and equipment layout, Hazop, Hazid and MAHAR reports for All flow stations and incorporating results in issued documents

• Preparing scorecard, design intent and Preparing risk matrix table for Echo and Papa flow stations and contribution in preparing risk matrix table for other flowstations

• Attending in site visit of Uniform flowstation and Preparing site visit report for Uniform flowstation

• Liaise with other groups and the client's engineering team on technical matters.

3-3) Project: Vietnam Block 12W Development Platforms & Pipelines Project (Design completion, FEED project)

May 08-Jul 08

Client: Premier Oil Vietnam Offshore B.V. (POVO)

Position: Sr Process Engineer

POVO is the operator of the Dua and Chim Sao discoveries in Block 12W. These discoveries are located in the Nam Con Son Basin, offshore Vietnam approximately 400 kms south east of Ho Chi Minh City.

The wellhead platforms will be Normally Unmanned Installations (NUI). They will be tied back to the FPSO (Floating Production Storage Offloading) by means of infield production pipelines, water injection flowlines and gas lift flowlines, together with umbilicals, carrying chemical injection fluids, control fluids and power cable and fiber optic as required.

Reporting to Lead Engineer/Process Department Head, I was responsible for:

• Reviewing conceptual design dossier for any errors, omissions, deficiencies, inaccuracies, contradictions and/or discrepancies and Liaise with other groups on technical matters

• Supervision on preparing Simulation of Platforms and Thermodynamic Simulation of reservoir fluid (@ Reservoir conditions and wellhead) with HYSYS Software,Hydraulic Simulation of Pipelines (infield flowlines, water injection lines and gas lift lines) with PIPESIM Software, preparing P&ID’s, Process design basis/criteria, well testing philosophy ,heat tracing study document, line list and answering to IDC’s.

4) PIRE Co., Tehran, Iran

Jul 03-March 08

4-1) Project: Reshadat Renovation & Development Project-EPC project

Feb 07-May 07 & Aug 07-March 08

Client: SADRA / IOOC (Iranian Offshore Oil Company)

Position: Senior Process Engineer/Lead Process Engineer

The Reshadat oil field is located in the Persian Gulf, 110 km south-west of Lavan Island. The project comprises one satellite wellhead platform and a central complex including production, living quarters, wellhead and flare platforms. Produced oil from the facilities will be exported via a 16" pipeline to Lavan Island. The produced gas will be compressed for export and also for injection into the gas injection well.

Reporting to Engineering Manager / project Coordinator, I was responsible for:

• Reviewing basic design dossier for any errors, omissions, deficiencies, inaccuracies, contradictions and/or discrepancies; and preparing endorsement report and Attending kick-off meeting to review endorsement report,

• Preparing Process document register and participating in preparing the project schedule and resource management plan,Simulation of Platforms and Thermodynamic Simulation of reservoir fluid (@ Reservoir conditions and wellhead) with HYSYS Software, and Hydraulic simulation of pipelines/flowlines with PIPESIM Software

• Supervision on preparing Flare and Blowdown study report,Process design criteria, P&ID’s and

Liaise with other groups and the client's engineering team on technical matters.

4-2) Project: Tabriz HIPS II Project-EPC project (FEED, Detail engineering, Procurement and Construction)

May 05-March 07

Client: SADRA / TPC (Tabriz Petrochemical Company)

Position: Lead Process Engineer /Senior Process Engineer

The objective of this plant is to produce 54,700 tons/year High Impact Poly Styrene (HIPS) from Styrene Monomer and Poly Butadiene Rubber (PBR). The HIPS production plant is located at Tabriz Petrochemical Complex in north-west of Iran.

Reporting to Project Manager / Lead Engineer, I was responsible for:

• Reviewing tender documents for any errors, omissions, deficiencies, inaccuracies, contradictions, ambiguities and/or discrepancies; and preparing endorsement report and Attending kick-off meeting to review endorsement report and Liaise with other groups and the client's engineering team on technical matters.

• Preparing Process document register and participating in preparing the project schedule and resource management plan, Supervision on preparation / Preparation of PFD, UFD, P&ID, Block Flow Diagram(BFD) and Cause and Effect chart, Line list, Pressure Safety-Relief Valves / Rupture disks, Process description, process data sheets for equipment, Main Equipment list, Material balance, Operating manual, answering to IDC’s and Corporation of process team in meetings and kick-off meetings with vendors of equipments and packages and Evaluation of vendors from process point of view and Supervision on applying engineering procedures to insure compliance with the quality program,

• Contribution to a whole HAZOP study of the HIPS II Plant.

4-3) Project: Khesht Project-EPC project (FEED, Detail engineering, Procurement and Construction)

Aug 06-Feb 07

Client: SADRA / OEID (Oil and Energy Industries Development)

Position: Senior Process Engineer

The Khesht oil field is located in central area of Iran and the project consists of four oil well heads, oil gathering pipe lines, one water injection wellhead and pipeline, one gas injection wellhead and pipe line ,Central Processing Facility (CPF), a 100km export pipeline, and a permanent camp. The CPF has been designed for production of approximately 30,000 bbl/d crude oil to export to Genaveh. The produced gas will be compressed for injection into the wells.

Reporting to Lead Engineer / Engineering Manager, I was responsible for:

• Reviewing basic design dossier for any errors, omissions, deficiencies, inaccuracies, contradictions, ambiguities and/or discrepancies; contribution to preparing endorsement report. And attending kick-off meeting to review endorsement report and

• Preparing Process document Register, Simulation of plant with HYSYS Software, Hydraulic Simulation of wellhead flow lines with PIPESYS and PIPEPHASE Software’s, Simulation of export pipeline with PIPESYS and PIPEPHASE Software’s and Process Datasheets Air coolers and preparing TQ’s

4-4) Doris Engineering Co., Paris, France (Secondment basis from PIRE Co)

South Pars Field Development Phases 13 & 14 Offshore Project – FEED Engineering studies and basic design

May 07-Aug 07

Client: SHELL and REPSOL/ POGC (Pars Oil & Gas Company)

Position: Process Engineer

The South Pars gas field is located in the Persian Gulf. The South Pars Phases 13 & 14 facilities comprise four topsides decks including flare system, two platforms being designed for 1 BSCFD and two Platforms being for 0.6 BSCFD.

I was there on secondment from PIRE Co. and reporting to Lead engineer /Project Coordinator, I was responsible for:

• P&ID’s development, Preparation of Emergency depressurization Calculation Note, Startup philosophy , Design criteria , Operating Philosophy, Design basis, Electrical heaters sizing Note ,Vessel sizing, Flare network, Flare radiation report, Flare load summary, line sizing Calculation Notes, pressure relief valves and control valves Datasheet.

• Providing technical assistance to other groups for preparation of their documents (answering to some IDC’s),

4-5) Project: Demercaptanization of Liquid Hydrocarbons (DMD)-Detail design and procurement project

Jul 03-Dec 04

Client: RIPI (Research industry petroleum institute) / Kharg Petrochemical

Position: Process engineer

The objective of DMD Unit is the elimination of sulfuric compounds as CS2,COS, H2S & heavy and light mercaptanes of liquid hydrocarbons of Kharg petrochemical (Propane, Butane and Naphtha streams) is done by washing & extraction and heavy elimination is done by oxidation and stationary based mercaptane reactor, using UVKO-2 catalyst.

Reporting to Lead Engineer, I was responsible for:

• Preparing Process datasheet and indents for trays of Extractor towers, Air compressor package, water pump, process equipment list, typical P&ID for sampling bottles and Corporation in Preparing TBE of process pumps and Checking of Pumps and Heat exchangers manufacturer drawings /documents from process point of view answering to some IDC’s

4-6) Project: Normal Pentane Production Plant- Detail design and procurement project

Jul 03-Feb 05

Client: Kharg Petrochemical / RIPI (Research industry petroleum institute)

Position: Process engineer

The objective of Normal Pentane Production Unit is the separation of the normal pentane from out put light gasoline at Kermanshah Refinery plant. Pentane separation is carried out by a two stage distillation with a capacity of 850 barrel per day.

Reporting to Lead Engineer, I was responsible for:

• Preparing datasheet/indent for Air compressor package, fire water pumps and typical P&ID for sampling bottles and Checking of process Heat and mass balance table,

• Corporation in Preparing TBE of process pumps and Providing technical assistance to other groups for preparation of their documents (answering to some IDC’s),

• Checking of Pumps manufacturer drawings /documents from process point of view

4-7) Project: Sulfiran super pilot Plant- Detail design and procurement project

Jul 03-Feb 05

Client: Kangan gas refinery / RIPI (Research industry petroleum institute)

Position: Process engineer

The objective of Sulfiran Unit is the sweetening of the output sour gas of Kangan gas refinery amine unit. The main productions of this unit are sweet gas and pure sulfur with the unit capacity of 450,000 cubic feet per day acidic gas.

Reporting to Lead Engineer, I was responsible for:

• Checking of Pumps manufacturer drawings /documents from process point of view, Corporation in preparing HMI of plant for Instrument discipline and Providing technical assistance to other groups for preparation of their documents (answering to some IDC’s),

5) Aria Petro gas

Nov 2000-Jul 03

Position: Process engineer(Part time)

• Debottlenecking of hot oil furnace of Kangan gas refinery plant

• Preparing feasibility study(economical and technical) for Methanol production plant

• Preparing feasibility study(economical and technical) for Alpha olefin production plant

• Preparing feasibility study(economical and technical) of 12,000 bbl/day Gasoline plant in Bandar Abbas

REFRENCES

• Available Upon Request

CERTIFICATE

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