03.1_mercury removal project.pdf

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NO. CUSTOMER CONTRACT LOCATION PRODUCT YEAR OF MATERIAL OF PRODUCT CONDITION TYPE STREAM INSTALLATION CONSTRUCTION Flow Rate Design Design PURASPEC Volume Hg Removal Pressure Temperature Type (m3) 1 OWNER / CLIENT : EPCC Kertih Refinery, Light Naptha July 2010 Carbon Steel 340 m3/hr 19.6 barg 200/ 20 deg C 5158 68 Inlet < 25 ppb(wt) PETRONAS PENAPISAN Terengganu Outlet < 1 ppb (wt) (TERENGGANU) SDN BHD 2 OWNER : EPC PM329 East Piatu Natural Gas Sept 2011 Duplex 32.44 mmscfd 45.5/FV barg 93/ -29 deg C 1163 6 Inlet 600 ug/Nm3 NEWFIELD PENINSULA Offshore Platform Outlet <1 ug/Nm3 MALAYSIA INC. MAIN CONTRACTOR: KENCANA HL SDN BHD SUB-CONTRACTOR: JET ALLIED SDN BHD 3 OWNER/CLIENT FEED Paritutu Tank Farm NGL July 2012 Carbon Steel 60 m3/hr 127.6 barg 38/ -5 deg C 5158 5.5 Inlet 3-6 ppb(wt) SHELL TODD OIL New Plymouth Outlet < 1 ppb (wt) SERVICES New Zealand (New Zealand) 4 OWNER: EPCC IRPC Plant Light Naptha+LPG Sept 2013 Carbon Steel 70m3/hr 15.3/ FV barg 87/ 20 deg C 5168 19.7 Inlet 1000 ppb(wt) IRPC PUBLIC COMPANY Rayong Outlet < 1 ppb (wt) LIMITED Thailand Heavy Naptha 90 m3/hr 10.3/ FV barg 100/ 20 deg C 5158 22.5 Inlet 1000 ppb(wt) Outlet < 1 ppb (wt) Offgas 2500 Nm3/hr 6.8/ FV barg 87/ 20 deg C Activated Carbon 1 Inlet 1000 ppb(wt) Outlet < 1 ppb (wt) FEED/EPC/EPCC MRU JOBS JMC 5 OWNER:

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Page 1: 03.1_Mercury Removal Project.pdf

NO. CUSTOMER CONTRACT LOCATION PRODUCT YEAR OF MATERIAL OF PRODUCT CONDITIONTYPE STREAM INSTALLATION CONSTRUCTION Flow Rate Design Design PURASPEC Volume Hg Removal

Pressure Temperature Type (m3)

1 OWNER / CLIENT : EPCC Kertih Refinery, Light Naptha July 2010 Carbon Steel 340 m3/hr 19.6 barg 200/ 20 deg C 5158 68 Inlet < 25 ppb(wt)PETRONAS PENAPISAN Terengganu Outlet < 1 ppb (wt)(TERENGGANU) SDN BHD

2 OWNER : EPC PM329 East Piatu Natural Gas Sept 2011 Duplex 32.44 mmscfd 45.5/FV barg 93/ -29 deg C 1163 6 Inlet 600 ug/Nm3NEWFIELD PENINSULA Offshore Platform Outlet <1 ug/Nm3MALAYSIA INC.MAIN CONTRACTOR:KENCANA HL SDN BHDSUB-CONTRACTOR:JET ALLIED SDN BHD

3 OWNER/CLIENT FEED Paritutu Tank Farm NGL July 2012 Carbon Steel 60 m3/hr 127.6 barg 38/ -5 deg C 5158 5.5 Inlet 3-6 ppb(wt)SHELL TODD OIL New Plymouth Outlet < 1 ppb (wt)SERVICES New Zealand(New Zealand)

4 OWNER: EPCC IRPC Plant Light Naptha+LPG Sept 2013 Carbon Steel 70m3/hr 15.3/ FV barg 87/ 20 deg C 5168 19.7 Inlet 1000 ppb(wt)IRPC PUBLIC COMPANY Rayong Outlet < 1 ppb (wt)LIMITED Thailand

Heavy Naptha 90 m3/hr 10.3/ FV barg 100/ 20 deg C 5158 22.5 Inlet 1000 ppb(wt)Outlet < 1 ppb (wt)

Offgas 2500 Nm3/hr 6.8/ FV barg 87/ 20 deg C Activated Carbon 1 Inlet 1000 ppb(wt)Outlet < 1 ppb (wt)

FEED/EPC/EPCC MRU JOBS

JMC

5 OWNER:

Page 2: 03.1_Mercury Removal Project.pdf

PROJECT : PETROCHEMICAL NAPHTHA TREATING UNIT (MERCURY REMOVAL)

CLIENT : PETRONAS PENAPISAN (TERENGGANU) SDN BHD

LOCATION : KERTIH AROMATICS MALAYSIA SDN BHD, KERTIH TERENGGANU

CONTRACT COMPLETION PERIOD : MAY 2009 - JULY 2010

DIALOG E & C SDN BHD

DIALOG

Design, supply, fabricate, installation and precommisioning: BASE PRODUCT- 6 units of Pressure Vessels c/w platforms & ladders CAPACITY: ie Feed Surge Drum, Prefilter, Coalescer, Afterfilter and Absorber. DESIGN PRESSURE:- Fireproofing of Vessel Skirts and Steel Columns DESIGN TEMPERATURE:- 2 units of Centrifugal Pumps CATALYST PROVIDER- One Closed System Sampling Connections Cabinet CATALYST TECHNOLOGY- Structural Steel works(24 tons) MERCURY REMOVAL SPEC.- Piping works (4220 dia-inches)- Underground Piping for DOC (Oil Contaminated Drain)- Electrical & Instrumentation works including DCS upgrade. (E & I cable runs 4880 meter) PECO PREFILTER- 9 Tie In Points including one 10"/ 30" hot tap branch. PECO COALESCER Down to 15ppm (wt) or 10 ppm (v) H2O- Supply and loading of Mercury Removal Absorbent (Puraspec) PECO AFTERFILTER- Estimated Project Manhours - 145,000 m-hr

LUMP SUM EPCC SCOPE OF WORKS GENERAL SPECIFICATION OF SYSTEM

From 25 wt ppb to <1 wt ppb

LIGHT NAPHTHA

19.6 barg200 deg CJOHNSON MATTHEY CATALYSTPURASPEC

340 M3/HR

Remove 99+% solids 5μ and larger

Remove 99+% solids 5μ and largerst ated oject a ou s 5,000

Page 3: 03.1_Mercury Removal Project.pdf

PROJECT : GAS MERCURY REMOVAL UNIT FOR PM329 EAST PIATU TOPSIDES

CLIENT : NEWFIELD PENINSULA PTE. INC.

LOCATION : TOPSIDES OF PM329 EAST PIATU DEVELOPMENT PROJECT

CONTRACT COMPLETION PERIOD : OCT 2010 - JULY 2011

DIALOG E & C SDN BHD

DIALOG

Design, supply, fabricate, installation : BASE PRODUCT- 3 units of pressure vessels c/w platforms & ladders SKID DIMENSION ie Coalescer, Absorber and After Filter WEIGHT- One Closed Gas Sampling System CAPACITY: - Structural Steel works (10 tons) DESIGN PRESSURE: 45.5/ FV barg- Piping works (1050 dia-inches) DESIGN TEMPERATURE: 93/ -29 deg C- 5 piping tie in points CATALYST JOHNSON MATTHEY CATALYST- Supply and loading of Mercury Removal Absorbent (PURASPEC 1163) MERCURY REMOVAL SPEC. from 600 ug/Nm3 to <1 ug/Nm3- Estimated Project Manhours - 42,500 m-hr COALESCER

AFTERFILTER

32.44 MMSCFD

Remove 99.98% solids 1 μ and largerRemove 99.99% solids particles & liquid droplet => 0.3 μ

EPC SCOPE OF WORKS GENERAL SPECIFICATION OF SYSTEMHYDROCARBON GAS

29 tons / 37.5 tons (Empty/Operating)7.5m X 4m x 9 m(L X W X H)

Page 4: 03.1_Mercury Removal Project.pdf

PROJECT : NATURAL GAS LIQUID (NGL) MERCURY REMOVAL UNIT

CLIENT : SHELL TODD OIL SERVICES (NEW ZEALAND)

LOCATION : PARITUTU TANK FARM

CONTRACT COMPLETION PERIOD : MAY 2012 - JUNE 2012

DIALOG E & C SDN BHD

DIALOG

FEED Development of: BASE PRODUCT- 3 units of pressure vessels c/w platforms & ladders SKID DIMENSION ie Pre-Filter, Coalescer & Absorber WEIGHT- One Closed Gas Sampling System CAPACITY: - Structural Steel works DESIGN PRESSURE: 127.6 barg- Piping works DESIGN TEMPERATURE: 38/ -5 deg C- 4 piping tie in points CATALYST JOHNSON MATTHEY CATALYST- Supply and loading of Mercury Removal Absorbent (PURASPEC) MERCURY REMOVAL SPEC. from 3-6 ppb (wt) to <1 ppb (wt)

COALESCERAFTERFILTER

60 m3/hr

15 ppm (v) freewaterRemove 99 % solids 5 μ and larger

EPC SCOPE OF WORKS GENERAL SPECIFICATION OF SYSTEMNatural Gas Liquid7 m X 5 m x 8 m (L X W X H)22 tons /30 tons (Empty/Operating)

Page 5: 03.1_Mercury Removal Project.pdf

PROJECT : EPCC OF IRPC MERCURY REMOVAL UNIT FOR CRUDE OIL OPPORTUNITY PROJECT

CLIENT : INTERNATIONAL REFINERY PUBLIC COMPANY (IRPC) THAILAND

LOCATION : RAYONG, THAILAND

CONTRACT COMPLETION PERIOD : FEB 2013 - SEPT 2013

DIALOG E & C SDN BHD

DIALOG

Design, supply, fabricate, installation, precommisioning and commissioning assistance: BASE PRODUCT LN (Light Naphtha) +LPG Stream HN (Heavy Naphtha) Stream- 10 units of Pressure Vessels c/w platforms & ladders CAPACITY: 70 M3/HR 90 M3/HR ie Prefilter, Coalescer and Absorber. DESIGN PRESSURE: 15.3/FV barg 10.3/FV barg- Fireproofing of Vessel Skirts and Steel Columns DESIGN TEMPERATURE: 87/20 deg C 100/20 deg C- Two Manual Sampling Connections Cabinets (Open System & Closed System) CATALYST PROVIDER JMC JMC- Structural Steel works CATALYST TECHNOLOGY PURASPEC 5158 PURASPEC 5156- Piping works MERCURY REMOVAL SPEC. From <1000 ppb(wt) to <1 ppb(wt) From <1000 ppb(wt) to <1 ppb(wt)- Underground Piping for OWS (Oil Water System) PECO PREFILTER Remove 99 % solids 1μ and larger Remove 99 % solids 1μ and larger- Electrical & Instrumentation works including DCS upgrade. PECO COALESCER Down to 15 -20 ppm (v) free water Down to 15 -20 ppm (v) free water- 11 Piping Tie In Points - Supply and loading of Mercury Absorbent (PURASPEC)- Precommissioning, Start-up & Commissioning Assistance- Performance Guarantee Test

LUMP SUM EPCC SCOPE OF WORKS GENERAL SPECIFICATION OF SYSTEMS

- Performance Guarantee Test

Page 6: 03.1_Mercury Removal Project.pdf

PROJECT : EPCC OF IRPC MERCURY REMOVAL UNIT FOR CRUDE OIL OPPORTUNITY PROJECT

CLIENT : INTERNATIONAL REFINERY PUBLIC COMPANY (IRPC) THAILAND

LOCATION : RAYONG, THAILAND

CONTRACT COMPLETION PERIOD : FEB 2013 - SEPT 2013

DIALOG E & C SDN BHD

DIALOG

Design, supply, fabricate, installation, precommisioning and commissioning assistance: BASE PRODUCT OFFGAS to Flareline- 1 units of Activated Adsorber c/w platforms & ladders CAPACITY: 2500/1260 Nm3/hr- One Standalone Manual Sampling Connections Cabinets DESIGN PRESSURE: 6.8/FV barg- Piping works DESIGN TEMPERATURE: 87/20 deg C- 4 Piping Tie In Points ADSORBENT PROVIDER CALGON- Supply and loading of Activated Carbon (CALGON HGR 4x10) ADSORBENT TECHNOLOGY HGR 4 X10- Precommissioning MERCURY REMOVAL SPEC. From <1000 ppb(wt) to <1 ppb(wt)- Start-up and Commissioning- Performance Guarantee Test

LUMP SUM EPCC SCOPE OF WORKS GENERAL SPECIFICATION OF SYSTEMS