Web ContactsURL : www.pyramidenc.com Procurement : procurement@pyramidenc.comEnquiry : sales@pyramidenc.com Employment : hr@pyramidenc.com

31st Floor, JBC1, Cluster ‘G’Jumeirah Lake TowersP.O. Box 643857, DubaiUnited Arab Emirates

PRAVEER JOSHITel. : +971 4 363 5200Fax : +971 4 421 4351

Berkshire House, 252/256Kings Road, ReadingBerkshire RG14HPUnited Kingdom

JOHN OAKEYTel. : +44 (0) 118 953 3710Fax : +44 (0) 118 956 6415

Plot 23, Providence StreetLekki Phase 1Lagos, Nigeria

HENRY OKOLIE-ABOHTel. : +234 8060 203203Fax : +234 7066 077312

UNITED KINGDOM

NIGERIA

DUBAI INDIA

• Early Production Facilities

• Field Diesel Units

• Crude Oil Topping Units

• Gasoline Refineries

FAST TRACKPRODUCTION SOLUTIONS

6th Floor, Wing - BI-Think Techno CampusThane, MumbaiIndia - 400 607

SASHI WARRIERTel. : +91 22 6212 1000Fax : +91 22 6212 1001

Suite 300800 Town & Country Blvd.Houston, TX 77024, USA

BYRON TALBOTTel. : +1 (832) 431 3122Fax : +1 (832) 431 3001

2nd Floor Tamimah BldgAl Nahdah Road, P.O.Box 395Pc 118 MuscatSultanate Of Oman

MOHAMMED S AL SIBANITel. : + 968 99 38 8299Fax : + 968 24 66 7777

OMAN

Unit No 6, Level 27Binjai 8 Soho Lorong BinjaiKuala Lumpur, Malaysia

ABHISHEK SASEENDRANATHTel. : +603 28569810Fax : +603 28569811

MALAYSIA UNITED STATES SAUDI ARABIAPost Box 9967Dammam 31423 Kingdom Of Saudi Arabia

ASHOK GUPTATel. : + 966 13 827 6916Fax : + 966 13 827 6917

ISO 9001 ISO 14001OHSAS 18001 ISO/IEC 27001

Pyramid E&C is a multicultural company having the core competence of delivering comprehen-sive solutions for Oil and Gas Production, Storage, Transportation and Refining facilities. We endeavor to service Oil and Gas asset owners in all stages of development, commencing from Feasibility Studies through Engineering, Project Execution, Delivery and Operation of facilities.

Pyramid E&C specializes in fast track deliveries by investing in pre-engineered and/or pre-fabricat-ed equipment ready in stock. Most of the solutions offered by us are in modular construction and can be shipped in sizes to suit site logistics.

Pyramid E&C has its own Modular Fabrication Yard measuring 20,000 m² with 8,000 m² of covered area. The yard is close to Mundra port in Gujarat, Western India. Due to its proximity to jetty, Pyramid E&C can ship large process equip-ment and modules weighing up to 800 tons in a single piece.

Pyramid E&C has flexible business models to suit needs of asset owners including rentals of production systems with or without operation support or Build, Own and Operate services

with option to purchase. We also carry out financial engineering and participation for qual-ified opportunities.

32

About Pyramid E&C

Our Clients:

5,000 BOPD Early Production Facility, Sweet Crude

w w w . p y r a m i d e n c . c o mS o l u t i o n s 2 0 1 6w w w . p y r a m i d e n c . c o mS o l u t i o n s 2 0 1 5

Pyramid E&C has generic, pre-engineered modu-lar units available for rental for 5,000 BOPD Crude Oil Production. These facilities fit into several containerised modules suitable for sea and road transport. The rental EPF is reasonably complex to provide saleable product for mid-range Crude Oil. The use of the unit on a rental basis allows the customer to start produc-tion and thus revenue generation as soon as possible. Our robust equipment design ensures hassle-free operation for customers.

Design BasisThe following lists the inlet parameters and prod-uct specifications for the 5,000 BOPD rental EPF.

Inlet Parameters • Capacity : 5,000 BOPD • Nature of Crude : Sweet • Crude Grade : API 22+

Product Specification • BS&W (volume) : 0.5% • Salt Content : 8 PTB • RVP : <10psia

Process Description:

First Stage Separation: The well stream fluid from the Inlet Manifold is flashed in the First Stage Separator which operates at a pressure of 20 bar(g).This provides the initial separation between oil, gas and water.

Crude Preheat Exchanger: The Oil from the First

Stage Separator is heated in Stabilised Oil-Crude Interchanger by recovering heat from treated Crude exiting the Heater Treater.

Second-Stage Separation: Heated Crude along with Condensate from the Flare Knockout Drum enters the Second Stage Separator which is a Three-Phase Separator. It operates at a pressure of 5 bar(g) for oil, gas and water separation. Gas from the Separator is flared. The produced water is cooled prior to disposal.

Crude Stabilizer: Crude from Second Stage Separator is stabilized in a Heater Treater to remove light ends and achieve required RVP of the Crude. Associated gas is sent from Heater Treater to Flare. In case of desalting require-ment, the Heater Treater will be provided with an electrode grid and Wash Water System to achieve the required Crude specifications.

Crude Oil Storage: Stabilized Oil is pumped through the Stabilized Oil-Crude Interchanger, where it is cooled by the Crude feed. The stabi-lized oil is further cooled by an Air Cooler and then stored in Crude Oil Storage Tanks.

Crude Oil Transfer: Stored Oil is pumped using Crude Oil Transfer Pumps to loading bays for truck loading.

Utilities: Supporting utilities required for opera-tion can be either be tapped off from the existing unit or provided along with the facility.

Ecomar Refinery, Fujairah, UAE

Pyramid E&C is a multicultural company having the core competence of delivering comprehen-sive solutions for Oil and Gas Production, Storage, Transportation and Refining facilities. We endeavor to service Oil and Gas asset owners in all stages of development, commencing from Feasibility Studies through Engineering, Project Execution, Delivery and Operation of facilities.

Pyramid E&C specializes in fast track deliveries by investing in pre-engineered and/or pre-fabricat-ed equipment ready in stock. Most of the solutions offered by us are in modular construction and can be shipped in sizes to suit site logistics.

Pyramid E&C has its own Modular Fabrication Yard measuring 20,000 m² with 8,000 m² of covered area. The yard is close to Mundra port in Gujarat, Western India. Due to its proximity to jetty, Pyramid E&C can ship large process equip-ment and modules weighing up to 800 tons in a single piece.

Pyramid E&C has flexible business models to suit needs of asset owners including rentals of production systems with or without operation support or Build, Own and Operate services

with option to purchase. We also carry out financial engineering and participation for qual-ified opportunities.

32

About Pyramid E&C

Our Clients:

5,000 BOPD Early Production Facility, Sweet Crude

w w w . p y r a m i d e n c . c o mS o l u t i o n s 2 0 1 5w w w . p y r a m i d e n c . c o mS o l u t i o n s 2 0 1 6

Pyramid E&C has generic, pre-engineered modu-lar units available for rental for 5,000 BOPD Crude Oil Production. These facilities fit into several containerised modules suitable for sea and road transport. The rental EPF is reasonably complex to provide saleable product for mid-range Crude Oil. The use of the unit on a rental basis allows the customer to start produc-tion and thus revenue generation as soon as possible. Our robust equipment design ensures hassle-free operation for customers.

Design BasisThe following lists the inlet parameters and prod-uct specifications for the 5,000 BOPD rental EPF.

Inlet Parameters • Capacity : 5,000 BOPD • Nature of Crude : Sweet • Crude Grade : API 22+

Product Specification • BS&W (volume) : 0.5% • Salt Content : 8 PTB • RVP : <10psia

Process Description:

First Stage Separation: The well stream fluid from the Inlet Manifold is flashed in the First Stage Separator which operates at a pressure of 20 bar(g).This provides the initial separation between oil, gas and water.

Crude Preheat Exchanger: The Oil from the First

Stage Separator is heated in Stabilised Oil-Crude Interchanger by recovering heat from treated Crude exiting the Heater Treater.

Second-Stage Separation: Heated Crude along with Condensate from the Flare Knockout Drum enters the Second Stage Separator which is a Three-Phase Separator. It operates at a pressure of 5 bar(g) for oil, gas and water separation. Gas from the Separator is flared. The produced water is cooled prior to disposal.

Crude Stabilizer: Crude from Second Stage Separator is stabilized in a Heater Treater to remove light ends and achieve required RVP of the Crude. Associated gas is sent from Heater Treater to Flare. In case of desalting require-ment, the Heater Treater will be provided with an electrode grid and Wash Water System to achieve the required Crude specifications.

Crude Oil Storage: Stabilized Oil is pumped through the Stabilized Oil-Crude Interchanger, where it is cooled by the Crude feed. The stabi-lized oil is further cooled by an Air Cooler and then stored in Crude Oil Storage Tanks.

Crude Oil Transfer: Stored Oil is pumped using Crude Oil Transfer Pumps to loading bays for truck loading.

Utilities: Supporting utilities required for opera-tion can be either be tapped off from the existing unit or provided along with the facility.

Ecomar Refinery, Fujairah, UAE

54

10,000 BOPD Early Production Facility, Sour Crude Field Diesel Units

Field Diesel Units are effective in areas where there is a ready supply of Crude Oil but limited supply of Diesel fuel, such as unpopulated areas, remote oil fields or drilling locations. A Field Diesel Unit can fulfill local fuel require-ments for power generation and Drilling oper-ation. This unit extracts the Diesel component from the Crude Oil and then blends rest of the products back to Crude Oil. The Field Diesel Unit is split into easily transportable skids; it is quick to install and self-sufficient. The unit can be started when needed and stopped when the tanks are full. The Diesel produced by these units largely depends on the type of Crude Oil, the lighter varieties will provide greater diesel yield and higher cetane number.

Process Description:

The Crude Oil is pumped from Storage Tanks and pre-heated in Crude Interchanger before further heating in a Hot Oil Heater. The tem-perature of Crude Oil at outlet of Heater is carefully controlled for optimal operation. The heated Crude Oil is flashed into vapour and liquid fractions in the flash zone of Distillation Column. At certain temperature, the Diesel fraction is drawn into Diesel Stripper for flash point control and sent to storage after cooling.

The light fraction (condensate) is condensed in Overhead Condenser and collected into Reflux Drum. Part of condensate is fed as reflux and the balance is blended with the residue from the Column bottom and mixed with the Crude Oil. The uncondensed gases are vented to Flare system.

Supporting utilities required for operationcan be tapped off from the existing system unit (Power, IA/PA, CBD, Flare etc.) or provided along with the unit as per the requirement.

Pyramid E&C has generic, pre-engineered modu-lar units available for rental for 10,000 BOPD Crude Oil Production. These facilities fit into several containerized modules suitable for sea and road transport. The rental EPF is reasonably complex to provide saleable product for mid-range Crude Oil. The use of the unit on a rental basis allows the Customer to start produc-tion and thus revenue generation as soon as pos-sible. Our robust equipment design ensures has-sle-free operation for customers.

Design Basis

The following lists the inlet parameters and prod-uct specifications for the 10,000 BOPD rental EPF.

Inlet Parameters • Capacity : 10,000 BOPD • Nature of Crude : Sour • Crude Grade : API 15+

Product Specification • BS & W (volume) : 0.5% • Salt Content : 8 PTB • RVP : <10psia • H2S Content : 20 ppm wt.

Process Description:

First Stage Separation: The well stream fluid from the Inlet Manifold is flashed in the First Stage Separator, which is a three-phase separator and operates at a pressure of 20 bar(g). This provides the initial separation between oil, gas and water.

Crude Preheat Exchanger: The Oil from the First Stage Separator is heated in Stabilized Oil-Crude Interchanger by recovering heat from treated

Crude exiting from Stabilizer bottom.

Second Stage Separation: Heated Crude along with Condensate from the Flare Knockout Drum enters the Second Stage Separator, which oper-ates at a pressure of 5 bar (g) for oil, gas and water separation. Gas from the Separator is flared. The produced water is cooled prior to disposal.

Desalter (optional): The Oil from the Second Stage Separator is pumped to the Desalter using Desalter Feed Pumps. Wash Water is pumped through a Wash Water Pre-Heater and then mixed with the Crude Oil using a mixing valve or static mixer. The brine is mixed with the produced water for disposal.

Crude Stabilizer: Desalted Crude is stabilized in a Stabilizer Column provided with reboiler (Nitro-gen Stripping optional). This process removes H2S and also reduces the Reid vapour pressure of the Crude. The gas from the Stabilizer is flared.

Crude Oil Storage: Stabilized Oil is pumped through the Stabilized Oil-Crude Interchanger, where it is cooled by the feed. The Stabilized Oil is further cooled by an Air Cooler and then stored in Crude Oil Storage Tanks.

Crude Oil Transfer: Stored Oil is pumped using Crude Oil Transfer Pumps to loading bays for truck loading.

Utilities: Supporting utilities required for opera-tion can be either be tapped off from the existing unit or provided along with the facility.

w w w . p y r a m i d e n c . c o m w w w . p y r a m i d e n c . c o mS o l u t i o n s 2 0 1 5S o l u t i o n s 2 0 1 6

54

10,000 BOPD Early Production Facility, Sour Crude Field Diesel Units

Field Diesel Units are effective in areas where there is a ready supply of Crude Oil but limited supply of Diesel fuel, such as unpopulated areas, remote oil fields or drilling locations. A Field Diesel Unit can fulfill local fuel require-ments for power generation and Drilling oper-ation. This unit extracts the Diesel component from the Crude Oil and then blends rest of the products back to Crude Oil. The Field Diesel Unit is split into easily transportable skids; it is quick to install and self-sufficient. The unit can be started when needed and stopped when the tanks are full. The Diesel produced by these units largely depends on the type of Crude Oil, the lighter varieties will provide greater diesel yield and higher cetane number.

Process Description:

The Crude Oil is pumped from Storage Tanks and pre-heated in Crude Interchanger before further heating in a Hot Oil Heater. The tem-perature of Crude Oil at outlet of Heater is carefully controlled for optimal operation. The heated Crude Oil is flashed into vapour and liquid fractions in the flash zone of Distillation Column. At certain temperature, the Diesel fraction is drawn into Diesel Stripper for flash point control and sent to storage after cooling.

The light fraction (condensate) is condensed in Overhead Condenser and collected into Reflux Drum. Part of condensate is fed as reflux and the balance is blended with the residue from the Column bottom and mixed with the Crude Oil. The uncondensed gases are vented to Flare system.

Supporting utilities required for operationcan be tapped off from the existing system unit (Power, IA/PA, CBD, Flare etc.) or provided along with the unit as per the requirement.

Pyramid E&C has generic, pre-engineered modu-lar units available for rental for 10,000 BOPD Crude Oil Production. These facilities fit into several containerized modules suitable for sea and road transport. The rental EPF is reasonably complex to provide saleable product for mid-range Crude Oil. The use of the unit on a rental basis allows the Customer to start produc-tion and thus revenue generation as soon as pos-sible. Our robust equipment design ensures has-sle-free operation for customers.

Design Basis

The following lists the inlet parameters and prod-uct specifications for the 10,000 BOPD rental EPF.

Inlet Parameters • Capacity : 10,000 BOPD • Nature of Crude : Sour • Crude Grade : API 15+

Product Specification • BS & W (volume) : 0.5% • Salt Content : 8 PTB • RVP : <10psia • H2S Content : 20 ppm wt.

Process Description:

First Stage Separation: The well stream fluid from the Inlet Manifold is flashed in the First Stage Separator, which is a three-phase separator and operates at a pressure of 20 bar(g). This provides the initial separation between oil, gas and water.

Crude Preheat Exchanger: The Oil from the First Stage Separator is heated in Stabilized Oil-Crude Interchanger by recovering heat from treated

Crude exiting from Stabilizer bottom.

Second Stage Separation: Heated Crude along with Condensate from the Flare Knockout Drum enters the Second Stage Separator, which oper-ates at a pressure of 5 bar (g) for oil, gas and water separation. Gas from the Separator is flared. The produced water is cooled prior to disposal.

Desalter (optional): The Oil from the Second Stage Separator is pumped to the Desalter using Desalter Feed Pumps. Wash Water is pumped through a Wash Water Pre-Heater and then mixed with the Crude Oil using a mixing valve or static mixer. The brine is mixed with the produced water for disposal.

Crude Stabilizer: Desalted Crude is stabilized in a Stabilizer Column provided with reboiler (Nitro-gen Stripping optional). This process removes H2S and also reduces the Reid vapour pressure of the Crude. The gas from the Stabilizer is flared.

Crude Oil Storage: Stabilized Oil is pumped through the Stabilized Oil-Crude Interchanger, where it is cooled by the feed. The Stabilized Oil is further cooled by an Air Cooler and then stored in Crude Oil Storage Tanks.

Crude Oil Transfer: Stored Oil is pumped using Crude Oil Transfer Pumps to loading bays for truck loading.

Utilities: Supporting utilities required for opera-tion can be either be tapped off from the existing unit or provided along with the facility.

w w w . p y r a m i d e n c . c o m w w w . p y r a m i d e n c . c o mS o l u t i o n s 2 0 1 6S o l u t i o n s 2 0 1 5

76

Pyramid E&C builds topping refineries which are suitable for light, low Sulphur Crudes to produce automotive fuels, i.e., Diesel and Gaso-line from Crude Oil and Condensate. The build-ing blocks of these refineries include Desalting, Atmospheric Distillation, and Side Stream Strip-ping. The yields and the treatment required depend on the API gravity, Sulphur and other properties of the Crude. Utilities include a Fuel Gas System, IA/PA System, CBD System, Water Treatment System, Steam System, etc. and Tanks for feed and product storage.

Equipment

• Crude Charge Pump • Fired Heater• Distillation Column • Flare System• Stripper Column • Pumps• Chemical Injection System • Desalter System• Diesel Generator Set • Steam Boiler• Fuel Oil System • Storage Tanks• Truck Loading Terminal • CBD System• Water Treatment System • Flare Systems• Product Transfer Pumps

Process Description

Crude Oil is heated in pre-heat train and then treated in a Desalter Unit where salt in water, or brine, is removed. The Crude Oil leaving the Desalter Unit is heated in a Fired Heater from which it enters the flash zone of an Atmospheric

Column. Natural Gas condensate can also be included in the feed or introduced directly into the Column.

The Crude Oil mixture is separated into differ-ent cuts by boiling range. The Crude Column produces Naphtha, Kerosene, and Diesel as the side streams. The Crude Column bottom prod-uct, also called Reduced Crude is used as Fuel Oil.

In large Atmospheric Columns, pump arounds are used for intermediate heat recovery in addi-tion to product feed exchangers to the crude feed which reduces furnace firing. For small refineries of the order of 10,000 BOPD, allowing all heat removal to occur in the Overhead Con-denser often minimizes CAPEX.

Products are withdrawn from the tower under temperature control; by simulation modeling the tower, it is possible to predict the tempera-ture, pressure, and number of trays required to produce the desired product specifications. The tower products are stripped of light ends using steam or Reboilers. This controls the inlet specification such as flash point of the product.

Depending on the viscosity, Reduced Crude can be used as Fuel Oil directly. Alternatively, Kero-sene or Diesel can be blended with the Reduced Crude to produce Fuel Oil.

Crude Oil Topping Units Gasoline Refineries

• Crude Pre-Heater • Distillation Column • Debutanizer • Flare System / SRU • Naphtha Splitter • Reformer • Pumps • Fuel Oil System • Steam Boiler • Storage Tanks

Pyramid E&C builds plants for processing Naphtha to produce Gasoline for automotive usage. These plants, also termed as Hydro-Skimming Units, can be added down-stream of the Topping Unit to consume Naph-tha stream for production of Gasoline.

Equipment

• Crude Charge Pumps • Fired Heater • Desalter System • Naphtha Hydrotreater • Light Ends Processing • Isomerization Unit • Hydrogen Purification Unit • Diesel Generator Set • Chemical Injection System • Truck Loading Terminal • Product Transfer Pumps

The building blocks of the Naphtha Treatment line include Hydrotreaters, Naphtha Splitter, Reformer and Isomerization Units. The yields and the treatment required depend on the properties of the Crude Oil and Product Speci-fication. The Reformer also produces Hydro-gen as by-product, which is utilized in Hydro-treater. The Hydrotreater treats Naphtha and removes sulfur compound thereby preventing catalyst poisoning in downstream processign units. The plants can be supplied complete with utilities including Hydrogen Purification and Sulphur Recovery Units.

Crude Oil is treated in a Topping unit, which yields Naphtha, Kerosene, Diesel and Fuel Oil as products. Amongst these, the Naptha stream is utilized for production of Gasoline. The wide Naphtha cut is fed into Debutanizer to separate LPG from Naphtha. Naphtha is then Hydrotreated using a catalytic process to remove Sulphur and fed into Naphtha Splitter to separate Light and Heavy Naphtha.

The Light Naphtha is processed in an Isomeri-zation Unit to increase its octane number prior to blending into the Gasoline pool. The Heavy Naphtha is processed in a Reformer, which creates aromatic rings to increase octane number and liberates Hydrogen. The Reformer is a fixed-bed, semi-regen type catalyst system. The Hydrogen is purified in a Pressure Swing Absorption Unit and used for Hydro-treating Naphtha. The Gasoline produced is stored in Gasoline Storage Tank.

The Light Ends Processing System fraction-ates Butane for use in Gasoline Blending, or Propane and Butane for product LPG (Lique-fied Petroleum Gas) which is stored in Mound-ed Bullets.

The Kerosene side stream goes to Kerosene Storage Tank, while Diesel product goes to Diesel Storage. Depending on the viscosity, Reduced Crude can be used as Fuel Oil direct-ly. Alternatively, Kerosene or Diesel can be blended with the Reduced Crude to produce Fuel Oil.

w w w . p y r a m i d e n c . c o m w w w . p y r a m i d e n c . c o mS o l u t i o n s 2 0 1 5S o l u t i o n s2 0 1 6

76

Pyramid E&C builds topping refineries which are suitable for light, low Sulphur Crudes to produce automotive fuels, i.e., Diesel and Gaso-line from Crude Oil and Condensate. The build-ing blocks of these refineries include Desalting, Atmospheric Distillation, and Side Stream Strip-ping. The yields and the treatment required depend on the API gravity, Sulphur and other properties of the Crude. Utilities include a Fuel Gas System, IA/PA System, CBD System, Water Treatment System, Steam System, etc. and Tanks for feed and product storage.

Equipment

• Crude Charge Pump • Fired Heater• Distillation Column • Flare System• Stripper Column • Pumps• Chemical Injection System • Desalter System• Diesel Generator Set • Steam Boiler• Fuel Oil System • Storage Tanks• Truck Loading Terminal • CBD System• Water Treatment System • Flare Systems• Product Transfer Pumps

Process Description

Crude Oil is heated in pre-heat train and then treated in a Desalter Unit where salt in water, or brine, is removed. The Crude Oil leaving the Desalter Unit is heated in a Fired Heater from which it enters the flash zone of an Atmospheric

Column. Natural Gas condensate can also be included in the feed or introduced directly into the Column.

The Crude Oil mixture is separated into differ-ent cuts by boiling range. The Crude Column produces Naphtha, Kerosene, and Diesel as the side streams. The Crude Column bottom prod-uct, also called Reduced Crude is used as Fuel Oil.

In large Atmospheric Columns, pump arounds are used for intermediate heat recovery in addi-tion to product feed exchangers to the crude feed which reduces furnace firing. For small refineries of the order of 10,000 BOPD, allowing all heat removal to occur in the Overhead Con-denser often minimizes CAPEX.

Products are withdrawn from the tower under temperature control; by simulation modeling the tower, it is possible to predict the tempera-ture, pressure, and number of trays required to produce the desired product specifications. The tower products are stripped of light ends using steam or Reboilers. This controls the inlet specification such as flash point of the product.

Depending on the viscosity, Reduced Crude can be used as Fuel Oil directly. Alternatively, Kero-sene or Diesel can be blended with the Reduced Crude to produce Fuel Oil.

Crude Oil Topping Units Gasoline Refineries

• Crude Pre-Heater • Distillation Column • Debutanizer • Flare System / SRU • Naphtha Splitter • Reformer • Pumps • Fuel Oil System • Steam Boiler • Storage Tanks

Pyramid E&C builds plants for processing Naphtha to produce Gasoline for automotive usage. These plants, also termed as Hydro-Skimming Units, can be added down-stream of the Topping Unit to consume Naph-tha stream for production of Gasoline.

Equipment

• Crude Charge Pumps • Fired Heater • Desalter System • Naphtha Hydrotreater • Light Ends Processing • Isomerization Unit • Hydrogen Purification Unit • Diesel Generator Set • Chemical Injection System • Truck Loading Terminal • Product Transfer Pumps

The building blocks of the Naphtha Treatment line include Hydrotreaters, Naphtha Splitter, Reformer and Isomerization Units. The yields and the treatment required depend on the properties of the Crude Oil and Product Speci-fication. The Reformer also produces Hydro-gen as by-product, which is utilized in Hydro-treater. The Hydrotreater treats Naphtha and removes sulfur compound thereby preventing catalyst poisoning in downstream processign units. The plants can be supplied complete with utilities including Hydrogen Purification and Sulphur Recovery Units.

Crude Oil is treated in a Topping unit, which yields Naphtha, Kerosene, Diesel and Fuel Oil as products. Amongst these, the Naptha stream is utilized for production of Gasoline. The wide Naphtha cut is fed into Debutanizer to separate LPG from Naphtha. Naphtha is then Hydrotreated using a catalytic process to remove Sulphur and fed into Naphtha Splitter to separate Light and Heavy Naphtha.

The Light Naphtha is processed in an Isomeri-zation Unit to increase its octane number prior to blending into the Gasoline pool. The Heavy Naphtha is processed in a Reformer, which creates aromatic rings to increase octane number and liberates Hydrogen. The Reformer is a fixed-bed, semi-regen type catalyst system. The Hydrogen is purified in a Pressure Swing Absorption Unit and used for Hydro-treating Naphtha. The Gasoline produced is stored in Gasoline Storage Tank.

The Light Ends Processing System fraction-ates Butane for use in Gasoline Blending, or Propane and Butane for product LPG (Lique-fied Petroleum Gas) which is stored in Mound-ed Bullets.

The Kerosene side stream goes to Kerosene Storage Tank, while Diesel product goes to Diesel Storage. Depending on the viscosity, Reduced Crude can be used as Fuel Oil direct-ly. Alternatively, Kerosene or Diesel can be blended with the Reduced Crude to produce Fuel Oil.

w w w . p y r a m i d e n c . c o m w w w . p y r a m i d e n c . c o mS o l u t i o n s 2 0 1 6S o l u t i o n s2 0 1 5

Web ContactsURL : www.pyramidenc.com Procurement : procurement@pyramidenc.comEnquiry : sales@pyramidenc.com Employment : hr@pyramidenc.com

31st Floor, JBC1, Cluster ‘G’Jumeirah Lake TowersP.O. Box 643857, DubaiUnited Arab Emirates

UMESH JOSHITel. : +971 4363 5200Fax : +971 4421 4351

12121 Wickchester LaneSuite 200, HoustonTexas 77079United States of America

MIKE HILLERYTel. : +1 281 531 9000Fax : +1 281 531 9215

2nd Floor Tamimah BldgAl Nahdah Road, P.O.Box 395Pc 118 MuscatSultanate Of Oman

MANISH PANDEYTel. : +968 9938 8299Fax : +968 2466 7777

USA

OMAN

UAE INDIA

• Early Production Facilities

• Field Diesel Units

• Crude Oil Topping Units

• Gasoline Refineries

FAST TRACKPRODUCTION SOLUTIONS

6th Floor, Wing - BI-Think Techno CampusThane (W), MumbaiIndia

B M NICHATTel. : +91 22 6212 1000Fax : +91 22 6212 1001

Plot 23Providence StreetLekki Phase 1, LagosNigeria

HENRY OKOLIE-ABOHTel. : +234 806 020 3203Fax : +234 706 607 7312

1210 Parkview,Arlington Business Park, ThealeReading, Berkshire, RG7 4TYUnited Kingdom

JOHN OAKEYTel. : +44 118 965 4088Fax : +44 118 965 7788

UNITED KINGDOM

Level 3A, Menara RKTNo. 36 Jalan Raja AbdullahOff Jalan Sultan Ismail50300 Kuala Lumpur, Malaysia

ABHISHEK SASEENDRANATHTel. : +60 32 856 9810Fax : +60 32 856 9813

MALAYSIA NIGERIA SAUDI ARABIAPost Box 9967Dammam 31423Kingdom Of Saudi Arabia

FURQAN UR RASHIDTel. : +966 13 827 6916Fax : +966 13 827 6917

ISO 9001 ISO 14001OHSAS 18001 ISO/IEC 27001