FAST TRACK PRODUCTION SOLUTIONS. Early Production Facilities Field Diesel Units Crude Oil Topping Units Gasoline Refineries
|
|
- Reynard Briggs
- 5 years ago
- Views:
Transcription
1 FAST TRACK PRODUCTION SOLUTIONS Early Production Facilities Field Diesel Units Crude Oil Topping Units Gasoline Refineries
2 Pyramid E&C is a multicultural company having the core competence of delivering comprehensive 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-fabricated 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 equipment and modules weighing up to 800 tons in a single piece. About Pyramid E&C with option to purchase. We also carry out financial engineering and participation for qualified opportunities. 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 Ecomar Refinery, Fujairah, UAE Our Clients: 2
3 5,000 BOPD Early Production Facility, Sweet Crude Pyramid E&C has generic, pre-engineered modular 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 production and thus revenue generation as soon as possible. Our robust equipment design ensures hassle-free operation for customers. Design Basis The following lists the inlet parameters and product 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 requirement, 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 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 operation can be either be tapped off from the existing unit or provided along with the facility. 3
4 10,000 BOPD Early Production Facility, Sour Crude Pyramid E&C has generic, pre-engineered modular 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 production and thus revenue generation as soon as possible. Our robust equipment design ensures hassle-free operation for customers. Design Basis The following lists the inlet parameters and product 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 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. 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 (Nitrogen 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 operation can be either be tapped off from the existing unit or provided along with the facility. 4
5 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 requirements for power generation and Drilling operation. 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 temperature 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. 5
6 Crude Oil Topping Units Pyramid E&C builds topping refineries which are suitable for light, low Sulphur Crudes to produce automotive fuels, i.e., Diesel and Gasoline from Crude Oil and Condensate. The building blocks of these refineries include Desalting, Atmospheric Distillation, and Side Stream Stripping. 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 different cuts by boiling range. The Crude Column produces Naphtha, Kerosene, and Diesel as the side streams. The Crude Column bottom product, also called Reduced Crude is used as Fuel Oil. In large Atmospheric Columns, pump arounds are used for intermediate heat recovery in addition 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 Condenser often minimizes CAPEX. Products are withdrawn from the tower under temperature control; by simulation modeling the tower, it is possible to predict the temperature, 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, Kerosene or Diesel can be blended with the Reduced Crude to produce Fuel Oil. 6
7 Gasoline Refineries 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 downstream of the Topping Unit to consume Naphtha 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 Crude Pre-Heater Distillation Column Debutanizer Flare System / SRU Naphtha Splitter Reformer Pumps Fuel Oil System Steam Boiler Storage Tanks 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 Specification. The Reformer also produces Hydrogen as by-product, which is utilized in Hydrotreater. 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 Isomerization 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 Hydrotreating Naphtha. The Gasoline produced is stored in Gasoline Storage Tank. The Light Ends Processing System fractionates Butane for use in Gasoline Blending, or Propane and Butane for product LPG (Liquefied Petroleum Gas) which is stored in Mounded 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 directly. Alternatively, Kerosene or Diesel can be blended with the Reduced Crude to produce Fuel Oil. 7
8 ISO 9001 ISO OHSAS ISO/IEC Web Contacts URL : Procurement : procurement@pyramidenc.com Enquiry : sales@pyramidenc.com Employment : hr@pyramidenc.com UAE INDIA USA UNITED KINGDOM 31st Floor, JBC1, Cluster G Jumeirah Lake Towers P.O. Box , Dubai United Arab Emirates UMESH JOSHI Tel. : Fax : th Floor, Wing - B I-Think Techno Campus Thane (W), Mumbai India B M NICHAT Tel. : Fax : Wickchester Lane Suite 200, Houston Texas United States of America MIKE HILLERY Tel. : Fax : Parkview, Arlington Business Park, Theale Reading, Berkshire, RG7 4TY United Kingdom JOHN OAKEY Tel. : Fax : MALAYSIA NIGERIA OMAN SAUDI ARABIA Level 3A, Menara RKT No. 36 Jalan Raja Abdullah Off Jalan Sultan Ismail Kuala Lumpur, Malaysia ABHISHEK SASEENDRANATH Tel. : Fax : Plot 23 Providence Street Lekki Phase 1, Lagos Nigeria HENRY OKOLIE-ABOH Tel. : Fax : nd Floor Tamimah Bldg Al Nahdah Road, P.O.Box 395 Pc 118 Muscat Sultanate Of Oman MANISH PANDEY Tel. : Fax : Post Box 9967 Dammam Kingdom Of Saudi Arabia FURQAN UR RASHID Tel. : Fax :
Crude Distillation Chapter 4
Crude Distillation Chapter 4 Gases Gas Sat Gas Plant Polymerization LPG Sulfur Plant Sulfur Alkyl Feed Alkylation Butanes Fuel Gas LPG Gas Separation & Stabilizer Light Naphtha Heavy Naphtha Isomerization
More informationUnit 7. Vaccum Distillation of Crude
Unit 7. Vaccum Distillation of Crude Assistant teacher Belinskaya Nataliya Segeevna 2015 Introduction To extract more distillates from the atmospheric residue, the bottom from the atmospheric crude distillation
More informationHOW OIL REFINERIES WORK
HOW OIL REFINERIES WORK In order to model oil refineries for model railroads some research was conducted into how they operate and what products a refinery produces. Presented below is a basic survey on
More informationHOW OIL REFINERIES WORK
HOW OIL REFINERIES WORK In order to model oil refineries for model railroads some research was conducted into how they operate and what products a refinery produces. Presented below is a basic survey on
More informationOn-Line Process Analyzers: Potential Uses and Applications
On-Line Process Analyzers: Potential Uses and Applications INTRODUCTION The purpose of this report is to provide ideas for application of Precision Scientific process analyzers in petroleum refineries.
More informationHOW OIL REFINERIES WORK
HOW OIL REFINERIES WORK In order to model oil refineries for model railroads some research was conducted into how they operate and what products a refinery produces. Presented below is a basic survey on
More informationConversion Processes 1. THERMAL PROCESSES 2. CATALYTIC PROCESSES
Conversion Processes 1. THERMAL PROCESSES 2. CATALYTIC PROCESSES 1 Physical and chemical processes Physical Thermal Chemical Catalytic Distillation Solvent extraction Propane deasphalting Solvent dewaxing
More informationCRUDE DISTILLATION. Overview. Purpose To recover light materials. Fractionate into sharp light fractions.
Overview Purpose To recover light materials. Fractionate into sharp light fractions. CRUDE DISTILLATION Configuration May be as many as three columns in series Crude Stabilizer/Preflash Column Reduce traffic
More informationDistillation process of Crude oil
Distillation process of Crude oil Abdullah Al Ashraf; Abdullah Al Aftab 2012 Crude oil is a fossil fuel, it was made naturally from decaying plants and animals living in ancient seas millions of years
More informationTHE OIL & GAS SUPPLY CHAIN: FROM THE GROUND TO THE PUMP ON REFINING
THE OIL & GAS SUPPLY CHAIN: FROM THE GROUND TO THE PUMP ON REFINING J. Mike Brown, Ph.D. Senior Vice President Technology BASICS OF REFINERY OPERATIONS Supply and Demand Where Does The Crude Oil Come From?
More informationReport. Refining Report. heat removal, lower crude preheat temperature,
Delayed coker FCC feed hydrotreater FCCU Crude unit Hydrotreater Hydrotreater P r o c e s s i n g Better fractionation hikes yields, hydrotreater run lengths Scott Golden Process Consulting Services Houston
More informationRefinery Maze Student Guide
Refinery Maze Student Guide Petroleum Refining Student Text Distillation In its crude form, petroleum is of little use to us. To make it into products we know and use, petroleum must be refined or separated
More informationPetroleum Refining Fourth Year Dr.Aysar T. Jarullah
Catalytic Reforming Catalytic reforming is the process of transforming C 7 C 10 hydrocarbons with low octane numbers to aromatics and iso-paraffins which have high octane numbers. It is a highly endothermic
More informationPetroleum Refining Fourth Year Dr.Aysar T. Jarullah
Catalytic Operations Fluidized Catalytic Cracking The fluidized catalytic cracking (FCC) unit is the heart of the refinery and is where heavy low-value petroleum stream such as vacuum gas oil (VGO) is
More informationFundamentals of Petroleum Refining Refinery Products. Lecturers: assistant teachers Kirgina Maria Vladimirovna Belinskaya Natalia Sergeevna
Fundamentals of Petroleum Refining Refinery Products Lecturers: assistant teachers Kirgina Maria Vladimirovna Belinskaya Natalia Sergeevna 1 Refinery Products Composition There are specifications for over
More informationBottom of Barrel Processing. Chapters 5 & 8
Bottom of Barrel Processing Chapters 5 & 8 Gases Gas Sat Gas Plant Polymerization LPG Sulfur Plant Sulfur Alkyl Feed Alkylation Butanes Fuel Gas LPG Gas Separation & Stabilizer Light Naphtha Heavy Naphtha
More informationLecture 3: Petroleum Refining Overview
Lecture 3: Petroleum Refining Overview In this lecture, we present a brief overview of the petroleum refining, a prominent process technology in process engineering. 3.1 Crude oil Crude oil is a multicomponent
More informationConverting Visbreakers to Delayed Cokers - An Opportunity for European Refiners
Converting Visbreakers to Delayed Cokers - An Opportunity for European Refiners European Coking.com Conference Sept. 30 - Oct. 2, 2008 Alex Broerse Lummus Technology a CB&I company Overview Introduction
More informationPreface... xii. 1. Refinery Distillation... 1
Preface... xii Chapter Breakdown... xiii 1. Refinery Distillation... 1 Process Variables... 2 Process Design of a Crude Distillation Tower... 5 Characterization of Unit Fractionation... 11 General Properties
More informationCrude Oil Distillation. Chapter 4
Crude Oil Distillation Chapter 4 Gases Gas Sat Gas Plant Polymerization LPG Sulfur Plant Sulfur Alkyl Feed Alkylation Butanes Fuel Gas LPG Gas Separation & Stabilizer Light Naphtha Heavy Naphtha Isomerization
More informationOptimizing Distillate Yields and Product Qualities. Srini Srivatsan, Director - Coking Technology
Optimizing Distillate Yields and Product Qualities Srini Srivatsan, Director - Coking Technology Email: srini.srivatsan@amecfw.com Optimizing Distillate Yields and Product Properties Overview Delayed coker
More informationA) Particulars of organization
CHAPTER-I PARTICULARS OF ORGANISATION, ITS FUNCTIONS AND DUTIES A) Particulars of organization a) MRPL A Profile Mangalore Refinery and Petrochemicals Limited (MRPL) operates a grass root refinery with
More informationMini refinery feasibility study
Mini refinery feasibility study Introduction The first part of any study into a mini-refinery application is an initial assessment of its economic feasibility. This requires an understanding of what a
More informationFig:1.1[15] Fig.1.2 Distribution of world energy resources. (From World Energy Outlook 2005, International Energy Agency.)[16,17]
Introduction :Composition of petroleum,laboratory tests,refinery feedstocks and products Fig:1.1[15] Fig.1.2 Distribution of world energy resources. (From World Energy Outlook 2005, International Energy
More informationFEASIBILITY REPORT 100% BS-V AUTO FUEL PRODUCTION AT 13.7 MMTPA
FOR 100% BS-V AUTO FUEL PRODUCTION INDIAN OIL CORPORATION LIMITED GUJRAT REFINERY JANUARY -2016 FOR 100% BS-V AUTO FUEL PRODUCTION AT 13.7 MMTPA CLIENT INDIAN OIL CORPORATION LIMITED GUJRAT REFINERY PREPARED
More informationThe Role of the Merox Process in the Era of Ultra Low Sulfur Transportation Fuels. 5 th EMEA Catalyst Technology Conference 3 & 4 March 2004
The Role of the Merox Process in the Era of Ultra Low Sulfur Transportation Fuels 5 th EMEA Catalyst Technology Conference 3 & 4 March 2004 Dennis Sullivan UOP LLC The specifications for transportation
More informationCHAPTER 2 REFINERY FEED STREAMS: STREAMS FROM THE ATMOSPHERIC AND VACUUM TOWERS
CHAPTER 2 REFINERY FEED STREAMS: STREAMS FROM THE ATMOSPHERIC AND VACUUM TOWERS About This Chapter The previous chapter introduced crude oil as a mixture of compounds. The characteristics of these compounds
More informationOil & Gas. From exploration to distribution. Week 3 V19 Refining Processes (Part 1) Jean-Luc Monsavoir. W3V19 - Refining Processes1 p.
Oil & Gas From exploration to distribution Week 3 V19 Refining Processes (Part 1) Jean-Luc Monsavoir W3V19 - Refining Processes1 p. 1 Crude Oil Origins and Composition The objective of refining, petrochemical
More informationMARKETS & APPLICATIONS. Elliott Turbomachinery for Refineries
MARKETS & APPLICATIONS Elliott Turbomachinery for Refineries Elliott in the Refinery C 2 To LPG Facility C 3 To LPG Facility Absorber ic 4 Gas Plant nc 4 Plant Power Turbine Generator Package Refrigeration
More information5.0 DIESEL HYDROTREATING UNIT
5.0 DIESEL HYDROTREATING UNIT 5.1 INTRODUCTION 5.1.1 PURPOSE The main purpose of the DHDT unit is to hydrotreat the diesel components from atmospheric and vacuum units of existing and expansion units,
More informationPETROLEUM: CHEMISTRY, REFINING, FUELS AND PETROCHEMICALS - Petroleum: Chemistry, Refining, Fuels and Petrochemicals Refining - James G.
PETROLEUM: CHEMISTRY, REFINING, FUELS AND PETROCHEMICALS -REFINING James G. Speight 2476 Overland Road,Laramie, WY 82070-4808, USA Keywords: Dewatering, desalting, atmospheric distillation, vacuum distillation,
More informationCatalytic Reforming for Aromatics Production. Topsoe Catalysis Forum Munkerupgaard, Denmark August 27 28, 2015 Greg Marshall GAM Engineering LLC 1
Catalytic Reforming for Aromatics Production Topsoe Catalysis Forum Munkerupgaard, Denmark August 27 28, 2015 Greg Marshall GAM Engineering LLC GAM Engineering LLC 1 REFINERY CONFIURATION LPG NAPHTHA HYDROTREATING
More informationGTC Technology Day. 16 April Hotel Le Meridien New Delhi. Isomalk Technologies for Light Naphtha Isomerization
16 April Hotel Le Meridien New Delhi Isomalk Technologies for Light Naphtha Isomerization Naphtha Processing Technology by GTC n-c4 Isomalk-3 i-c4 Light Naphtha Isomalk-2 C5/C6 Isomerate C7 Paraffins Isomalk-4
More informationBitumen has become an
Revamping crude and vacuum units to process bitumen Revamping crude and vacuum units to process dilbit can involve extensive equipment replacement as well as major changes to the crude preheating scheme
More informationSulzer Chemtech. Process Technology and Equipment for Oil Refineries and Crude Oil Production
Sulzer Chemtech Process Technology and Equipment for Oil Refineries and Crude Oil Production 0696 2523 Excellence in Refining Technology Sulzer Chemtech is the process engineering division of the international
More informationREFINERY PROCESS AND PETROLEUM PRODUCTS
Training Title REFINERY PROCESS AND PETROLEUM PRODUCTS Training Duration 5 days Training Date Refinery Process & Petroleum Products 5 15-19 Mar $4,250 Dubai, UAE In any of the 5 star hotels. The exact
More informationADVANCED DISTILLATION
ADVANCED DISTILLATION Dividing Wall Columns in Petrochemical Industry Taking Advanced Distillation into the Modern Era Manish Bhargava - Director Advanced Distillation GTC Technology K Shreya BPCL Mumbai
More informationSimulation of Hydrodesulphurization (HDS) Unit of Kaduna Refining and Petrochemical Company Limited
Simulation of Hydrodesulphurization (HDS) Unit of Kaduna Refining and Petrochemical Company Limited 1 Bilal S., 1 Mohammed Dabo I.A., 1 Mujahid A. U., 2 Kasim S.A., 1 Nuhu M., 1 Mohammed A., 1 Abubakar
More informationCrude Assay, ASTM, TBP distillations, Evaluation of crude oil properties.
Crude Assay, ASTM, TBP distillations, Evaluation of crude oil properties. Crude Oil Distillation Crude oil distillation is an open art technology. The crude oil is distilled at atmospheric pressure and
More informationCHAPTER 3 OIL REFINERY PROCESSES
CHAPTER 3 OIL REFINERY PROCESSES OUTLINE 1. Introduction 2. Physical Processes 3. Thermal Processes 4. Catalytic Processes 5. Conversion of Heavy Residues 6. Treatment of Refinery Gas Streams INTRODUCTION
More informationPILOT PLANT DESIGN, INSTALLATION & OPERATION Training Duration 5 days
Training Title PILOT PLANT DESIGN, INSTALLATION & OPERATION Training Duration 5 days Training Date Pilot Plant Design, Installation & Operation 5 21 25 Sep $3,750 Dubai, UAE In any of the 5 star hotels.
More informationAnnex A: General Description of Industry Activities
Annex A: General Description of Industry Activities 65. The EHS Guidelines for Petroleum Refining cover processing operations from crude oil to finished liquid products, including liquefied petroleum gas
More informationSolvent Deasphalting Conversion Enabler
Kevin Whitehead Solvent Deasphalting Conversion Enabler 5 th December 2017 Bottom of the Barrel Workshop NIORDC, Tehran 2017 UOP Limited Solvent Deasphalting (SDA) 1 Natural Gas Refinery Fuel Gas Hydrogen
More informationUnit 1. Naphtha Catalytic Reforming. Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna
Unit 1. Naphtha Catalytic Reforming Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna Introduction Catalytic reforming of heavy naphtha and isomerization of light naphtha constitute
More information1. Crude oil Atmospheric Distillation Unit
Petroleum Refining Chapter 7: Distillation Chapter 7 Distillation The first processing units in the refinery are based on physical separation. There are two types: 1. Atmospheric distillation Units 2.
More informationRefining/Petrochemical Integration-A New Paradigm Joseph C. Gentry, Director - Global Licensing Engineered to Innovate
Refining/Petrochemical Integration-A New Paradigm Introduction The global trend in motor fuel consumption favors diesel over gasoline. There is a simultaneous increase in demand for various petrochemicals
More informationKolmetz Handbook of Process Equipment Design REFINERY ATMOSPHERIC CRUDE TOWER SELECTION AND SIZING (ENGINEERING DESIGN GUIDELINE)
Page: 1 of 164 SOLUTIONS, STANDARDS AND SOFTWARE www.klmtechgroup.com Rev 01 KLM Technology #03-12 Block Aronia, Jalan Sri Perkasa 2 Taman Tampoi Utama 81200 Johor Bahru Malaysia Kolmetz Handbook of TOWER
More informationThe Role of a New FCC Gasoline Three-Cut Splitter in Transformation of Crude Oil Hydrocarbons in CRC
8 The Role of a New FCC Gasoline Three-Cut Splitter in Transformation of Crude Oil Hydrocarbons in CRC Hugo Kittel, Ph.D., Strategy and Long Term Technical Development Manager tel. +0 7 80, e-mail hugo.kittel@crc.cz
More informationOlefins Recovery CRYO PLUS TECHNOLOGY
Olefins Recovery CRYO PLUS TECHNOLOGY 02 Refining & petrochemical experience. Linde Engineering North America Inc. (LENA) has constructed more than twenty (20) CRYO-PLUS units since 1984. Proprietary technology.
More informationCHALLENGES = OPPORTUNITIES
CHALLENGES = OPPORTUNITIES PRESENTER: ABDULAZIZ NAWAB AL BLOOSHI TOKYO, 25 TH JANUARY 2018 ABU DHABI NATIONAL ADNOC OIL COMPANY REFINING FUTURE REFINING & PETROLEUM INDUSTRY REFORMATION OUTLINE Overview
More informationUSES FOR RECYCLED OIL
USES FOR RECYCLED OIL What happens to your recycled used oil? Used oil, or 'sump oil' as it is sometimes called, should not be thrown away. Although it gets dirty, used oil can be cleaned of contaminants
More informationGTC TECHNOLOGY WHITE PAPER
GTC TECHNOLOGY WHITE PAPER Refining/Petrochemical Integration FCC Gasoline to Petrochemicals Refining/Petrochemical Integration - FCC Gasoline to Petrochemicals Introduction The global trend in motor fuel
More informationReliable. Efficient. Economical. Distillation Technology ENGINEERING - EQUIPMENT - TURNKEY SYSTEMS
TM Economical Efficient Reliable Distillation Technology ENGINEERING - EQUIPMENT - TURNKEY SYSTEMS DISTILLATION TECHNOLOGY Distillation is by far the most important separation process in the petroleum
More informationIncreased recovery of straight-run
Maximising diesel recovery from crude The CDU/DU process flow scheme is reviewed, including equipment design and operating fundamentals used to maximise straight-run diesel recovery. Factors important
More informationCrude Tower Simulation Aspen Plus v8.6. The feedstock to the crude system will be an equal mix of Light, Medium, & Heavy Crude oils.
Crude Tower Simulation Aspen Plus v8.6 Steps to set up a simulation in Aspen Plus v8.6 to model a crude tower system consisting of: Crude Oil Preheat Train Atmospheric Crude Tower Vacuum Crude Tower Debutanizer
More informationOIL REFINERY PROCESSES
OIL REFINERY PROCESSES 1 Types of hydrocarbons Types of hydrocarbons (parafffins, naphthenes, and aromatics). This rating is important to the refinery since the value of the crude oil decreases from classification
More informationSensitivity analysis and determination of optimum temperature of furnace for commercial visbreaking unit
ISSN : 0974-7443 Sensitivity analysis and determination of optimum temperature of furnace for commercial visbreaking unit S.Reza Seif Mohaddecy*, Sepehr Sadighi Catalytic Reaction Engineering Department,
More informationUnipar Oxo Alcohols Plant. Start Up: August, 1984 Location: Mauá - São Paulo - Brasil. Nameplate Capacity:
page 1 Unipar Oxo Alcohols Plant Start Up: August, 1984 Location: Mauá - São Paulo - Brasil Nameplate Capacity:! Oxo plant: 33 KTA in Isodecyl Alcohol [6 t/day of Isodecyl Alcohol or 70 t/day of Tridecyl
More informationRefining/Petrochemical Integration-A New Paradigm
Refining/Petrochemical Integration-A New Paradigm Introduction The global trend in motor fuel consumption favors diesel over gasoline. There is a simultaneous increase in demand for various petrochemicals
More informationAtmospheric Crude Tower with Aspen HYSYS V8.0
Atmospheric Crude Tower with Aspen HYSYS V8.0 1. Lesson Objectives Assign petroleum assay to stream Configure column pre-heater Configure crude tower 2. Prerequisites Aspen HYSYS V8.0 Introduction to distillation
More informationUOP UNITY Hydrotreating Products
Satyam Mishra UOP UNITY Hydrotreating Products 19 February 2018 Honeywell UOP ME-TECH Seminar Dubai, UAE UOP 8080A-0 2018 UOP LLC. A Honeywell Company All rights reserved. Outline 1 Unity UNITY UOP Unity
More informationHow. clean is your. fuel?
How clean is your fuel? Maurice Korpelshoek and Kerry Rock, CDTECH, USA, explain how to produce and improve clean fuels with the latest technologies. Since the early 1990s, refiners worldwide have made
More informationOnce a waste of lamp oil production
Refinery All processes and activities described so far happened on the upstream side. he next step to convert crude to e.g. gasoline is happening on the downstream side in refineries. olie 1 Once a waste
More informationFouling tendency is a critical
Balanced distillation equipment design Fouling resistance and efficiency requirements for distillation equipment are balanced and optimised for reliable unit performance SOUN HO LEE GTC Technology Fouling
More informationCrude and vacuum distillation
APPLICATION REPORT Crude and vacuum distillation Crude oil Wash water Reflux drum Overhead flare valve Gas to flare Steam Non-condens - able gases Water Desalter Stripping steam Light naphtha Separator
More informationDistillation in Refining
CHAPTER Distillation in Refining 4 Stuart Fraser Consultant. London, UK, Formerly Head of Separations Group, BP Oil CHAPTER OUTLINE 4.1 Scale of the operation... 155 4.2 Refinery flow schemes... 158 4.3
More informationTYPES OF BLENDING PROCESS
SYSTEMS LTD Blending operations became a major strategy as an answer to the ever-growing competitions between refineries. The strategy of blending crude oils and refinery products is to increase refining
More informationSupply of Services for Detailed OEB Crude Assay Analysis
Tender Number [9900009229] Supply of Services for Detailed OEB Crude Assay Analysis SCOPE OF WORK SCOPE OF WORK 1. Introduction Orpic is the brand name for Oman Oil Refineries and Petroleum Industries
More informationNPRA 2010 Q&A and Technology Forum
HYDROPROCESSING Safety 1 What is your experience with emergency isolation equipment (such as a check valve or actuated valve) on the outlet of reactor charge heaters to prevent loss of containment of the
More information20,000 bpd CRUDE OIL REFINERY FOR SALE AND RELOCATION
Ref.-No.: ProOil-278 20,000 bpd CRUDE OIL REFINERY FOR SALE AND RELOCATION Presented by: Lohrmann International Germany FACTS The Refinery was built at 20,000 BPD by UOP/Chyoda in 1974 and mothballed in
More informationThermal cracking Introduction
5.3 Thermal cracking 5.3.1 Introduction Thermal cracking is the thermal decomposition of straight-run and recycled heavy s at temperatures between about 450 and 540 C under moderate pressure conditions.
More informationAnnexure-I. Product Pattern after Implementation of Projects
Annexure-I Product Pattern after Implementation of Projects Sl No Project Case (A) Crude 1 Assam 320 2 Imported 2,380 3 Total 2,700 (B) Products 1 LPG 249 2 Naphtha 26 3 MS 529 4 SKO 136 5 HSD 1,407 6
More information100,000 bpd Refurbished Oil Refinery FOR SALE AND RELOCATION
Ref.-No.: ProOil-276 100,000 bpd Refurbished Oil Refinery FOR SALE AND RELOCATION Presented by: LOHRMANN RBD (Refinery Business Division) 1. Process Units Capacity Description barrels per day Licensor
More informationSCANFINING TECHNOLOGY: A PROVEN OPTION FOR PRODUCING ULTRA-LOW SULFUR CLEAN GASOLINE
SCANFINING TECHNOLOGY: A PROVEN OPTION FOR PRODUCING ULTRA-LOW SULFUR CLEAN GASOLINE Mohan Kalyanaraman Sean Smyth John Greeley Monica Pena LARTC 3rd Annual Meeting 9-10 April 2014 Cancun, Mexico Agenda
More informationProduct Blending & Optimization Considerations. Chapters 12 & 14
Product Blending & Optimization Considerations Chapters 12 & 14 Gases Polymerization Sulfur Plant Sulfur Gas Sat Gas Plant LPG Butanes Fuel Gas Gas Separation & Stabilizer Light Naphtha Isomerization Alkyl
More informationFSR on Expansion and Modernization of the MOIN Refinery Project
1 EXECUTIVE SUMMARY 1.1 Introduction SORESCO S.A., a Joint Venture between RECOPE and CNPCI, have been evaluating the feasibility of the Moín Refinery expansion from 166 m 3 /h (25,000 barrels per day,
More informationREFORMATE Crude Condensate Naphtha Ethane Reformate
REFORMATE Crude The Crude Overview gives a summary of the daily price movements of the benchmark WTI (West Texas Intermediate) and Brent futures contracts on the NYMEX and IPE exchanges, detailing any
More informationAs the global energy sector
Improved distillation efficiency Dividing wall technology applied to a xylenes separation project delivered superior energy efficiency compared to a two- arrangement MANISH BHARGAVA, ROOMI KALITA and JOSEPH
More informationУверенная модернизация
Уверенная модернизация Compact refineries (mini-refineries) Rustranstek through its partners offers wide range of compact refineries (mini-refineries) with crude oil output from 10 to 500 thousand tons
More informationUsing Pyrolysis Tar to meet Fuel Specifications in Coal-to-Liquids Plants
Using Pyrolysis Tar to meet Fuel Specifications in Coal-to-Liquids Plants Jaco Schieke, Principal Process Engineer, Foster Wheeler Business Solutions Group, Reading, UK email: Jaco_Schieke@fwuk.fwc.com
More informationNational Iranian Oil Engineering & Construction Co.
Introduction National Iranian Oil Engineering and Construction Company (NIOEC) intend to build a new 15, barrel per day oil refinery in Tabriz, Iran. The new refinery, named Shahriar, will be integrated
More informationEnhance Naphtha Value and Gasoline Reformer Performance Using UOP s MaxEne TM Process
Enhance Naphtha Value and Gasoline Reformer Performance Using UOP s MaxEne TM Process Mark Turowicz UOP IPL, A Honeywell Company 1st IndianOil Petrochemical Conclave March 16, 2012 Gurgaon, India 2011
More informationOptimal Model-Based Production Planning for Refinery Operation
Optimal Model-Based Production Planning for Refinery Operation Abdulrahman Alattas Advisor: Ignacio Grossmann Chemical Engineering Department Carnegie Mellon University EWO Meeting March 2009 1 Outline
More informationPetroleum Refining-Production Planning, Scheduling and Yield Optimization
An Intensive 10-Day Training Course Petroleum Refining-Production Planning, Scheduling and Yield Optimization 06-17 Dec 2015 03-14 Apr 2016 04-15 Dec 2016 Dubai, United Arab Emirates 18-OCT-15 This course
More informationGTC Technology Day. 16 April Hotel Le Meridien New Delhi. Latest Applications of GT-DWC
16 April Hotel Le Meridien New Delhi Latest Applications of GT-DWC Agenda GTC: The Trendsetter in implementing DWC technology Optimization of Process Complexes using GT-DWC Gasoline Production (MS Block)
More informationHandbook of Petroleum Processing
Handbook of Petroleum Processing Handbook of Petroleum Processing Edited by DAVID S. J. STAN JONES retired chemical engineer (Fluor) Calgary, Canada and PETER R. PUJADÓ UOP LLC (retired)-illinois, U.S.A.
More informationIn 2000, the ConocoPhillips Sweeny, Texas, refinery began
Reprinted from: September 2004 issue, pgs 49 58 Used with permission. www.hydrocarbonprocessing.com SPECIALREPORT Consider retrofits to handle high-viscosity crudes Refiners must fine-tune crude unit process
More informationCONTENTS 1 INTRODUCTION SUMMARY 2-1 TECHNICAL ASPECTS 2-1 ECONOMIC ASPECTS 2-2
CONTENTS GLOSSARY xxiii 1 INTRODUCTION 1-1 2 SUMMARY 2-1 TECHNICAL ASPECTS 2-1 ECONOMIC ASPECTS 2-2 3 INDUSTRY STATUS 3-1 TRENDS IN TRANSPORTATION FUEL DEMAND 3-3 TRENDS IN ENVIRONMENTAL REGULATION 3-3
More informationAchieving Ultra-Low Sulfur Diesel with IsoTherming Technology
Achieving Ultra-Low Sulfur Diesel with IsoTherming Technology Matthew Clingerman ERTC Annual Meeting 13 15 November, 2017 DuPont Clean Technologies www.cleantechnologies.dupont.com Copyright 2017 E. I.
More informationPCE154. Refinery Process and Products. H.H. Sheikh Sultan Tower (0) Floor Corniche Street Abu Dhabi U.A.E
PCE154 Refinery Process and Products H.H. Sheikh Sultan Tower (0) Floor Corniche Street Abu Dhabi U.A.E www.ictd.ae ictd@ictd.ae Course Introduction: To provide broad technical information on refining
More informationBACKGROUND INFORMATION DOCUMENT
BACKGROUND INFORMATION DOCUMENT March 2014 PROPOSED NATREF CLEAN N FUELS II IN SASOLBURG, FREE STATE (NEAS Ref No: DEA/EIA/0001446/2012; DEA Ref. No: 14/12/16/3/3/2/413) 1. PURPOSE OF THIS DOCUMENT C O
More informationRefining 101. January 11, 2011
Refining 101 January 11, 2011 Safe Harbor Statement Statements contained in this presentation that state the Company s or management s expectations or predictions of the future are forward looking statements
More informationMEG/WRI s Partial Bitumen Upgrader Project Adding Value to MEG and Alberta
MEG/WRI s Partial Bitumen Upgrader Project Adding Value to MEG and Alberta February 2015 Presentation Format Who we are - MEG and WRI Introduction to Alberta oil sands Resource recovery, transportation
More informationPre-Owned OIL REFINERY 280,000 bpd FOR SALE AND RELOCATION
Ref.-No.: ProOil-306 Pre-Owned OIL REFINERY 280,000 bpd FOR SALE AND RELOCATION Presented by: Lohrmann International Germany 1. REFINERY HISTORY The Refinery was designed by Mobil and built between 1973
More informationMaximizing Refinery Margins by Petrochemical Integration
Topic Maximizing Refinery Margins by Petrochemical Integration Presented by : Rajeev Singh Global Demand for Refined Products 29% 29% 29% 29% 30% 30% 33% 10% 10% 10% 9% 8% 8% 7% 7% 7% 7% 7% 7% 7% 22% 22%
More informationMethanol distribution in amine systems and its impact on plant performance Abstract: Methanol in gas treating Methanol impact on downstream units
Abstract: Presented at the AIChE Spring 2015 meeting in Austin, TX, USA Methanol distribution in amine systems and its impact on plant performance Anand Govindarajan*, Nathan A. Hatcher, and Ralph H. Weiland
More informationChanges to America s Gasoline Pool. Charles Kemp. May 17, Baker & O Brien, Inc. All rights reserved.
Changes to America s Gasoline Pool Charles Kemp May 17, 2016 Baker & O Brien, Inc. All rights reserved. Discussion Points Light Naphtha Definitions Sources and Uses of Light Naphtha Octane Challenges Tier
More informationclean Efforts to minimise air pollution have already led to significant reduction of sulfur in motor fuels in the US, Canada, Keeping it
Maurice Korpelshoek, CDTECH, The Netherlands, and Kerry Rock and Rajesh Samarth, CDTECH, USA, discuss sulfur reduction in FCC gasoline without octane loss. Keeping it clean without affecting quality Efforts
More informationFCC Gasoline Treating Using Catalytic Distillation. Texas Technology Showcase March 2003, Houston, Texas. Dr. Mitchell E. Loescher
F Gasoline Treating Using atalytic Distillation Texas Technology Showcase March 2003, Houston, Texas Dr. Mitchell E. Loescher Gasoline of the Future Lead is out Olefins reduced Aromatics reduced Benzene
More informationRecent increases in hydraulic
Novel processing ideas for a condensate refinery Synergised unit flow schemes for a condensate refinery aim for high value refined products DONALD EIZENGA, DAVID SHECTERLE and FRANK ZHU UOP, a Honeywell
More information