Fluid coking is a continuous process that thermally converts heavy hydrocarbons like residue into lighter products using two fluidized bed vessels, a reactor and a burner. In the reactor, feedstock is cracked into vapor and coke deposits on circulating coke particles, which transfer heat to the reactor. Flexicoking integrates fluid coking with coke gasification to upgrade residues. It uses an air gasifier to burn coke for heat and a steam gasifier to produce syngas that can be further processed. Dual gasification flexicoking employs both gasifiers, with the air gasifier providing heat and the steam gasifier generating syngas for downstream use or hydrogen production.
In petroleum refining, the Crude Distillation Unit (CDU) (often referred to as the Atmospheric Distillation Unit) is usually the first processing equipment through which crude oil is fed. Once in the CDU, crude oil is distilled into various products, like naphtha, kerosene, and diesel, that then serve as feedstocks for all other processing units at the refinery.
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/petroleum-refining/
COURSE DESCRIPTION:
The main scope of the course is to create strong basis and fundamentals regarding the processes in the Petroleum Refining. We take a look to the Oil&Gas Industry briefly and continue directly with the Refining Process. We then make a focus in each individual unit operation in the refinery.
Learn about:
* Oil& Gas Industry
* Difference between Petroleum Refining vs. Petrochemical Industry
* Overview of the most important operations and products
* Market insight (supply/demand) as well as (production/consumption)
* Several Petroleum Refineries around the World
Unit Operations & Processes
* Refining and Fractionation
* Atmospheric Distillation Column
* Vacuum Distillation
* Hydrotreating (Hydrogenation)
* Blending
* Reforming
* Isomerization
* Alkylation
* Steam Cracking
* Fluid Catalytic Cracking
* Gas Sweetening (Hydrodesulfurization)
* Coking
Components:
* Fuel Gas / Natural Gas
* Liquified Petroleum Gases (LPG)
* Propane, Butane
* Sulfur / Hydrogen Sulfide
* Gasoline / Automotive Gas Oil
* Naphtha Cuts (Light/Heavy)
* Kerosene
* Diesel
* Gasoil
* Lubricants
* Vacuum Residues
* Asphalt
* Coke
NOTE: This course is focused for Process Simulation
At the end of the course you will feel confident in the Petroleum Refining Industry. You will know the most common Process & Unit Operations as well as their distribution, production and importance in daily life.
----
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CONTACT ME
Chemical.Engineering.Guy@Gmail.com
www.ChemicalEngineeringGuy.com
http://facebook.com/Chemical.Engineering.Guy
You speak spanish? Visit my spanish channel -www.youtube.com/ChemEngIQA
Project of Introduction to Petroleum and Gas Engineering and Explanation of the cracking process and types.Cracking, as the name suggests, is a process in which large hydrocarbon molecules are broken down into smaller and more useful ones,The cracking products, such as ethene, propene, buta-1,3-diene and C4 alkenes, are used to make many important chemicals. Others such as branched and cyclic alkanes are added to the gasoline fraction obtained from the distillation of crude oil to enhance the octane rating.
In petroleum refining, the Crude Distillation Unit (CDU) (often referred to as the Atmospheric Distillation Unit) is usually the first processing equipment through which crude oil is fed. Once in the CDU, crude oil is distilled into various products, like naphtha, kerosene, and diesel, that then serve as feedstocks for all other processing units at the refinery.
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/petroleum-refining/
COURSE DESCRIPTION:
The main scope of the course is to create strong basis and fundamentals regarding the processes in the Petroleum Refining. We take a look to the Oil&Gas Industry briefly and continue directly with the Refining Process. We then make a focus in each individual unit operation in the refinery.
Learn about:
* Oil& Gas Industry
* Difference between Petroleum Refining vs. Petrochemical Industry
* Overview of the most important operations and products
* Market insight (supply/demand) as well as (production/consumption)
* Several Petroleum Refineries around the World
Unit Operations & Processes
* Refining and Fractionation
* Atmospheric Distillation Column
* Vacuum Distillation
* Hydrotreating (Hydrogenation)
* Blending
* Reforming
* Isomerization
* Alkylation
* Steam Cracking
* Fluid Catalytic Cracking
* Gas Sweetening (Hydrodesulfurization)
* Coking
Components:
* Fuel Gas / Natural Gas
* Liquified Petroleum Gases (LPG)
* Propane, Butane
* Sulfur / Hydrogen Sulfide
* Gasoline / Automotive Gas Oil
* Naphtha Cuts (Light/Heavy)
* Kerosene
* Diesel
* Gasoil
* Lubricants
* Vacuum Residues
* Asphalt
* Coke
NOTE: This course is focused for Process Simulation
At the end of the course you will feel confident in the Petroleum Refining Industry. You will know the most common Process & Unit Operations as well as their distribution, production and importance in daily life.
----
Please show the love! LIKE, SHARE and SUBSCRIBE!
More likes, sharings, suscribers: MORE VIDEOS!
-----
CONTACT ME
Chemical.Engineering.Guy@Gmail.com
www.ChemicalEngineeringGuy.com
http://facebook.com/Chemical.Engineering.Guy
You speak spanish? Visit my spanish channel -www.youtube.com/ChemEngIQA
Project of Introduction to Petroleum and Gas Engineering and Explanation of the cracking process and types.Cracking, as the name suggests, is a process in which large hydrocarbon molecules are broken down into smaller and more useful ones,The cracking products, such as ethene, propene, buta-1,3-diene and C4 alkenes, are used to make many important chemicals. Others such as branched and cyclic alkanes are added to the gasoline fraction obtained from the distillation of crude oil to enhance the octane rating.
Processing of petroleum types of refluxKarnav Rana
PROCESSING OF PETROLEUM :TYPES OF REFLUX
arrangements of distillation towers
Pump back reflux and pump around reflux
Side stripping columns
process refining & petrochemicals
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/petroleum-refining/
COURSE DESCRIPTION:
The main scope of the course is to create strong basis and fundamentals regarding the processes in the Petroleum Refining. We take a look to the Oil&Gas Industry briefly and continue directly with the Refining Process. We then make a focus in each individual unit operation in the refinery.
Learn about:
* Oil& Gas Industry
* Difference between Petroleum Refining vs. Petrochemical Industry
* Overview of the most important operations and products
* Market insight (supply/demand) as well as (production/consumption)
* Several Petroleum Refineries around the World
Unit Operations & Processes
* Refining and Fractionation
* Atmospheric Distillation Column
* Vacuum Distillation
* Hydrotreating (Hydrogenation)
* Blending
* Reforming
* Isomerization
* Alkylation
* Steam Cracking
* Fluid Catalytic Cracking
* Gas Sweetening (Hydrodesulfurization)
* Coking
Components:
* Fuel Gas / Natural Gas
* Liquified Petroleum Gases (LPG)
* Propane, Butane
* Sulfur / Hydrogen Sulfide
* Gasoline / Automotive Gas Oil
* Naphtha Cuts (Light/Heavy)
* Kerosene
* Diesel
* Gasoil
* Lubricants
* Vacuum Residues
* Asphalt
* Coke
NOTE: This course is focused for Process Simulation
At the end of the course you will feel confident in the Petroleum Refining Industry. You will know the most common Process & Unit Operations as well as their distribution, production and importance in daily life.
----
Please show the love! LIKE, SHARE and SUBSCRIBE!
More likes, sharings, suscribers: MORE VIDEOS!
-----
CONTACT ME
Chemical.Engineering.Guy@Gmail.com
www.ChemicalEngineeringGuy.com
http://facebook.com/Chemical.Engineering.Guy
You speak spanish? Visit my spanish channel -www.youtube.com/ChemEngIQA
This is course on Plant Simulation will show you how to setup hypothetical compounds, oil assays, blends, and petroleum characterization using the Oil Manager of Aspen HYSYS.
You will learn about:
Hypothetical Compounds (Hypos)
Estimation of hypo compound data
Models via Chemical Structure UNIFAC Component Builder
Basis conversion/cloning of existing components
Input of Petroleum Assay and Crude Oils
Typical Bulk Properties (Molar Weight, Density, Viscosity)
Distillation curves such as TBP (Total Boiling Point)
ASTM (D86, D1160, D86-D1160, D2887)
Chromatography
Light End
Oil Characterization
Using the Petroleum Assay Manager or the Oil Manager
Importing Assays: Existing Database
Creating Assays: Manually / Model
Cutting: Pseudocomponent generation
Blending of crude oils
Installing oils into Aspen HYSYS flowsheets
Getting Results (Plots, Graphs, Tables)
Property and Composition Tables
Distribution Plot (Off Gas, Light Short Run, Naphtha, Kerosene, Light Diesel, Heavy Diesel, Gasoil, Residue)
Oil Properties
Proper
Boiling Point Curves
Viscosity, Density, Molecular Weight Curves
This is helpful for students, teachers, engineers and researchers in the area of R&D, specially those in the Oil and Gas or Petroleum Refining industry.
This is a "workshop-based" course, there is about 25% theory and about 75% work!
At the end of the course you will be able to handle crude oils for your fractionation, refining, petrochemical process simulations!
Natural Gas (from a natural reservoir or associated to a crude production) can contain acid gas (H2S and/or CO2)..
The Gas Sweetening Process aims to remove part or all of the acid gas.
Episode 3 : Production of Synthesis Gas by Steam Methane ReformingSAJJAD KHUDHUR ABBAS
Episode 3 : Production of Synthesis Gas by Steam Methane Reforming
History of Synthesis Gas
In 1780, Felice Fontana discovered that combustible gas develops if water vapor is passed over carbon at temperatures over 500 °C. This CO and H2 containing gas was called water gas and mainly used for lighting purposes in the19th century.
As of the beginning of the 20th century, H2/CO-mixtures were used for syntheses of hydrocarbons and then, as a consequence, also called synthesis gas.
Haber and Bosch discovered the synthesis of ammonia from H2 and N2 in 1910 and the first industrial ammonia synthesis plant was commissioned in 1913.
The production of liquid hydrocarbons and oxygenates from syngas conversion over iron catalysts was discovered in 1923 by Fischer and Tropsch.
Much of the syngas conversion processes were being developed in Germany during the first and second world wars at a time when natural resources were becoming scare and alternative routes for hydrogen production, ammonia synthesis, and transportation fuels were a necessity.
In 1943/44, this was applied for large-scale production of artificial fuels from synthesis gas in Germany.
Oil 101 - A Free Introduction to Oil and Gas
Introduction to Refining
This refining overview includes segments on: Why we refine crude oil, a basic summary of the refining distillation process, and some historical perspective on the evolution of refining.
The complete Refining Module includes lessons on crude oil and products, refinery processes, key business drivers that impact refining profitability, and more.
Why Do We Refine Crude Oil?
Crude oil cannot be used as it occurs in nature, other than burning for fuel, which is wasteful, It must be refined to manufacture finished products such as gasoline and heating oil.
In the refinery, crude oil components can first be split by carefully applying heat to capture various parts, called fractions, within certain boiling ranges. This is called distillation. The quality of these initial fractions produced is not sufficient to be sold directly as petroleum products without further treatment.
Moreover, the yield of products from straight distillation of crude oil is not the same as the “demand barrel” needed for the marketplace. Crude oil must therefore be further processed using both heat and pressure to improve qualities and meet market demand.
A large part of refinery processing is concerned with converting unwanted heavy fuel oil into marketable gasoline and diesel, using various processing methods.
This is a report on the design of a plant to produce 20 million standard cubic feet per day (0.555 × 106 standard m3/day) of hydrogen (H2) of at least 95% purity from heavy fuel oil (HFO) with an upstream time of 7680 hours/year applying the process of partial oxidation of the heavy oil feedstock.
Processing of petroleum types of refluxKarnav Rana
PROCESSING OF PETROLEUM :TYPES OF REFLUX
arrangements of distillation towers
Pump back reflux and pump around reflux
Side stripping columns
process refining & petrochemicals
COURSE LINK:
https://www.chemicalengineeringguy.com/courses/petroleum-refining/
COURSE DESCRIPTION:
The main scope of the course is to create strong basis and fundamentals regarding the processes in the Petroleum Refining. We take a look to the Oil&Gas Industry briefly and continue directly with the Refining Process. We then make a focus in each individual unit operation in the refinery.
Learn about:
* Oil& Gas Industry
* Difference between Petroleum Refining vs. Petrochemical Industry
* Overview of the most important operations and products
* Market insight (supply/demand) as well as (production/consumption)
* Several Petroleum Refineries around the World
Unit Operations & Processes
* Refining and Fractionation
* Atmospheric Distillation Column
* Vacuum Distillation
* Hydrotreating (Hydrogenation)
* Blending
* Reforming
* Isomerization
* Alkylation
* Steam Cracking
* Fluid Catalytic Cracking
* Gas Sweetening (Hydrodesulfurization)
* Coking
Components:
* Fuel Gas / Natural Gas
* Liquified Petroleum Gases (LPG)
* Propane, Butane
* Sulfur / Hydrogen Sulfide
* Gasoline / Automotive Gas Oil
* Naphtha Cuts (Light/Heavy)
* Kerosene
* Diesel
* Gasoil
* Lubricants
* Vacuum Residues
* Asphalt
* Coke
NOTE: This course is focused for Process Simulation
At the end of the course you will feel confident in the Petroleum Refining Industry. You will know the most common Process & Unit Operations as well as their distribution, production and importance in daily life.
----
Please show the love! LIKE, SHARE and SUBSCRIBE!
More likes, sharings, suscribers: MORE VIDEOS!
-----
CONTACT ME
Chemical.Engineering.Guy@Gmail.com
www.ChemicalEngineeringGuy.com
http://facebook.com/Chemical.Engineering.Guy
You speak spanish? Visit my spanish channel -www.youtube.com/ChemEngIQA
This is course on Plant Simulation will show you how to setup hypothetical compounds, oil assays, blends, and petroleum characterization using the Oil Manager of Aspen HYSYS.
You will learn about:
Hypothetical Compounds (Hypos)
Estimation of hypo compound data
Models via Chemical Structure UNIFAC Component Builder
Basis conversion/cloning of existing components
Input of Petroleum Assay and Crude Oils
Typical Bulk Properties (Molar Weight, Density, Viscosity)
Distillation curves such as TBP (Total Boiling Point)
ASTM (D86, D1160, D86-D1160, D2887)
Chromatography
Light End
Oil Characterization
Using the Petroleum Assay Manager or the Oil Manager
Importing Assays: Existing Database
Creating Assays: Manually / Model
Cutting: Pseudocomponent generation
Blending of crude oils
Installing oils into Aspen HYSYS flowsheets
Getting Results (Plots, Graphs, Tables)
Property and Composition Tables
Distribution Plot (Off Gas, Light Short Run, Naphtha, Kerosene, Light Diesel, Heavy Diesel, Gasoil, Residue)
Oil Properties
Proper
Boiling Point Curves
Viscosity, Density, Molecular Weight Curves
This is helpful for students, teachers, engineers and researchers in the area of R&D, specially those in the Oil and Gas or Petroleum Refining industry.
This is a "workshop-based" course, there is about 25% theory and about 75% work!
At the end of the course you will be able to handle crude oils for your fractionation, refining, petrochemical process simulations!
Natural Gas (from a natural reservoir or associated to a crude production) can contain acid gas (H2S and/or CO2)..
The Gas Sweetening Process aims to remove part or all of the acid gas.
Episode 3 : Production of Synthesis Gas by Steam Methane ReformingSAJJAD KHUDHUR ABBAS
Episode 3 : Production of Synthesis Gas by Steam Methane Reforming
History of Synthesis Gas
In 1780, Felice Fontana discovered that combustible gas develops if water vapor is passed over carbon at temperatures over 500 °C. This CO and H2 containing gas was called water gas and mainly used for lighting purposes in the19th century.
As of the beginning of the 20th century, H2/CO-mixtures were used for syntheses of hydrocarbons and then, as a consequence, also called synthesis gas.
Haber and Bosch discovered the synthesis of ammonia from H2 and N2 in 1910 and the first industrial ammonia synthesis plant was commissioned in 1913.
The production of liquid hydrocarbons and oxygenates from syngas conversion over iron catalysts was discovered in 1923 by Fischer and Tropsch.
Much of the syngas conversion processes were being developed in Germany during the first and second world wars at a time when natural resources were becoming scare and alternative routes for hydrogen production, ammonia synthesis, and transportation fuels were a necessity.
In 1943/44, this was applied for large-scale production of artificial fuels from synthesis gas in Germany.
Oil 101 - A Free Introduction to Oil and Gas
Introduction to Refining
This refining overview includes segments on: Why we refine crude oil, a basic summary of the refining distillation process, and some historical perspective on the evolution of refining.
The complete Refining Module includes lessons on crude oil and products, refinery processes, key business drivers that impact refining profitability, and more.
Why Do We Refine Crude Oil?
Crude oil cannot be used as it occurs in nature, other than burning for fuel, which is wasteful, It must be refined to manufacture finished products such as gasoline and heating oil.
In the refinery, crude oil components can first be split by carefully applying heat to capture various parts, called fractions, within certain boiling ranges. This is called distillation. The quality of these initial fractions produced is not sufficient to be sold directly as petroleum products without further treatment.
Moreover, the yield of products from straight distillation of crude oil is not the same as the “demand barrel” needed for the marketplace. Crude oil must therefore be further processed using both heat and pressure to improve qualities and meet market demand.
A large part of refinery processing is concerned with converting unwanted heavy fuel oil into marketable gasoline and diesel, using various processing methods.
This is a report on the design of a plant to produce 20 million standard cubic feet per day (0.555 × 106 standard m3/day) of hydrogen (H2) of at least 95% purity from heavy fuel oil (HFO) with an upstream time of 7680 hours/year applying the process of partial oxidation of the heavy oil feedstock.
IJERA (International journal of Engineering Research and Applications) is International online, ... peer reviewed journal. For more detail or submit your article, please visit www.ijera.com
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptxR&R Consult
CFD analysis is incredibly effective at solving mysteries and improving the performance of complex systems!
Here's a great example: At a large natural gas-fired power plant, where they use waste heat to generate steam and energy, they were puzzled that their boiler wasn't producing as much steam as expected.
R&R and Tetra Engineering Group Inc. were asked to solve the issue with reduced steam production.
An inspection had shown that a significant amount of hot flue gas was bypassing the boiler tubes, where the heat was supposed to be transferred.
R&R Consult conducted a CFD analysis, which revealed that 6.3% of the flue gas was bypassing the boiler tubes without transferring heat. The analysis also showed that the flue gas was instead being directed along the sides of the boiler and between the modules that were supposed to capture the heat. This was the cause of the reduced performance.
Based on our results, Tetra Engineering installed covering plates to reduce the bypass flow. This improved the boiler's performance and increased electricity production.
It is always satisfying when we can help solve complex challenges like this. Do your systems also need a check-up or optimization? Give us a call!
Work done in cooperation with James Malloy and David Moelling from Tetra Engineering.
More examples of our work https://www.r-r-consult.dk/en/cases-en/
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Dr.Costas Sachpazis
Terzaghi's soil bearing capacity theory, developed by Karl Terzaghi, is a fundamental principle in geotechnical engineering used to determine the bearing capacity of shallow foundations. This theory provides a method to calculate the ultimate bearing capacity of soil, which is the maximum load per unit area that the soil can support without undergoing shear failure. The Calculation HTML Code included.
NO1 Uk best vashikaran specialist in delhi vashikaran baba near me online vas...Amil Baba Dawood bangali
Contact with Dawood Bhai Just call on +92322-6382012 and we'll help you. We'll solve all your problems within 12 to 24 hours and with 101% guarantee and with astrology systematic. If you want to take any personal or professional advice then also you can call us on +92322-6382012 , ONLINE LOVE PROBLEM & Other all types of Daily Life Problem's.Then CALL or WHATSAPP us on +92322-6382012 and Get all these problems solutions here by Amil Baba DAWOOD BANGALI
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Final project report on grocery store management system..pdfKamal Acharya
In today’s fast-changing business environment, it’s extremely important to be able to respond to client needs in the most effective and timely manner. If your customers wish to see your business online and have instant access to your products or services.
Online Grocery Store is an e-commerce website, which retails various grocery products. This project allows viewing various products available enables registered users to purchase desired products instantly using Paytm, UPI payment processor (Instant Pay) and also can place order by using Cash on Delivery (Pay Later) option. This project provides an easy access to Administrators and Managers to view orders placed using Pay Later and Instant Pay options.
In order to develop an e-commerce website, a number of Technologies must be studied and understood. These include multi-tiered architecture, server and client-side scripting techniques, implementation technologies, programming language (such as PHP, HTML, CSS, JavaScript) and MySQL relational databases. This is a project with the objective to develop a basic website where a consumer is provided with a shopping cart website and also to know about the technologies used to develop such a website.
This document will discuss each of the underlying technologies to create and implement an e- commerce website.
Cosmetic shop management system project report.pdfKamal Acharya
Buying new cosmetic products is difficult. It can even be scary for those who have sensitive skin and are prone to skin trouble. The information needed to alleviate this problem is on the back of each product, but it's thought to interpret those ingredient lists unless you have a background in chemistry.
Instead of buying and hoping for the best, we can use data science to help us predict which products may be good fits for us. It includes various function programs to do the above mentioned tasks.
Data file handling has been effectively used in the program.
The automated cosmetic shop management system should deal with the automation of general workflow and administration process of the shop. The main processes of the system focus on customer's request where the system is able to search the most appropriate products and deliver it to the customers. It should help the employees to quickly identify the list of cosmetic product that have reached the minimum quantity and also keep a track of expired date for each cosmetic product. It should help the employees to find the rack number in which the product is placed.It is also Faster and more efficient way.
Hierarchical Digital Twin of a Naval Power SystemKerry Sado
A hierarchical digital twin of a Naval DC power system has been developed and experimentally verified. Similar to other state-of-the-art digital twins, this technology creates a digital replica of the physical system executed in real-time or faster, which can modify hardware controls. However, its advantage stems from distributing computational efforts by utilizing a hierarchical structure composed of lower-level digital twin blocks and a higher-level system digital twin. Each digital twin block is associated with a physical subsystem of the hardware and communicates with a singular system digital twin, which creates a system-level response. By extracting information from each level of the hierarchy, power system controls of the hardware were reconfigured autonomously. This hierarchical digital twin development offers several advantages over other digital twins, particularly in the field of naval power systems. The hierarchical structure allows for greater computational efficiency and scalability while the ability to autonomously reconfigure hardware controls offers increased flexibility and responsiveness. The hierarchical decomposition and models utilized were well aligned with the physical twin, as indicated by the maximum deviations between the developed digital twin hierarchy and the hardware.
1. Department of Presented By
Chemical Engineering, KAMALJEET CHAUHAN
UIET, Kanpur CSJMA14001390203
A
Power Point Presentation
on
FLUID COKING
2. FLUID COKING
Fluid coking is a continuous fluid bed technology.
It thermally converts heavy hydrocarbons such as vacuum
residuum, atmospheric residuum, oil sands bitumen, heavy
whole crudes, deasphalter bottoms, or FCC bottoms to lighter
products.
Fluid Coking is currently used commercially in refineries for
deep conversion and as the resource to upgrade heavy
oils/bitumens.
3. FLUID COKING
Fluid coking uses two vessels.
A reactor and a burner.
Both the reactor vessel and burner vessel contain
fluidized beds with coke particles circulating between
the two vessel by fluidized solids techniques.
Coke particles are circulated to transfer heat to the
reactor.
The residuum is cooled by distributing it as a thin
film of liquid on the outside of the hot coke particles.
5. PROCESS DESCRIPTION
Heated by the produced coke
Cracking reactions occur inside the heater and the fluidized-bed reactor.
The fluid coke is partially formed in the heater.
Hot coke slurry from the heater is recycled to the fluid reactor to
provide the heat required for the cracking reactions.
Fluid coke is formed by spraying the hot feed on the already-formed
coke particles.
Reactor temperature is about 520°C, and the conversion into coke is
immediate, with complete disorientation of the crystallites of product
coke.
The burning process in fluid coking tends to concentrate the metals, but
it does not reduce the sulfur content of the coke.
6. Characteristics of fluid coke:
High sulfur content,
Low volatility, poor crystalline structure, and low
grindability index.
Flexicoking, integrates fluid coking with coke
gasification.
Most of the coke is gasified. Flexicoking
gasification produces a substantial concentration of
the metals in the coke product.
7. Flexicoking
Flexicoking process integrates
conventional fluid coking with coke
gasification process for upgrading heavy
resids.
The gasification is effected by the
addition of air and steam to a fluidized
solids vessels.
The gaseous products are subsequently
treated to produce a clean fuel gas.
9. Conventional
flexicoking
In the simplified flexicoking process residuum
feed is injected into the reactor where it is
thermally cracked to a full range of vaporized
products plus coke, which is deposited on the
fluidized coke particles.
The heavier fractions are condensed in the
scrubber and are normally recycled back to the
coking reactor.
The lighter fractions proceeds overhead from
the scrubber to a conventional fractionator.
10. The heat required for the endothermic reaction
in the reactor is supplied by a circulating hot-
coke stream from the heater.
In the gasifier, oxygen which enters at the
bottom of the bed can react in two ways.
If it reaches a coke particles, it reacts to
produce a mixture of CO and CO2.
Secondly, oxygen can react in the void space
between particles with the CO which has been
formed to produce more CO2.
Throughout most of the bed, the slow reaction
are dominant.
12. Dual gasification
flexicoking
In the air gasifier, coke is burned with air to
provide heat of reaction for the reactor.
The steam gasifier with resulting production
of low heating value coke gas.
In the steam gasifier, a H2/CO rich synthesis
gas is produced which can either be water
gas shifted for H2 manufacture or used as a
synthesis gas.
The synthesis gas produced in dual
gasification flaxicoking can be used in a
variety of ways, including manufacture of
13. Coke is circulated to the air gasifier where it is
burned with air to form CO2.
Hot coke is also circulated to the steam
gasifier where the gasification of carbon with
steam to form CO and H2 is one of the
predominant reactions taking place.
As the result of the steam gasification, all of
the components necessary for water gas shift
reaction are present, and at the condition of
the steam gasifier this reaction is at
equilibrium.
Since the water gas shift reaction produces
some CO2, gasification of coke with this
14. Synthesis
Gas
Coke Gas
Steam
Figure: Dual gasification flexicoking process.
Steam
Heate
r
Reacto
r
Air
Gasifie
r
Steanm
Gasifier
Coke Fines
Removal
Sulphur
Removel
Sulphur
Resi
Feed
Recycle
Feed
Scrubber
Reactio
n
Product
s
Purge
Coke
Air
Coke
Fines