SlideShare a Scribd company logo
1 of 4
Download to read offline
1
CATALYST ISOMERIZATION UNIT
KIT
General purpose
The unit is designed for manufacturing
high-octane gasoline with a MON of 76-82 (RON 80
to 92) by means of processing light petroleum
fractions and gas condensates.
The unit provides a boost in octane number by
13 to 30 points, as well as an improvement of
performance attributes and parameters of
hydrocarbon fuels.
The technological process is based on the
reactions of splitting and isomerization of normal
alcanes on a zeolite catalyst.
Raw material
Straight run gasolines and gas condensates
with boiling temperatures below 180°C.
Product
The product is an isomer with a MON of 76-83 (80-92 RON), which is subsequently used as a raw
material in manufacturing finished gasoline with a RON of 92 to 95.
The petrol produced fully complies with the state standards GOST 2084-77 and GOST R 51105-97.
Adaptations
The unit is supplied in various adaptations, which differ in capacity, embodiment, and equipment in
accordance with the Customer’s requirements.
FEATURES
 Weight: below 5000 kg for KIT-24 and below 8000 kg for KIT-48;
 The weight of the catalyst: 1 ton for KIT-24 and 2 tons for KIT-48.
 Capacity by feed stock: 24 or 48 m3
per day;
 Capacity of the charging pump: 1 or 2 m3
per hour;
 Heating to operation temperature: below 6 hours;
 Shipping dimensions of the container (L-W-H): 6000-2300-2500 mm.
 Productivity:
o Gasoline: 95%;
o Propane and butane compound: 5%.
2
The productivity ratings can slightly fluctuate depending on the raw material and the depth of the
conversion.
TECHNOLOGICAL PROCESS
An octane number boost is accounted for the process of catalyst isomerization of low-octane
gasoline into high-octane unleaded petrol.
The isomerization of gasoline fractions is a structural transformation of straight-chain hydrocarbons
into branched-chain hydrocarbons with a higher octane number. It is a continuous process, involving
direct heating of the hydrocarbon liquids with an electric stream induction heater.
The raw material goes through a cascade of recuperators where gets preheated while cooling the
isomer. Afterwards, the heated raw material enters the coiler of the heater where reaches the operation
temperature. The resulting gases enter the reactor where isomerization occurs. The depth of the process is
controlled by the rate of feed of the raw material. The resulting isomer enters the storage tanks after
getting cooled in a cascade of heat exchangers.
The manufacture is organized in a closed circuit in hermetic appliances, excluding any form of
contact between the raw material and the environment.
Electric equipment is fire-safe and flameproof. The unit can be operated and controlled in both
automated and manual mode.
The unit is equipped with a GSM module, providing remote control and monitoring.
Firefighting and alarm system
 Powder fire extinguisher Buran-2,5-2C: 2 self-actuating modules.
 2 fire extinguishers OP-8.
 Light-audible alarm system BC-3.
 Emergency trip button.
3
Additional equipment in the container
 Explosion-proof LED lighting.
 Maintenance stand with an operating floor.
 Hoisting eyes.
 Maintenance hatch, providing access to the
upper deck of the plant.
 Lightning rod.
 Ground rod.
Material specification
Light hydrocarbons with boiling temperature below 180°C.
 Sulfur rate: below 0,1% (by weight);
 Water contents: not allowed.
 Mechanical impurities: not allowed.
 Oxygen based or other additives: not allowed.
Climatic version
 Ambient air temperature: from -60°C to 40°C
 Realtive humidity at 25°C: 80%.
Power requirements
 Voltage: ~380V
 Frequency: 50 Hz
 Capacity:
o KIT-24: 100 kWh (operating mode); 165
kWh (initialization mode).
o KIT-48: 180 kWh (operating mode); 240
kWh (initialization mode).
Energy self-sufficiency
The unit can be equipped with a furnace fed with the propane-butane compound produced as a by-product
of the unit.
Control block features
 Main fuse box.
 Distribution board.
 Inductive current generator.
 Operator’s touch pad with firmvare.
Organization requirements
 Availability of storage tanks for raw and processed hydrocarbons
 An even site, excluding settling under the weight of the plant, as the latter is delivered fully
mounted in a container.
As an alternative, a light screw pile foundation can be used.
4
 Staff: 1 or 2 operators in shifts.
CATALIST KIT-2
 Zeolite catalyst used for the isomerization of hydrocarbons.
 Service cycle: 3 months (depending on the raw material).
 Warranty: 10 months.
 Reactivation: 48 hours.
 Precious metals: absent.
DELIVERED COMPLETE WITH
 Control block.
 Power module.
 Technological module.
 Catalyst KIT-2: 1 charge.
 Passport.
 User’s manual.
 Declaration of compliance to Technical Regulation in the Customs Union
 Operating touch pad.
WARRANTY
 The manufacturer guarantees compliance with performance ratings provided that exploitation,
transportation and storage requirements are observed.
 Service life: over 5 years.
 Warranty: 12 months.
 Post-warranty: on contractual terms.
ECONOMIC ADVANTAGES
 Octane number boost by up to 30 points.
 Payback period: 6 months.
 The service does not require more than 1 operator.
Price includes
 KIT 24/48 unit as described above;
 Supervision of mounting;
 Commissioning and adjustment;
 A year’s supply of catalyst;
 Shipping within Russia;
 1 year warranty.
You are welcome to require samples of the product for an independent examination. Alternatively,
you can test unit with your own raw material to make sure of the high quality of the product.

More Related Content

What's hot

SYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDS
SYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDSSYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDS
SYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDSGerard B. Hawkins
 
The Selection of Flocculants and other Solid-Liquid Separation Aids
The Selection of Flocculants and other Solid-Liquid Separation AidsThe Selection of Flocculants and other Solid-Liquid Separation Aids
The Selection of Flocculants and other Solid-Liquid Separation AidsGerard B. Hawkins
 
Biological Systems - A Special Case
Biological Systems - A Special CaseBiological Systems - A Special Case
Biological Systems - A Special CaseGerard B. Hawkins
 
In-Situ Oxidation Procedure for High and Low Temperature Shift Catalysts
In-Situ Oxidation Procedure for High and Low Temperature Shift CatalystsIn-Situ Oxidation Procedure for High and Low Temperature Shift Catalysts
In-Situ Oxidation Procedure for High and Low Temperature Shift CatalystsGerard B. Hawkins
 
Hydrogen Plant Monitoring & Methane Steam Reformer Troubleshooting
Hydrogen Plant Monitoring & Methane Steam Reformer TroubleshootingHydrogen Plant Monitoring & Methane Steam Reformer Troubleshooting
Hydrogen Plant Monitoring & Methane Steam Reformer TroubleshootingGerard B. Hawkins
 
Determination of Residue on Evaporation in Anhydrous Ammonia
Determination of Residue on Evaporation in Anhydrous AmmoniaDetermination of Residue on Evaporation in Anhydrous Ammonia
Determination of Residue on Evaporation in Anhydrous AmmoniaGerard B. Hawkins
 
Naphtha Steam Reforming Catalyst Reduction with Methanol
Naphtha Steam Reforming Catalyst Reduction with MethanolNaphtha Steam Reforming Catalyst Reduction with Methanol
Naphtha Steam Reforming Catalyst Reduction with MethanolGerard B. Hawkins
 
Isothermal Methanol Converter (IMC) UA Distribution Analysis
Isothermal Methanol Converter (IMC) UA Distribution AnalysisIsothermal Methanol Converter (IMC) UA Distribution Analysis
Isothermal Methanol Converter (IMC) UA Distribution AnalysisGerard B. Hawkins
 
Catalytic reforming process
Catalytic reforming processCatalytic reforming process
Catalytic reforming processIhsan Wassan
 
ACTIVATED CARBON- AIR-STEAM REGENERATION PROCEDURE
ACTIVATED CARBON-  AIR-STEAM REGENERATION PROCEDUREACTIVATED CARBON-  AIR-STEAM REGENERATION PROCEDURE
ACTIVATED CARBON- AIR-STEAM REGENERATION PROCEDUREGerard B. Hawkins
 
Reactor Modeling Tools - An Overview
Reactor Modeling Tools - An OverviewReactor Modeling Tools - An Overview
Reactor Modeling Tools - An OverviewGerard B. Hawkins
 
Discharge and Reduction Procedures for Methanation Catalyst
Discharge and Reduction Procedures for Methanation CatalystDischarge and Reduction Procedures for Methanation Catalyst
Discharge and Reduction Procedures for Methanation CatalystGerard B. Hawkins
 
Reactor Arrangement for Continuous Vapor Phase Chlorination
Reactor Arrangement for Continuous Vapor Phase ChlorinationReactor Arrangement for Continuous Vapor Phase Chlorination
Reactor Arrangement for Continuous Vapor Phase ChlorinationGerard B. Hawkins
 
Study 4: Construction / Design Verification
Study 4: Construction / Design VerificationStudy 4: Construction / Design Verification
Study 4: Construction / Design VerificationGerard B. Hawkins
 
Design and Operation of NHT Strippers to Protect Catalytic Reformers
Design and Operation of NHT Strippers to Protect Catalytic Reformers Design and Operation of NHT Strippers to Protect Catalytic Reformers
Design and Operation of NHT Strippers to Protect Catalytic Reformers Gerard B. Hawkins
 
Debottlenecking Claus Sulfur Recovery Units: An Investigation of the applicat...
Debottlenecking Claus Sulfur Recovery Units: An Investigation of the applicat...Debottlenecking Claus Sulfur Recovery Units: An Investigation of the applicat...
Debottlenecking Claus Sulfur Recovery Units: An Investigation of the applicat...Gerard B. Hawkins
 
Steam Reforming Catalyst Reduction with LPG Feed
Steam Reforming Catalyst Reduction with LPG FeedSteam Reforming Catalyst Reduction with LPG Feed
Steam Reforming Catalyst Reduction with LPG FeedGerard B. Hawkins
 
METHANOL PRODUCTION USING VULCAN SYSTEMS COMBINED REFORMING TECHNOLOGY (ATR) ...
METHANOL PRODUCTION USING VULCAN SYSTEMS COMBINED REFORMING TECHNOLOGY (ATR) ...METHANOL PRODUCTION USING VULCAN SYSTEMS COMBINED REFORMING TECHNOLOGY (ATR) ...
METHANOL PRODUCTION USING VULCAN SYSTEMS COMBINED REFORMING TECHNOLOGY (ATR) ...Gerard B. Hawkins
 

What's hot (20)

SYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDS
SYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDSSYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDS
SYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDS
 
The Selection of Flocculants and other Solid-Liquid Separation Aids
The Selection of Flocculants and other Solid-Liquid Separation AidsThe Selection of Flocculants and other Solid-Liquid Separation Aids
The Selection of Flocculants and other Solid-Liquid Separation Aids
 
Biological Systems - A Special Case
Biological Systems - A Special CaseBiological Systems - A Special Case
Biological Systems - A Special Case
 
In-Situ Oxidation Procedure for High and Low Temperature Shift Catalysts
In-Situ Oxidation Procedure for High and Low Temperature Shift CatalystsIn-Situ Oxidation Procedure for High and Low Temperature Shift Catalysts
In-Situ Oxidation Procedure for High and Low Temperature Shift Catalysts
 
catalytic reforming
catalytic reformingcatalytic reforming
catalytic reforming
 
Hydrogen Plant Monitoring & Methane Steam Reformer Troubleshooting
Hydrogen Plant Monitoring & Methane Steam Reformer TroubleshootingHydrogen Plant Monitoring & Methane Steam Reformer Troubleshooting
Hydrogen Plant Monitoring & Methane Steam Reformer Troubleshooting
 
Determination of Residue on Evaporation in Anhydrous Ammonia
Determination of Residue on Evaporation in Anhydrous AmmoniaDetermination of Residue on Evaporation in Anhydrous Ammonia
Determination of Residue on Evaporation in Anhydrous Ammonia
 
Naphtha Steam Reforming Catalyst Reduction with Methanol
Naphtha Steam Reforming Catalyst Reduction with MethanolNaphtha Steam Reforming Catalyst Reduction with Methanol
Naphtha Steam Reforming Catalyst Reduction with Methanol
 
HAZARD STUDY 1: REPORTING
HAZARD STUDY 1: REPORTINGHAZARD STUDY 1: REPORTING
HAZARD STUDY 1: REPORTING
 
Isothermal Methanol Converter (IMC) UA Distribution Analysis
Isothermal Methanol Converter (IMC) UA Distribution AnalysisIsothermal Methanol Converter (IMC) UA Distribution Analysis
Isothermal Methanol Converter (IMC) UA Distribution Analysis
 
Catalytic reforming process
Catalytic reforming processCatalytic reforming process
Catalytic reforming process
 
ACTIVATED CARBON- AIR-STEAM REGENERATION PROCEDURE
ACTIVATED CARBON-  AIR-STEAM REGENERATION PROCEDUREACTIVATED CARBON-  AIR-STEAM REGENERATION PROCEDURE
ACTIVATED CARBON- AIR-STEAM REGENERATION PROCEDURE
 
Reactor Modeling Tools - An Overview
Reactor Modeling Tools - An OverviewReactor Modeling Tools - An Overview
Reactor Modeling Tools - An Overview
 
Discharge and Reduction Procedures for Methanation Catalyst
Discharge and Reduction Procedures for Methanation CatalystDischarge and Reduction Procedures for Methanation Catalyst
Discharge and Reduction Procedures for Methanation Catalyst
 
Reactor Arrangement for Continuous Vapor Phase Chlorination
Reactor Arrangement for Continuous Vapor Phase ChlorinationReactor Arrangement for Continuous Vapor Phase Chlorination
Reactor Arrangement for Continuous Vapor Phase Chlorination
 
Study 4: Construction / Design Verification
Study 4: Construction / Design VerificationStudy 4: Construction / Design Verification
Study 4: Construction / Design Verification
 
Design and Operation of NHT Strippers to Protect Catalytic Reformers
Design and Operation of NHT Strippers to Protect Catalytic Reformers Design and Operation of NHT Strippers to Protect Catalytic Reformers
Design and Operation of NHT Strippers to Protect Catalytic Reformers
 
Debottlenecking Claus Sulfur Recovery Units: An Investigation of the applicat...
Debottlenecking Claus Sulfur Recovery Units: An Investigation of the applicat...Debottlenecking Claus Sulfur Recovery Units: An Investigation of the applicat...
Debottlenecking Claus Sulfur Recovery Units: An Investigation of the applicat...
 
Steam Reforming Catalyst Reduction with LPG Feed
Steam Reforming Catalyst Reduction with LPG FeedSteam Reforming Catalyst Reduction with LPG Feed
Steam Reforming Catalyst Reduction with LPG Feed
 
METHANOL PRODUCTION USING VULCAN SYSTEMS COMBINED REFORMING TECHNOLOGY (ATR) ...
METHANOL PRODUCTION USING VULCAN SYSTEMS COMBINED REFORMING TECHNOLOGY (ATR) ...METHANOL PRODUCTION USING VULCAN SYSTEMS COMBINED REFORMING TECHNOLOGY (ATR) ...
METHANOL PRODUCTION USING VULCAN SYSTEMS COMBINED REFORMING TECHNOLOGY (ATR) ...
 

Viewers also liked

Key Considerations for a Reforming Unit Revamp
Key Considerations for a Reforming Unit RevampKey Considerations for a Reforming Unit Revamp
Key Considerations for a Reforming Unit RevampGerard B. Hawkins
 
Reactions of isomerization of n butane
Reactions of isomerization of n butaneReactions of isomerization of n butane
Reactions of isomerization of n butaneKareem Tharaa
 
Reduction and Start-Up of Steam Reforming Catalyst
Reduction and Start-Up of Steam Reforming CatalystReduction and Start-Up of Steam Reforming Catalyst
Reduction and Start-Up of Steam Reforming CatalystGerard B. Hawkins
 
006 isomerization of hydrocarbons
006 isomerization of hydrocarbons006 isomerization of hydrocarbons
006 isomerization of hydrocarbonsElizabeth Indah P
 
PD230 Catalytic Reforming
PD230 Catalytic ReformingPD230 Catalytic Reforming
PD230 Catalytic ReformingpetroEDGE
 
Fuel and combustion
Fuel and combustionFuel and combustion
Fuel and combustionRaju Mirdha
 
octane and cetane numbers
octane and cetane numbersoctane and cetane numbers
octane and cetane numbersajitthorat
 
Fuels, Octane number & Cetane number
Fuels, Octane number & Cetane numberFuels, Octane number & Cetane number
Fuels, Octane number & Cetane numberRipal Maravia
 
Isomerization And Dextrinization S
Isomerization And Dextrinization SIsomerization And Dextrinization S
Isomerization And Dextrinization Sanshulber
 
03 Chemical Engineering Plant Design And Economics
03 Chemical Engineering Plant Design And Economics03 Chemical Engineering Plant Design And Economics
03 Chemical Engineering Plant Design And Economicsguestac67362
 
ppt of fuel and combustion
ppt of fuel and combustionppt of fuel and combustion
ppt of fuel and combustionSiddiqui Arif
 
Isomerism Power point
Isomerism Power pointIsomerism Power point
Isomerism Power pointsuresh gdvm
 
CI Engine Knocking
CI Engine KnockingCI Engine Knocking
CI Engine KnockingRajat Seth
 
Process design for chemical engineers
Process design for chemical engineersProcess design for chemical engineers
Process design for chemical engineersAmanda Ribeiro
 
Chemical Equipment Design, Lecture 1
Chemical Equipment Design, Lecture 1Chemical Equipment Design, Lecture 1
Chemical Equipment Design, Lecture 1yousifmagdi
 

Viewers also liked (20)

Isome hoa pdf
Isome hoa pdfIsome hoa pdf
Isome hoa pdf
 
Key Considerations for a Reforming Unit Revamp
Key Considerations for a Reforming Unit RevampKey Considerations for a Reforming Unit Revamp
Key Considerations for a Reforming Unit Revamp
 
Naphtha Sulfur Guards
Naphtha Sulfur GuardsNaphtha Sulfur Guards
Naphtha Sulfur Guards
 
Reactions of isomerization of n butane
Reactions of isomerization of n butaneReactions of isomerization of n butane
Reactions of isomerization of n butane
 
Reduction and Start-Up of Steam Reforming Catalyst
Reduction and Start-Up of Steam Reforming CatalystReduction and Start-Up of Steam Reforming Catalyst
Reduction and Start-Up of Steam Reforming Catalyst
 
006 isomerization of hydrocarbons
006 isomerization of hydrocarbons006 isomerization of hydrocarbons
006 isomerization of hydrocarbons
 
PD230 Catalytic Reforming
PD230 Catalytic ReformingPD230 Catalytic Reforming
PD230 Catalytic Reforming
 
cv
cvcv
cv
 
Fuel and combustion
Fuel and combustionFuel and combustion
Fuel and combustion
 
octane and cetane numbers
octane and cetane numbersoctane and cetane numbers
octane and cetane numbers
 
Octane number
Octane numberOctane number
Octane number
 
Fuels, Octane number & Cetane number
Fuels, Octane number & Cetane numberFuels, Octane number & Cetane number
Fuels, Octane number & Cetane number
 
Isomerization And Dextrinization S
Isomerization And Dextrinization SIsomerization And Dextrinization S
Isomerization And Dextrinization S
 
03 Chemical Engineering Plant Design And Economics
03 Chemical Engineering Plant Design And Economics03 Chemical Engineering Plant Design And Economics
03 Chemical Engineering Plant Design And Economics
 
ppt of fuel and combustion
ppt of fuel and combustionppt of fuel and combustion
ppt of fuel and combustion
 
Isomerism Power point
Isomerism Power pointIsomerism Power point
Isomerism Power point
 
2.1 fuels and combustion
2.1 fuels and combustion2.1 fuels and combustion
2.1 fuels and combustion
 
CI Engine Knocking
CI Engine KnockingCI Engine Knocking
CI Engine Knocking
 
Process design for chemical engineers
Process design for chemical engineersProcess design for chemical engineers
Process design for chemical engineers
 
Chemical Equipment Design, Lecture 1
Chemical Equipment Design, Lecture 1Chemical Equipment Design, Lecture 1
Chemical Equipment Design, Lecture 1
 

Similar to KIT_Isomerization unit

Chapter 5b -_cracking_ffcu
Chapter 5b -_cracking_ffcuChapter 5b -_cracking_ffcu
Chapter 5b -_cracking_ffcuHelena Francis
 
PresentationGGSSTP_Atul
PresentationGGSSTP_AtulPresentationGGSSTP_Atul
PresentationGGSSTP_AtulAtul Kataria
 
Final internship refinery Presentation (1).pptx
Final internship refinery Presentation (1).pptxFinal internship refinery Presentation (1).pptx
Final internship refinery Presentation (1).pptxAdisanu
 
We produce the Equipment to ginger up the Power Transformers!
We produce the Equipment to ginger up the Power Transformers!We produce the Equipment to ginger up the Power Transformers!
We produce the Equipment to ginger up the Power Transformers!Igor Bevza
 
Bench Top Muffle Furnace (1750 °C) by ACMAS Technologies Pvt Ltd.
Bench Top Muffle Furnace (1750 °C) by ACMAS Technologies Pvt Ltd.Bench Top Muffle Furnace (1750 °C) by ACMAS Technologies Pvt Ltd.
Bench Top Muffle Furnace (1750 °C) by ACMAS Technologies Pvt Ltd.Acmas Technologies Pvt. Ltd.
 
New ag associates heatpulse 210 rapid thermal annealing system
New ag associates heatpulse 210 rapid thermal annealing systemNew ag associates heatpulse 210 rapid thermal annealing system
New ag associates heatpulse 210 rapid thermal annealing systemPeter Chen
 
AccuThermo AW 610 Rapid Thermal Annealing Equipment
AccuThermo AW 610 Rapid Thermal Annealing EquipmentAccuThermo AW 610 Rapid Thermal Annealing Equipment
AccuThermo AW 610 Rapid Thermal Annealing EquipmentPeter Chen
 
New ag associates heatpulse 410 rapid thermal annealing system
New ag associates heatpulse 410 rapid thermal annealing systemNew ag associates heatpulse 410 rapid thermal annealing system
New ag associates heatpulse 410 rapid thermal annealing systemPeter Chen
 
New ag associates heatpulse 610 rapid thermal annealing system
New ag associates heatpulse 610 rapid thermal annealing systemNew ag associates heatpulse 610 rapid thermal annealing system
New ag associates heatpulse 610 rapid thermal annealing systemPeter Chen
 
السيره الذاتيه محدثه الى شهر أكتوبر _ 2016
السيره الذاتيه محدثه الى شهر أكتوبر  _  2016السيره الذاتيه محدثه الى شهر أكتوبر  _  2016
السيره الذاتيه محدثه الى شهر أكتوبر _ 2016Mohamed Wanan
 
Introduction to operation and Control of Thermal Power Plant
Introduction to operation and Control of Thermal Power PlantIntroduction to operation and Control of Thermal Power Plant
Introduction to operation and Control of Thermal Power PlantSWAPNILTRIVEDI6
 
Pyromax, Btg, Mag Presentation 2008
Pyromax, Btg, Mag Presentation 2008Pyromax, Btg, Mag Presentation 2008
Pyromax, Btg, Mag Presentation 2008Pyromax
 
Duncan cairnie ccm energy solutions hvacr seminar- april 2016
Duncan cairnie ccm energy solutions   hvacr seminar- april 2016Duncan cairnie ccm energy solutions   hvacr seminar- april 2016
Duncan cairnie ccm energy solutions hvacr seminar- april 2016ARAaus
 
Allwin21 and main products
Allwin21 and main productsAllwin21 and main products
Allwin21 and main productsPeter Chen
 
Summary Industrial Boilers market Spain 2019
Summary Industrial Boilers market Spain 2019Summary Industrial Boilers market Spain 2019
Summary Industrial Boilers market Spain 2019KONTAGION HUB LIMITED
 
Vertical steam boiler
Vertical steam boilerVertical steam boiler
Vertical steam boilerxindagroup1
 
IRJET-Smart System for Food Industries and Bakeries
IRJET-Smart System for Food Industries and BakeriesIRJET-Smart System for Food Industries and Bakeries
IRJET-Smart System for Food Industries and BakeriesIRJET Journal
 

Similar to KIT_Isomerization unit (20)

MOST_Fractionation unit
MOST_Fractionation unitMOST_Fractionation unit
MOST_Fractionation unit
 
Chapter 5b -_cracking_ffcu
Chapter 5b -_cracking_ffcuChapter 5b -_cracking_ffcu
Chapter 5b -_cracking_ffcu
 
PresentationGGSSTP_Atul
PresentationGGSSTP_AtulPresentationGGSSTP_Atul
PresentationGGSSTP_Atul
 
Final internship refinery Presentation (1).pptx
Final internship refinery Presentation (1).pptxFinal internship refinery Presentation (1).pptx
Final internship refinery Presentation (1).pptx
 
We produce the Equipment to ginger up the Power Transformers!
We produce the Equipment to ginger up the Power Transformers!We produce the Equipment to ginger up the Power Transformers!
We produce the Equipment to ginger up the Power Transformers!
 
Bench Top Muffle Furnace (1750 °C) by ACMAS Technologies Pvt Ltd.
Bench Top Muffle Furnace (1750 °C) by ACMAS Technologies Pvt Ltd.Bench Top Muffle Furnace (1750 °C) by ACMAS Technologies Pvt Ltd.
Bench Top Muffle Furnace (1750 °C) by ACMAS Technologies Pvt Ltd.
 
New ag associates heatpulse 210 rapid thermal annealing system
New ag associates heatpulse 210 rapid thermal annealing systemNew ag associates heatpulse 210 rapid thermal annealing system
New ag associates heatpulse 210 rapid thermal annealing system
 
AccuThermo AW 610 Rapid Thermal Annealing Equipment
AccuThermo AW 610 Rapid Thermal Annealing EquipmentAccuThermo AW 610 Rapid Thermal Annealing Equipment
AccuThermo AW 610 Rapid Thermal Annealing Equipment
 
New ag associates heatpulse 410 rapid thermal annealing system
New ag associates heatpulse 410 rapid thermal annealing systemNew ag associates heatpulse 410 rapid thermal annealing system
New ag associates heatpulse 410 rapid thermal annealing system
 
New ag associates heatpulse 610 rapid thermal annealing system
New ag associates heatpulse 610 rapid thermal annealing systemNew ag associates heatpulse 610 rapid thermal annealing system
New ag associates heatpulse 610 rapid thermal annealing system
 
السيره الذاتيه محدثه الى شهر أكتوبر _ 2016
السيره الذاتيه محدثه الى شهر أكتوبر  _  2016السيره الذاتيه محدثه الى شهر أكتوبر  _  2016
السيره الذاتيه محدثه الى شهر أكتوبر _ 2016
 
Eco Mobile
Eco MobileEco Mobile
Eco Mobile
 
Introduction to operation and Control of Thermal Power Plant
Introduction to operation and Control of Thermal Power PlantIntroduction to operation and Control of Thermal Power Plant
Introduction to operation and Control of Thermal Power Plant
 
Pyromax, Btg, Mag Presentation 2008
Pyromax, Btg, Mag Presentation 2008Pyromax, Btg, Mag Presentation 2008
Pyromax, Btg, Mag Presentation 2008
 
Duncan cairnie ccm energy solutions hvacr seminar- april 2016
Duncan cairnie ccm energy solutions   hvacr seminar- april 2016Duncan cairnie ccm energy solutions   hvacr seminar- april 2016
Duncan cairnie ccm energy solutions hvacr seminar- april 2016
 
Allwin21 and main products
Allwin21 and main productsAllwin21 and main products
Allwin21 and main products
 
Summary Industrial Boilers market Spain 2019
Summary Industrial Boilers market Spain 2019Summary Industrial Boilers market Spain 2019
Summary Industrial Boilers market Spain 2019
 
Vertical steam boiler
Vertical steam boilerVertical steam boiler
Vertical steam boiler
 
IRJET-Smart System for Food Industries and Bakeries
IRJET-Smart System for Food Industries and BakeriesIRJET-Smart System for Food Industries and Bakeries
IRJET-Smart System for Food Industries and Bakeries
 
PRESENTATION ON HYDROGEN GAS PRODUCTION BY PARTIAL OXIDATION OF HEAVY FUEL OI...
PRESENTATION ON HYDROGEN GAS PRODUCTION BY PARTIAL OXIDATION OF HEAVY FUEL OI...PRESENTATION ON HYDROGEN GAS PRODUCTION BY PARTIAL OXIDATION OF HEAVY FUEL OI...
PRESENTATION ON HYDROGEN GAS PRODUCTION BY PARTIAL OXIDATION OF HEAVY FUEL OI...
 

KIT_Isomerization unit

  • 1. 1 CATALYST ISOMERIZATION UNIT KIT General purpose The unit is designed for manufacturing high-octane gasoline with a MON of 76-82 (RON 80 to 92) by means of processing light petroleum fractions and gas condensates. The unit provides a boost in octane number by 13 to 30 points, as well as an improvement of performance attributes and parameters of hydrocarbon fuels. The technological process is based on the reactions of splitting and isomerization of normal alcanes on a zeolite catalyst. Raw material Straight run gasolines and gas condensates with boiling temperatures below 180°C. Product The product is an isomer with a MON of 76-83 (80-92 RON), which is subsequently used as a raw material in manufacturing finished gasoline with a RON of 92 to 95. The petrol produced fully complies with the state standards GOST 2084-77 and GOST R 51105-97. Adaptations The unit is supplied in various adaptations, which differ in capacity, embodiment, and equipment in accordance with the Customer’s requirements. FEATURES  Weight: below 5000 kg for KIT-24 and below 8000 kg for KIT-48;  The weight of the catalyst: 1 ton for KIT-24 and 2 tons for KIT-48.  Capacity by feed stock: 24 or 48 m3 per day;  Capacity of the charging pump: 1 or 2 m3 per hour;  Heating to operation temperature: below 6 hours;  Shipping dimensions of the container (L-W-H): 6000-2300-2500 mm.  Productivity: o Gasoline: 95%; o Propane and butane compound: 5%.
  • 2. 2 The productivity ratings can slightly fluctuate depending on the raw material and the depth of the conversion. TECHNOLOGICAL PROCESS An octane number boost is accounted for the process of catalyst isomerization of low-octane gasoline into high-octane unleaded petrol. The isomerization of gasoline fractions is a structural transformation of straight-chain hydrocarbons into branched-chain hydrocarbons with a higher octane number. It is a continuous process, involving direct heating of the hydrocarbon liquids with an electric stream induction heater. The raw material goes through a cascade of recuperators where gets preheated while cooling the isomer. Afterwards, the heated raw material enters the coiler of the heater where reaches the operation temperature. The resulting gases enter the reactor where isomerization occurs. The depth of the process is controlled by the rate of feed of the raw material. The resulting isomer enters the storage tanks after getting cooled in a cascade of heat exchangers. The manufacture is organized in a closed circuit in hermetic appliances, excluding any form of contact between the raw material and the environment. Electric equipment is fire-safe and flameproof. The unit can be operated and controlled in both automated and manual mode. The unit is equipped with a GSM module, providing remote control and monitoring. Firefighting and alarm system  Powder fire extinguisher Buran-2,5-2C: 2 self-actuating modules.  2 fire extinguishers OP-8.  Light-audible alarm system BC-3.  Emergency trip button.
  • 3. 3 Additional equipment in the container  Explosion-proof LED lighting.  Maintenance stand with an operating floor.  Hoisting eyes.  Maintenance hatch, providing access to the upper deck of the plant.  Lightning rod.  Ground rod. Material specification Light hydrocarbons with boiling temperature below 180°C.  Sulfur rate: below 0,1% (by weight);  Water contents: not allowed.  Mechanical impurities: not allowed.  Oxygen based or other additives: not allowed. Climatic version  Ambient air temperature: from -60°C to 40°C  Realtive humidity at 25°C: 80%. Power requirements  Voltage: ~380V  Frequency: 50 Hz  Capacity: o KIT-24: 100 kWh (operating mode); 165 kWh (initialization mode). o KIT-48: 180 kWh (operating mode); 240 kWh (initialization mode). Energy self-sufficiency The unit can be equipped with a furnace fed with the propane-butane compound produced as a by-product of the unit. Control block features  Main fuse box.  Distribution board.  Inductive current generator.  Operator’s touch pad with firmvare. Organization requirements  Availability of storage tanks for raw and processed hydrocarbons  An even site, excluding settling under the weight of the plant, as the latter is delivered fully mounted in a container. As an alternative, a light screw pile foundation can be used.
  • 4. 4  Staff: 1 or 2 operators in shifts. CATALIST KIT-2  Zeolite catalyst used for the isomerization of hydrocarbons.  Service cycle: 3 months (depending on the raw material).  Warranty: 10 months.  Reactivation: 48 hours.  Precious metals: absent. DELIVERED COMPLETE WITH  Control block.  Power module.  Technological module.  Catalyst KIT-2: 1 charge.  Passport.  User’s manual.  Declaration of compliance to Technical Regulation in the Customs Union  Operating touch pad. WARRANTY  The manufacturer guarantees compliance with performance ratings provided that exploitation, transportation and storage requirements are observed.  Service life: over 5 years.  Warranty: 12 months.  Post-warranty: on contractual terms. ECONOMIC ADVANTAGES  Octane number boost by up to 30 points.  Payback period: 6 months.  The service does not require more than 1 operator. Price includes  KIT 24/48 unit as described above;  Supervision of mounting;  Commissioning and adjustment;  A year’s supply of catalyst;  Shipping within Russia;  1 year warranty. You are welcome to require samples of the product for an independent examination. Alternatively, you can test unit with your own raw material to make sure of the high quality of the product.