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1
2
Made by :-
Salah_Eldin Mohammed Ibrahim 12012083
Abd_Elrahman Khalid Ramadan Mohammed 12012057
Ahmed Essam El_sayed El_sayed 12012106
Moutaz Bellah Anwar Ibrahim 12012226
Mohammed Essam Gamil Hassan 12012202
Mohammed Mousa Abd-Elmaboad Ali 22013122
Ahmed Salah Ahmed El_Sayed 12012102
Hadeer Ashraf Fahmy 12012062
Supervisor:-
Dr. Eng. Prof/ Mohammed saad
3
Agenda
*Introduction To Refining process
*Overview of refining of petroleum
*Conversion processes
*Types of reforming processes
*feed perparation
*Platform process
*process variables
*chemistry of catalytic reforming
*Catalyst deactivation and generation
*Troubleshooting of catalytic reforming
4
*Introduction To Refining process
5
6
• History of Refining Crude Oil.
• Timeline – Global Petroleum Industry.
• Summary of the history of refining
processing.
• The top countries in oil producing.
Overview of refining of petroleum
7
8
Conversion process
9
10
*Re-arrangement processes
A-reforming
B-Isomerization
A-reforming
Types of reforming processes
11
12
Catalytic reforming unit
Aim of catalytic reforming
13
* Typical naphtha feed stock :
* Typical heavy naphtha feed stock :
14
Naphtha hydrotreating
15
16
* Naphtha hydrotreating :
It is the first step in catalytic reforming used to prepare
clean feed stock to protect
Catalyst used in naphtha reforming .
* Purpose of naphtha hydrotreating process
Is to remove various catalyst poison such as :
Sulphur , nitrogen , oxygen , halogen , etc ….
17
Platform process
1-process description
2-feed and product
18
19
process variables
1- Reactor Pressure :
2 - Reactor Temperature :
3 - Space Velocity :
4 - Hydrogen (H2) /Hydrocarbon Molar (HC) Ratio
5 - Charge/ feed stock Properties or characteristics
6 - Catalyst Selectivity :
6 - a) Catalyst Activity and Stability
6 - b) CatalysDifferent
20
chemistry of catalytic reforming
21
The four major REACTIONS IN CATALYTIC REFORMING
Desirable
• Dehydrogenation of naphthenes to aromatics
• Isomerisation of paraffins and naphthenes
• Dehydrocyclisation of paraffins to aromatics
Non-Desirable
• Hydrocracking of paraffins to lower molecular
weight compounds
22
Conditions for Different Reforming Reactions
TemperaturPressureReaction
High temperatureLow pressureDehydrogenation of
naphthenes to aromatics
IndeterminateIndeterm-inateIsomerisation of
naphthenes
High temperatureLow pressureDehydrocylistion of
paraffins to aromatics
High temperatureHigh pressureHydrocracking
23
Catalyst deactivation and regeneration
24
25
CATALYST DEACTIVATION/POISONING :-
Catalyst poisoning refers to the partial or total deactivation of a catalyst
caused by exposure to a range of chemical compounds.
FACTORS CAUSING DEACTIVATION :-
•High temperature exposure: automobile catalytic converter, close to 1000 C
•Poisoning: exhaust or process contaminants adsorbing onto or blocking active sites
•Attrition and erosion of the wash coat from the support.
26
TYPES OF POISONING :-
1-SELECTIVE-POISONING .
2-NONSELECTIVE-POISONING.
Deactivation by Fouling :-
form of fouling Generally fouling covers all phenomena where
the surface is covered with a deposit.
Catalytic Fouling:-
Fouling is a real life issue that takes place during chemical processes. The
deposit of unwanted materials on a surface is defined as fouling, and affects
how a chemical process proceeds. Fouling adds a layer of organic, inorganic or
even living organisms to the surface which affects the properties of the catalyst
and the mechanism of the process
Chemical Deactivation – Poisoning :-
Poisoning occurs when there is a strong chemical interaction of reactants,
products, or impurities with active sites on the catalyst surface.
27
Deactivation by Thermal Degradation and
Sintering
For a catalyst to be effective it must have an effective interface with the reactants,
thus heterogeneous catalysts are prepared with high surface areas
Removal ways :-
Coke Removal
General Mechanism of Coke Removal
Specifically the coke undergoes several different processes during
removal:
1- Pyrolysis 2- Combustion
3- Gasification 4- addition
The following equation describes the reversible gas phase water
gasshif Treaction:-
Troubleshooting of catalytic reforming
28
29
30
* 1-charge stock less naphthenic
* 2-sulfur contamination
* 3-high chloride
* 4-high water
* None
* Eliminate source
* Do not increase reactor inlet
temperature
*Reduce chloride injection
* Reduce water injection and
eliminate source of excess water
31
32
33
34
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Presentation 1-2-3-4-5-6-7-8-9-10

  • 1. 1
  • 2. 2 Made by :- Salah_Eldin Mohammed Ibrahim 12012083 Abd_Elrahman Khalid Ramadan Mohammed 12012057 Ahmed Essam El_sayed El_sayed 12012106 Moutaz Bellah Anwar Ibrahim 12012226 Mohammed Essam Gamil Hassan 12012202 Mohammed Mousa Abd-Elmaboad Ali 22013122 Ahmed Salah Ahmed El_Sayed 12012102 Hadeer Ashraf Fahmy 12012062 Supervisor:- Dr. Eng. Prof/ Mohammed saad
  • 3. 3 Agenda *Introduction To Refining process *Overview of refining of petroleum *Conversion processes *Types of reforming processes *feed perparation *Platform process *process variables *chemistry of catalytic reforming *Catalyst deactivation and generation *Troubleshooting of catalytic reforming
  • 4. 4
  • 6. 6 • History of Refining Crude Oil. • Timeline – Global Petroleum Industry. • Summary of the history of refining processing. • The top countries in oil producing.
  • 7. Overview of refining of petroleum 7
  • 8. 8
  • 11. Types of reforming processes 11
  • 13. Aim of catalytic reforming 13
  • 14. * Typical naphtha feed stock : * Typical heavy naphtha feed stock : 14
  • 16. 16
  • 17. * Naphtha hydrotreating : It is the first step in catalytic reforming used to prepare clean feed stock to protect Catalyst used in naphtha reforming . * Purpose of naphtha hydrotreating process Is to remove various catalyst poison such as : Sulphur , nitrogen , oxygen , halogen , etc …. 17
  • 20. 1- Reactor Pressure : 2 - Reactor Temperature : 3 - Space Velocity : 4 - Hydrogen (H2) /Hydrocarbon Molar (HC) Ratio 5 - Charge/ feed stock Properties or characteristics 6 - Catalyst Selectivity : 6 - a) Catalyst Activity and Stability 6 - b) CatalysDifferent 20
  • 21. chemistry of catalytic reforming 21
  • 22. The four major REACTIONS IN CATALYTIC REFORMING Desirable • Dehydrogenation of naphthenes to aromatics • Isomerisation of paraffins and naphthenes • Dehydrocyclisation of paraffins to aromatics Non-Desirable • Hydrocracking of paraffins to lower molecular weight compounds 22
  • 23. Conditions for Different Reforming Reactions TemperaturPressureReaction High temperatureLow pressureDehydrogenation of naphthenes to aromatics IndeterminateIndeterm-inateIsomerisation of naphthenes High temperatureLow pressureDehydrocylistion of paraffins to aromatics High temperatureHigh pressureHydrocracking 23
  • 24. Catalyst deactivation and regeneration 24
  • 25. 25 CATALYST DEACTIVATION/POISONING :- Catalyst poisoning refers to the partial or total deactivation of a catalyst caused by exposure to a range of chemical compounds. FACTORS CAUSING DEACTIVATION :- •High temperature exposure: automobile catalytic converter, close to 1000 C •Poisoning: exhaust or process contaminants adsorbing onto or blocking active sites •Attrition and erosion of the wash coat from the support.
  • 26. 26 TYPES OF POISONING :- 1-SELECTIVE-POISONING . 2-NONSELECTIVE-POISONING. Deactivation by Fouling :- form of fouling Generally fouling covers all phenomena where the surface is covered with a deposit. Catalytic Fouling:- Fouling is a real life issue that takes place during chemical processes. The deposit of unwanted materials on a surface is defined as fouling, and affects how a chemical process proceeds. Fouling adds a layer of organic, inorganic or even living organisms to the surface which affects the properties of the catalyst and the mechanism of the process Chemical Deactivation – Poisoning :- Poisoning occurs when there is a strong chemical interaction of reactants, products, or impurities with active sites on the catalyst surface.
  • 27. 27 Deactivation by Thermal Degradation and Sintering For a catalyst to be effective it must have an effective interface with the reactants, thus heterogeneous catalysts are prepared with high surface areas Removal ways :- Coke Removal General Mechanism of Coke Removal Specifically the coke undergoes several different processes during removal: 1- Pyrolysis 2- Combustion 3- Gasification 4- addition The following equation describes the reversible gas phase water gasshif Treaction:-
  • 29. 29
  • 30. 30
  • 31. * 1-charge stock less naphthenic * 2-sulfur contamination * 3-high chloride * 4-high water * None * Eliminate source * Do not increase reactor inlet temperature *Reduce chloride injection * Reduce water injection and eliminate source of excess water 31
  • 32. 32
  • 33. 33