Crude oil Treatment process

Slides:



Advertisements
Similar presentations
AROMATIC HYDROCARBONS
Advertisements

Petroleum and Gas Processing(TKK-2136)
GTL Taken Partly from the Internet and Edited and Revised by H M Fahmy.
A Quick Lesson On Crude Oil
Fractional Distillation Activity. Asphalt Coke Tar Wax Feedstock from Residue.
Mohan Konde HPCL Mumbai refinery SYMPOSIUM ON SOLVENT EXTRACTION REVISITED FEBRUARY 5 TH – 6th, 2010 IIChE (NRC) Auditorium NEW DELHI-INDIA Solvent De-asphalting.
Refining and Processing
Chapter 3 Refinery Feed stocks
Chapter 2: Refinery Products Over 2000 individual products distributed in 17 classes as shown in table below:
1. © 2013 Petroch Services Pty Ltd BP Version J11002– Occupational Hygiene in the Oil & Gas Industry Occupational Hygiene in the Oil & Gas Industry Day.
mmcl
Chapter 7: Catalytic Hydrocracking
Occupational Hygiene in the Basic Petroleum Chemistry
Petroleum and Gas Processing(TKK-2136) 14/15 Fall semester Instructor: Rama Oktavian Office Hr.: M.13-15, Tu , W.
Petroleum and Gas Processing(TKK-2136) 14/15 Fall semester Instructor: Rama Oktavian Office Hr.: M.13-15, Tu , W.
Crude Oil.
Chapter 4: Crude distillation
Catalytic cracking Catalytic cracking
Petroleum The Refining Process.
Oil refining and its Products
Chemistry and technology of petroleum
Reactor Models in Romeo
Chemistry and technology of petroleum
chemistry and technology of petroleum
Specific Industrial Waste
Hydrocracking for Naphtha
Agenda 1. Composition & Molecular Types
Refinery Processes Muhammad Fahad Ansari.
Energy (TKK-2129) 14/15 Academic Year Instructor: Rama Oktavian Office Hr.: M - F.13-15, oktavianrama.lecture.ub.ac.id.
Organic Chemistry Carbon Based
The Oil Industry.
C1a 3 Crude oil Burning fuels and cleaner fuels. Learning objectives Understand what is produced when fuels burn Understand what is produced when fuels.
The Plan Section 9.5 Crude Oil Refining Section 9.6 (very brief) on Combustion Review (if time)
Quality of Distillates From Recycle Coking Mohamed Shakir Japanwala Department of Chemical & Materials Eng., University of Alberta.
Fluid Catalytic Cracking A.Meenakshisundaram Chennai Petroleum Corporation Limited.
VISHWAKARMA GOVT. ENGG. COLLEGE TOPIC : DISTILLATION OF PETROLEUM SUPERVISED BY : K.K.GURJAR.
R E F I N I N G F U N D A M E N T A L S.
Submitted by: Akhilesh Pathak B.Tech(CH) ( )
Crude oil.
Distillation and Cracking
The oil industry Wan Chi Chao (Jessie) 12F.
Petroleum Refining Process
Conversion Process: Catalytic cracking Hydrocracking Thermal cracking
Click to edit Master title style Click to edit Master subtitle style.
Crude Oil Refining & Upgrading By: Faiz Ahmed - F16CH07 Pirbhat Nadir - F16CH06 Abdul Rehman - F16CH05.
Introduction to Petroleum Refinery
Environmental Aspects
Crude oil Treatment process
Petroleum Refining Process
Petroleum and Gas Processing(TKK-2136)
Hydrocracking.
Gasoline Manufacturing Processes
Conversion Processes: Cracking
The refining process Cracking Reforming Alkylation Polymerisation
Conversion Processes: Cracking
Catalytic Reforming Catalytic Reforming
Crude oil Treatment process
Hydrocracking.
Crude oil Treatment process
In this section we shall talk about: Refinery Configurations
Conversion Processes: Cracking
Chapter Eight: Gasoline Manufacturing Processes
Chapter Seven: Solvent Deasphalting and Thermal Cracking (Bottom of the Barrel) Processes.
Introduction to Petrochemical Processes
Hydrocracking.
Cracking and related refinery processes
Petroleum and Gas Processing(TKK-2136)
Conversion Processes: Cracking
Conversion Processes: Cracking
Presentation transcript:

Crude oil Treatment process Hydrotreatment Sulfur recovery Amine recovery

Hydrotreating A number of contaminants are found in crude oil. As the fractions travel through the refinery processing units, these impurities can damage the equipment, the catalysts and the quality of the products. There are also legal limits on the contents of some impurities, like sulphur, in products. Hydrotreating is one way of removing many of the contaminants from many of the intermediate or final products. In the hydrotreating process, the entering feedstock is mixed with hydrogen and heated to 300 – 380 oC. The oil combined with the hydrogen then enters a reactor loaded with a catalyst which promotes several reactions: Hydrogen combines with sulphur to form hydrogen sulphide (H2S). Nitrogen compounds are converted to ammonia. Any metals contained in the oil are deposited on the catalyst. Some of the olefins, aromatics or naphthenes become saturated with hydrogen to become paraffins and some cracking takes place, causing the creation of some methane, ethane, propane and butanes. 2

Hydrotreating 3

Hydrotreatment Remove contaminants from many of the intermediate or final products. Feedstock is mixed with hydrogen and heated to 300 - 380oC. The oil combined with the hydrogen then enters a reactor loaded with a catalyst which promotes several reactions: - Hydrogen combines with sulphur to form hydrogen sulphide (H2S) - Nitrogen compounds are converted to ammonia - Metals contained in the oil are deposited on the catalyst - Some of the olefins, aromatics or naphthenes become saturated with hydrogen to become paraffins - Some cracking takes place, creating methane, ethane, propane and butanes.

Hydrotreatment Remove: contaminants such as sulfur, nitrogen, condensed ring aromatics, or metals Feedstocks: range from naphtha, solvents, distillate fuels, residual fuels, vacuum residuum Product: mainly used as environmentally acceptable clean fuels.

Hydrotreater GTC Technology

Feedstock - treatment Residual fuels: Hydro-desulfurization (HDS) since the sole object is sulfur removal. Other than residual fuels :Hydrofining. improve the odor, color, stability, combustion characteristics, removes sulfur, nitrogen and other nonhydrocarbon In the catalytic cracking feed stocks: Hydrofining significantly improves cracking quality. Carbon yield is reduced, gasoline yield is increased The need for low sulfur residual fuel oils to alleviate the air pollution problem has led to the development of the required hydrotreating technology.

Difference between Hydrotreating and hydrocracking Hydrotreating and hydrocracking both can be called as Hydroprocessing

Naphtha Hydrotreating Objectives Sulphur Reduced to less than 0.5 wt ppm. Nitrogen Metals Reduced to ppm levels. Oxygen/Water Reduced to less than 1 wt ppm Olefins & di-olefins Saturated to avoid exchanger fouling and reactor coking

Diesel Hydrotreating Objectives Sulphur Reduced to between 0.2 - 0.02 wt%   Nitrogen - Reduced as much as possible  Cetane - An improvement of 1-3 cetane numbers   Aromatics/polyaromatics   Stability - Olefins are saturated.

Guard Reactor

Increasing Difficulty Desulfurization Increasing Difficulty

Denitrogenation More complex reaction

Oxygen Removal

Olefin Saturation Very rapid and exothermic reaction

Aromatic Saturation

Hydrotreater BP-UK