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Direct Catalytic Cracking of Crude Oil Using Temperature Gradient Process

一种催化裂化、温度梯度的技术,应用在催化裂化、裂化、烃裂化制烃等方向,能够解决催化剂污染、催化剂失活、难以使用等问题,达到避免资金费用的效果

Active Publication Date: 2016-05-25
SAUDI ARABIAN OIL CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are two main challenging issues for the cracking of hydrocarbon feeds in the full boiling point range, which prevent the application of these two processes: due to the formation of coke and poisons from heavy metals and Catalyst contamination, leading to rapid catalyst deactivation, making it difficult to use catalyst-based systems
The wide temperature range over which "crackable" crude oil groups crack leads to problems with process control and long-term system integrity (i.e., temperature / time based stress failure) for purely thermal processes

Method used

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  • Direct Catalytic Cracking of Crude Oil Using Temperature Gradient Process
  • Direct Catalytic Cracking of Crude Oil Using Temperature Gradient Process

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Embodiment Construction

[0024] The specification includes a summary of the invention, a brief description of the drawings and a detailed description of the preferred embodiments, and the specification and appended claims refer to particular features (including process or method steps) of the invention. Those skilled in the art will understand that the present invention includes all possible combinations and uses of the specific features described in the specification. Those skilled in the art should understand that the present invention is not limited to the description of the embodiments given in the specification, nor is the present invention limited by the description of the embodiments given in the specification. The inventive subject matter is not limited except in the spirit of the specification and appended claims.

[0025] Those skilled in the art will also understand that the terminology used to describe particular embodiments does not limit the scope or breadth of the invention. In interpr...

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Abstract

A direct catalytic cracking system for converting undistilled and unfractionated hydrocarbon material into hydrocarbon products comprising light olefins and C6-8 aromatics. The direct catalytic cracking system includes a moving catalyst bed reactor having one or more catalytic reaction zones and configured to be able to adjust its internal temperature. The direct catalytic cracking system also includes a catalyst regeneration system. A method of converting undistilled and unfractionated hydrocarbon material to hydrocarbon products utilizing the direct catalytic cracking system. The method includes the step of introducing a moving bed reactor feed comprising steam and undistilled and unfractionated hydrocarbon material. The method further comprises the steps of introducing a direct cracking catalyst into a catalytic reaction zone of a moving catalyst bed reactor, operating the direct catalytic cracking system to convert hydrocarbon material to product hydrocarbons in the presence of the direct cracking catalyst, and extracting from The moving catalyst bed reactor discharges product hydrocarbons.

Description

technical field [0001] The field of the invention relates to methods and systems for converting undistilled and unfractionated hydrocarbon material into product hydrocarbons. More specifically, the field of the invention relates to systems and methods for converting hydrocarbon material, particularly undistilled and unfractionated crude oil, into hydrocarbon products comprising a mixture of light olefins and C6-8 aromatics . Background technique [0002] With the growing global awareness related to our use of non-renewable resources (including crude oil, gas condensate and natural gas) as the basis for making transportation fuels, the long-term upward trend in the use of gasoline and diesel fuel may finally stabilize, even in the next decades to come, even taking into account the increase in global population. However, the overall demand for petrochemical products or chemicals partially derived from hydrocarbon materials will continue to rise. Human society and its contin...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G3/00C10G49/00C10G51/02C10G11/16C10G11/20
CPCC10G11/16C10G11/20C10G47/02C10G51/026C10G65/10C10G3/55C10G49/007Y02P30/20C07C4/06
Inventor W·徐易卜拉欣·阿巴
Owner SAUDI ARABIAN OIL CO
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