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Residual oil hydrogenation treatment and catalytic cracking combined processing method

A catalytic cracking and residual oil hydrogenation technology, which is applied in the fields of hydrogenation treatment process, petroleum industry, and hydrocarbon oil treatment, can solve the problems of reduced total yield, high heat energy loss, increased investment cost, etc., and achieve the reduction of heat exchange equipment , Reduce equipment investment and improve utilization

Active Publication Date: 2014-05-21
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In addition, it is also necessary to set up a more sophisticated fractionation system to fractionate naphtha and diesel fractions, which increases investment costs; due to heat exchange in the process, heat energy loss is more; at the same time, both hydrotreating units and catalytic cracking units have diesel products, which are relatively The overall yield of gasoline and gas products will be reduced

Method used

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  • Residual oil hydrogenation treatment and catalytic cracking combined processing method
  • Residual oil hydrogenation treatment and catalytic cracking combined processing method
  • Residual oil hydrogenation treatment and catalytic cracking combined processing method

Examples

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Embodiment

[0033] In this example, the combined method of residue hydrotreating and catalytic cracking provided by the present invention is used, and the liquid phase product of hydrotreating is fractionated to obtain light components and heavy components, and the cutting point is 350° C. The light components are directly improved by catalytic cracking. The first-stage feed port at the bottom of the tube enters the reactor and contacts with the high-temperature regenerated catalyst. The heavy component is used as the second-stage feed of the riser, and enters the catalytic cracking riser reactor from the second-stage feed port; the second-stage feed port Above the first-stage feed, the height from the first feed port accounts for 1 / 10 of the total height of the riser; the catalytic cracking reaction effluent is separated into dry gas, liquefied gas, and gasoline fractions, and the fractions above diesel are no longer separated. After filtration, it is recycled back to the residual oil hyd...

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Abstract

The invention discloses a residual oil hydrogenation treatment and catalytic cracking combined processing method, which comprises: performing the hydrogenation reaction of a residual oil raw material in the presence of hydrogen and a hydrogenation treatment catalyst, and performing gas-liquid separation of efflux of hydrogenation reaction, wherein a gas phase is circularly used in a hydrogenation reaction, and a liquid phase is fractioned to form a light component and a heavy component; allowing a light component to enter a reactor from the bottom of a catalytic cracking riser reactor, allowing a heavy component to enter the reactor as secondary feed of the catalytic cracking riser reactor and performing a catalytic cracking reaction; and separating a dry gas, a liquefied gas and a gasoline fraction from efflux of a catalytic cracking reaction, wherein the fractions of diesel are not separated and enter a residual oil hydrogenation device after filtration. Compared with the prior art, the method can produce high-octane number gasoline and high-added-value liquefied gas to a maximum degree; meanwhile, the method can fully utilizes reaction heat and reduces production energy consumption.

Description

technical field [0001] The invention relates to a method for lightening residual oil, in particular to a process method for organically combining residual oil hydrotreating and catalytic cracking, and using residual oil as a raw material to mainly produce high-octane gasoline products. Background technique [0002] As crude oil becomes heavier and worse, more and more residual oil needs to be processed. The processing of heavy and residual oil should not only crack it into low-boiling products, such as naphtha, middle distillate oil and vacuum gas oil, etc., but also increase their hydrogen-to-carbon ratio, which requires decarbonization or hydrogenation method to achieve. Among them, decarbonization processes include coking, solvent deasphalting, heavy oil catalytic cracking, etc.; hydrogenation includes hydrocracking, hydrorefining, etc. The hydrogenation method can not only hydrogenate and convert residual oil, improve the yield of liquid products, but also remove heter...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G69/00
Inventor 蒋立敬张学萍胡长禄韩照明初人庆矫德卫
Owner CHINA PETROLEUM & CHEM CORP
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