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Shale oil processing method

A processing method and technology for shale oil, applied in the petroleum industry, hydrotreating process, processing hydrocarbon oil, etc., can solve the problems of complex process flow, many hydrogenation processes, and high operating costs, and achieve simple process flow and extended operation. cycle, the effect of improving the removal rate

Active Publication Date: 2012-05-23
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of this method are: complex process flow and high investment; at the same time, due to the use of hydrochloric acid to produce acid slag, which pollutes the environment, it is necessary to use acid-resistant materials
The disadvantages of this method are: too many hydrogenation processes, high hydrogen consumption, high operating costs, and high construction investment
Its disadvantages are: the use of two-stage all-hydrogen technology, high hydrogen consumption, high operating costs, high construction investment; and the fluidized bed technology is not mature enough

Method used

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Embodiment 1

[0031] use figure 1 In the process flow shown, the raw material oil used is a mixed oil of shale oil and VGO, wherein the shale oil accounts for 90wt% of the mixed raw material oil. Its properties are listed in Table 1. The catalyst used is a commercial catalyst of Sinopec Fushun Petrochemical Research Institute, and its properties are listed in Table 2. The cut-off temperature for shale oil fractionation is 320°C. The operating conditions of the two refining reactors are listed in Table 3, and the quality of the resulting products is listed in Table 4.

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Abstract

The invention discloses a shale oil processing method, comprising the steps of: segmenting shale oil into light components and heavy components, leading the heavy components and hydrogen to pass through an up-flow type hydrogenation reactor, leading an effluent and the light components as well as hydrogen to pass through a conventional hydrorefining reactor for reaction, and separating and distilling a hydrorefined effluent to obtain a light product. According to the method disclosed by the invention, the shale oil is firstly segmented into the light components and the heavy components so as to make metal, colloids and other easily precipitated impurities in the shale oil enter the heavy components, and then the characteristic of the up-flow type reactor is utilized to uniformly precipitate the colloids, the metal and other pollutants in a catalyst bed, so that the excessive increase of the pressure drop in the catalyst bed is effectively slowed down; a material flow in which most of impurities are removed is subjected to the conventional hydrorefining, on the one hand, sulfur, nitrogen and other impurities in the shale oil can be removed, on the other hand, the operating cycle of the hydrorefining catalyst can be prolonged, and thus, an ideal processing effect is achieved.

Description

technical field [0001] The invention relates to a processing method of shale oil, in particular to a combined process of shale oil fractionation and hydrofining. Background technique [0002] Shale oil is a liquid product obtained by thermal decomposition of kerogen in oil shale. In addition to a large amount of unsaturated hydrocarbons, shale oil also contains many non-hydrocarbon compounds such as sulfur, nitrogen and oxygen. Unsaturated hydrocarbons and non-hydrocarbon compounds in shale oil are the main reasons for the increase of oil colloid and the formation of sediment, resulting in poor stability and black color; in addition, shale oil often entrains some metals during upstream processing Impurities. Therefore, when producing light products from shale oil, it is necessary to remove non-hydrocarbon compounds, saturated olefins, and metals to ensure product quality. [0003] US4338186 discloses a method for processing shale oil. Firstly, the whole distillate shale oi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G67/00
Inventor 彭冲刘涛刘继华黄新露白振民王仲义
Owner CHINA PETROLEUM & CHEM CORP
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