Poor-quality raw material hydrocracking method

A technology for hydrocracking and low-quality raw oil, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment. It can solve the problems of poor crude oil quality, reduced processing capacity, and shortened operation cycle, etc., and achieves the improvement of hydrogen partial pressure. , Prolong the operation cycle, reduce the effect of reaction temperature

Active Publication Date: 2015-05-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] At present, the quality of crude oil is deteriorating, the impurity content is increasing, and the development of crude oil vacuum deep drawing and other unconventional energy sources makes the impurity content of hydrocracking raw materials higher and higher, especially the nitrogen content of certain hydrocracking raw materials. However, when the existing hydrocracking method deals with the hydrocracking feedstock with high nitrogen content, higher reaction temperature or lower operating space velocity is required, the processing capacity of the unit will decrease, energy consumption will increase, and the operation cycle will be shortened

Method used

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  • Poor-quality raw material hydrocracking method

Examples

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Effect test

Embodiment 1

[0041] use figure 1 In the process flow shown, the hydrocracking in the third stage is a one-way pass flow. The first stage is loaded with catalyst A, and the second stage is filled with catalyst B. The upper part of the refining reaction zone of the second stage adopts gas-liquid parallel flow reaction, and the lower part adopts gas-liquid countercurrent reaction, and the catalyst loading volume ratio of the parallel flow section and the countercurrent section is 1:1.

Embodiment 2

[0043] Both the first section and the second section are filled with hydrotreating catalyst B, and the others are the same as in Example 1.

Embodiment 3

[0057] The main process is as figure 1 As shown, the >370°C distillate part is recycled to the inlet of the second-stage hydrotreating reactor, and the circulation amount is 25% of the tail oil. Control the denitrification rate of the first stage reaction zone to 75wt%. The test results are listed in Table 3.

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Abstract

The present invention discloses a poor-quality raw material hydrocracking method. According to the method, a poor-quality raw material is firstly subjected to a first-stage hydrorefining reaction, and the reaction effluent is separated; and the liquid enters a second-stage refining stage to carry out a deep denitrogenation and aromatic hydrocarbon saturation reaction, a gas-liquid co-current flow process and a gas-liquid counter flow process are concurrently adopted in the second stage, the refining generated oil obtained in the second stage and hydrogen gas are mixed and then enter a third-stage reaction zone to carry out a hydrocracking reaction. With the method of the present invention, the nitrogen-containing impurities in the poor-quality raw material can be subjected to hydrotreating under the relatively mild condition so as to make the poor-quality raw material meet the hydrocracking feeding requirement, such that the hydrocracking raw material source is broadened; and the hydrorefining temperature is substantially reduced so as to increase the operation period of the device and process the poor-quality raw material, or increase the processing capacity of the device in the same operation period.

Description

technical field [0001] The invention discloses a hydrocracking method, in particular to a hydrocracking method for processing nitrogen-containing inferior raw materials. Background technique [0002] With the rapid development of my country's economy, the oil processing capacity has grown rapidly. At the same time, domestic hydrocracking technology has also obtained large-scale industrial applications. By the end of 2011, there were more than 40 sets of hydrocracking units in operation in my country, with a total processing capacity of more than 50.0Mt / a, and the processing capacity leapt to the top of the world. second. In addition, due to the year-by-year deterioration of the quality of domestic crude oil, the substantial increase in the processing volume of imported high-sulfur crude oil, the increasingly stringent requirements for environmental protection on the refining process and the quality of petroleum products, and the increasing market demand for clean fuel oil an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G65/10
CPCC10G67/02C10G2300/202
Inventor 白振民王凤来曹均丰王平
Owner CHINA PETROLEUM & CHEM CORP
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