Method for treating inferior oil product by combined process

A combined process, inferior technology, applied in the treatment of hydrocarbon oil, hydrotreating process, petroleum industry, etc., can solve problems such as complex operation

Active Publication Date: 2019-11-05
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

This method can prolong the stable operation period of the device, but the operation of this method is more complicated

Method used

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  • Method for treating inferior oil product by combined process
  • Method for treating inferior oil product by combined process
  • Method for treating inferior oil product by combined process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0085] according to figure 1 In the process flow, the hydrogenation pretreatment reaction zone includes a switchable first hydrogenation pretreatment reaction zone and a second hydrogenation pretreatment reaction zone, the first hydrogenation pretreatment reaction zone is provided with a reactor 1, and the second hydrogenation pretreatment reaction zone is provided with a reactor 1. A reactor 2 is arranged in the second hydrogenation pretreatment reaction zone, and the hydrogenation treatment reaction zone includes a reactor 3 and a reactor 4 arranged in series. According to the material flow direction, the reactor in the hydrogenation pretreatment reaction zone (only one hydrogenation pretreatment reaction zone is online during operation) is filled with catalyst A, catalyst B and catalyst C, and the loading volume ratio of each catalyst is 2:7 : 1. Catalyst B and Catalyst C are installed in the reactor 3 of the hydrotreating reaction zone, and the loading volume ratio of the...

Embodiment 2

[0091] according to figure 1 In the process flow, the hydrogenation pretreatment reaction zone includes a switchable first hydrogenation pretreatment reaction zone and a second hydrogenation pretreatment reaction zone, the first hydrogenation pretreatment reaction zone is provided with a reactor 1, and the second hydrogenation pretreatment reaction zone is provided with a reactor 1. A reactor 2 is arranged in the second hydrogenation pretreatment reaction zone, and the hydrogenation treatment reaction zone includes a reactor 3 and a reactor 4 arranged in series. According to the material flow direction, the reactor in the hydrogenation pretreatment reaction zone (only one hydrogenation pretreatment reaction zone is online during operation) is filled with catalyst A, catalyst B and catalyst C, and the loading volume ratio of each catalyst is 3:6 : 1. Catalyst B and catalyst C are housed in hydrotreating reaction zone reactor 3, and the loading volume ratio of two kinds of cata...

Embodiment 3

[0094] according to figure 1 In the process flow, the hydrogenation pretreatment reaction zone includes a switchable first hydrogenation pretreatment reaction zone and a second hydrogenation pretreatment reaction zone, the first hydrogenation pretreatment reaction zone is provided with a reactor 1, and the second hydrogenation pretreatment reaction zone is provided with a reactor 1. A reactor 2 is arranged in the second hydrogenation pretreatment reaction zone, and the hydrogenation treatment reaction zone includes a reactor 3 and a reactor 4 arranged in series. According to the material flow direction, the reactor in the hydrogenation pretreatment reaction zone (only one hydrogenation pretreatment reaction zone is online during operation) is filled with catalyst A, catalyst B and catalyst C, and the loading volume ratio of each catalyst is 4:5 : 1. Catalyst B and Catalyst C are installed in the reactor 3 of the hydroprocessing reaction zone, and the filling volume ratio of t...

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Abstract

The invention discloses a method for treating an inferior oil product by a combined process. The method comprises the following steps: allowing an inferior oil raw material and hydrogen to enter a mixer for saturated hydrogen dissolution, and allowing an obtained mixture to pass through a hydropretreating zone; and separating a reaction effluent, allowing a separated reaction effluent and catalytic-cracked circulating oil to enter a hydrotreating reaction zone, separating an obtained reaction effluent, allowing obtained hydrotreated residual oil to undergo a catalytic cracking reaction, allowing obtained circulating oil and/or an oil slurry to be circulated to a hydropretreating reaction zone, and allowing a part of obtained circulating oil to be circulated to the hydrotreating reaction zone; wherein the reaction temperature t1 of the hydropretreating reaction zone is higher than the reaction temperature t2 of the hydrotreating reaction zone. The method provided by the invention can increase the utilization rate of a main hydrotreating catalyst, prolongs the operation cycle of a combined device, and increases the operation efficiency of a device.

Description

technical field [0001] The invention relates to the field of petroleum refining, in particular to a method for treating heavy residue by adopting a combined process of residue oil hydrotreating and catalytic cracking. Background technique [0002] At present, the demand for light and medium oil products in the domestic and foreign oil product markets will continue to rise, while the demand for heavy oil products such as fuel oil will show a downward trend. In addition, due to the increasing pressure of environmental protection, countries have generally raised the quality standard requirements of petroleum products, especially gasoline and diesel products for vehicles. Under the above-mentioned market trend, the refining technology that can not only realize the lightening of heavy oil at a more economical and reasonable price, but also make the obtained products meet the increasingly stringent specifications of gasoline and diesel products has become a key technology develope...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G67/02
CPCC10G67/02
Inventor 吴锐刘涛韩照明黄新露吴长安
Owner CHINA PETROLEUM & CHEM CORP
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