Light aromatic hydrocarbon hydrogenation pre-hydrogenation process

A pre-hydrogenation and light aromatics technology, applied in the field of chemical processing, can solve problems such as deterioration of oil properties and product failure to meet requirements, and achieve the effects of reduced olefin content, long operating cycle, and complete reaction

Inactive Publication Date: 2019-01-11
DAQING E SHINE CHEM CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] Cracking of light aromatic hydrocarbon aromatic components contains more impurities such as sulfides, nitrides, oxides and some unsaturated

Method used

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Examples

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Embodiment Construction

[0012] Below in conjunction with example the present invention will be further described:

[0013] A hydrogenation and pre-hydrogenation process for light aromatics, the process comprises the following steps:

[0014] (1) After de-weighting, the de-heavy product oil comes from the tank area and is pressurized to 2.1MPa by the hydrogenation feed pump P2101A / B, and then mixed with the pre-hydrogenation reaction circulating fluid and new hydrogen to enter the pre-hydrogenation reaction After the inlet distributor at the bottom of R2103, it passes through the catalyst bed from bottom to top to carry out the selective hydrogenation reaction of dienes, styrene and a small amount of monoolefins. The reaction is a low temperature liquid phase hydrogenation reaction, and the reaction process is an exothermic reaction. Discharge from the top of the pre-hydrogenation reactor to the main hydrogenation reaction; the liquid-phase circulating material is drawn from the side of the pre-hydrog...

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Abstract

The invention provides a light aromatic hydrocarbon hydrogenation pre-hydrogenation process, wherein the process includes the following steps: a deweighted product oil after deweighting comes from a tank area, is pressurized to 2.1 MPa by a hydrogenation feed pump and is mixed with a pre-hydrogenation reaction circulating liquid and new hydrogen, then the mixture enters an inlet distributor of thebottom of a pre-hydrogenation reactor, and then passes through a catalyst bed layer from bottom to top; selective hydrogenation reaction of diene, styrene and a small amount of monoolefins is preformed; a liquid phase circulating material extracted from the side face of the pre-hydrogenation reactor is pressurized by a pre-hydrogenation circulating pump, is cooled by a pre-hydrogenation circulating cooler, is mixed with new hydrogen and raw materials, enters an inlet of the pre-hydrogenation reactor again, is circulated, is discharged from the top of the pre-hydrogenation reactor and is subjected to main hydrogenation reaction. Through the process, the olefin content of the pre-hydrogenated oil product of the process is obviously reduced, the bromine number is also obviously reduced, coking of the main hydrogenation reaction is effectively prevented, the main hydrogenation reaction with high catalytic activity is completed, and the operation cycle of the device is long.

Description

technical field [0001] The process relates to the technical field of chemical processing, in particular to a process for hydrogenation and prehydrogenation of light aromatics. Background technique [0002] The cracking of light aromatic hydrocarbons contains more impurities such as sulfides, nitrides, oxides and some unsaturated hydrocarbons. The existence of these substances will deteriorate the properties of oil products, so that the products cannot meet the requirements. It is necessary to saturate these unsaturated hydrocarbons, remove sulfur, nitrogen, and oxygen compound impurities, and improve the quality of the product at the same time. Before removing sulfur, nitrogen, and oxygen compound impurities, a pre-hydrogenation reaction is carried out, which saturates the diene and prevents coking in the main hydrogenation reaction. Invention content: [0003] In order to solve the technical problems existing in the background technology, the present invention proposes a...

Claims

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Application Information

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IPC IPC(8): C10G45/36C10G45/48
CPCC10G45/36C10G45/48
Inventor 刘潇
Owner DAQING E SHINE CHEM CO LTD
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