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Low-temperature crude benzene hydrogenation process

A crude benzene and low temperature technology, applied in the field of crude benzene low temperature hydrogenation process, can solve the problems of low added value, large loss of aromatic compounds, environmental pollution, etc., and achieve the effect of improving processing quality and reducing processing technology.

Inactive Publication Date: 2021-06-11
山东汇能新材料科技股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In the crude benzene hydrogenation process, the crude benzene needs to be pre-hydrogenated to remove diolefins, styrene and other substances before it can undergo deep desulfurization, denitrogenation and other reactions. During the processing process, the loss of aromatic compounds is large, and the by-product waste acid tar There is still no effective treatment method for residues and residues, which causes environmental pollution. The quality of the final product is quite different from that of petroleum-grade products. There are relatively large limitations in use, low added value, and relatively poor economic benefits. There are many deficiencies in the process, not only the waste of raw materials, so we propose a crude benzene low-temperature hydrogenation process to solve the above problems

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] A kind of crude benzene low-temperature hydrogenation process is proposed in this embodiment, comprising the following steps:

[0023] S1: Preliminary distillation: the crude benzene raw material enters the distillation mechanism after being filtered, and the crude benzene component is separated at the top of the distillation mechanism;

[0024] S2: liquid-phase catalytic prehydrogenation: the crude benzene component in S1 is mixed with hydrogen and heated to 80°C under the condition of Co-Mo as catalyst and hydrogen oil to obtain the first product;

[0025] S3: gas-phase catalytic prehydrogenation step: heating the first product obtained by liquid-phase catalytic pre-hydrogenation in S2 to 160°C under the condition of NiW as catalyst and hydrogen oil to obtain the second product;

[0026] S4: The main catalytic hydrogenation reaction, the second product obtained in S3 is subjected to the main catalytic hydrogenation reaction, the reaction temperature of the main cataly...

Embodiment 2

[0037] A kind of crude benzene low-temperature hydrogenation process is proposed in this embodiment, comprising the following steps:

[0038] S1: Preliminary distillation: the crude benzene raw material enters the distillation mechanism after being filtered, and the crude benzene component is separated at the top of the distillation mechanism;

[0039] S2: liquid-phase catalytic prehydrogenation: the crude benzene component in S1 is mixed with hydrogen and heated to 90°C under the condition of Co-Mo as catalyst and hydrogen oil to obtain the first product;

[0040] S3: gas-phase catalytic prehydrogenation step: heating the first product obtained by liquid-phase catalytic pre-hydrogenation in S2 to 170°C under the condition of NiW as catalyst and hydrogen oil to obtain the second product;

[0041] S4: The main catalytic hydrogenation reaction, the second product obtained in S3 is subjected to the main catalytic hydrogenation reaction, the reaction temperature of the main cataly...

Embodiment 3

[0052] A kind of crude benzene low-temperature hydrogenation process is proposed in this embodiment, comprising the following steps:

[0053] S1: Preliminary distillation: the crude benzene raw material enters the distillation mechanism after being filtered, and the crude benzene component is separated at the top of the distillation mechanism;

[0054] S2: liquid-phase catalytic prehydrogenation: the crude benzene component in S1 is mixed with hydrogen and heated to 100°C under the condition of Co-Mo as catalyst and hydrogen oil to obtain the first product;

[0055] S3: gas-phase catalytic prehydrogenation step: heating the first product obtained by liquid-phase catalytic pre-hydrogenation in S2 to 180°C under the condition of NiW as catalyst and hydrogen oil to obtain the second product;

[0056] S4: The main catalytic hydrogenation reaction, the second product obtained in S3 is subjected to the main catalytic hydrogenation reaction, the reaction temperature of the main catal...

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Abstract

The invention discloses a low-temperature crude benzene hydrogenation process which comprises the following steps: S1, primary distillation: filtering a raw material of crude benzene, feeding the filtered raw material into a distillation mechanism, and separating a crude benzene component at the top of the distillation mechanism; S2, liquid-phase catalytic pre-hydrogenation: mixing the crude benzene component in the S1 with hydrogen, and conducting heating to 80-140 DEG C under the condition of Co-Mo serving as a catalyst and hydrogen oil, so as to obtain a first product; and S3, gas-phase catalytic pre-hydrogenation: heating the first product obtained by liquid-phase catalytic pre-hydrogenation in the S2 to 160-210 DEG C under the condition of NiW serving as a catalyst and hydrogen oil to obtain a second product. According to the process, unsaturated olefin in crude benzene is hydrogenated to prepare saturated hydrocarbon at a low reaction temperature. The condition that unsaturated hydrocarbon which is contained in the crude benzene and is easily polymerized at high temperature is polymerized and coked at high temperature to block a system in a subsequent process is avoided, the processing technology is reduced, and the processing quality is improved.

Description

technical field [0001] The invention relates to the technical field of hydrogenation process, in particular to a low-temperature hydrogenation process of crude benzene. Background technique [0002] With the development of the organic synthesis industry, the demand for industrial pure benzene is increasing, and the increasing shortage of petroleum resources has seriously restricted the output of petroleum crude benzene. As another source of pure benzene, coking crude benzene is becoming more and more important. However, due to the improvement of environmental quality requirements, countries around the world have increasingly strict restrictions on the amount of sulfur in oil products. Coking crude benzene is a light fraction recovered from coal coking crude gas, the main components are benzene, toluene, xylene, and a small amount of non-aromatic components. In its purification process, the most critical thing is the removal of organic sulfur and coking substances. [0003...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C7/163C07C7/04C07C7/10C07C15/04C07C15/06C07C15/08C10G45/38C10G45/34C10G45/08C10G45/04
CPCC07C7/163C07C7/04C07C7/10C10G45/38C10G45/34C10G45/08C10G45/04C10G2300/202C10G2300/201C10G2300/1096C10G2400/30C07C15/04C07C15/06C07C15/08
Inventor 王明印马忠洋韩宗鑫
Owner 山东汇能新材料科技股份有限公司
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