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A kind of recovery process and device of benzene partial hydrogenation catalyst

A technology of hydrogenation catalyst and recovery device, which is applied in chemical recovery, catalyst activation/preparation, physical/chemical process catalyst, etc. It can solve the problems of secondary environmental pollution, scaling and corrosion, and high environmental pressure, and reduce flushing Use of water, prevention of poisoning, effect of reducing loss

Active Publication Date: 2022-05-13
河北美邦膜科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to provide a new recovery process and device for benzene partial hydrogenation catalyst to solve the problems of high environmental protection pressure, catalyst loss and high production cost in the existing process, so as to reduce the loss of expensive catalyst and reduce production cost and to prevent fouling and corrosion of equipment caused by catalyst slurry entering subsequent processes, and to avoid secondary environmental pollution caused by catalyst slurry entering wastewater

Method used

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  • A kind of recovery process and device of benzene partial hydrogenation catalyst
  • A kind of recovery process and device of benzene partial hydrogenation catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] Process of the present invention such as figure 1 As shown, the specific steps are as follows:

[0050] a) Sedimentation separation

[0051] Send the mixture of product oil and catalyst slurry from the hydrogenation reaction unit at a temperature of 130°C and a pressure of 4.9 MPa into the settling tank 1, and separate by gravity sedimentation. The catalyst slurry with high specific gravity settles to the lower part, and the product oil with low specific gravity Separation to the upper part; the catalyst slurry is sent to the hydrogenation reaction unit of the original production process to continue to participate in the reaction, and the generated oil is depressurized by the flow-limiting orifice 4 and then sent to the flash tank 2.

[0052] Among them, the generated oil mainly contains solutions of cyclohexene, cyclohexane and benzene, as well as a small amount of dissolved gases (hydrogen, methane, nitrogen), catalyst and water; the catalyst slurry is composed of ru...

Embodiment 2

[0070] a) Sedimentation separation

[0071] Send the mixture of product oil and catalyst slurry from the hydrogenation reaction unit at a temperature of 140°C and a pressure of 5.2 MPa into the settling tank 1, and separate by gravity sedimentation. The catalyst slurry with high specific gravity settles to the lower part, and the product oil with low specific gravity Separation to the upper part, the catalyst slurry is sent to the hydrogenation reaction unit of the original production process to continue to participate in the reaction, and the generated oil is depressurized by the flow-limiting orifice 4 and then sent to the flash tank 2.

[0072] Among them, the generated oil is a solution mainly containing cyclohexene, cyclohexane and benzene, and contains a small amount of dissolved gas, catalyst and water, and the dissolved gas is a mixture of hydrogen, methane and nitrogen; the catalyst slurry is made of ruthenium series noble metal (catalyst) + Zirconia (dispersant) + Zi...

Embodiment 3

[0089] The difference between Example 3 and Example 1 is that the membrane element used in the special membrane separation is a ceramic membrane with a filtration precision of 10 nm. The final catalyst recovery was 83%.

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Abstract

The invention discloses a new process and device for recovering benzene partial hydrogenation catalyst. The process is to sequentially undergo sedimentation separation, degassing, oil-water separation, and catalyst sedimentation of the mixed solution of the catalyst slurry from the hydrogenation reaction unit and the generated oil. Separation, membrane separation and other processes, recover the water and catalyst in the mixed solution, the catalyst is reused in the original production process, part of the water is used as flushing water for the flash tank and its feed, and the tank bottom discharge pipeline, and the other part is reused in the in the original production process. The process and device of the present invention use oil-water separators and special membrane separators for the recovery of hydrogenation catalysts, and improve related equipment and pipeline materials to reduce the loss of catalysts and avoid catalyst poisoning. The 100,000 tons / year scale The cyclohexanol plant saves tens of millions of yuan in annual production costs. In addition, the recycling of flushing water can reduce the discharge of wastewater by more than 98%, and the economic and environmental benefits are remarkable.

Description

technical field [0001] The invention relates to the recovery of a benzene partial hydrogenation catalyst, in particular to a new recovery process and device for a benzene partial hydrogenation catalyst. Background technique [0002] Cyclohexene is an important organic synthesis intermediate and chemical raw material, mainly used in organic synthesis, oil extraction and as a solvent, in medicine, pesticides, dyes, detergents, explosives, feed additives, polyester and other fine The production of chemicals has broad application prospects; in addition, cyclohexanone and adipic acid, the deep-processing products of cyclohexene, are widely used intermediates in the synthesis of polyamide fibers. [0003] So far, the process of preparing cyclohexene by partial hydrogenation of benzene is the best method for industrial large-scale production of cyclohexene. The process flow is: benzene, hydrogen and catalyst slurry are sent to the first hydrogenation reactor and the second hydroge...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C5/11C07C13/20B01J27/053B01J37/00B01D3/06B01D17/02B01D19/00C02F1/40C02F1/44
CPCC07C5/11B01J27/053B01J37/009B01D19/00B01D3/06B01D17/02C02F1/40C02F1/44C07C2601/10C07C13/20Y02P20/584Y02P20/52
Inventor 张玉新付海杰张玉妹王素霞金作宏
Owner 河北美邦膜科技有限公司
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