Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Preparation and use method of a coking benzene hydrodesulfurization catalyst

A technology for hydrodesulfurization and coking of benzene, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc. The effect of catalytic hydrogenation effect

Active Publication Date: 2016-09-07
BEIJING SJ ENVIRONMENTAL PROTECTION & NEW MATERIAL CO LTD
View PDF5 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] For this reason, the technical problem to be solved by the present invention lies in the problems of higher hydrogenation temperature and higher operating energy consumption required in the existing process for refining coked benzene by catalytic hydrotreating to achieve a higher thiophene removal rate, and then provide a A method for preparing a coked benzene hydrodesulfurization catalyst that has high dethiophene efficiency and can significantly reduce the hydrogenation reaction temperature; the present invention also provides a method for hydrotreating coked benzene using the hydrodesulfurization catalyst

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] This embodiment provides a method for preparing a coked benzene hydrodesulfurization catalyst, comprising the following steps:

[0042] S1. Weigh two portions of 30g aluminum oxide powder and 20g titanium dioxide powder, and mix them respectively to prepare a mixed powder carrier of aluminum oxide and titanium dioxide;

[0043] S2. Use the impregnation method to load active metal components on the mixed powder carrier: one part of the mixed powder carrier is immersed in a solution containing tungsten and a solution containing nickel successively twice, wherein the loading amount of tungsten is represented by oxidation The amount of nickel is 0.5g; the loading of nickel is 0.05g in terms of oxides, citric acid is added to the solution containing tungsten, and the amount of citric acid added is 0.25g to obtain an active catalyst carrier Z1;

[0044] Another part of the mixed powder carrier was immersed twice in a solution containing cobalt and in a solution containing mol...

Embodiment 2

[0059] This embodiment provides a method for preparing a coked benzene hydrodesulfurization catalyst, comprising the following steps:

[0060] S1. Weigh two portions of 42g aluminum oxide powder and 18g titanium dioxide powder, and mix them respectively to prepare a mixed powder carrier of aluminum oxide and titanium dioxide;

[0061] S2. Use the impregnation method to load active metal components on the mixed powder carrier: one part of the mixed powder carrier is immersed twice in a solution containing molybdenum and a solution containing nickel, wherein the loading amount of molybdenum is represented by oxidation The amount of nickel is 2.4g; the loading of nickel is 0.6g in terms of oxide, and citric acid is added in the solution containing molybdenum, and the amount of citric acid added is 2.4g to obtain an active catalyst carrier Z1;

[0062] Another part of the mixed powder carrier was immersed twice in the solution containing cobalt, in the solution containing molybden...

Embodiment 3

[0077] This embodiment provides a method for preparing a coked benzene hydrodesulfurization catalyst, comprising the following steps:

[0078] S1. Weigh two portions of 52g aluminum oxide powder and 13g titanium dioxide powder, and mix them respectively to prepare a mixed powder carrier of aluminum oxide and titanium dioxide;

[0079] S2. Use the impregnation method to load active metal components on the mixed powder carrier: one part of the mixed powder carrier is immersed in a solution containing tungsten and a solution containing nickel successively twice, wherein the loading amount of tungsten is represented by oxidation The amount of nickel is 1.95g; the loading of nickel is 1.95g in terms of oxide, and citric acid is added in the solution containing molybdenum, and the amount of citric acid added is 3.9g to obtain an active catalyst carrier Z1;

[0080] Another part of the mixed powder carrier was immersed twice successively in the solution containing cobalt, in the solu...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

A method for hydrodesulfurization of coked benzene, wherein the preparation process of the hydrodesulfurization catalyst used in the hydrodesulfurization reaction is: adding aluminum oxide and titanium dioxide mixed powder carriers to solutions containing molybdenum, nickel, cobalt, and tungsten active metal elements respectively The solution contains citric acid; the NaZSM‑5 molecular sieve is added to the solution containing copper and / or zinc for impregnation; after drying and roasting, the two are mixed, and the coking benzene is treated by a rectification tower before hydrodesulfurization , and then complete sulfur removal through pre-hydrogenation, main hydrogenation and inorganic sulfur removal processes. The NaZSM-5 molecular sieve loaded with active ingredients has a selective adsorption effect on thiophene; the mixed powder of aluminum oxide and titanium dioxide loaded with active metals has a good catalytic hydrogenation effect on thiophene, and the two synergistically work together to achieve a low reaction rate. Excellent removal effect can also be achieved at low temperature, citric acid can promote the formation of active phase, improve the hydrogenation activity of the catalyst and prolong the retention time of the catalyst activity.

Description

technical field [0001] The invention belongs to the technical field of hydrorefining of coked benzene, and in particular relates to a method for preparing and using a catalyst for hydrodesulfurization of coked benzene. Background technique [0002] Benzene is an important petrochemical basic raw material, which is widely used in the production of synthetic rubber, plastics, fibers, fuels, pesticides, and medicines, and can also be used as a solvent. One of the important symbols. At present, the raw material used to produce benzene and other chemical products is mainly petroleum benzene. With the development of economy, petroleum as a non-renewable resource is decreasing day by day, and coking benzene has gradually become an important raw material for benzene production. my country is rich in coking benzene resources. With the rapid development of the coal chemical industry, the proportion of coking benzene in the total benzene production has risen to nearly 30%. The high co...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/48C07C7/163C07C7/148C07C15/04
CPCY02P20/52
Inventor 王培崔永君任相坤黄国胜荣斌斌
Owner BEIJING SJ ENVIRONMENTAL PROTECTION & NEW MATERIAL CO LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products