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Preparation method and catalytic method of catalyst for converting phenolic compound in coal tar

A technology of phenolic compounds and catalysts, which is applied in the field of catalyst preparation and catalysis, can solve the problems of expensive, deficient, large-scale preparation and storage of non-supported transition metal sulfide catalysts, and achieve good stability and good pore size distribution Effect

Active Publication Date: 2020-02-07
XI'AN PETROLEUM UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among all kinds of catalysts, for coal tar phenolic fractions containing sulfur, nitrogen, metal impurities and high oxygen content, the reduced metal catalysts are easily poisoned and expensive (for noble metals), and the phosphides, carbides and nitrides are easily poisoned and The stability is still lacking, and the large-scale preparation and storage of non-supported transition metal sulfide catalysts are difficult, and their formability and mechanical strength are also facing great challenges when used in fixed beds

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] A catalyst for converting phenolic compounds in coal tar, consisting of an active component, a carrier and an auxiliary agent, characterized in that the active component is cobalt oxide and molybdenum oxide, and the carrier is monoclinic zirconia trioxide Aluminum composite, the auxiliary agent is phosphorus, wherein the active components account for 2.35wt% to 5.54wt% and 0.62wt% to 2.84wt% of the catalyst weight in terms of molybdenum and cobalt, and the auxiliary agent phosphorus accounts for 1.0wt%-2.0wt% of the total weight of the catalyst, and the rest is carrier.

[0023] Further, the specific surface area of ​​the monoclinic zirconia is 60-90m 2 / g, the pore volume is 0.140-0.20cm 3 / g, the average pore diameter is 8-13nm; the precursor of the aluminum oxide has a specific surface area of ​​350-450m 2 / g, the pore volume is 0.6-1.0cm 3 / g, pseudo-boehmite with an average pore size of 6-8nm.

[0024] A preparation method of a catalyst for converting phenolic ...

Embodiment 2

[0034] Catalysts were prepared as follows:

[0035] S1, weigh a certain amount of zirconium oxychloride octahydrate (ZrOCl 2 ·8H 2 (2) and urea, respectively dissolved in distilled water, then slowly add the urea solution dropwise to the octahydrate zirconium oxychloride solution under stirring, fully stir the solution to mix evenly, then move the mixed solution to the inner lining PPL (para-position poly Benzene) in a stainless steel reaction kettle, heat up to 80°C for 2 hours, continue to heat up to 200°C for 8 hours, cool to room temperature, and wash the product repeatedly with distilled water until no Cl is detected. - and dried at 60°C for 8 hours to obtain ZrO 2 , followed by the alumina precursor pseudoboehmite, ZrO 2 Mix evenly with extrusion aid squash gum to obtain a mixture, then add distilled water to the mixture at a water-to-powder ratio of 0.6:1, knead in a kneader for 80 minutes, put it into an extruder for extrusion molding, and then dry at 15°C 6h, afte...

Embodiment 3

[0044] Catalysts were prepared as follows:

[0045] S1, weigh a certain amount of zirconium oxychloride octahydrate (ZrOCl 2 ·8H 2 (2) and urea, respectively dissolved in distilled water, then slowly add the urea solution dropwise to the octahydrate zirconium oxychloride solution under stirring, fully stir the solution to mix evenly, then move the mixed solution to the inner lining PPL (para-position poly Benzene) in a stainless steel reaction kettle, heat up to 80°C for 2 hours, continue to heat up to 200°C for 8 hours, cool to room temperature, and wash the product repeatedly with distilled water until no Cl is detected. - and dried at 60°C for 8 hours to obtain ZrO 2 , followed by the alumina precursor pseudoboehmite, ZrO 2 Mix evenly with extrusion aid squash gum to obtain a mixture, then add distilled water to the mixture at a water-to-powder ratio of 0.7:1, knead in a kneader for 90 minutes, put it into an extruder for extrusion molding, and then dry at 25°C After dr...

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Abstract

The invention discloses a preparation method and a catalytic method of a catalyst for converting a phenolic compound in coal tar. The catalyst consists of active components, a carrier and an aid, wherein the active components are cobalt oxide and molybdenum oxide; the carrier is a composition of monoclinic zirconium oxide and aluminum oxide; the aid is phosphorus; the active components account for2.35 to 5.54 percent and 0.62 to 2.84 percent of the total weight of the catalyst correspondingly based on molybdenum and cobalt elementary substances; the aid accounts for 1.0 to 2.0 percent of thetotal weight of the catalyst based on the elementary substance; and the rest is the carrier. The preparation method comprises the steps of preparing the carrier and preparing the catalyst from the carrier and the active component solution. The catalytic method comprises the steps of performing presulfurization on the catalyst, activating the catalyst and performing catalytic reaction on the phenolic compound by the catalyst. The phenolic compound can be selectively converted into high-valued aromatic hydrocarbon, the deoxygenation rate of the phenolic compound is close to 100 percent and the yield of the aromatic hydrocarbon can reach to 87.72 percent.

Description

technical field [0001] The invention relates to the technical field of coal tar deep processing, in particular to a preparation and a catalytic method of a catalyst for converting phenolic compounds in coal tar. Background technique [0002] Coal tar is one of the main products of coal thermal processing, which is a black or dark brown viscous liquid with a pungent odor. Coal tar can be divided into three types according to the carbonization temperature: high temperature (900-1000°C), medium temperature (700-900°C) and low temperature (500-700°C). [0003] High-temperature coal tar is black, dense, and contains a large amount of pitch. It is a complex mixture of aromatic compounds. It has less alkyl hydrocarbon content, more high-boiling point substances, and good thermal stability. Therefore, the main processing method of high-temperature coal tar in my country is Separating and refining to obtain a variety of chemical raw materials, providing very important basic raw mater...

Claims

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Application Information

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IPC IPC(8): B01J27/19C07C1/20C07C15/02C10C1/20
CPCB01J27/19C07C1/20C10C1/20C07C15/02Y02P20/584
Inventor 邱泽刚李志勤尹婵娟
Owner XI'AN PETROLEUM UNIVERSITY