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A kind of polyvalent metal oxide desulfurizer and preparation method thereof

A desulfurization agent and oxide technology, applied in chemical instruments and methods, separation methods, combustible gas purification, etc., can solve the problems of high operating conditions, economic losses, high costs, etc., to improve desulfurization efficiency, reduce particle size, and apply strong effect

Active Publication Date: 2021-02-02
LUOYANG NORMAL UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Hydrofining coal pyrolysis synthesis gas to produce high-quality chemical raw materials such as olefins, methanol, and ethylene glycol is an important measure for the sustainable development of coal chemical enterprises. Sulfides in coal pyrolysis synthesis gas such as CS 2 、CH 3 SH, COS and thiophene, etc., can easily poison and deactivate downstream catalysts, shorten catalyst life, and cause economic losses
Existing sulfide removal methods, such as hydrogenation, require higher hydrogen pressure to increase the hydrogen concentration on the surface of the catalyst (hydrogen pressure 2.5-15MPa), and transition metals such as Co-Mo, Ni-Mo, and Ni-W are used to support Chemical and physical changes such as hydrocarbon cracking, CO disproportionation, and carbon deposition are prone to occur on the surface of the catalyst, and the operating conditions are high (temperature 280-420°C). High, unsatisfactory desulfurization effect, etc.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] A multivalent metal oxide desulfurizer, which is composed of the following components in parts by mass: 15 parts of hematite ore, 15 parts of magnetite ore, 20 parts of soft manganese ore, 20 parts of red copper ore, and 10 parts of magnesium powder 10 parts of iron powder, 8 parts of anthracite, and 2 parts of silicon dioxide.

[0016] Further, the particle size of the hematite ore, the magnetite ore, the soft manganese ore and the red copper ore is 20-38 μm.

[0017] Further, the particle size of the magnesium powder and the iron powder are both 50-74 μm.

[0018] A method for preparing a polyvalent metal oxide desulfurizer, comprising the following preparation steps:

[0019] 1) Add the following materials in parts by mass in the ball mill tank in sequence: 15 parts of hematite ore, 15 parts of magnetite ore, 20 parts of soft manganese ore, 20 parts of red copper ore, 10 parts of magnesium powder, 10 parts of iron powder, 8 parts of anthracite, 2 parts of silicon d...

Embodiment 2

[0026] A multivalent metal oxide desulfurizer, which is composed of the following components in parts by mass: 15 parts of hematite ore, 15 parts of magnetite ore, 20 parts of soft manganese ore, 20 parts of red copper ore, and 10 parts of magnesium powder 10 parts of iron powder, 8 parts of anthracite, and 2 parts of silicon dioxide.

[0027] Further, the particle size of the hematite ore, the magnetite ore, the soft manganese ore and the red copper ore is 20-38 μm.

[0028] Further, the adsorbent undergoes the following pretreatment steps:

[0029] a) The following components in parts by mass: 15 parts of hematite ore, 15 parts of magnetite ore, 20 parts of soft manganese ore, 20 parts of red copper ore and 5 parts of solid sodium hydroxide are respectively added to the grinding ball Carry out ball milling in the machine, the ball milling time is 0.5~1h, then carry out centrifugal washing, filtering and drying;

[0030] b) putting each component obtained in step a) into a ...

Embodiment 3

[0039] A multivalent metal oxide desulfurizer, which is composed of the following components in parts by mass: 20 parts of hematite ore, 20 parts of magnetite ore, 15 parts of soft manganese ore, 20 parts of red copper ore, and 10 parts of magnesium powder 10 parts of iron powder, 8 parts of anthracite, and 2 parts of silicon dioxide.

[0040] Further, the particle size of the hematite ore, the magnetite ore, the soft manganese ore and the red copper ore is 20-38 μm.

[0041] Further, the particle size of the magnesium powder and the iron powder are both 50-74 μm.

[0042] Its preparation process is with embodiment 1.

[0043] The following tests were carried out on the multivalent metal oxide desulfurizer product:

[0044] Load the multivalent metal oxide desulfurizer into a continuously operating fixed-bed reactor, heat it to 150°C, and feed the normal-pressure coal pyrolysis synthesis gas with a gas space velocity of 1000 hours-1. The total sulfur concentration of coke o...

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Abstract

The invention provides a multivalent metal oxide desulfurizer, which is composed of the following components in parts by mass: 70-85 parts of adsorbent, 10-20 parts of reducing agent, and 5-10 parts of grinding aid; The adsorbent is composed of the following components in parts by mass: 15-20 parts of hematite ore, 15-20 parts of magnetite ore, 15-20 parts of soft manganese ore, 20-25 parts of red copper ore, the reducing agent It consists of the following components in parts by mass: 5-10 parts of magnesium powder, 5-10 parts of iron powder, and the grinding aid is composed of the following components in parts by mass: 4-8 parts of anthracite, silicon dioxide 1-2 parts, the raw material cost of the desulfurizer is low, the preparation method is simple, the use conditions are mild, and the desulfurization efficiency is high.

Description

technical field [0001] The invention belongs to the technical field of energy saving and environmental protection, and in particular relates to a multivalent metal oxide desulfurizer and a preparation method thereof. Background technique [0002] The reduction of overcapacity in the coal industry is an important part of the country's economic structural reform. Hydrofining coal pyrolysis synthesis gas to produce high-quality chemical raw materials such as olefins, methanol, and ethylene glycol is an important measure for the sustainable development of coal chemical enterprises. Sulfides in coal pyrolysis synthesis gas such as CS 2 、CH 3 SH, COS and thiophene, etc., can easily poison and deactivate downstream catalysts, shorten catalyst life, and cause economic losses. Existing sulfide removal methods, such as hydrogenation, require higher hydrogen pressure to increase the hydrogen concentration on the surface of the catalyst (hydrogen pressure 2.5-15MPa), and transition me...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10K1/20C10K1/32B01D53/48B01D53/81
CPCB01D53/48B01D53/81B01D2257/306B01D2257/308C10K1/004C10K1/20C10K1/32
Inventor 陈海鹏冯勋刘金强刘贵龙袁巍巍马宁宁王晔
Owner LUOYANG NORMAL UNIV
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