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Catalyst for producing chlorine by catalytic oxidation of hydrogen chloride, preparation method and application thereof

A technology of catalytic oxidation and hydrogen chloride, applied in the direction of preparation of chloride, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc., can solve problems such as catalyst corrosion, catalyst bed blockage, activity decline, etc.

Active Publication Date: 2020-10-30
SHANGHAI CHLOR ALKALI CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

If the raw material hydrogen chloride contains impurities such as phosgene, if the raw material hydrogen chloride is not pretreated, or the impurity phosgene in the hydrogen chloride is not cleaned up despite the pretreatment, when the catalyst prepared by using alumina as the carrier is completely As the reaction progresses, it will cause corrosion of the catalyst and lead to blockage of the catalyst bed.
When fully using silica as a carrier, the activity will decrease as the reaction proceeds

Method used

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  • Catalyst for producing chlorine by catalytic oxidation of hydrogen chloride, preparation method and application thereof
  • Catalyst for producing chlorine by catalytic oxidation of hydrogen chloride, preparation method and application thereof
  • Catalyst for producing chlorine by catalytic oxidation of hydrogen chloride, preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] The preparation steps of the catalyst carrier with a silica content of about 35% are as follows:

[0036] Add 1000g of water to 100g of alumina powder to form a slurry, and heat the slurry to 95°C; add about 290g of sodium silicate solution (15% based on silica content) to the oxidation chamber at a flow rate of 3mL / min. In the aluminum slurry, keep the slurry temperature at 95°C, stir for 60min; within 30min, add 1mol L -1 hydrochloric acid to reduce the pH of the slurry to 7.5; then wash the slurry with 1% by weight ammonium carbonate solution to remove residual sodium, and dry the filter cake formed after filtration at a temperature of 100°C. The powder was calcined at 650°C for 7h.

[0037] Mix the above-mentioned treated powder with about 46g of silica sol (25% by weight of silicon dioxide), then add about 62g of water, 5g of citric acid, and 8g of methylcellulose to the mixture, and mix, Then it is extruded on an extruder, dried at a temperature of 100°C for 5 h...

Embodiment 2

[0046] The preparation method of the catalyst carrier with a silica content of about 29% is different from Example 1 in that about 196 g of sodium silicate solution is added to the alumina slurry.

[0047] Catalyst preparation steps are as follows:

[0048] 30gCuCl 2 2H 2 O, 15gLaCl 3 ·7H 2 O and 10g KCl were dissolved in 40mL deionized water, then 60g of the prepared catalyst carrier was added, and finally stirred at a constant temperature for 1h at a temperature of 80°C, kept at a constant temperature for 10h at a temperature of 50°C, dried at a temperature of 100°C for 16h, and Calcined at 550°C for 4 hours in air to obtain the catalyst.

[0049] Wherein: the catalyst, in terms of element weight percentage, contains:

[0050]

[0051] The catalytic reaction process conditions are the same as in Example 1.

[0052] After 25 hours of reaction, the conversion rate of hydrogen chloride was 79.5%, and after 1000 hours of reaction, the conversion rate of hydrogen chlorid...

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PUM

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Abstract

The present invention discloses a catalyst for chlorine gas preparation through catalytic oxidation of hydrogen chloride, a preparation method and applications thereof, wherein the catalyst comprises, by weight, 23-32% of Al, 5-14% of Si, 0.8-16% of Cu, 4-8% of La, and 0.8-16% of K. According to the present invention, silica-coated alumina is adopted as the carrier to prepare the catalyst, such that the high hydrogen chloride conversion rate is ensured while the corrosion of the impurity phosgene and the like in the hydrogen chloride on the catalyst during the reaction process can be prevented or reduced so as to avoid the catalyst bed layer clogging.

Description

technical field [0001] The invention relates to a catalyst for producing chlorine by catalytic oxidation of hydrogen chloride. Background technique [0002] Chlorine is an important basic chemical raw material, which can be produced by electrolysis, but at the same time, sodium hydroxide will be produced, making it difficult to adjust the supply and demand balance between chlorine and sodium hydroxide; moreover, chlorine will produce hydrogen chloride as a by-product in the process of phosgene and chlorination reactions , For example, in the process of producing MDI and TDI by the phosgene method, a large amount of by-product hydrogen chloride will be produced, the price of hydrogen chloride is cheap, the demand is small, and a large amount of processing costs are required to deal with a large amount of hydrogen chloride. Therefore, using hydrogen chloride as a raw material to catalyze and oxidize chlorine gas can not only consume by-product hydrogen chloride, but also reali...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/83B01J32/00B01J21/12C01B7/04
Inventor 孙策马斌全缪晖陈斌武袁茂全张建顾海霞鲁迪
Owner SHANGHAI CHLOR ALKALI CHEM