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Method for the dehydrogenation of low-carbon alkanes

A low-carbon alkane, dehydrogenation technology, applied in the direction of hydrocarbons, hydrocarbons, chemical instruments and methods, etc., can solve the problems of poor catalyst stability, low mechanical strength of catalysts, easy to crush, etc., and achieve the effect of stable performance

Active Publication Date: 2015-08-12
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] One of the technical problems to be solved by the present invention is that the existing preparation technology has the problems of low mechanical strength of the catalyst, easy crushing, and poor stability of the catalyst. A new method for preparing a catalyst carrier for dehydrogenation of low-carbon alkanes is provided. The carrier is used in the process of dehydrogenating low-carbon alkanes to low-carbon olefins. It has the advantages of high mechanical strength, not easy to be crushed under high temperature conditions, and stable performance of the catalyst.

Method used

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  • Method for the dehydrogenation of low-carbon alkanes
  • Method for the dehydrogenation of low-carbon alkanes
  • Method for the dehydrogenation of low-carbon alkanes

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Add 90g of pseudo-boehmite raw powder with an average particle size of 9-30μm or other inorganic oxygen-containing compounds of aluminum to 220.2g of pseudo-boehmite raw powder with an average particle size of 40μm, and then add 9g of safflower powder Then add 130ml of deionized water, knead well, extrude, leave at room temperature for 12 hours, then hold at 90°C for 3 hours, then dry at 120°C for 10 hours, and process at 750°C to obtain the carrier.

[0028] The mixed alumina carrier obtained adopts impregnation technology to support platinum and tin components, that is, the aqueous solution of chloroplatinic acid and tin chloride is impregnated with the obtained alumina carrier at room temperature for 24 hours (metal platinum loading 0.4%, Pt:Sn=1:5), then dried at 60°C, baked at 530°C in air flow for 3 hours, then treated with water vapor at 530°C for 4 hours, and finally treated with dry air at 530°C for 1 hour.

[0029] The sample was reductively activated with hyd...

Embodiment 2

[0036] Add 98g of alumina component B pseudo-boehmite raw powder with different average particle sizes to 236g of pseudo-boehmite raw powder alumina component A main material with an average particle size of 32μm, then add 12g of turmeric powder and then add 140ml of deionized water was fully kneaded, extruded, left at room temperature for 12 hours, then kept at 90°C for 3 hours, then dried at 120°C for 10 hours, and treated at 750°C to obtain a carrier.

[0037] The mixed alumina carrier obtained adopts impregnation technology to support platinum and tin components, that is, the aqueous solution of chloroplatinic acid and tin chloride is impregnated with the obtained alumina carrier at room temperature for 24 hours (metal platinum loading 0.4%, Pt:Sn=1:2), then dried at 60°C, baked at 530°C in air flow for 3 hours, then treated with water vapor at 530°C for 4 hours, and finally treated with dry air at 530°C for 1 hour.

[0038] The sample was reductively activated with hydrog...

Embodiment 3

[0042] In 220g of alumina component A pseudo-boehmite raw powder with an average particle size of 40 μm, different amounts of alumina component B pseudo-boehmite raw powder with an average particle size of 26 μm were added respectively, and then 9 g of fenugreek was added Add 130ml of deionized water to the powder, knead well, extrude, place at room temperature for 12 hours, then keep at 90°C for 3 hours, and then dry at 120°C for 10 hours, and process at 750°C to obtain the carrier. The obtained mixed carrier was loaded with platinum tin active components in the same manner as in Example 1.

[0043] The sample was reductively activated with hydrogen at 500°C for 90 minutes before the dehydrogenation reaction, and was used for isobutane dehydrogenation reaction. Catalyst at 550°C, normal pressure, isobutane mass space velocity 4.6 hours -1 , H 2 / C 4 h 10 Under the condition of 2:5, the reaction results after 72 hours are shown in Table 3.

[0044] table 3

[0045]

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Abstract

The invention relates to a low-carbon alkane dehydrogenation catalyst carrier and a preparation method thereof, and mainly solves the problem of low mechanical strength of the catalyst after a current carrier is formed in the prior art. The low-carbon alkane dehydrogenation catalyst carrier is prepared from the following components by weight percent in the technical scheme: a) 50-90% of aluminum oxide component A, which is selected from at least one of pseudo-boehmite raw powder, hydrated aluminum oxide raw powder and aluminum oxide raw powder with crystal phase structures of gamma-Al2O3, delta-Al2O3 and theta-Al2O3; and b) the balance of aluminum oxide component B, which is selected from at least one of pseudo-boehmite raw powder, hydrated aluminum oxide raw powder and aluminum oxide raw powder with crystal phase structures of gamma-Al2O3, delta-Al2O3 and theta-Al2O3. According to the technical scheme, the problem of the low mechanical strength of the catalyst after the current carrier is formed is solved well. The catalyst carrier can be used for industrial production of preparing a low-carbon olefin catalyst from low-carbon alkane through dehydrogenation.

Description

technical field [0001] The invention relates to a carrier of an alkane dehydrogenation catalyst and a preparation method thereof. Background technique [0002] Propylene / isobutylene mainly comes from the co-production or by-product of steam cracking and fluid catalytic cracking in refineries, and can be widely used in the synthesis of polymers, gasoline additives, rubber and various chemical intermediates. With the increasing demand for low-carbon olefins, the traditional production process is difficult to meet the rapid growth of market demand. A large amount of low-carbon alkanes obtained from refineries are the main components of liquefied petroleum gas, which are mainly used as civil fuels. The development of the process of producing low-carbon alkenes from low-carbon alkanes is of great significance for making full use of low-carbon alkanes to open up new sources of alkenes. At present, propane catalytic dehydrogenation technology is represented by Oleflex process of ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J32/00B01J23/62C07C11/06C07C11/09C07C5/333
CPCY02P20/52
Inventor 吴文海吴省樊志贵马春景张磊缪长喜
Owner CHINA PETROLEUM & CHEM CORP