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Method for adjusting properties of alumina carrier by selecting hydrated alumina with different grain size, carrier obtained by method and application

A kind of ethylene oxidation, solid technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, catalyst carrier, chemical instrument and method, etc., can solve the problem of low catalyst activity and selectivity

Active Publication Date: 2013-05-01
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

EP0150238 (US4428863) uses a small amount of barium aluminate or barium silicate binder in the manufacturing process of high-purity, low-surface alumina carrier, claiming that it can improve the crushing strength and wear resistance of the carrier, and the specific surface of the prepared carrier is less than 0.3m 2 / g, the activity and selectivity of the prepared catalyst are relatively low

Method used

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  • Method for adjusting properties of alumina carrier by selecting hydrated alumina with different grain size, carrier obtained by method and application
  • Method for adjusting properties of alumina carrier by selecting hydrated alumina with different grain size, carrier obtained by method and application
  • Method for adjusting properties of alumina carrier by selecting hydrated alumina with different grain size, carrier obtained by method and application

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Embodiment

[0065] The present invention will be further described below in conjunction with specific examples, but the scope of the present invention is not limited to these examples. For the convenience of expression, the particle size grades of trihydrate α-alumina are named as coarse particles, medium particles and fine particles, and the detailed specification requirements are shown in Table 1.

[0066] Table 1 Particle size specifications of trihydrate α-alumina

[0067]

preparation Embodiment 1

[0069] 3725g of coarse grained α-Al trihydrate 2 o 3 , 1095g fake Al monohydrate 2 o 3and 10 g BaSO 4 Put it in a mixer and mix well, then mix another part according to this raw material ratio, and then transfer both parts to the kneader. 160g NH 4 F is completely dissolved in 1.60 liters of dilute nitric acid solution (nitric acid: water = 1: 3, volume ratio) and then poured into a kneader and kneaded into a paste that can be extruded. Finally, put the paste into the extruder, extrude it into a column with an outer diameter of 8.0mm and a length of 6.0mm, and dry it at 80-120°C for more than 2 hours to reduce the free water content to 10% by weight the following.

[0070] Put the dried column into a natural gas kiln, raise it from room temperature to 1300 ° C over 19 hours, and then keep the temperature for 4 hours to obtain α-Al 2 o 3 The sample number is carrier 1, and the relevant physical performance data of the carrier are shown in Table 2.

preparation Embodiment 2

[0072] 3725g of granulated α-Al trihydrate 2 o 3 , 1095g fake Al monohydrate 2 o 3 and 10 g BaSO 4 Put it in a mixer and mix well, then mix another part according to this raw material ratio, and then transfer both parts to the kneader. 160g NH 4 F is completely dissolved in 1.70 liters of dilute nitric acid solution (nitric acid: water = 1: 3, volume ratio) and then poured into a kneader and kneaded into a paste that can be extruded. Finally, put the paste into the extruder, extrude it into a column with an outer diameter of 8.0mm and a length of 6.0mm, and dry it at 80-120°C for more than 2 hours to reduce the free water content to 10% by weight the following.

[0073] Put the dried column into a natural gas kiln, raise it from room temperature to 1300 ° C over 19 hours, and then keep the temperature for 4 hours to obtain α-Al 2 o 3 The sample number is carrier 2, and the relevant physical performance data of the carrier are shown in Table 2.

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Abstract

The invention relates to a method for preparing alumina carrier which is used for silver catalyst for producing epoxy ethane by ethylene oxidization, a carrier prepared by the method and a silver catalyst prepared from the carrier, and also relates to the application of the catalyst in producing epoxy ethane by ethylene oxidization. In the invention, the carriers are prepared by selecting hydrated alumina with different grain size levels, and rhenium-containing silver catalyst with adjustable catalytic properties can be prepared by the carriers. The method can meet the application demands under a plurality of epoxy ethane synthesizing conditions.

Description

technical field [0001] The present invention relates to a method for preparing a carrier for silver catalysts, the carrier thus prepared and applications thereof, and more particularly the present invention relates to a method for preparing a silver catalyst for ethylene oxidation to produce ethylene oxide. The method, the support prepared thereby and the silver catalyst prepared by the support also relate to the use of this catalyst in the production of ethylene oxide by oxidation of ethylene. Background technique [0002] Under the action of silver catalyst, the oxidation of ethylene mainly produces ethylene oxide, and at the same time, side reactions produce carbon dioxide and water. Among them, activity, selectivity and stability are the main performance indicators of silver catalyst. The so-called activity refers to the reaction temperature required when the production process of ethylene oxide reaches a certain reaction load. The lower the reaction temperature, the hi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J32/00B01J21/04B01J23/68C07D303/04C07D301/10
CPCY02P20/52
Inventor 林伟李金兵陈建设曹淑媛林强薛茜王淑娟汤之强
Owner CHINA PETROLEUM & CHEM CORP