Straight chain paraffin dehydrogenation catalyst carrier production process

A dehydrogenation catalyst, straight-chain alkane technology, applied in the direction of catalyst carrier, physical/chemical process catalyst, alumina/aluminum hydroxide, etc., can solve the problems of large loss of active component platinum, high catalyst price, and more dust, etc. achieve good stability

Inactive Publication Date: 2005-02-16
BC P INC CHINA NAT PETROLEUM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] At present, there is only one set of domestic linear alkane dehydrogenation catalyst carrier production equipment (Taiyuan Daily Chemical Institute), with a production capacity of 60 tons per year, and two catalyst production equipment (Nanjing Alkyl Benzene Plant and Fushun Petrochemical Company Petrochemical Plant No. 5 ), foreign dehydrogenation catalyst suppliers are mainly UOP, which only sells finished catalysts, not carriers, and

Method used

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  • Straight chain paraffin dehydrogenation catalyst carrier production process

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Embodiment Construction

[0021] specific implementation

[0022] (1) Effect of gelling conditions on bulk ratio

[0023] The gelling temperature is low, the colloidal particles are fine, difficult to filter, and the bulk ratio is large. If the temperature is high, the added ammonia is easy to volatilize, making it difficult to maintain a stable pH value during the gelation and washing process, and the smell of ammonia is too large, which is inconvenient to operate. The more suitable gelation temperature is 70°C. See Table 1:

[0024] experiment

[0025] (2) Effect of PH value of gelling on bulk specific gravity

[0026] If the PH value of gelling is too low, the bulk ratio will be large, and if the PH value is too high, the bulk ratio will gradually increase, but slowly, so it is very important to control the PH value during gelling.

[0027]

[0028] (3) Effect of acidification conditions on bulk specific gravity

[0029] Under the same conditions, tests with different conce...

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Abstract

The invention relates to linear alkanes dehydrogenation catalyst carrier technics used in petrochemical industry. Its aperture distribution can be adjusted through producing macroporous alumina globule. Then add surface active agent in globule dropping process. Finally conduct hydrothermal treatment in supporter producing process. On base of self-research, globule dropping technics is designed by self to make product cost reduce remarkably. Using self produced macroporous alumina dropping globule, side pressure intensity of alumina globule can reach more than 20N per grain. Using self-researched macroporous gamma-Al2O3 with binocular construction, reaction performance of linear alkanes dehydrogenation catalyst can reach conversion>12-13 percent and selectivity>90 percent. Compared with international like products, its stability is better.

Description

[0001] Field: [0002] The invention belongs to a catalyst production process used in petrochemical plants, in particular to a straight-chain alkane dehydrogenation catalyst carrier production process. Background technique: [0003] Before the 1990s, dehydrogenation catalysts were monopolized by foreign companies, with an average annual price increase of more than 20%. In the early 1990s, domestic linear alkane dehydrogenation catalysts were put into the market, breaking the monopoly of foreign companies on this product, but the output was very small. At present, there are three alkylbenzene factories in China (Fushun Detergent Chemical Factory, Nanjing Alkylbenzene Factory, Nanjing Jintong Petrochemical Co., Ltd.), and the production capacity of alkylbenzene units has reached nearly 400,000 tons. The production capacity of benzene plant has reached 200,000 tons / year. The demand for linear alkane dehydrogenation catalyst is 70 tons / year. [0004] At present, there is only o...

Claims

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Application Information

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IPC IPC(8): B01J21/04B01J32/00C01F7/02
Inventor 崔德强贺新杨恒吉赵悦
Owner BC P INC CHINA NAT PETROLEUM CORP
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