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Catalyst for preparing butadiene through oxidative dehydrogenation of butene

A technology of oxidative dehydrogenation and butadiene, applied in the direction of physical/chemical process catalysts, organic chemistry, hydrocarbons, etc., can solve the problems of high water-ene ratio, low catalyst activity, high energy consumption, etc., and achieve good butene Effect of oxidative dehydrogenation catalytic activity, good technical effect

Active Publication Date: 2018-05-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] One of the technical problems to be solved by the present invention is that the prior art has the problems of elevated catalyst reaction temperature, high water-to-ene ratio, high energy consumption, and low catalyst activity. A new method for preparing butadiene by oxidative dehydrogenation of butene is provided. catalyst

Method used

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  • Catalyst for preparing butadiene through oxidative dehydrogenation of butene
  • Catalyst for preparing butadiene through oxidative dehydrogenation of butene
  • Catalyst for preparing butadiene through oxidative dehydrogenation of butene

Examples

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Effect test

Embodiment 1

[0016] Dissolve 181.3 grams of zinc nitrate, 153.4 grams of chromium nitrate and 1425.9 grams of ferric nitrate in 3L of distilled water, add dropwise 15% ammonia solution under rapid stirring, the pH of the precipitation end point is 9.0, stir at 50°C for 30 minutes, and let stand at room temperature For 2 hours, the resulting slurry was filtered and washed to a nitrate ion concentration of less than 1000 ppm. Add 63.4 grams of phosphoric acid, 200 grams of 10% PVA, and deionized water to the above-mentioned active component slurry to make a slurry, control the solid content to 30%, stir for about 10 minutes, and ball mill at room temperature for 2 hours to obtain the slurry. The microspheres were formed in a dryer, and finally dried at 90°C for 12 hours, then transferred to a muffle furnace for calcination at a temperature of 750°C for 6 hours to obtain a catalyst sample.

Embodiment 2

[0018] Dissolve 367.9 grams of zinc nitrate, 216.7 grams of chromium nitrate and 1241.0 grams of ferric nitrate in 3L of distilled water, add dropwise 15% ammonia solution under rapid stirring, the precipitation end point pH=9.0, stir at 50°C for 30 minutes, and let stand at room temperature For 2 hours, the resulting slurry was filtered and washed to a nitrate ion concentration of less than 1000 ppm. Add 78.6 grams of phosphoric acid, 600 grams of 2% glycerin solution, and deionized water to the above-mentioned active component slurry to make a slurry, control the solid content to 30%, stir for about 10 minutes, and ball mill at room temperature for 2 hours to obtain the slurry. The microspheres were formed in a spray dryer, and finally dried at 90°C for 12 hours and then transferred to a muffle furnace for 6 hours of roasting at a furnace temperature of 650°C to obtain a catalyst sample.

Embodiment 3

[0020] Dissolve 284.9 grams of zinc nitrate, 198.4 grams of chromium nitrate and 1245.6 grams of ferric nitrate in 3L of distilled water, add dropwise 15% ammonia solution under rapid stirring, the pH of the precipitation end point is 8.0, stir at 50°C for 30 minutes, and let stand at room temperature For 2 hours, the resulting slurry was filtered and washed to a nitrate ion concentration of less than 1000 ppm. Add 32.8 grams of phosphoric acid, 600 grams of 2% glycerin solution, and deionized water to the above-mentioned active component slurry to make a slurry, control the solid content to 30%, stir for about 10 minutes, and ball mill at room temperature for 2 hours to obtain the slurry. Microspheres were formed in a spray dryer, and finally dried at 90°C for 12 hours and then transferred to a muffle furnace for calcination for 10 hours at a furnace temperature of 650°C to obtain a catalyst sample.

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Abstract

The invention relates to a fluidized bed catalyst for preparing butadiene through oxidative dehydrogenation of butene, and a preparation method thereof. A purpose of the present invention is to solvethe problems of high water ratio and high energy consumption in the prior art. According to the present invention, the catalyst with a structure general formula of AaBbCcFeOx is used, wherein A is atleast one element selected from Zn and Mg, B is at least one element selected from Group VIB of the periodic table, and C is at least one element selected from P, Sb and Bi; the preparation method comprises: precipitating a metal precursor and ammonia water or sodium hydroxide to form the slurry of an insoluble compound, washing, filtering, adding a binder, carrying out ball milling, carrying outspray drying granulation, and roasting to obtain the catalyst; with the application of the prepared catalyst in the butadiene preparation reaction through oxidative dehydrogenation of butene, the reaction water ratio is effectively reduced, and the good activity can be provided at the water ratio of 4-8; and the catalyst can be used for the industrial production of the butadiene preparation catalyst through oxidative dehydrogenation of butene.

Description

technical field [0001] The invention relates to a catalyst for oxidative dehydrogenation of butene to produce butadiene and a preparation method thereof; in particular to a catalyst for oxidative dehydrogenation of butene in a fluidized bed to produce butadiene. Background technique [0002] Butadiene is the basic raw material of petrochemical industry and an important monomer for the production of synthetic rubber and other polymer synthetic materials. It can be copolymerized with various compounds to produce various synthetic rubbers and synthetic resins. At present, there are mainly two production methods of butadiene: steam cracking in refinery to ethylene co-production, C4 extraction and separation and butene oxidation. Almost all butadiene in my country comes from C4 extraction and separation. This process has economic advantages, but it is obtained as a by-product of the refinery cracking unit. In recent years, the rapid development of the rubber and resin industry ha...

Claims

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Application Information

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IPC IPC(8): B01J27/188B01J27/19C07C5/333C07C11/167
CPCB01J27/188B01J27/19C07C5/3332C07C11/167
Inventor 樊志贵吴文海缪长喜曾铁强张磊
Owner CHINA PETROLEUM & CHEM CORP