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Catalyst for oxidative dehydrogenation of butene to prepare butadiene

A technology for oxidative dehydrogenation and butadiene, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, heterogeneous catalyst chemical elements, etc., can solve the problem of low catalyst activity and water-ene ratio High, catalyst reaction temperature rise and other problems, to achieve good technical effect, good catalytic activity of butene oxidative dehydrogenation

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 oxidative dehydrogenation of butene to prepare butadiene
  • Catalyst for oxidative dehydrogenation of butene to prepare butadiene
  • Catalyst for oxidative dehydrogenation of butene to prepare butadiene

Examples

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Effect test

Embodiment 1

[0016] Dissolve 230.8 grams of magnesium nitrate, 178.5 grams of zinc nitrate and 1532.3 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 35.8 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. Carry out microsphere molding in a desiccator, and finally dry at 90°C for 12 hours, then transfer to a muffle furnace for calcination for 6 hours at a furnace temperature of 750°C to obtain a catalyst sample.

Embodiment 2

[0018] Dissolve 243.6 grams of magnesium nitrate, 238.0 grams of zinc nitrate and 1725.3 grams of ferric nitrate in 3L of distilled water, add dropwise 15% ammonia solution under rapid stirring, the precipitation end point pH=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 54.6 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 200.6 grams of magnesium nitrate, 119.00 grams of zinc nitrate and 1345.3 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 39.2 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 catalyst for oxidative dehydrogenation of butene to prepare butadiene, and mainly solves the problems of high water butene ratio and high energy consumption in the prior art. The catalyst adopted by the invention has a structural general formula of ZnaAbMcFeOx, wherein M is selected from at least one element of Be, Mg, Ca, Sr, Mn, Ba, Cu, Co, and Ni, and A is selected from at least one element of P, Sb and Bi. The method includes: precipitating a metal precursor and ammonia water or sodium hydroxide to generate an insoluble compound slurry, conducting washing and filtering, then adding a binder, conducting ball milling, and then carrying out spray drying granulation and roasting to obtain the catalyst. The catalyst prepared by the method provided by the inventioncan be used for the reaction of oxidative dehydrogenation of butene to prepare butadiene, effectively reduces the reaction water butene ratio, when the water butene ratio is 4-8, the catalyst still has good activity, and can be used for the industrial production of oxidative dehydrogenation of butane to prepare butadiene.

Description

technical field [0001] The invention relates to a catalyst for producing butadiene by oxidative dehydrogenation of butene and a preparation method thereof; in particular to a catalyst for producing butadiene by oxidative dehydrogenation of butene in a fluidized bed. 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 industr...

Claims

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Application Information

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IPC IPC(8): B01J27/185B01J23/843B01J27/186B01J27/187C07C5/48C07C11/16
CPCB01J23/002B01J23/8435B01J23/8437B01J27/1853B01J27/186B01J27/187B01J2523/00C07C5/48C07C11/16B01J2523/22B01J2523/27B01J2523/51B01J2523/842B01J2523/17B01J2523/25B01J2523/24B01J2523/847
Inventor 樊志贵吴文海缪长喜曾铁强张新玉姜冬宇
Owner CHINA PETROLEUM & CHEM CORP