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Catalyst for preparing butadiene through oxidative dehydrogenation of butene and preparation method thereof

An oxidative dehydrogenation and catalyst technology, which is applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problem of low selectivity of butadiene

Inactive Publication Date: 2021-04-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] One of the technical problems to be solved by the present invention is the low selectivity of butadiene used in the production process of butadiene by oxidative dehydrogenation of butene. ene catalyst

Method used

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  • Catalyst for preparing butadiene through oxidative dehydrogenation of butene and preparation method thereof
  • Catalyst for preparing butadiene through oxidative dehydrogenation of butene and preparation method thereof
  • Catalyst for preparing butadiene through oxidative dehydrogenation of butene and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] Weigh an appropriate amount of ferric nitrate (Fe(NO 3 ) 3 9H 2 O), magnesium nitrate (Mg(NO 3 ) 2 ·6H 2 O) and antimony trichloride (SbCl 3 ) was dissolved in 4L deionized water, and stirred evenly to form a solution. Then the above solution was co-precipitated with 20% ammonia solution, stirred at a high speed during the precipitation process, the pH value of the precipitation was kept at 7, and the precipitation temperature was room temperature. Washed with water, the resulting solid was dried in an oven at 110°C for 5 hours. The dried sample was calcined in a muffle furnace at 500°C for 4 hours to obtain Catalyst 1, which was ground into 40-60 mesh particles for catalyst evaluation. The average grain size of catalyst 1 calculated by Scherrer's formula is 9.5nm. The elemental composition of Catalyst 1 has a molar ratio of MgFe 2 o 4 · Fe 0.2 Sb 0.01 o x .

Embodiment 2

[0040] Weigh an appropriate amount of ferric nitrate (Fe(NO 3 ) 3 9H 2 O), magnesium nitrate (Mg(NO 3 ) 2 ·6H 2 O) and antimony trichloride (SbCl 3 ) was dissolved in 4L deionized water, and stirred evenly to form a solution. Then the above solution was co-precipitated with 10% ammonia solution, stirred at high speed during the precipitation process, the pH value of the precipitation was kept at 5, and the precipitation temperature was room temperature. Washed with water, the resulting solid was dried in an oven at 90°C for 24 hours. The dried sample was calcined in a muffle furnace at 400° C. for 24 hours to obtain Catalyst 2, which was ground into 40-60 mesh particles for catalyst evaluation. The average grain size of catalyst 2 calculated by Scherrer's formula is 8.2nm. The molar ratio of the element composition of catalyst 2 is MgFe 2 o 4 · Fe 0.01 Sb 0.01 o x .

Embodiment 3

[0042] Weigh an appropriate amount of ferric nitrate (Fe(NO 3 ) 3 9H 2 O), magnesium nitrate (Mg(NO 3 ) 2 ·6H 2 O) and antimony trichloride (SbCl 3 ) was dissolved in 4L deionized water, and stirred evenly to form a solution. Then the above solution was co-precipitated with 30% ammonia solution, stirred at a high speed during the precipitation process, the pH value of the precipitation was kept at 8, and the precipitation temperature was room temperature, and then the solid sample in the precipitation product was separated with a centrifuge, and deionized Washed with water, the resulting solid was dried in an oven at 150°C for 2 hours. The dried sample was calcined in a muffle furnace at 600°C for 3 hours to obtain catalyst 3, which was ground into 40-60 mesh particles for catalyst evaluation. The average grain size of catalyst 3 calculated by Scherrer's formula is 24.6 nm. The molar ratio of the element composition of catalyst 3 is MgFe 2 o 4 · Fe 0.05 Sb 0.01 o ...

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Abstract

The invention relates to a catalyst for preparing butadiene by oxidative dehydrogenation of butene and a preparation method of the catalyst, and mainly solves the problem of low butadiene selectivity in the existing technology for preparing butadiene by oxidative dehydrogenation of butene. According to the technical scheme, the average grain size of the catalyst for preparing butadiene through oxidative dehydrogenation of butene is smaller than 30nm, the catalyst comprises: a) spinel structure MIIFe2O4 serving as a main active component, wherein M is selected from at least one of Zn, Mg, Mn, Co and Ni; b) a compound with a structural general formula of AaBbOx serving as an auxiliary agent, wherein MIIFe2O4 forms a catalyst with a chemical formula of MIIFe2O4.AaBbOx according to a molar ratio, and A is selected from at least one of Fe or Cr; and B is selected from at least one of Sb or Te, and the catalyst can be used in production of butadiene through oxidative dehydrogenation of butene.

Description

technical field [0001] The invention relates to a catalyst for preparing butadiene by oxidative dehydrogenation of butene and a preparation method thereof. Background technique [0002] Butadiene is the main raw material for the production of synthetic rubber, second only to ethylene and propylene in petrochemical olefin raw materials. From the perspective of downstream consumption, butadiene is mainly used to produce synthetic rubber such as polybutadiene rubber, styrene-butadiene rubber, and SBS elastomer, accounting for a total of 79%, and the production of ABS resin accounts for 16%. Butadiene is also used in the production of adiponitrile (nylon 66 monomer), sulfolane, anthraquinone, tetrahydrofuran and other products. [0003] The industrial production methods of butadiene mainly include steam cracking to ethylene co-production C4 extraction separation and butene dehydrogenation. It is economically advantageous to obtain butadiene by C4 extraction. At present, about...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/843B01J23/86B01J27/057B01J23/889B01J35/02C07C5/333C07C11/167
Inventor 曾铁强缪长喜吴文海樊志贵姜冬宇
Owner CHINA PETROLEUM & CHEM CORP