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Cobalt-based catalyst for directly preparing olefin from synthesis gas, and preparation method and application thereof

A cobalt-based catalyst, synthesis gas technology, applied in carbon compound catalysts, catalysts, catalysts for physical/chemical processes, etc., can solve the problems of poor catalytic activity, low olefin selectivity, and high methane selectivity

Active Publication Date: 2017-02-15
上海睿碳能源科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The FTO catalysts in the above literature generally have the disadvantages of poor catalytic activity, product distribution biased toward heavy hydrocarbons, low olefin selectivity, and high methane selectivity.

Method used

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  • Cobalt-based catalyst for directly preparing olefin from synthesis gas, and preparation method and application thereof
  • Cobalt-based catalyst for directly preparing olefin from synthesis gas, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0056] Fully stir and dissolve according to the molar ratio of cobalt nitrate:water=1:25 to obtain the first solution; fully stir and dissolve the molar ratio of sodium carbonate:water=1:25 to obtain the second solution. At a precipitation temperature of 80° C. and pH controlled at 7, the first solution and the second solution were dropped into deionized water with a cobalt:water mass ratio=1 at the same time. After the dropwise addition, it was crystallized at 30°C for 48 hours, centrifuged, and the obtained solid product was dried at 100°C for 4 hours, and the dried solid product was calcined at 300°C for 4 hours.

[0057] The solid obtained by roasting is impregnated in equal volume according to the mass ratio of cobalt source: sodium hydroxide = 1:0.001, dried at 60 °C for 24 hours, and the solid obtained by drying is roasted at 400 °C for 3 hours.

[0058] With 10%H 2 / Ar mixed gas is reducing gas, reduced at 300℃, 1MPa, space velocity is 4000h -1 , reduced for 5 hours,...

Embodiment 2

[0060] Fully stir and dissolve according to the molar ratio of cobalt acetate: manganese nitrate: water = 1:2:500 to obtain the first solution; fully stir and dissolve the molar ratio of ammonium carbonate: water = 1:800 to obtain the second solution. At the precipitation temperature of 0°C, the pH was controlled at 10, and the first solution and the second solution were simultaneously dropped into deionized water with a mass ratio of cobalt:water=1:10. After the dropwise addition, it was crystallized at 0°C for 72 hours, separated by filtration, dried at 60°C for 24 hours, and calcined at 200°C for 12 hours.

[0061] The solid obtained by roasting was impregnated in equal volume according to the mass ratio of cobalt source: lithium hydroxide = 1:0.01, dried at 100°C for 4 hours, and the solid obtained by drying was roasted at 300°C for 12 hours.

[0062] With 20% Syngas / N 2 The mixed gas is reducing gas, reduced at 500°C, 0.1MPa, and the space velocity is 500h -1 , reduced ...

Embodiment 3

[0064] Fully stir and dissolve according to the molar ratio of cobalt formate: ammonium vanadate: water = 1:10:1000 to obtain the first solution; fully stir and dissolve the molar ratio of sodium bicarbonate: water = 1:1000 to obtain the second solution. At a precipitation temperature of 90°C and a pH control of 12, the first solution and the second solution were dropped into deionized water with a cobalt:water mass ratio of 1:100 at the same time. After the dropwise addition, hydrothermal crystallization was carried out at 200°C for 1 hour, separated by filtration, and the obtained solid product was dried at 30°C for 48 hours, and the dried solid product was calcined at 500°C for 1 hour.

[0065] The solid obtained by roasting is impregnated in equal volume according to the mass ratio of cobalt source: sodium nitrate = 1:0.0001, dried at 160 °C for 4 hours, and the solid obtained by drying is roasted at 500 °C for 1 hour.

[0066] with H 2 It is reducing gas, reduced at 150℃...

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Abstract

The invention discloses a cobalt-based catalyst for directly preparing olefin from synthesis gas, and a preparation method and application thereof. The preparation method comprises the following steps that (1) any one of the steps (1a) and (1b) is selected: (1a) precipitation method preparation: a cobalt source and water, or the cobalt source, an electronic auxiliary agent and the water are mixed to obtain a first solution; a precipitating agent and the water are mixed to obtain a second solution; the first solution and the second solution are added into water or are added into the water and a structure auxiliary agent to perform precipitation; crystallization, separation, drying and calcination are performed; (1b) impregnation method preparation: the cobalt source and the water, or the cobalt source, the electronic auxiliary agent and the water are mixed to obtain a third solution; the solution is loaded on the structure auxiliary agent by an impregnation method; drying and roasting are performed; (2) solid obtained in the step (1) is used for dipping an alkali metal auxiliary agent by the impregnation method; drying and calcination are performed. The preparation method is simple; the obtained catalyst has the characteristics of good selectivity and high conversion rate.

Description

technical field [0001] The invention relates to the technical field of catalysts, in particular to a cobalt-based catalyst used for directly preparing olefins from synthesis gas, a preparation method and application thereof. Background technique [0002] Low-carbon olefins are one of the important chemical raw materials, usually used in the production of polymers, solvents, pharmaceuticals and cleaning agents. Low-carbon olefins are mainly produced from naphtha cracking and low-carbon alkanes dehydrogenation. Long-chain linear α-olefin is also one of the important chemical raw materials, usually used in ethylene / α-olefin copolymerization, long-chain alcohol production and lubricating oil production. There are usually two production methods for long-chain linear α-olefins, ethylene polymerization and cracking of Fierde synthesis products. [0003] Fischer-Tropsch synthesis is a synthesis gas (Syngas, hydrogen H 2 Mixed gas with carbon monoxide (CO) reacts to produce hydroc...

Claims

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Application Information

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IPC IPC(8): B01J27/22C07C1/04C07C11/02
CPCB01J27/22C07C1/0435C07C2527/22C07C11/02
Inventor 李正甲钟良枢孙予罕于飞安芸蕾李晋平肖亚宁刘斌
Owner 上海睿碳能源科技有限公司