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Application of catalyst in catalyzing synthesis gas conversion to prepare liquid fuel

A synthesis gas conversion and catalyst technology, applied in the preparation of liquid hydrocarbon mixtures, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of metal active component Ru loss, metal Ru interaction Insufficient effect, low catalyst activity and other problems, to achieve superior low-temperature activity and high-temperature stability, conducive to large-scale production and use, and high metal utilization

Inactive Publication Date: 2020-12-11
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The carrier of Fischer-Tropsch synthesis mostly uses Al 2 o 3 , SiO 2 and other metal oxides, and since Al 2 o 3 , SiO 2 The interaction between such supports and metal Ru is not strong. During the process of Fischer-Tropsch synthesis, CO adsorption on metal Ru can easily form volatile Ru(CO) 5 and Ru 3 (CO) 12 (Applied Catalysis,1986,24,199–209), resulting in Ru / Al 2 o 3 、Ru / SiO 2 The metal active component Ru of the catalyst is continuously lost during the reaction, resulting in low activity and poor stability of the catalyst

Method used

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  • Application of catalyst in catalyzing synthesis gas conversion to prepare liquid fuel
  • Application of catalyst in catalyzing synthesis gas conversion to prepare liquid fuel
  • Application of catalyst in catalyzing synthesis gas conversion to prepare liquid fuel

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Take RuCl with a Ru content of 0.06g 3 ·3H 2 O solution, add deionized water to dilute to 50ml homogeneous solution, stir evenly, add 1.94g rutile type TiO to this solution 2 The carrier formed a homogeneous mixture; the mixture was heated and stirred at 60° C. until the solvent evaporated to dryness, and the obtained solid was dried in an oven at 110° C. for 12 h, and then calcined in a muffle furnace at 300° C. in an air atmosphere for 3 h. Calcined Ru / TiO 2 The catalyst was redispersed in 200ml, 1mol / L dilute ammonia water, stirred at room temperature for 12h; filtered, washed with dilute ammonia water, and then deionized water until the pH of the filtrate was 7; the filtered solid was dried in an oven at 80°C for 12h, That is, a catalyst for removing chlorine is obtained. Catalyst for dechlorination in H 2 Reduction treatment at 400°C for 3 hours in the atmosphere can obtain Ru / TiO 2 -400 Catalyst.

Embodiment 2

[0031] Take RuCl with a Ru content of 0.06g 3 ·3H 2 O solution, add deionized water to dilute to 50ml homogeneous solution, stir evenly, add 1.94g rutile type TiO to this solution 2 The carrier formed a homogeneous mixture; the mixture was heated and stirred at 60° C. until the solvent evaporated to dryness, and the obtained solid was dried in an oven at 110° C. for 12 h, and then calcined in a muffle furnace at 300° C. in an air atmosphere for 3 h. Calcined Ru / TiO 2 The catalyst was redispersed in 200ml, 1mol / L dilute ammonia water, stirred at room temperature for 12h; filtered, washed with dilute ammonia water, and then deionized water until the pH of the filtrate was 7; the filtered solid was dried in an oven at 80°C for 12h, That is, a catalyst for removing chlorine is obtained. Catalyst for dechlorination in H 2 Reduction treatment at 450°C for 3 hours in the atmosphere can obtain Ru / TiO 2 -450 Catalyst.

Embodiment 3

[0033] Take RuCl with a Ru content of 0.06g 3 ·3H 2 O solution, add deionized water to dilute to 50ml homogeneous solution, stir evenly, add 1.94g rutile type TiO to this solution 2 The carrier formed a homogeneous mixture; the mixture was heated and stirred at 60° C. until the solvent evaporated to dryness, and the obtained solid was dried in an oven at 110° C. for 12 h, and then calcined in a muffle furnace at 300° C. in an air atmosphere for 3 h. Calcined Ru / TiO 2 The catalyst was redispersed in 200ml, 1mol / L dilute ammonia water, stirred at room temperature for 12h; filtered, washed with dilute ammonia water, and then deionized water until the pH of the filtrate was 7; the filtered solid was dried in an oven at 80°C for 12h, That is, a catalyst for removing chlorine is obtained. Catalyst for dechlorination in H 2 Reduction treatment at 500°C for 3 hours in the atmosphere can obtain Ru / TiO 2 -500 catalyst.

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Abstract

The invention relates to a catalyst for efficiently catalyzing conversion of synthesis gas to prepare liquid fuel, a preparation method and application thereof. The catalyst is composed of a TiO2 carrier and a metal Ru active component, wherein the metal Ru active component is loaded on the TiO2 carrier through an impregnation method. According to the invention, a Ru / TiO2 catalyst is subjected toreduction treatment at different temperatures, so that the interaction degree between a metal Ru and a carrier TiO2 can be effectively adjusted so as to regulate and control the reaction performance of the Ru / TiO2 catalyst; when the Ru / TiO2 catalyst reduced at 400-600 DEG C is used for a Fischer-Tropsch synthesis reaction, the catalyst shows excellent low-temperature activity and high-temperaturestability, and the selectivity of C5+ in the product is kept at 90% or above; and in the catalyst provided by the invention, the TiO2 carrier can be directly used for loading the metal Ru active component without treatment, the active component Ru is highly dispersed, the metal utilization rate is remarkably improved, and the catalyst remarkably improves the activity and stability of a Fischer-Tropsch synthesis reaction.

Description

technical field [0001] The invention relates to a high-efficiency catalyst for converting synthetic gas into liquid fuel, a preparation method and application thereof. Background technique [0002] In recent years, the global economy has grown rapidly, and the demand for energy in modern society has continued to increase. With the reduction of fossil energy reserves and deteriorating environmental problems, it is imminent to develop alternative energy sources. Combined with my country's basic energy structure of rich coal, poor oil, and little gas, the development of coal-to-oil industry has a pivotal position. Although the direct coal liquefaction technology can realize the utilization of coal-to-oil resources, the direct coal liquefaction technology requires a large amount of hydrogen, consumes a lot of energy, and has low economic benefits. In the Fischer-Tropsch synthesis process, synthesis gas (CO+H 2 ) into high value-added oil products, which has attracted more and ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/46C10G2/00
CPCB01J23/462C10G2/333C10G2/341
Inventor 黄延强张亚茹苏雄张涛王国建
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI