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Cobalt-based Fischer-Tropsch synthesis catalyst with high heavy hydrocarbon selectivity as well as preparation method and application thereof

A catalyst and Tropsch synthesis technology, applied in the field of cobalt-based Fischer-Tropsch synthesis catalysts and their preparation, can solve the problems of large differences in thermal stability of cobalt catalysts, expensive SiC support, limited practical application, etc., and achieves good reproducibility , enhance the interaction force, the effect of simple preparation process

Active Publication Date: 2020-04-21
SOUTH CENTRAL UNIVERSITY FOR NATIONALITIES
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Carriers with different characteristics have different mass and heat transfer properties, and can form different interaction forces with Co metal, which makes the thermal stability of the supported cobalt catalysts vary greatly.
Using SiC carrier with high thermal conductivity to support cobalt catalyst is beneficial to avoid the generation of hot spots in the reaction process and improve the performance of the catalyst, but SiC carrier is expensive and has low specific surface area, which limits its practical application.

Method used

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  • Cobalt-based Fischer-Tropsch synthesis catalyst with high heavy hydrocarbon selectivity as well as preparation method and application thereof
  • Cobalt-based Fischer-Tropsch synthesis catalyst with high heavy hydrocarbon selectivity as well as preparation method and application thereof
  • Cobalt-based Fischer-Tropsch synthesis catalyst with high heavy hydrocarbon selectivity as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] In the first step, 20g of titanium isopropoxide was added to 5g of citric acid (in the two substances, the mass ratio of titanium to carbon was 1:2.7) and 26mL of absolute ethanol, stirred evenly at 60°C, and the resulting mixture was transferred to Put it into a reaction kettle lined with polytetrafluoroethylene, collect the product after solvothermal reaction at 200 °C for 24 h, filter under reduced pressure, dry at 100 °C for 12 h, place in a tube furnace under NH 3 Nitriding at 1000°C under air atmosphere to obtain TiN carrier;

[0043] In the second step, use 300mL of ethanol aqueous solution (mixed with water and absolute ethanol at a volume ratio of 50:1) as a solvent to dissolve 4.7g of cobalt acetate tetrahydrate, then add 25mL of 15mol / L ammonia water, and use acid and alkali to neutralize The precursor of nano-cobalt oxide was obtained by the method, and the nano-cobalt oxide particles were obtained after hydrothermal treatment at 180°C for 5h, drying at 100°...

Embodiment 2

[0048] Catalyst A was placed in a fixed-bed reactor (TORCH) for catalytic reaction performance evaluation, and the activation conditions were: under normal pressure, H 2 In the atmosphere, the temperature is 300°C and the volume space velocity is 1000h -1 , the activation time is 8h; the reaction conditions are: the reaction temperature is 240℃, 260℃ and 300℃ respectively, H 2 : CO (volume ratio) is 2:1, volume flow rate is 600h -1 , the pressure is 2.0MPa. to N 2 As an internal standard, used to calculate the conversion rate of CO. The tail gas after the reaction was connected to an Agilent GC3000A gas chromatograph for online analysis. Table 1 shows the average reaction data within 100 hours of stable operation of the catalytic reaction to reach the target temperature.

Embodiment 3

[0050] Take 4g of the TiN carrier and 0.96g of nano-cobalt oxide particles prepared in Example 1, first use the mechanical dispersion method to grind for 2h, mix evenly, and then add 60mL of ethanol aqueous solution (the volume ratio of ethanol to water is 1:2) and ultrasonically disperse for 1h Catalyst B was obtained after vacuum rotary evaporation at 60°C for 3h and drying at 100°C for 12h.

[0051] The mass of Co element in catalyst B accounts for about 15% of the mass of the catalyst (theoretical calculation value).

[0052] The catalyst evaluation test was carried out in a fixed-bed reactor (TORCH), and the activation conditions were: under normal pressure, H 2 In the atmosphere, the temperature is 300°C and the volume space velocity is 1000h -1 , the activation time is 8h; the reaction conditions are: the reaction temperature is 240℃, 260℃ and 300℃ respectively, H 2 : CO (volume ratio) is 2:1, volume flow rate is 600h -1 , the pressure is 1.0MPa. The reaction time w...

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Abstract

The invention relates to the technical field of preparation of high-quality liquid fuel and chemicals by catalytic conversion of synthesis gas, and particularly discloses a cobalt-based Fischer-Tropsch synthesis catalyst with high heavy hydrocarbon (C<5+>) selectivity. In the catalyst, nano TiN is adopted as a carrier, cobaltosic oxide nanoparticles are loaded on the carrier; the particle size distribution range of the TiN particles is 18-48 nm, the particle size distribution range of the cobaltosic oxide particles is 6-14 nm, and the mass of the cobalt element in the catalyst accounts for 10%-15% of the mass of the catalyst. The cobalt-based Fischer-Tropsch synthesis catalyst provided by the invention is relatively wide in suitable reaction temperature range, and relatively low CH4 and CO2 selectivity and high heavy hydrocarbon selectivity can be maintained at a relatively high reaction temperature (240-300 DEG C).

Description

technical field [0001] The invention relates to the technical field of preparing high-quality liquid fuels and chemicals through catalytic conversion of syngas, in particular to a high-heavy hydrocarbon (C 5+ ) Selective cobalt-based Fischer-Tropsch synthesis catalyst and its preparation method and application. Background technique [0002] In recent years, the rapid consumption of petroleum resources has caused serious energy and environmental problems, and it is urgent to develop clean energy production technologies that can replace petroleum resources. Fischer-Tropsch synthesis (FTS) technology, which converts carbon-based raw materials such as coal, natural gas, biomass, and organic waste, into clean fuels and high value-added chemicals through syngas, has received extensive attention. The product selectivity of FTS reaction generally follows the ASF distribution, and the product composition is relatively complex. The selectivity is affected by factors such as catalyst ...

Claims

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Application Information

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IPC IPC(8): B01J27/24C10G2/00
CPCB01J27/24C10G2/332B01J35/394Y02P20/52
Inventor 赵燕熹龙彩燕刘成超李金林张煜华林爱华
Owner SOUTH CENTRAL UNIVERSITY FOR NATIONALITIES
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