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A highly dispersed heavy hydrocarbon Fischer-Tropsch synthesis catalyst based on a carbonization treatment method and its preparation method

A Fischer-Tropsch synthesis and carbonization technology, used in catalyst activation/preparation, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc. and selectivity issues

Active Publication Date: 2021-03-02
SYNFUELS CHINA INNER MONGOLIA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The above-mentioned modification methods have made significant progress in improving the activity of cobalt-based Fischer-Tropsch synthesis catalysts, product selectivity, long-term operation stability and reactor adaptability, but still have not taken into account the performance of the above aspects at the same time. There is still a strong chemical interaction between the carrier and the active center cobalt, forming a compound that is difficult to reduce, and the dispersion is poor, which reduces the activity and selectivity of the catalyst, making CH 4 The content in the reaction product increases, C 5 + Reduced selectivity

Method used

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  • A highly dispersed heavy hydrocarbon Fischer-Tropsch synthesis catalyst based on a carbonization treatment method and its preparation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] Embodiment 1, preparation catalyst cat1, carbonization treatment and application

[0042] (1) Weigh 0.5g of nitric acid (according to HNO 3 ), weighed 1.5g of citric acid, and dissolved the two together in 30mL of deionized water; weighed 50g of commercially available Al 2 o 3 , add 2g of scallop powder and mix evenly; mix the above-mentioned powder with the solution thoroughly, extrude into strips, dry at 100°C for 8 hours, and roast at 500°C for 6 hours.

[0043] (2) Weigh 50g of the above-mentioned carrier, the final catalyst is calculated by (Ag+Ce) / Co=2 / 100, Ag / Ce=1 / 1, and weigh AgNO 3 and Ce(NO 3 ) 3 ·6H 2 O was dissolved in 50 mL of water, added to the above carrier for impregnation, impregnated for 4 hours, dried at 100°C for 8 hours, and calcined at 500°C for 6 hours.

[0044] (3) Weigh 50 g of the above-mentioned Ag and Ce-containing carrier, the final catalyst is based on the Co content of 20wt%, the final catalyst is based on the total content of ethyl...

Embodiment 2

[0047] Embodiment 2, preparation catalyst cat2, carbonization treatment and application

[0048] (1) Weigh 2 g of citric acid and dissolve it in 30 mL of deionized water; weigh 40 g of Al 2 o 3 and 10gSiO 2 Mix evenly, and then add 2 g of scallop powder and mix evenly; mix the above powder and solution thoroughly, extrude, dry at 90°C for 8 hours, and roast at 500°C for 8 hours.

[0049] (2) Weigh 50g of the above-mentioned carrier, and the final catalyst is calculated according to Ru / Co=0.5 / 100, and Ru(NO)(NO 3 ) 3 , dissolved in 50mL of water, added to the above carrier for impregnation, impregnated for 4 hours, dried at 90°C for 8 hours, and calcined at 500°C for 8 hours.

[0050] (3) Weigh 50g of the above-mentioned Ru-containing carrier, the final catalyst is based on the Co content of 22wt%, the final catalyst is based on the total content of ethylenediamine and citric acid / carrier=0.065, ethylenediamine: citric acid=1:1, weigh Cobalt nitrate, ethylenediamine and ci...

Embodiment 3

[0053] Embodiment 3, preparation catalyst cat3, carbonization treatment and application

[0054] (1) Weigh 0.5g of nitric acid (according to HNO 3 ), weighed 1.5g of citric acid, and dissolved the two together in 30mL of deionized water; weighed 50g of commercially available Al 2 o 3 , add 2g of scallop powder and mix evenly; mix the above-mentioned powder with the solution thoroughly, extrude into strips, dry at 100°C for 8 hours, and roast at 500°C for 6 hours.

[0055] (2) Weigh 50g of the above-mentioned carrier, the final catalyst is calculated by (Ag+Ce) / Co=2 / 100, Ag / Ce=1 / 1, and weigh AgNO 3 and Ce(NO 3 ) 3 ·6H 2 O was dissolved in 50 mL of water, added to the above carrier for impregnation, impregnated for 4 hours, dried at 100°C for 8 hours, and calcined at 500°C for 6 hours.

[0056] (3) Weigh 50g of the above-mentioned carrier containing Ag and Ce, the final catalyst is based on the Co content of 20wt%, the final catalyst is based on the total content of ethyle...

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Abstract

The invention discloses a highly dispersed heavy hydrocarbon Fischer-Tropsch synthesis catalyst based on a carbonization treatment method and a preparation method thereof. The preparation method of the highly dispersed heavy hydrocarbon Fischer-Tropsch synthesis catalyst comprises the following steps: using an impregnation method to load a soluble salt of a metal additive on a shaped carrier, and obtain a pretreated carrier through drying and roasting; And the organic matter is loaded on the pretreatment carrier, and it is obtained after drying. The present invention introduces the process of "carbonization" treatment in the evaluation step "reduction-Fischer-Tropsch synthesis" of conventional catalysts, and optimizes it to "reduction-synthesis gas treatment-carbonization-H 2 After the above-mentioned catalyst, the average grain size of Co decreases; the carbonized catalyst undergoes a second reduction to remove excess carbon deposits, thereby improving the Fischer-Tropsch reaction activity of the catalyst; after the second reduction, not only the crystal The particle size is reduced, the active sites are increased, and the reduction degree of the catalyst will be further improved, which leads to the improvement of the catalyst performance.

Description

technical field [0001] The invention relates to a highly dispersed heavy hydrocarbon Fischer-Tropsch synthesis catalyst based on a carbonization treatment method and a preparation method thereof, belonging to the technical field of catalyst preparation. Background technique [0002] The Fischer-Tropsch synthesis (FTS) process is a chemical process that converts synthesis gas into hydrocarbons, and is one of the most important ways to efficiently convert and utilize non-petroleum carbon-containing resources (natural gas, coal, residual oil, and biomass, etc.). Syngas generates a series of hydrocarbons with different carbon numbers under the action of catalysts (C 1 ~C 200 ), mainly straight-chain alkanes, and some low-carbon olefins and alcohols are obtained at the same time. The initial product is further processed (such as separation, hydrocracking or hydroisomerization, etc.) to obtain certain specifications of gasoline, diesel and other oil fuels, as well as chemicals s...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/89B01J23/83B01J37/02B01J37/08B01J37/18C10G2/00
CPCB01J23/83B01J23/8913B01J23/894B01J37/0201B01J37/0207B01J37/084B01J37/088B01J37/18C10G2/332C10G2/333
Inventor 燕来周建强郜文斌索海云王晓婷白皓宇杨勇李永旺
Owner SYNFUELS CHINA INNER MONGOLIA CO LTD
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