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Preparation method of Fischer-Tropsch synthesis iron-based catalyst

An iron-based catalyst and Fischer-Tropsch synthesis technology, applied in the preparation of liquid hydrocarbon mixtures, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of inability to realize continuous production of catalysts and affect the quality of catalysts, and achieve excellent results Catalyst quality and performance, good pore structure and wear strength, good stability

Inactive Publication Date: 2017-04-26
CHNA ENERGY INVESTMENT CORP LTD +1
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Problems solved by technology

[0006] However, in the prior art method for preparing precipitated iron-based catalysts, it is usually carried out intermittently in a tank reactor with a stirrer, wherein the precipitation reaction and the aging process are often carried out in the same reaction vessel, which leads to inability to Realize the continuous production of catalyst preparation, and there are concentration gradients, temperature gradients and pH gradients in the flow of materials in the tank reactor, which affect the quality of the final catalyst

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  • Preparation method of Fischer-Tropsch synthesis iron-based catalyst

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[0020] The invention provides a method for preparing a precipitated catalyst precursor, comprising: (1) fully mixing the solution of the precipitating agent with the solution of the precursor containing the effective component of the precipitated catalyst in a precipitation container, thereby producing a precipitation reaction containing Precipitation coarse slurry of the precursor of the active component of the precipitation catalyst; (2) aging the above-mentioned sediment coarse slurry in an aging container, so that the tiny sediment particles are gradually agglomerated or aggregated, thereby further improving the precipitation of the precipitate The physical structure, wherein, the precipitation vessel and the aging vessel are different vessels connected in series, so that the precipitation reaction and the aging process are sequentially and continuously carried out in the precipitation vessel and the aging vessel.

[0021] The invention provides a preparation method of a Fi...

Embodiment 1

[0059] This example illustrates the preparation method of the Fischer-Tropsch synthesis iron-based catalyst precursor and catalyst of the present invention.

[0060] (1) Precipitation reaction stage: 25kg ferric nitrate nonahydrate, 0.77kg copper nitrate, 0.77kg cobalt nitrate hexahydrate are dissolved in deionized water, and are made into 160 liters of metal salt solution (metal salt concentration is 16.59% by weight); 12.5 kg sodium carbonate is dissolved in deionized water, and is made into 140 liters of precipitant solution (sodium carbonate concentration is 8.9% by weight);

[0061] The metal salt solution and the precipitant solution are passed through the corresponding feed pumps, and are respectively added to a static mixer (sedimentation vessel) (250 mm in diameter, 10 in length-to-diameter ratio) for precipitation reaction. The temperature of the precipitation reaction is 90 ° C, and the online pH The value detector controls the pH value of the precipitation reaction...

Embodiment 2

[0069] This example illustrates the preparation method of the Fischer-Tropsch synthesis iron-based catalyst precursor and catalyst of the present invention.

[0070] (1) precipitation reaction stage: 25kg ferric nitrate nonahydrate, 0.20kg copper nitrate, 2.15kg manganese nitrate solution are dissolved in deionized water, are made into 50 liters of metal salt solution (metal salt concentration is 51% by weight); 12.5kg Potassium carbonate is dissolved in deionized water, and is made into 20 liters of precipitant solution (concentration of potassium carbonate is 63% by weight);

[0071] The metal salt solution and the precipitating agent solution are put into the static mixer (precipitation vessel) (diameter 500mm, length-to-diameter ratio 5) respectively through the corresponding feed pump to carry out the precipitation reaction. The temperature of the precipitation reaction is 30°C. The pH value of the precipitation reaction controlled by the instrument is 10, and the precipi...

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Abstract

The invention discloses a preparation method of a precipitating catalyst precursor and a preparation method of Fischer-Tropsch synthesis iron-based catalyst. The method comprises the steps that 1, a precipitator solution and a metal salt solution containing iron salt perform precipitation reaction in a precipitation container to produce iron-based precipitate coarse slurry; 2, the iron-based precipitate coarse slurry is aged in an ageing container; 3, the aged iron-based precipitate is washed and filtered to remove impurities, and then slurry is prepared; 4, the slurry is mixed with a silicon source, a pH value is regulated, and a Fischer-Tropsch synthesis iron-based catalyst precursor is obtained through filtration and optimal drying, wherein the precipitation reaction and the ageing process are sequentially performed in the precipitation container and the ageing container which are different and are serially connected mutually so as to perform the precipitation reaction and the ageing process. By the adoption of the method, continuous production of the prepared Fischer-Tropsch synthesis iron-based catalyst precursor can be achieved, and the quality and the performance of the catalyst can be also improved.

Description

technical field [0001] The invention relates to a preparation method of a precipitated catalyst precursor and a preparation method of a Fischer-Tropsch synthesis iron-based catalyst. Background technique [0002] Fischer-Tropsch synthesis is the synthesis gas (CO+H 2 ) The reaction process in which liquid fuels and other chemicals are synthesized under the action of a catalyst. Commonly used commercial catalysts include iron-based catalysts. Different methods of preparing precipitated iron-based catalysts will significantly affect the morphology, phase, surface structure and strength of the catalyst, and ultimately affect the reaction performance of the catalyst. Therefore, it is very necessary to develop iron-based catalysts suitable for industrial plants of coal liquefaction technology. [0003] CN201061758Y discloses a pipeline continuous mixing reactor for plasma precipitation reaction, comprising a reaction tube, a refrigerant jacket and an outer shell are arranged ou...

Claims

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Application Information

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IPC IPC(8): B01J23/78B01J23/889C10G2/00
Inventor 朱加清常海刘庆华程萌武鹏张魁罗明生
Owner CHNA ENERGY INVESTMENT CORP LTD
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