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Nickel-based molecular sieve catalyst and preparation method of same

A molecular sieve and catalyst technology, which is applied in the field of nickel-based molecular sieve catalysts and their preparation, can solve the problems of poor catalyst uniformity, large catalyst consumption, high energy consumption of alloys, etc., and achieve the effect of uniform distribution

Inactive Publication Date: 2017-09-15
CHINA TIANCHEN ENG +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the main problems of this catalyst are low activity and selectivity, large amount of catalyst, serious environmental pollution, etc. Therefore, it is necessary to develop new and more efficient catalyst materials to improve the yield of hexamethylenediamine products and achieve atom economy.
[0003] At present, there are mainly the following methods for modifying the Raney catalyst: one is to add a modifier to melt during the preparation of the parent alloy, and then crush and activate it to obtain it. The disadvantage is that the high-temperature melting of the alloy consumes a lot of energy; After the modifier is added in the preparation process, the catalyst is modified by means of ultrasonic treatment. The disadvantage is that the performance improvement of the catalyst by ultrasonic treatment alone is small; the third is to use the impregnation method to modify the prepared catalyst. The catalyst uniformity is poor

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Each component TS-1: NiO: Cr 2 o 3 The mass ratio is 75:15:10, wherein the metal salt is calculated as the corresponding oxide.

[0036] S1: Mix nickel nitrate and chromium nitrate according to the calculated mass ratio of 15:10 in terms of oxides and dissolve them in water to prepare a mixed solution with a mass fraction of 10%;

[0037] S2: Immerse the TS-1 molecular sieve into the prepared sodium hydroxide solution with a mass fraction of 5%, treat it in a closed hydrothermal reaction kettle at 80°C for 12h, and wash it with pure water until the pH of the eluate is 7. Dry in an oven at 90°C for 8 hours for later use;

[0038] S3: Mix the mixed solution prepared in step S1 with the TS-1 molecular sieve treated in step S2 at a mass ratio of 25:75 in terms of oxides, let it stand for 8 hours, dry it in an oven at 90°C, and then dry it in a horse Roast at 400°C for 6 hours in a Furnace;

[0039] S4: Heat the catalyst powder obtained in step S3 in an atmosphere with a...

Embodiment 2

[0041] Each component S-1: NiO: Cr 2 o 3 The mass ratio is 79.5:20:0.5, wherein the metal salt is calculated as the corresponding oxide.

[0042] S1: Mix nickel nitrate and chromium nitrate in an oxide-based mass ratio of 20:0.5 and dissolve them in water to prepare a mixed solution with a mass fraction of 10%;

[0043] S2: Immerse the S-1 molecular sieve into the prepared sodium hydroxide solution with a mass fraction of 25%, treat it in a closed hydrothermal reaction kettle at 200°C for 24h, and wash it with pure water until the pH of the eluate is 7. Dry in an oven at 90°C for 8 hours for later use;

[0044] S3: Mix the mixed solution prepared in step S1 with the S-1 molecular sieve treated in step S2 at a mass ratio of 20.5:79.5 in terms of oxides, let it stand for 8 hours, dry it in an oven at 90°C, and then place it in a muffle Baking at 700°C for 24 hours in a furnace;

[0045] S4: Heat the catalyst powder obtained in step S3 in an atmosphere with a hydrogen-nitroge...

Embodiment 3

[0047] The mass ratio of each component ZSM-5:NiO:CuO is 98:1:1, and the metal salt is calculated as the corresponding oxide.

[0048] S1: Mix nickel nitrate and copper nitrate in an oxide-based mass ratio of 1:1 and dissolve them in water to prepare a mixed solution with a mass fraction of 10%;

[0049] S2: Immerse the ZSM-5 molecular sieve in the prepared potassium hydroxide solution with a mass fraction of 10%, treat it in a closed hydrothermal reaction kettle at 130°C for 20h, and wash it with pure water until the pH of the eluate is 7. Dry in an oven at 90°C for 8 hours for later use;

[0050] S3: Mix the mixed solution prepared in step S1 with the ZSM-5 molecular sieve treated in step S2 at a mass ratio of 2:98 in terms of oxides, let it stand for 8 hours, dry it in an oven at 90°C, and then place it in a muffle Roasting in the furnace at 500°C for 12h;

[0051] S4: Heat the catalyst powder obtained in step S3 for 6 hours in an atmosphere with a hydrogen-nitrogen volum...

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PUM

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Abstract

The invention provides a nickel-based molecular sieve catalyst and a preparation method of same. The nickel-based molecular sieve catalyst includes: a component (A): a molecular sieve carrier, a component (B): nickel metal, and a component (C): including one or more selected from the following metals: Mg, Ca, Cr, Bi, Ce, Sn, Cd and Cu, wherein the metals in the components (B) and (C) are supported on a framework structure of the component (A) in the form of metal oxides; the component (B) and the component (C) are respectively measured by mass of the metal oxides; and the mass ratio of the component (A), the component (B) to the component (C) is (75-98):(1-20):(0.5-10). The nickel-based molecular sieve catalyst is produced through a chemical method and has uniform distribution of active components. The catalyst is high in conversion rate of adiponitrile and selectivity of hexanediamine when being sued for catalyzing the adiponitrile to produce the hexanediamine.

Description

technical field [0001] The invention belongs to the technical field of petrochemical catalysis, and in particular relates to a nickel-based molecular sieve catalyst and a preparation method thereof. Background technique [0002] Raney catalyst is a widely used reduction catalyst, mainly used in the catalytic hydrogenation of organic compounds. According to the different metal active centers, there are Raney iron, Raney cobalt, Raney nickel, etc. Among them, the Raney nickel catalyst with nickel as the active center is the most widely used. For example, hexamethylenediamine is used as a monomer for the production of nylon-66. At present, adiponitrile is mainly used as a raw material, and Raney nickel catalyst is used to prepare it in a tank reactor or a fluidized bed reactor. At present, the main problems of this catalyst are low activity and selectivity, large amount of catalyst, and serious environmental pollution. Therefore, it is necessary to develop new and more efficie...

Claims

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Application Information

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IPC IPC(8): B01J29/89B01J29/035B01J29/46B01J29/48B01J29/80
CPCB01J29/0358B01J29/46B01J29/48B01J29/80B01J29/89
Inventor 刘文庄大为杨琦武张媛
Owner CHINA TIANCHEN ENG
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