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Industrial naphthalene selective hydrogenation catalyst and preparation method thereof

A hydrogenation catalyst, naphthalene selectivity technology, applied in catalyst activation/preparation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of increasing processing cost, affecting the yield of refined naphthalene, The problem of multiple hydrogen raw materials, etc., achieves the effect of good hydrogenation activity, stable activity and improved yield.

Active Publication Date: 2022-01-28
NINGBO INST OF MATERIALS TECH & ENG CHINESE ACADEMY OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] It can be seen that the problem existing in the prior art is the generation of tetralin by-products, thus affecting the yield of refined naphthalene, although adopting the method of tetralin circulation makes up some yields to a certain extent, but consumes More hydrogen feedstock is added, which increases processing costs

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  • Industrial naphthalene selective hydrogenation catalyst and preparation method thereof

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preparation example Construction

[0038] The preparation method of a kind of industrial naphthalene selective hydrogenation catalyst provided by an aspect of the embodiment of the present invention comprises:

[0039]1) First prepare the carbon nanotube dispersion;

[0040] 2) mixing aluminum oxide with the carbon nanotube dispersion obtained in step 1) and then extruding into strips, followed by drying and roasting to obtain the carrier;

[0041] 3) Add the nonionic surfactant used in step 2) to the aqueous solution of the precursor of the metal active component to form a mixed solution, the precursor of the metal active component is selected from the group consisting of Group VIB and / or Group VIII metals A water-soluble compound of an element, the metal active component is selected from metal oxides, and then the carrier obtained in step 2) is impregnated in the mixed solution, followed by drying and roasting to obtain the selective hydrogenation catalyst.

[0042] In some embodiments, the industrial cataly...

Embodiment 1

[0062] (1) Preparation of modified carrier

[0063] Take 100g of small-pore alumina (commercially available ordinary small-pore alumina powder with a pore volume of 0.3-0.6ml / g), 60g of the aforementioned carbon nanotube dispersion, and 4g of turnip powder are mixed evenly, and then add 50ml of lemon-containing An aqueous solution of 2 g of acid was kneaded, extruded, dried at 100°C for 5 hours, and then calcined at 600°C for 3 hours to obtain a strip carrier.

[0064] (2) Preparation of catalyst:

[0065] a, the preparation of the metal impregnating solution is as mentioned above, take the tungsten-nickel solution (WO 3 Content 20.0g / 100ml, NiO content 7.0g / 100ml) 40ml, add polyethylene glycol octyl phenyl ether Triton X-100, the addition amount is about 6g, and make an aqueous solution;

[0066] b. Take 100 g of the modified carrier prepared in step (1), add it to the prepared aqueous solution (which contains metal ions) for impregnation, and filter;

[0067] c. Place the...

Embodiment 2

[0071] (1) Preparation of carrier

[0072] Take 100g of small-pore alumina (commonly available commercially available small-pore alumina powder with a pore volume of 0.3-0.6ml / g), 36g of carbon nanotube dispersion, and 3g of turnip powder are mixed evenly, and then add 50ml of citric acid 1.5g of aqueous solution was kneaded, extruded, dried at 120°C for 3 hours, and then calcined at 500°C for 4 hours to obtain a strip carrier.

[0073] (2) Preparation of catalyst:

[0074] a, the preparation of the metal impregnating solution is as mentioned above, take the tungsten-nickel solution (WO 3 content of 10.0g / 100ml, NiO content of 10.0g / 100ml) 40ml, add polyethylene glycol octyl phenyl ether Triton X-100, the addition amount is about 8g, and make an aqueous solution; b, take 100g of the preparation in step (1) The obtained carrier is added to the prepared aqueous solution (which contains metal ions) for impregnation, and filtered;

[0075] c. Place the product obtained in step ...

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Abstract

The invention discloses an industrial naphthalene selective hydrogenation catalyst and a preparation method thereof. The catalyst includes a metal active component and a modified support that supports the metal active component. The support is mainly formed by kneading, forming, drying and calcining carbon nanotubes and alumina. The metal active component includes Metal oxides, the metal oxides contain metal elements of Group VIB and / or Group VIII. In the catalyst, the pores with a pore diameter of 8-10 nm account for more than 90% of the total pore volume, the pore volume is 0.6-0.8ml / g, and the specific surface area is 240-300m 2 / g. Compared with the prior art, the catalyst provided by the present invention has the advantages of concentrated ideal pore size distribution, suitable pore volume, and large specific surface area, and has good selective hydrogenation activity for sulfur-containing impurities in industrial naphthalene-thianaphthene, and is suitable for industrial naphthalene. Selective hydrogenation to produce refined naphthalene.

Description

technical field [0001] The invention relates to a selective hydrogenation catalyst, in particular to a selective hydrogenation catalyst for producing refined naphthalene from industrial naphthalene, that is, a selective hydrogenation catalyst for sulfur compounds in industrial naphthalene, heavy benzene naphthalene or crude naphthalene. Background technique [0002] Naphthalene is an important chemical raw material, mainly used for catalytic oxidation of phthalic anhydride and dye intermediates, and also used as cement water reducer, surfactant, plasticizer, polyester, synthetic fiber and medicine. More than 70% of domestic naphthalene depends on the coking industry. The technology of producing industrial naphthalene from coal tar is very mature, but the purity of industrial naphthalene is only 95%, which cannot meet its requirements as a raw material for fine chemicals. Fine chemical products produced with naphthalene as raw material All products require refined naphthalene...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/888B01J35/10B01J37/02C07C15/24C07C7/163
CPCB01J23/888B01J23/002B01J37/0207B01J37/0201C07C7/163B01J2523/00B01J35/635B01J35/647B01J35/615C07C15/24B01J2523/31B01J2523/69B01J2523/847
Inventor 尹宏峰许杰
Owner NINGBO INST OF MATERIALS TECH & ENG CHINESE ACADEMY OF SCI