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Preparation method of roasting-free pre-vulcanized hydrogenation catalyst

A hydrogenation catalyst, catalyst technology, applied in catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of low activity phase I and uneven dispersion of active components , the problem of high cost, to achieve the effect of increasing the number of active centers, excellent hydrogenation activity, and reducing the interaction

Inactive Publication Date: 2017-11-17
湖北润驰环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

On the one hand, when the oxidized active component is used as the precursor, the precursor and Al 2 o 3 The surface often has a strong interaction, which easily leads to uneven dispersion of the active component on the surface of the carrier, and at the same time leads to the formation of too many Al-O-Mo chemical bonds, which in turn makes it difficult to completely vulcanize the active component and form too many low-activity I phases at the same time. Low active metal utilization
In addition, taking the preparation of Mo-based catalysts as an example, the commonly used precursor ion Mo 7 o 24 6- tends to induce Al 2 o 3 Surface dissociation produces Al 3+ , and subsequently react with it to form an Anderson-type heteropolyanion Al(OH) 6 Mo 6 o 18 3- , after calcination, it is difficult to be fully vulcanized and large-grained MoO is not conducive to the improvement of catalytic activity. 3 and Al 2 (MoO 4 ) 3 species, therefore, it is difficult to achieve both high activity and high sulfidation of hydrogenation catalysts by traditional impregnation technology, resulting in unsatisfactory catalytic activity
[0004] At present, the pre-sulfurization process in the preparation technology adopts the in-vehicle vulcanization technology. The catalyst in the oxidation state is loaded into the hydrogenation reactor, and then hydrogen and sulfurizing agents are introduced into the reactor during the process of continuous heating for vulcanization. The technology is still the most widely used technology at present, but it still has a series of problems: (1) the curing time is long; (2) the curing agent is flammable and toxic, and is not friendly to the environment; (3) the operation process is complicated and the cost is high, etc.
This method can improve sulfur holding rate and catalyst activity, but further improvement is needed

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Take 10g of basic nickel carbonate and 20g of molybdenum trioxide, add a certain amount of phosphoric acid and heat to dissolve, then add butanol and citric acid to adjust the solution to clarify, at this time, the pH is 2.5, then add 100g of alumina carrier for impregnation, after impregnation, dry at 180°C for 6 hours for later use , which is catalyst A. Wherein NiO content is 4.5wt%, MoO 3 The content is 20%, the amount of butanol is 0.5 times of the total amount of Ni+Mo metal, and the amount of citric acid is 0.5 times of the total amount of Ni+Mo metal.

[0025] Disperse sulfur powder and additive ethanolamine in the solvent of catalytic diesel oil, keep the temperature at 120°C for 2 hours, the amount of solvent used is 20% of the weight of the catalyst, the amount of sulfur used is 1.1 times the theoretical amount of sulfur required by the catalyst containing metal, and the amount of ethanolamine used is 20% of the weight of the solvent 5%, add the above-prepar...

Embodiment 2

[0027] Take 9.50g of nickel nitrate and 23.5g of ammonium metatungstate, heat and dissolve, add sorbitol and aminotriacetic acid to adjust the solution to clarify, at this time the pH is 3.0, then add 100g of alumina carrier for impregnation, after impregnation, dry at 220°C for 4 hours for later use, that is For Catalyst B. Wherein NiO content is 5wt%, WO 3 The content is 20%, the amount of sorbitol is 1 times of the total amount of Ni+W metal, and the amount of citric acid is 1 time of the total amount of Ni+W metal.

[0028] Disperse sulfur powder and additive DPTT in a biodiesel solvent, keep the temperature at 125°C for 3 hours, the amount of solvent is 10% of the weight of the catalyst, the amount of sulfur is 1.2 times the theoretical sulfur content of the catalyst containing metal, and the amount of DPTT is 1% of the weight of the solvent 8%, add the above-prepared catalyst B into this solvent and stir at a constant temperature of 125°C for 2 hours, then raise the tem...

Embodiment 3

[0030] Take 8g of basic nickel carbonate and 17.6g of molybdenum trioxide, add a certain amount of phosphoric acid to heat and dissolve, then add 19.6g of ammonium metatungstate, then add trimethylolethane and malic acid to adjust the solution to clarify, at this time the pH is 2.2, then add 100g The alumina carrier is impregnated, and dried at 250°C for 3 hours after impregnation, which is Catalyst C. . Wherein NiO content is 4.0wt%, MoO 3 The content is 17.0%, WO 3 The content is 16.7%, the amount of trimethylolethane is 0.2 times of the total amount of Ni+Mo+W metals, and the amount of malic acid is 2 times of the total amount of Ni+Mo+W metals.

[0031] Disperse sulfur powder and additive TMTD in a solvent of vegetable oil, keep the temperature at 130°C for 2.5 hours, the amount of solvent is 5% of the weight of the catalyst, the amount of sulfur is 1.4 times the theoretical amount of sulfur required by the catalyst containing metal, and the amount of TMTD is 5% of the w...

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Abstract

The invention discloses a preparation method of a roasting-free pre-vulcanized hydrogenation catalyst. The method comprises the steps that the environment-friendly dipping technology is adopted for preparing the hydrogenation catalyst, after the dipped catalyst is treated under the temperature of 180-250 DEG C, an organic solvent, elemental sulfur and auxiliaries are added to be mixed to be uniform, and thermal treatment is performed to obtain the roasting-free pre-vulcanized hydrogenation catalyst. The method solves the problems that a conventional catalyst is low in activity, poor in dispersity, long in vulcanization on-stream time and high in operation cost, and meanwhile overcomes the defects that the vulcanized catalyst preparation process is complex and concentrated heat release is easy. The pre-vulcanized hydrogenation catalyst prepared through the method is high in strength, good in activity and short in preparation process flow and has the good application value.

Description

technical field [0001] The invention relates to the technical field of catalysts, in particular to a method for preparing a roasting-free presulfided hydrogenation catalyst, which belongs to the improvement of the method for preparing a hydrogenation catalyst. . Background technique [0002] Hydrogenation catalysts generally consist of Group VIII metals and Group VIB metals or metal oxides with hydrogenation functions, and supports and additives with certain acidic functions. Among them, the Group VIII metals are mainly Ni or Co, the Group VIB metals are mainly Mo and W, and the additives in the catalyst may contain P, Si, F, B and other components. Generally, the catalyst metal component obtained in the production process exists in an oxidized state after being roasted, and in the hydrogenation reaction process, the active metal component of the catalyst has higher reactivity when it is in a sulfurized state. Therefore, the catalyst is used It needs to be pre-vulcanized b...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/883B01J23/888B01J23/882B01J37/20
CPCB01J23/002B01J23/882B01J23/883B01J23/888B01J23/8885B01J37/20B01J2523/00B01J2523/847B01J2523/68B01J2523/31B01J2523/69B01J2523/845
Inventor 张先茂陈宗杰王国兴王泽吴阳春王栋斌夏大寒瞿玖王瑜陈凯
Owner 湖北润驰环保科技有限公司
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