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Suspended bed hydrogenation multicomponent composite iron-based catalyst and preparation method thereof

An iron-based catalyst and multi-component composite technology, which is applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, preparation of liquid hydrocarbon mixtures, etc., can solve the problem of reduced iron usage, limited catalyst activity, Catalytic activity limitation and other problems, to achieve the effect of good dispersion, flexible composition of active components, and excellent catalytic performance

Active Publication Date: 2019-11-19
李大鹏
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Compared with industrial waste residue and natural ore catalysts, the dispersion of the active components of the above two catalysts is significantly improved, and the amount of iron used is significantly reduced. However, the catalysts are dominated by a single active component of iron, and the catalytic activity is still poor.
Patent CN104888797A discloses a FeOOH catalyst containing a structural aid and a second active element. The catalyst structure is doped with other components, but without a carrier, it is not easy to be effective in the suspension bed hydrogenation reaction system. spread out, the catalytic activity is limited
Patent CN104096563A discloses a FeOOH supported catalyst containing structural aids, patent 106732606A discloses a FeOOH supported catalyst doped with Ni, Co second active elements and Al, Zn structural aids, the above two patents Both have a certain effect on improving the dispersion of FeOOH catalyst active components and catalyst activity, but all use FeOOH as the main active component. Although the second active metal is doped, the catalyst activity is still limited and still needs to be improved.

Method used

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  • Suspended bed hydrogenation multicomponent composite iron-based catalyst and preparation method thereof
  • Suspended bed hydrogenation multicomponent composite iron-based catalyst and preparation method thereof
  • Suspended bed hydrogenation multicomponent composite iron-based catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] In terms of carrier, according to the loading of metal elements in Mg-Ni-Fe hydrotalcite as 5%, element molar ratio Mg:Ni:Fe=1:1:2, 0.23g MgSO 4 , 0.49g NiSO 4 ·6H 2 O, 1.03g FeSO 4 ·7H 2 O was dissolved in 75mL of deionized water, and then 6g of activated carbon with a particle size distribution of 400μm~2mm was added to the resulting solution, and the flow rate was 0.25m 3 At the same time, gradually add 0.25mol / L potassium hydroxide aqueous solution and 0.25mol / L sodium carbonate aqueous solution, control the pH of the reaction solution=6.5, stir and react at 60°C for 2 hours, filter with suction and keep at a constant temperature of 100°C Dry in a drying oven to obtain an activated carbon-supported Mg-Ni-Fe hydrotalcite catalyst.

Embodiment 2

[0023] Based on the support, according to the loading of metal elements in the Co-Zn-Fe-Al hydrotalcite as 3%, the element molar ratio Co:Zn:Fe:Al=1:0.5:0.5:0.5, 0.149g Co(NO 3 ) 2 ·6H 2 O, 0.076g Zn(NO 3 ) 2 ·6H 2 O, 0.096g Al(NO 3 ) 3 9H 2 O, 0.033g FeCl 2 Dissolve in 75mL of deionized water, then add 2.8g of blue carbon with a particle size distribution of 50-500μm to the resulting solution, and pass it in at a flow rate of 0.5m 3 Oxygen per hour, at the same time gradually add 0.25mol / L sodium hydroxide aqueous solution, control the pH of the reaction solution = 8.0, stir and react at 30°C for 2 hours, filter with suction and dry in a constant temperature drying oven at 100°C to obtain blue carbon loaded Co-Zn-Fe-Al hydrotalcite catalyst.

Embodiment 3

[0025]In terms of carrier, according to the loading of metal elements in Co-Fe-Mo hydrotalcite as 5%, element molar ratio Co:Fe:Mo=1:1:1, 0.63kg FeSO 4 ·7H 2 O, 0.63kg CoSO 4 ·7H 2 O, 0.61kg MoCl 5 Dissolve it in 35L deionized water, then transfer the resulting solution into a 50L reactor, add 9.4kg of coal powder with a particle size distribution of 5-150μm into the reactor, and feed it with a flow rate of 2m 3 / h of air, while gradually adding 1 mol / L ammonia solution, controlling the pH of the reaction solution to 8.5, stirring and reacting at 35°C for 3 hours, centrifugal dehydration and drying in a constant temperature drying oven at 130°C to obtain Co- Fe-Mo hydrotalcite catalyst.

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Abstract

The invention discloses a suspended bed hydrogenation multicomponent composite iron-based catalyst and a preparation method thereof. The catalyst uses layered bimetallic hydroxide Fe<3+> based hydrotalcite as an active component and uses at least one of coal powder, semi-coke and a porous carbon material as carriers. The composition of the active component is [(M<2+>)1-x(Fe<3+>M<e+>)x(OH)<2>]<X+>(A<n->)x / n.mH2O]<x->, wherein the M<2+> is one or more of Mg<2+>, Zn<2+>, Cu<2+>, Ni<2+>, Co<2+>, Ca<2+>, Mn<2+> and Fe<2+>, the M<e+> is 0-3 of Al<3+>, Co<3+>, Cr<3+>, Ti<3+> and Mo<5+>, the A<n-> is1-3 of OH<->, SO4<2->, NO3<->, CO3<2-> and Cl<->, 0.2<=x<=0.33, and m=0-10. The catalyst of the invention uses the Fe<3+> based hydrotalcite as the active component, the active component is uniformlydistributed on the surfaces of the carriers, and so the dispersion is better and the activity of the catalyst is higher. Moreover, the catalyst has the advantages of mild preparation conditions, simple preparation process and low raw material cost. The composition of the active component is flexible and changeable and can be flexibly adjusted according to needs of a suspended bed hydrogenation process and products.

Description

technical field [0001] The invention belongs to the technical fields of petroleum processing and coal chemical industry, and in particular relates to a high-activity multi-element composite iron-based catalyst applied to a suspension bed hydrogenation reaction (also called a slurry bed hydrogenation reaction) and a preparation method thereof. Background technique [0002] Suspended bed hydrogenation technology has a long history. Since Germany applied it in the field of coal-to-oil during World War II, the technology has been continuously updated and iterated. At present, the suspended bed hydrogenation technology has been widely used in the field of lightening heavy and inferior oil, the field of direct coal to oil, the field of kerosene co-refining (or the field of coal and oil co-processing, or the field of coal and oil co-hydrogenation) and the field of coal tar The field of hydrogenation technology, etc., involves two important aspects of energy and chemical industry, p...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/755B01J23/80C10G1/08
CPCB01J23/78B01J23/80B01J23/755C10G1/086B01J35/399
Inventor 李大鹏黄传峰蒋中山
Owner 李大鹏
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