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Preparation method of noble metal-modified Mo2N/OMC catalyst and application of noble metal-modified Mo2N/OMC catalyst in hydrodeoxygenation of biomass oil

A catalyst and precious metal technology, which is used in the preparation of Mo2N/OMC catalyst and the application field of biomass oil hydrodeoxygenation, can solve the problems of complex biomass oil composition, large reactant molecules, catalyst deactivation, etc., and achieve high stability properties, high specific surface area, and the effect of promoting adsorption and reaction

Active Publication Date: 2020-06-05
CHANGZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Because the model compound has a single reactant, less impurities, the reaction is relatively simple, and the catalyst activity and selectivity are relatively good, but the actual lignin-converted biomass oil has a complex composition, relatively large reactant molecules, and many impurities, which easily lead to catalyst deactivation.

Method used

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  • Preparation method of noble metal-modified Mo2N/OMC catalyst and application of noble metal-modified Mo2N/OMC catalyst in hydrodeoxygenation of biomass oil
  • Preparation method of noble metal-modified Mo2N/OMC catalyst and application of noble metal-modified Mo2N/OMC catalyst in hydrodeoxygenation of biomass oil

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Add 5.0 g of F127 to 40 ml of a mixture of absolute ethanol and water at a volume ratio of 1:1, and stir for 1 h, then add 3.3 g of resorcinol, continue stirring for 2 h, and then add 0.3 g of (NH 4 ) 6 Mo 7 o 24 4H 2O, stirred for 0.5h, then added 2g of urea, and added dropwise 0.5g of concentrated HCl, and continued stirring for 1h to form a green color. Add 5g of 37% formaldehyde dropwise and stir for 2h. Seal the mixed solution and let it stand for 7d. The solution is layered. The clear colorless solution in the upper layer is poured out, and the lower layer is a green wet gel. After standing at room temperature for 24h, dry at 85°C 7d, get xerogel. Then, the temperature was raised to 600° C. at a rate of 3° C. / min under a hydrogen atmosphere, and the temperature was maintained for 4 hours to obtain a catalyst precursor. Then 0.102 g of palladium chloride was dissolved in hydrochloric acid solution, and added dropwise to the catalyst precursor, soaked for 10 h,...

Embodiment 2

[0032] Add 5.0 g of F127 to 40 ml of a mixture of absolute ethanol and water at a volume ratio of 3:1, and stir for 1 h, then add 5 g of resorcinol, continue stirring for 2 h, and then add 0.3 g of (NH 4 ) 6 Mo 7 o 24 4H 2 O, stirred for 0.5h, then added 4g of urea, and added dropwise 2g of concentrated HCl, and continued stirring for 1h to form a green color. Add 5g of 37% formaldehyde dropwise and stir for 2h. Seal the mixed solution and let it stand for 7d. The solution is layered. The clear colorless solution in the upper layer is poured out, and the lower layer is a green wet gel. After standing at room temperature for 24h, dry at 85°C 7d, get xerogel. Then, the temperature was raised to 600° C. at a rate of 3° C. / min under a nitrogen atmosphere, and the temperature was maintained for 4 hours to obtain a catalyst precursor. Then 0.102 g of palladium chloride was dissolved in hydrochloric acid solution, and added dropwise to the catalyst precursor, soaked for 10 h, an...

Embodiment 3

[0035] Add 3.0 g of F127 to 40 ml of a mixture of absolute ethanol and water at a volume ratio of 5:1, and stir for 1 h, then add 1 g of resorcinol, continue stirring for 2 h, and then add 0.3 g of (NH 4 ) 6 Mo 7 o 24 4H 2 O, stirred for 0.5h, then added 4g of urea, and added dropwise 0.5g of concentrated HCl, and continued stirring for 1h to form a green color. Add 5g of 37% formaldehyde dropwise and stir for 2h. Seal the mixed solution and let it stand for 7d. The solution is layered. The clear colorless solution in the upper layer is poured out, and the lower layer is a green wet gel. After standing at room temperature for 36h, dry at 110°C 4d, get xerogel. Then, the temperature was raised to 600° C. at a rate of 3° C. / min under a nitrogen atmosphere, and the temperature was maintained for 4 hours to obtain a catalyst precursor. Then 0.102 g of palladium chloride was dissolved in hydrochloric acid solution, and added dropwise to the catalyst precursor, soaked for 10 h,...

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Abstract

The invention belongs to the field of catalysts, and relates to a preparation method of a noble metal-modified Mo2N / OMC catalyst and an application of the noble metal-modified Mo2N / OMC catalyst in hydrodeoxygenation of biomass oil, macromolecular reactants can be easily diffused to an active center for reaction by virtue of large ordered pores of an OMC carrier in the catalyst, and high dispersionof active components is facilitated by virtue of a large specific surface area; and the active component Mo2N is embedded in the pore wall of the OMC, so that the stability of the active component isimproved, and the inactivation of the active component due to sintering in the reaction process is avoided. The weak acidity of the OMC reduces carbon deposition in the reaction process and improvesthe stability of the catalyst, the noble metal and Mo2N interact with each other, the hydrogen activation capacity is improved, the possibility that the catalyst is oxidized and subjected to carbon deposition is reduced, and the reaction activity and stability of the catalyst are improved. The catalyst has the advantages of long service life, high reactant conversion rate and high selectivity to aromatic ring products in the hydrodeoxygenation reaction process of biomass oil converted from lignin.

Description

technical field [0001] The invention belongs to the technical field of catalysts, in particular to a precious metal-modified Mo 2 Preparation method of N / OMC catalyst and its application in hydrodeoxygenation of biomass oil. Background technique [0002] Lignin is the most abundant renewable aromatic polymer in nature for the production of biofuels and high value-added chemicals. In the petroleum-based modern energy and chemical industries, lignin has shown good application prospects as an alternative raw material. To realize the utilization of lignin, lignin must first be converted into biomass oil by pyrolysis. However, the biomass oil produced by pyrolysis of lignin has the disadvantages of high oxygen content (close to 50wt%), low calorific value, high viscosity and corrosiveness, and cannot be directly used as motor vehicle fuel. Therefore, biomass oil must be deoxidized to improve its quality before it can be used as a fuel for engines. [0003] Among various upgra...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/24B01J35/02B01J35/10C10G3/00
CPCB01J27/24C10G3/48C10G3/44C10G3/50B01J35/40B01J35/61Y02P30/20
Inventor 鲁墨弘张朋李明时张伟
Owner CHANGZHOU UNIV