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precious metal decorated mo 2 Preparation method of n/omc catalyst and its application in hydrodeoxygenation of biomass oil

A technology of biomass oil and catalyst, which is applied in the direction of physical/chemical process catalysts, chemical instruments and methods, and preparation of liquid hydrocarbon mixtures, etc. It can solve the problems of complex composition of biomass oil, large reactant molecules, and catalyst deactivation. Achieve high stability, high specific surface area, promote adsorption and reaction

Active Publication Date: 2022-06-17
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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  • precious metal decorated mo  <sub>2</sub> Preparation method of n/omc catalyst and its application in hydrodeoxygenation of biomass oil
  • precious metal decorated mo  <sub>2</sub> Preparation method of n/omc catalyst and its application in hydrodeoxygenation of biomass oil

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Experimental program
Comparison scheme
Effect test

Embodiment 1

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

Embodiment 2

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

Embodiment 3

[0035] 3.0g of F127 was added to 40ml of the mixed solution composed of absolute ethanol and water with a volume ratio of 5:1, and after stirring for 1h, 1g of resorcinol was added, and the stirring was continued for 2h, and then 0.3g of (NH) was added. 4 ) 6 Mo 7 O 24 ·4H 2 O, stir for 0.5h, then add 4g of urea, and dropwise add 0.5g of concentrated HCl, and continue to stir for 1h to form green color. 5g of 37% formaldehyde was added dropwise and stirred for 2h. The mixed solution was sealed and allowed to stand for 7d, the solution was separated into layers, the upper layer of clear colorless solution was poured out, and the lower layer was green wet gel, and then placed at room temperature for 36h and dried at 110°C 4d, get dry gel. Then, the temperature was raised to 600°C at a temperature rate of 3°C / min under a nitrogen atmosphere, and the temperature was maintained for 4 h to obtain a catalyst precursor. Then, 0.102 g of palladium chloride was dissolved in the hyd...

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Abstract

The invention belongs to the field of catalysts, in particular to a noble metal-modified Mo 2 The preparation method of the N / OMC catalyst and its application in the hydrodeoxygenation of biomass oil, the large ordered pores of the OMC carrier in the catalyst can make the macromolecular reactant diffuse to the active center for reaction easily, and the large specific surface area is beneficial High dispersion of active components; while the active component Mo 2 N is embedded in the pore wall of OMC, which improves the stability of the active components and avoids the sintering and inactivation of the active components during the reaction process. The weak acidity of OMC reduces the carbon deposition in the reaction process and improves the stability of the catalyst, noble metals and Mo 2 The N interaction improves the activation ability of hydrogen, reduces the possibility of catalyst oxidation and carbon deposition, and improves the reactivity and stability of the catalyst. The catalyst has long service life, high conversion rate of reactants 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, and in particular relates to a precious metal modified Mo 2 Preparation method of N / OMC catalyst and its application in biomass oil hydrodeoxygenation. Background technique [0002] Lignin is the most abundant renewable aromatic polymer in nature and can be used to produce 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, the lignin must first be converted into biomass oil by the method of pyrolysis. However, biomass oil obtained by pyrolysis of lignin has disadvantages such as high oxygen content (close to 50 wt%), low calorific value, high viscosity and corrosiveness, and cannot be directly used for motor vehicle fuel. Therefore, biomass oil must be improved in quality by deoxygenation before it can be used as a fuel for an e...

Claims

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Application Information

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