Unlock instant, AI-driven research and patent intelligence for your innovation.

Molybdenum carbide-molybdenum oxide catalyst, and preparation method and application thereof

A molybdenum carbide and catalyst technology, which is applied in the field of molybdenum carbide-molybdenum oxide catalyst and its preparation, can solve the problems of high cost and harsh reaction conditions, and achieve the effect of enhancing the activity of metal breaking carbon-carbon bonds and changing the distribution of electronic states

Active Publication Date: 2021-07-23
GUANGDONG UNIV OF TECH
View PDF6 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In view of this, the application provides a molybdenum carbide-molybdenum oxide catalyst and its preparation method and application, which can effectively solve the existing problem of selective hydrogenation hydrolysis of biomass The technical problems of harsh reaction conditions and high cost in the method of producing n-hexanol

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Molybdenum carbide-molybdenum oxide catalyst, and preparation method and application thereof
  • Molybdenum carbide-molybdenum oxide catalyst, and preparation method and application thereof
  • Molybdenum carbide-molybdenum oxide catalyst, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0054] The embodiment of the present application provides a molybdenum carbide-molybdenum oxide catalyst, the preparation method comprising:

[0055] 1. 10g ammonium paramolybdate (NH 4 ) 6 Mo 7 o 24 4H 2 O was loaded into a 200ml crucible, heated to 500°C in a muffle furnace at a rate of 10°C / min and kept at this temperature for 4h to prepare MoO 3 .

[0056] Get the 2.4000g MoO obtained above 3 Put 150ml / min of 20% CH 4 / H 2 in a quartz tube. Then it was heated from room temperature (RT) to 300°C at a rate of 5°C / min, then increased from 300°C to 700°C at a rate of 1°C / min, and kept at 700°C for 2 h. Cooling to room temperature yields Mo 2 C precursor. Take Mo 2 C precursor in 1% O at 15ml / min 2 / Ar gas passivation at 350°C for 2 hours and recorded as MoO x -Mo 2 c.

[0057] 2. Take 6.5g of MoO prepared in step 1 x -Mo 2 C was added to 3.5135ml of ruthenium trichloride solution containing 3.7wt% Ru, soaked for 10h, dried at 100°C for 10h, calcined at 350°C ...

Embodiment 2

[0059] The embodiment of the present application provides a molybdenum carbide-molybdenum oxide catalyst, the preparation method comprising:

[0060] 1. 10g ammonium paramolybdate (NH 4 ) 6 Mo 7 o 24 4H 2 O was loaded into a 200ml crucible, heated to 500°C in a muffle furnace at a rate of 10°C / min and kept at this temperature for 4h to prepare MoO 3 .

[0061] Get the 0.8000g MoO obtained above 3 NH at 150mL / min 3 Under the atmosphere, the temperature was programmed to rise to 700°C at 5°C / min and kept for 2h for ammoniation treatment. Cool to room temperature. Switch the reaction atmosphere to 20% CH at 150mL / min 4 / H 2 Mix the atmosphere, set the temperature rise program at 5°C / min to 700°C and keep it for 2h. Cool down to room temperature to obtain a MoC catalyst sample. Take the MoC catalyst sample at 15ml / min1%O 2 / Ar atmosphere at 5°C / min to 350°C and keep it for 2h as MoO x -MoC.

[0062] 2. Take 6.5g of MoO prepared in step 1 x -Mo 2 C was added to 3.5...

Embodiment 3

[0098] The embodiment of the present application provides an activity evaluation test using Cat1-Cat12 to catalyze the hydrodeoxygenation reaction of sorbitol. The method includes:

[0099] This embodiment uses Cat1~Cat12 as the activity evaluation of the catalyst: it is carried out in a continuous high-pressure fixed-bed reactor, and the Cat1~Cat12 catalyst loading is 5g, H 2 The flow rate is 30ml / min, the solution injection flow rate is 0.02ml / min, 20wt% sorbitol solution, the reaction pressure is 4MPa, and the reaction temperature is 250°C. The conversion rate of sorbitol was detected by HPLC (Waterse2695), the gas phase product was detected by online gas chromatography flame ionization detector (FID) and thermal conductivity detector (TCD), and the water phase and oil phase collected at 30 ° C were detected by GC ( Shimadzu GC-2030Pro). The test results are shown in Table 1.

[0100] Table 1 Activity evaluation results of different catalysts for sorbitol aqueous phase hy...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
thicknessaaaaaaaaaa
Login to View More

Abstract

The invention belongs to the technical field of catalysts, and particularly relates to a molybdenum carbide-molybdenum oxide catalystm and a preparation method and application thereof. The molybdenum carbide-molybdenum oxide catalyst comprises molybdenum carbide and amorphous MoOx compounded on the surface of the molybdenum carbide, wherein x is a natural number ranging from 0 to 3; the thickness of the MoOx is 2 to 10 nm; and the molybdenum carbide is selected from Mo2C or MoC. The preparation method of the catalyst comprises the following steps: carrying out oxidation treatment on molybdenum carbide to obtain molybdenum carbide-MoOx; calcining the molybdenum carbide-MoOx in an inert atmosphere to obtain an initial catalyst; and carrying out a reduction reaction on the initial catalyst to obtain the molybdenum carbide-molybdenum oxide catalyst. According to the molybdenum carbide-molybdenum oxide catalyst, and the preparation method and application thereof, the technical problems of harsh reaction conditions and high cost in the existing method for producing n-hexanol through selective hydrogenation and hydrolysis of biomass are effectively solved.

Description

technical field [0001] The application belongs to the technical field of catalysts, and in particular relates to a molybdenum carbide-molybdenum oxide catalyst and its preparation method and application. Background technique [0002] N-hexanol is a straight-chain higher alcohol with a six-carbon chain, an important chemical raw material or intermediate, widely used in perfumery, food, textile and polymer industries. The industrial production of n-hexanol still relies on petroleum-based production routes involving the synthesis of Ziegler alcohols, hydroformylation of n-pentene and subsequent hydrogenation. Such industrial syntheses involve multi-step synthesis, complex separation procedures, and harsh reaction conditions, making current methods neither sustainable nor environmentally friendly. In recent years, a biosynthetic method for the synthesis of n-hexanol from glucose using microbial engineering has been developed by extending the carbon chain length of n-butanol. H...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/22B01J23/652B01J23/28B01J23/883B01J23/881B01J23/882B01J23/885B01J37/08B01J37/14B01J37/02B01J37/18C07C29/132C07C31/125
CPCB01J27/22B01J23/6525B01J23/28B01J23/883B01J23/881B01J23/882B01J23/885B01J37/088B01J37/084B01J37/14B01J37/0201B01J37/18C07C29/132C07C31/125Y02P20/54Y02P20/52
Inventor 王铁军陈新仇松柏郑燕妮张浅
Owner GUANGDONG UNIV OF TECH