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Catalyst composition for preparing ethylene glycol from biomass raw materials as well as preparation method and application of catalyst composition

A technology of biomass raw materials and catalysts, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problems of non-renewable and limited storage of fossil resources, etc. Achieve the effects of accelerated transformation, high hydrothermal stability, and broad application prospects

Active Publication Date: 2021-03-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At the same time, both routes rely on fossil resources, but the storage of fossil resources is limited and non-renewable

Method used

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  • Catalyst composition for preparing ethylene glycol from biomass raw materials as well as preparation method and application of catalyst composition
  • Catalyst composition for preparing ethylene glycol from biomass raw materials as well as preparation method and application of catalyst composition
  • Catalyst composition for preparing ethylene glycol from biomass raw materials as well as preparation method and application of catalyst composition

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043] 40%Ni-SiO 2 The catalyst was prepared by precipitation method: 39.635g of nickel nitrate hexahydrate was dissolved in deionized water to prepare a 1mol / L nickel nitrate solution, and 4mol / L NaOH solution was added dropwise under vigorous stirring for precipitation. After pH>11, 30g of 40 % silica sol to form a gel, then heated to 100°C for aging for 4 hours, filtered and washed until the filtrate was neutral. Dry overnight at 120°C, bake at 500°C for 4 hours in an air atmosphere, and finally use H at 400°C 2 / N 2 (volume ratio of 20 / 80) reduction for 6h.

[0044] Nb-containing tungsten bronze Nb x WO 3 (Denoted as NbW-1) The catalyst preparation process is as follows: the required precursor niobium salt and tungsten salt (by atomic molar ratio) are 0.3:1, and 3.228g niobium oxalate, 5.392g ammonium metatungstate and 3.782g Dissolve oxalic acid dihydrate in 80ml of water, heat and dissolve at 60°C for 0.5h under stirring, then raise the temperature to 150°C, continu...

Embodiment 2

[0048] 40%Ni-SiO 2 Catalyst preparation method is the same as embodiment 1.

[0049] Nb-containing tungsten bronze Nb x WO 3 (denoted as NbW-2) catalyst preparation process is as follows: wherein the required precursor niobium salt and tungsten salt (by atomic molar ratio) is 0.3:1, weigh 3.228g niobium oxalate, 5.392g ammonium metatungstate and 6.304g Dissolve citric acid monohydrate in 80ml of water, heat and dissolve at 60°C for 0.5h under stirring, then raise the temperature to 150°C, keep stirring and reflux at a constant temperature for 48h, after cooling, the formed precipitate is filtered, washed with water until neutral, and dissolved at 120°C After drying at ℃ for 12 hours, finally in H 2 / N 2 NbW-2 was prepared by calcining at 400℃ for 2h under (60 / 40) atmosphere, and the actual value of Nb:W molar ratio in NbW-2 was 0.36 as measured by ICP.

[0050] The reaction of cellulose catalytic conversion to prepare ethylene glycol is carried out in a closed reactor. W...

Embodiment 3

[0052] 40%Ni-SiO 2 Catalyst preparation method is the same as embodiment 1.

[0053] Nb-containing tungsten bronze Nb x WO 3 (Denoted as NbW-3) The preparation process of the catalyst is as follows: the required precursor niobium salt and tungsten salt (by atomic molar ratio) are 0.3:1, and 3.228g niobium oxalate, 5.392g ammonium metatungstate and 4.503g Dissolve tartaric acid in 80ml of water, heat and dissolve at 60°C for 0.5h under stirring, then raise the temperature to 150°C, continue to keep stirring at a constant temperature and reflux for 48h, after cooling, the resulting precipitate is filtered, washed with water until neutral, and dried at 120°C After 12 hours, finally in H 2 / N 2 NbW-3 was prepared by calcining at 400℃ for 2h under (60 / 40) atmosphere, and the actual value of Nb:W molar ratio in NbW-3 was 0.34 as determined by ICP.

[0054] The reaction of cellulose catalytic conversion to prepare ethylene glycol is carried out in a closed reactor. Weigh 1.0g m...

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Abstract

The invention discloses a catalyst composition for preparing ethylene glycol from a biomass raw material as well as a preparation method and application of the catalyst composition. According to the invention, a composition formed by using a metal catalyst to be coupled with a tungsten bronze catalyst containing a transition metal M, and the catalyst composition is applied to the reaction of preparing ethylene glycol from biomass, so that efficient conversion from biomass raw materials to ethylene glycol is realized.

Description

technical field [0001] The invention relates to the field of biomass utilization, and mainly relates to a catalyst composition for preparing ethylene glycol from biomass raw materials, a preparation method and application thereof. Background technique [0002] Ethylene glycol is an important basic chemical raw material with a wide range of uses and can be directly used as antifreeze for motor vehicles; ethylene glycol and its high polymer polyethylene glycol can synthesize various types of surfactants; at the same time, ethylene glycol Alcohols are also important monomers for synthetic resins (such as polyethylene terephthalate) and synthetic fibers. [0003] At present, the technical route adopted in the industrial production of ethylene glycol is mainly the ethylene oxide hydration method, and the coal-to-ethylene glycol method has also developed rapidly in recent years. According to reports, the current production capacity of ethylene glycol from ethylene oxide accounts ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/888B01J23/652C07C29/00C07C31/20
CPCB01J23/888B01J23/6527C07C29/00C07C31/202Y02P20/52
Inventor 贾玉庆缪长喜孙清卢媛娇张新玉张磊
Owner CHINA PETROLEUM & CHEM CORP