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Concentrating apparatus for fluid containing levulinic acid compounds

A technology of levulinic acid and compound, applied in the field of concentration equipment, can solve the problems of low yield and high energy consumption of levulinic acid compounds, and achieve the effects of low cost, improved yield and easy realization

Active Publication Date: 2018-04-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The technical problem to be solved by the present invention is that there are problems of low yield and high energy consumption in the purification process of levulinic acid compounds in the prior art, and a new concentration equipment for fluid containing levulinic acid compounds is provided

Method used

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  • Concentrating apparatus for fluid containing levulinic acid compounds
  • Concentrating apparatus for fluid containing levulinic acid compounds
  • Concentrating apparatus for fluid containing levulinic acid compounds

Examples

Experimental program
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Embodiment approach

[0023] As an embodiment of the present invention, the fluid containing levulinic acid compounds is derived from biomass material hydrolyzate.

[0024] As an embodiment of the present invention, the fluid containing levulinic acid compounds is derived from at least one hydrolyzate of xylitol, glucose, cellobiose, cellulose, hemicellulose and lignin; or A hydrolyzate derived from at least one of paper sludge, waste paper, bagasse, glucose, wood, corn cobs, corn stover, and rice straw.

[0025] As an embodiment of the present invention, there is no particular limitation on the method of deriving the fluid containing levulinic acid compounds from the biomass material, and those conventionally known in the art can be used. For example, the derivatization method may include subjecting the biomass material to catalytic conversion (such as hydrolytic deoxygenation, inorganic acid catalyzed hydrolysis, organic acid catalyzed hydrolysis, solid acid catalyzed hydrolysis, molecular sieve ...

Embodiment 1

[0035] Take by weighing 1.5 kilograms of corn stalks, place in an autoclave and add 10 kilograms of water, then add a 5mol / L sulfuric acid solution with 7% water quality, heat up to 180° C. and react for 45 minutes, then cool to obtain levulinic acid containing The reaction solution. Experimental determination, the content of levulinic acid is 31%.

[0036] Take 6 kg of the reaction solution to pass through the alumina ceramic filter membrane with a membrane pore size of 1 μm, control the pressure at 1 MPa, and control the temperature at 20° C. to collect the permeate.

[0037] The permeate is passed through an ultrafiltration membrane with a rejection of more than 1000. The membrane material is polyvinylidene fluoride, the operating pressure is 7MPa, and the operating temperature is 30°C, and the ultrafiltration permeate is collected.

[0038] Pass the ultrafiltrate through a composite membrane of cellulose acetate and polyamide, reverse osmosis concentration and filtration,...

Embodiment 2

[0040] Take by weighing 1.1 kilograms of corn stalks, place in an autoclave and add 8.6 kilograms of water, then add a 5mol / L sulfuric acid solution with 5% water quality, heat up to 200°C and react for 45 minutes, then cool to obtain levulinic acid containing The reaction solution. Experimental determination, the content of levulinic acid is 34%.

[0041] Take 5kg of reaction solution with levulinic acid concentration of 34% and pass it through a titanium oxide ceramic filter membrane with a membrane pore size of 100um, control the pressure at 4MPa, and control the temperature at 100°C to collect the permeate.

[0042] The permeate is passed through an ultrafiltration membrane with a throw cut-off greater than 1000. The membrane material is polyvinyl chloride, the operating pressure is 0.5 MPa, and the operating temperature is 25° C. to collect the ultrafiltration permeate.

[0043] Pass the ultrafiltrate through a polyamide membrane, concentrate and filter by reverse osmosi...

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Abstract

The invention relates to a concentrating apparatus for a fluid containing levulinic acid compounds. The concentrating apparatus mainly overcomes the problems of low yield and high energy consumption in purifying of levulinic acid compounds in the prior art. The concentrating apparatus at least comprises a prefiltration membrane and an ultrafiltration membrane along the flowing direction of the fluid, wherein the prefiltration membrane comprises a filter paper membrane or a ceramic filter membrane, and the ultrafiltration membrane is prepared from at least one selected from a group consisting of polyvinylidene fluoride, polyvinyl chloride, polysulfone, polysulfonamide, polycarbonate and polystyrene. With such a technical scheme, the concentrating apparatus is applicable to the industrial production of purification of levulinic acid compounds.

Description

technical field [0001] The invention relates to a device for concentrating fluid containing levulinic acid compounds. Background technique [0002] The modern chemical industry produces a large amount of fuels and chemicals based on fossil resources, which greatly promotes the development and progress of society. In the long run, as non-renewable material resources, fossil resource reserves are limited. The non-renewability of fossil resources has prompted people to actively seek and develop renewable resources, and to continuously produce them to meet the growing social needs. As a large amount of renewable material resources, biomass has received extensive attention. Levulinic acid (4-oxopentanoic acid, levulonic acid or penteroic acid) is an important biomass platform compound, low toxicity, hygroscopicity, almost no decomposition under normal pressure distillation, rich functional groups in the molecule, easy to A series of chemical reactions such as esterification, h...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C51/42C07C51/44C07C59/185C07C67/48C07C67/54C07C69/716
CPCC07C51/42C07C51/44C07C67/48C07C67/54C07C59/185C07C69/716
Inventor 宋奇孔德金郑均林
Owner CHINA PETROLEUM & CHEM CORP