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Xylose production process

A production process and technology of xylose, applied in the production of sugar, sugar production, food science and other directions, can solve the problems of shortening the service life of electrodialysis, scaling on the surface of electrodialysis membrane, and easy pollution of ion exchange membrane, etc. Low, reducing pollution and scaling phenomenon, high desalination efficiency

Inactive Publication Date: 2016-01-06
FUTASTE PHARM CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The technology of electrodialysis equipment for desalination has become increasingly mature, and its application in xylose production has also been seen in academic papers, but no company has actually applied it to xylose production
The main reason is the limitation of technical bottlenecks. The content of organic impurities, organic acids and pigments in xylose hydrolyzate is large and miscellaneous, which is easy to contaminate the ion exchange membrane, cause scaling on the surface of the electrodialysis membrane, and cause polarization, which seriously affects the service life of electrodialysis. Shortening, desalination efficiency reduction, affecting stability and increasing power consumption
In addition, the electrodialysis concentrated water contains sulfate, and direct recycling for hydrolysis will lead to the accumulation of salt, resulting in insufficient hydrolysis and increased power consumption of electrodialysis

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Put 1000kg of corncobs into the hydrolysis tank, add 5000kg of dilute sulfuric acid solution with a mass percentage concentration of 1.0%, hydrolyze for 2 hours at a temperature of 120°C, and discharge the hydrolyzate; decolorize the hydrolyzate to 60% light transmission with decolorizing resin, and then enter the interception First-stage membrane filtration with a molecular weight of 3000Da, the intercepted liquid is recirculated and filtered for 3 times, and diluted with deionized water before each cycle of filtration; Filtrate 3 times, dilute 1 time with deionized water before each cycle of filtration; the permeate from the secondary membrane filtration enters the membrane concentration equipment to concentrate to 10% refraction, and the permeate from the acid-resistant nanofiltration membrane with a cut-off molecular weight of 100Da is used for Electrodialysis feed water, the concentrated solution is then concentrated by a multi-effect evaporator to a refraction of 3...

Embodiment 2

[0023] Put 4 tons of bagasse into the hydrolysis kettle, add 24 tons of dilute sulfuric acid solution with a mass percentage concentration of 1.5%, hydrolyze for 3 hours at a temperature of 110°C, filter out the hydrolyzate from the plate frame; decolorize the hydrolyzate to 20% light transmission with decolorizing resin, Enter the first-stage membrane filtration with a cut-off molecular weight of 5000Da, and the intercepted liquid is recirculated and filtered twice, and diluted 3 times with deionized water before each cycle of filtration; The liquid is circulated and filtered for 4 times, and diluted 2 times with deionized water before each cycle of filtration; the permeate of the secondary membrane filtration enters the membrane concentration equipment and is concentrated to a refractive index of 15%, and the permeate of the acid-resistant material nanofiltration membrane with a cut-off molecular weight of 200Da It is used for electrodialysis concentrated water to enter the l...

Embodiment 3

[0025] Put 3 tons of corn cobs into the hydrolysis kettle, add 21 tons of dilute sulfuric acid solution with a mass percentage concentration of 1.0%, hydrolyze for 2.5 hours at a temperature of 125°C, and filter out the hydrolyzate from the plate frame; decolorize the hydrolyzate to 80% light transmission with activated carbon , into the primary membrane filtration with a cut-off molecular weight of 2500Da, the intercepted liquid is circulated and filtered 4 times, and diluted with deionized water for 1 time before each cycle of filtration; the permeate of the primary membrane filter enters the secondary membrane filtration system with a cut-off molecular weight of 400Da for filtration , the intercepted liquid is recirculated and filtered 3 times, and diluted 2 times with deionized water before each cycle of filtration; the secondary membrane filtration permeate enters the membrane concentration equipment and is concentrated to a refractive index of 8%, and the cut-off molecular...

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PUM

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Abstract

The invention discloses a xylose production process. The xylose production process comprises the following steps: adding pretreated pentosan-enriched plant fiber into a 1.0%-1.5% sulfuric acid solution to generate hydrolysis reaction, and filtering liquid to obtain hydrolysate; decoloring the hydrolysate by virtue of activated carbon or decoloring resin until the transparency of the hydrolysate is 20%-80%, and filtering to remove impurities by virtue of membrane filter equipment; concentrating the filtered hydrolysate by virtue of membrane concentration equipment, and decoloring the hydrolysate until the transparency of the hydrolysate is 60%-90% to obtain feed liquid, wherein leachate of the membrane concentration equipment is used as inflow water of an electroosmosis concentrated water chamber; desalting the feed liquid by virtue of electroosmosis and ion exchange resin, wherein electroosmosis concentrated water is circularly applied to a hydrolysis step; concentrating the feed liquid until the refractive index is 80%, crystallizing in a crystallization tank, and centrifuging to separate mother liquid, so as to obtain xylose crystals. According to the xylose production process, the problem that the costs for sewage treatments including neutralization and ion exchange in the prior art are high is solved, and the problems of short service life, low desalting efficiency, poor stability and high power consumption of an electroosmosis manner in the production of xylose are solved.

Description

technical field [0001] The invention relates to the field of functional sugar production, in particular to a xylose production process. Background technique [0002] In traditional xylose production, sulfuric acid is needed to hydrolyze the plant fibers rich in pentosan (such as corncobs, etc.). The removal of sulfate ions usually uses neutralization precipitation and ion exchange. However, neutralization precipitation The introduced calcium ions reduce the exchange capacity of the cation exchange resin, and at the same time, the residual calcium salt precipitates and accumulates in the resin to block the pore size of the resin, affecting the performance and service life of the resin. The ion exchange method will produce a large amount of waste water containing acid and alkali, which increases the cost of sewage treatment. [0003] The technology of electrodialysis equipment for desalination has become increasingly mature, and its application in xylose production has also b...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C13K13/00
Inventor 孙鲁李毅邱学良曹玉华沈丽丽张瑞瑞孙艳
Owner FUTASTE PHARM CO LTD
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