Preparation process of lignocellulose pulping prehydrolyzate with high-efficiency fermentation capacity

A technology of lignocellulose and prehydrolyzate, which is applied in the fields of cellulose raw material pulping, fermentation, and fiber raw material treatment. Can not remove aromatic small molecule inhibitors and other problems, and achieve the effect of mild detoxification process conditions, easy industrial application, and easy control

Active Publication Date: 2017-06-06
QINGDAO INST OF BIOENERGY & BIOPROCESS TECH CHINESE ACADEMY OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

①Rotary evaporation can reduce the concentration of low-boiling organic substances in the hydrolyzate, such as acetic acid, furfural and aldehyde vanillin, etc., but new inhibitors will be produced at high temperature, resulting in a decrease in fermentation efficiency
②Using volatile organic solvents such as diethyl ether and ethyl acetate to extract the hydrolyzate can remove most of the inhibitors, but there are disadvantages of difficult recovery of organic solvents and residual organic solvents
③ Activated carbon has strong adsorption characteristics, but the adsorption of inhibitors by activated carbon is affected by the properties of the inhibitors, the pH of the prehydrolyzed solution, the pretreatment temperature, time and the concentration of activated carbon, and the degree of removal of inhibitors is limited
④Ion exchange resin adsorption has a significant effect on the removal of weakly acidic inhibitors, but the removal effect on furfural inhibitors is limited, and this method will remove a large amount of fermentable sugars while removing inhibitors, resulting in the loss of fermentation products. Yield is greatly reduced
⑤Membrane separation can remove inhibitors such as furfural, hydroxymethylfurfural, and acetic acid in the hydrolyzate, but cannot effectively remove small molecule phenolic compounds with molecular weights similar to glucose and xylose
In addition, the simple application of electrodialysis can only remove organic acid inhibitors such as formic acid and acetic acid in the pulping prehydrolyzate, and can hardly remove aromatic small molecule inhibitors, which leads to the fact that the pure application of electrodialysis cannot achieve pulping prehydrolysis Efficient detoxification of liquid

Method used

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  • Preparation process of lignocellulose pulping prehydrolyzate with high-efficiency fermentation capacity

Examples

Experimental program
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Effect test

Embodiment 1

[0034] Put 1 kg of peeled poplar wood chips and 6 kg of water into the cooking pot together, raise the temperature to 160°C for 20-60 minutes, keep this temperature for 2 hours, and separate the prehydrolyzed solution and pretreated wood chips after cooling down to 40°C. After the pre-hydrolyzate was concentrated by vacuum distillation at a temperature of 40°C for 5 times, the pH of the pre-hydrolyzate was adjusted to 2.5 with 1M sulfuric acid, allowed to stand for 30 minutes, filtered and the filtered pre-hydrolyzate was collected. Adjust the pH of the prehydrolyzate to 8.0 with sodium hydroxide, let stand for 30 minutes, filter and collect the filtered prehydrolyzate. Then add hydrogen peroxide to the prehydrolyzate to 5 g / L, pH 8.0, treat at 30° C. for 3 hours, and remove the precipitate by microfiltration. Adjust the pH to 4.5, and inject the prehydrolyzed solution with a volume of 400ml and an initial conductivity of 46ms / cm into the electrodialyzer. 95×215mm 2 , The ci...

Embodiment 2

[0036] Put 1 kg of peeled eucalyptus wood chips and 3 kg of water into the cooking pot together, raise the temperature to 170 degrees for 20-60 minutes, keep this temperature for 4 hours, and separate the prehydrolyzed solution and pretreated wood chips after cooling down to 50 degrees. After the prehydrolyzed solution was concentrated by vacuum distillation at 60°C by 10 times, the pH of the prehydrolyzed solution was adjusted to 2.0 with 1M hydrochloric acid, allowed to stand for 30 minutes, filtered and collected. Adjust the pH of the prehydrolyzate to 8.0 with potassium hydroxide, let stand for 30 minutes, filter and collect the filtered prehydrolyzate. Then add hydrogen peroxide and ferrous sulfate to the pre-hydrolyzate to 3g / L and 0.2g / L respectively, pH 3.0, treat at room temperature for 2 hours and then remove the precipitate by microfiltration. Adjust the pH to 5, and inject the prehydrolyzed solution with a volume of 400ml and an initial conductivity of 46ms / cm into...

Embodiment 3

[0038] Put 1 kg of peeled masson pine wood chips and 10 kg of water into the cooking pot together, raise the temperature to 180 degrees for 20-60 minutes, keep this temperature for 1 hour, and separate the prehydrolyzed solution and pretreated wood chips after cooling down to 60 degrees. After the prehydrolyzed solution was concentrated by vacuum distillation at a temperature of 50°C by 8 times, the pH of the prehydrolyzed solution was adjusted to 2.5 with 1M nitric acid, allowed to stand for 30 minutes, filtered and collected. Adjust the pH of the prehydrolyzate to 9.0 with ammonia water, let stand for 30 minutes, filter and collect the filtered prehydrolyzate. Then add hydrogen peroxide and ozone to the prehydrolyzate to 8g / L and 0.5g / L respectively, treat at 35 degrees Celsius for 7 hours, and remove the precipitate by microfiltration. Adjust the pH to 9, inject the prehydrolyzed solution with a volume of 500ml and an initial conductivity of 50ms / cm into the electrodialyzer...

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Abstract

The invention provides a preparation process of lignocellulose pulping pre-hydrolysis liquid having efficient fermentation capability based on an advanced oxidation process and electrodialysis treatment against the problems of lignocellulose hydrolysis liquid detoxification in the prior art. The preparation process comprises the following steps: 1, preparing pulping pre-hydrolysis liquid; 2, conducting concentration, and removing sediment; 3, conducting advanced oxidation treatment; 4, conducting electrodialysis treatment. According to the preparation process, the pre-hydrolysis liquid generated in the production processes of chemimechanical pulp and dissolving pulp in the pulping and papermaking industry serves as the treatment object, firstly, organic inhibitor molecules are degraded through advanced oxidized reagent, subsequently, electrolyte inhibitor in the hydrolysis liquid is removed through an electrodialysis method, and the advanced oxidized reagent and the electrodialysis method achieve a remarkable synergistic effect. The pre-hydrolysis liquid prepared through the preparation method can serve as a fermentation carbon source and be used for fermenting and producing unicellular protein or preparing high value-added compounds. By means of a detoxificaiton method of the preparation process, under the circumstance that fermentable sugar cannot be lost, small-molecule inhibitor such as phenols can be removed, and ionogenic inhibitor can be removed.

Description

technical field [0001] The invention belongs to the field of bio-energy and pulping and papermaking, and in particular relates to a preparation process of a lignocellulose pulping prehydrolyzate, in particular to a method for preparing lignocellulose pulping with high-efficiency fermentation capacity by using an advanced oxidation method and an electrodialysis method Process method of prehydrolyzate. Background technique [0002] Due to the shortage of high-quality pulp and paper raw materials, the continuous increase in the price of traditional resources, the rise in labor costs and the enormous pressure brought about by global competition, traditional pulp and paper enterprises are currently facing unprecedented difficulties. The old business model of simply converting lignocellulose into pulp and paper products is no longer suitable for the existing market. Combining the pulp and paper industry with biomass refining, pre-hydrolyzing plant fiber resources before pulping c...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): D21C3/00C12P19/02C12P7/18
CPCC12P7/18C12P19/02C12P2203/00D21C3/00
Inventor 孙志杰杜娟张杨崔球王丹丹
Owner QINGDAO INST OF BIOENERGY & BIOPROCESS TECH CHINESE ACADEMY OF SCI
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