CN107164433A - A kind of method of ultrasonic assistant alkalinity potassium permanganate preprocessing lignocellulose - Google Patents

A kind of method of ultrasonic assistant alkalinity potassium permanganate preprocessing lignocellulose Download PDF

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Publication number
CN107164433A
CN107164433A CN201710583320.8A CN201710583320A CN107164433A CN 107164433 A CN107164433 A CN 107164433A CN 201710583320 A CN201710583320 A CN 201710583320A CN 107164433 A CN107164433 A CN 107164433A
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lignocellulosic
potassium permanganate
residue
alkalinity potassium
pretreatment
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马立娟
杜丽平
肖冬光
马清
郭高杰
崔有志
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Tianjin University of Science and Technology
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Tianjin University of Science and Technology
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/14Preparation of compounds containing saccharide radicals produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase, e.g. by cellulase, hemicellulase
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/02Monosaccharides
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P2201/00Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P2203/00Fermentation products obtained from optionally pretreated or hydrolyzed cellulosic or lignocellulosic material as the carbon source

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Abstract

The present invention relates to a kind of method of ultrasonic assistant alkalinity potassium permanganate preprocessing lignocellulose, this method is comprised the following steps that:Lignocellulosic material is crushed, dried, controls ultrasonic power, alkalinity potassium permanganate concentration, solid-to-liquid ratio, pretreatment time and temperature in suitable scope respectively, filtering is washed to neutrality, and pretreated lignocellulosic residue is obtained after drying;Digested into residue obtained above in citrate buffer solution system using commercial cellulose enzyme and zytase, obtain fermentable reduction sugar juice.Preprocess method in the present invention improves the retention rate of the clearance of lignin, cellulose and hemi-cellulose components using the collaboration energy of ultrasonic wave, and effect substantially, reduces the consumption of alkalinity potassium permanganate;The lignocellulosic residue enzymolysis efficiency and Reducing sugar that the present invention is pre-processed are greatly enhanced.Meanwhile, the inventive method has environment-friendly, simple to operate, low cost and other advantages.

Description

A kind of method of ultrasonic assistant alkalinity potassium permanganate preprocessing lignocellulose
Technical field
The invention belongs to lignocellulose biomass application technology as the second resource field, and in particular to one kind is auxiliary using ultrasonic wave The method for helping alkalinity potassium permanganate preprocessing lignocellulose.
Background technology
Lignocellulosic is the renewable resource of reserves maximum in nature, can pass through chemistry and bioconversion generates energy Source substitute materials or chemical products, under fossil energy material increasingly depleted and the dual-pressure of environmental protection, lignocellulosic Effective trans-utilization turn into and realize the important subject of sustainable development, this problem has been included in country, long-term section Learn development plan.At present, the microorganism conversion of lignocellulosic is most commonly used that acidic hydrolysis.The main difficulty of acidic hydrolysis Point is producing for preconditioning technique and low-cost high-efficiency enzyme.Lignocellulosic is by groups such as cellulose, hemicellulose and lignin Into complicated, cellulose and hemicellulose are wrapped up layer by layer by lignin, and lignin plays screen during hydrocellulose Barrier is acted on.Therefore, the effect of pretreatment is to reduce the degree of polymerization and crystallinity of cellulose, it is impossible to be degraded to the wood of fermentable sugars The separation of quality component is sloughed, and increases the reaction surface area of cellulose.
In recent years, it is more to the research report in terms of the pretreatment of lignocellulosic material, including using traditional acid, alkali The processing method such as pretreatment and gas explosion method, the quick-fried method of ammonia, ionic liquid and bioanalysis in recent years newly developed.Although to a certain extent Improving the enzymatic hydrolyzation of lignocellulosic, but still there is complex procedures, energy consumption and equipment investment height causes pretreatment cost high And pretreatment waste liquid bring environmental pollution a series of problems, such as.Alkaline reagent and the preprocess method quilt of strong oxidizer combination Report can effectively remove the lignin in biomass, while the hydrogen bond and the crystalline substance of cellulose that destroy between hemicellulose, cellulose Body structure, so that the structure of stubbornly resisting destroyed in biomass, but research papers are less.
Potassium permanganate is a kind of strong oxidizer, is widely used in Water purification, both can by the oxidation operation in water, Organic substance in water can be adsorbed etc., play deodorization, demanganization and except iron etc. is acted on.Our early-stage Study is used first Alkalinity potassium permanganate preprocessing lignocellulose, as a result shows, this method can effectively destroy three components of lignocellulosic it Between the connection of chemical combination key, remove most of lignin in corncob, improve the enzymolysis yield of follow-up lignocellulosic.Using alkalescence Permanganate pretreatment lignocellulosic, compared with the oxidants such as ozone, chlorine dioxide and chlorine, the security of potassium permanganate is more Height, cost higher compared with alkaline hydrogen peroxide stability is lower, therefore, with feasible industrial applications prospect.
The content of the invention
The present invention establishes a kind of alkaline permanganate pretreatment lignocellulosic of collaboration energy auxiliary of utilization ultrasonic wave Process, it is intended to the retention rate of the clearance of lignin, cellulose and hemi-cellulose components is improved, while it is high to reduce alkalescence The consumption of potassium manganate, the final enzymolysis efficiency for improving lignocellulosic, reduction pretreatment cost.Specifically include following steps:
(1) it is lignocellulosic material is (any in maize straw, corncob, wheat stalk, rice straw and bagasse A kind of or its combination) crush, 40~80 mesh sieves are crossed after 90 DEG C of drying.
(2) raw material of a certain amount of size-reduced drying is taken, adding alkaline permanganate solution makes solid-to-liquid ratio control 1: 10~1 : 30, it is preferred with 1: 10;Make the concentration of alkalinity potassium permanganate control to be 0.5~4% (w/v), be preferred with 2%;Pretreatment temperature control System is preferred at 30~70 DEG C with 60 DEG C;Pretreatment time is controlled in 0.5~8h, is preferred with 4h.
(3) after lignocellulosic residue filtering after pretreatment, with distillation water washing until filtrate pH reaches neutrality, 90 DEG C dry to constant weight.
(4) residue obtained through above-mentioned pretreatment is added during 0.05mol/L pH are 4.5~5.0 citrate buffer solutions, It is 2~10% (w/v) to control its concentration, is preferred with 8%.
(5) the plain enzyme of commercial fibers and zytase from trichoderma are added into above-mentioned system, enzyme is controlled respectively Useful load is 20~50FPU/g substrates (being preferred with 30FPU/g substrates) and 5000~12000U/g substrates (with 8000U/g substrates It is preferred), 45~55 DEG C, 48~96h of reaction is digested under conditions of 100~200rpm of shaking speed, with 50 DEG C, shaking speed 150rpm, enzymolysis 72h is preferred.
(6) reduced sugar and glucose, xylose concentration in hydrolyzate are determined with DNS methods and HPLC methods respectively.
The present invention has the advantage that:The present invention is first using the method for ultrasonic assistant alkalinity potassium permanganate to wood fibre Plain raw material is pre-processed, under the synergy of ultrasonic energy, can strengthen alkaline permanganate solution to wood fibre The infiltration of element and swelling action, raw material microstructure analysis shows, after being pre-processed through this method, and lignocellulosic material surface is fluffy Porous, structure becomes loose, and mechanical strength weakens, the valence link that alkalinity potassium permanganate can be destroyed between hemicellulose and lignin Connection, oxidation ehter bond and ester bond removes lignin in dissolving corncob, this structure be conducive to cellulase and zytase with The contact of corncob, beneficial to the enzymolysis in later stage.Ultrasonic assistant can improve the clearance of lignin, reduce potassium permanganate alkalescence molten The consumption of liquid, after being pre-processed through the inventive method, delignification rate is up to more than 50%, and cellulose and hemicellulose retention rate divide Not up to 94% and more than 85%.The enzymatic hydrolyzation of lignocellulosic is greatly improved.The inventive method mild condition, simply It is easy to operate, safety non-pollution, with feasible industrial applications prospect.
Embodiment
Below by embodiment, the present invention will be further described, and following embodiments are illustrative, be not it is limited, Protection scope of the present invention can not be limited with following embodiments.
Embodiment 1
A kind of method that use ultrasonic assistant alkalinity potassium permanganate pre-processes maize straw, comprises the following steps:
(1) by corn straw smashing, 60 mesh sieves are crossed after 90 DEG C of drying to constant weight.
(2) corn stalk raw material of the size-reduced drying of 8.0g is taken, 100mL concentration is added molten for 2% (w/v) potassium permanganate Liquid, sodium hydroxide adjusts pH to be 11, and the triangular flask that will be equipped with the mixed liquor is placed in ultrasonic response device, and setting power is 250W, frequency 40kHz, 4h is handled at 60 DEG C.
(3) pretreated maize straw is filtered, with distillation water washing until filtrate pH reaches neutrality, 90 DEG C of drying are extremely Constant weight.
(4) (or pretreated maize straw is not former for the maize straw residue for taking after the above-mentioned pretreatments of 2.0g through drying Material), 25mL 0.05mol/L, pH is added in 4.8 citrate buffer solution, the commodity of Trichoderma source are added into the mixed liquor Cellulose enzyme and zytase, the useful load of its cellulase is 20FPU/g substrates, and the useful load of zytase is 12000U/g substrates, it is 40mL to control hydrolyzation system cumulative volume.
(5) above-mentioned system is digested under conditions of 50 DEG C, shaking speed 150rpm, is determined respectively also after reaction 72h Raw sugar, glucose and xylose concentration.
By determining and calculating, cellulose retention rate is 94.28% after pretreatment, and hemicellulose retention rate is 87.56%, Lignin removing rate is 56.79%.The enzymolysis more untreated maize straw of Reducing sugar improves 106.33%.
Embodiment 2
A kind of method that use ultrasonic assistant alkalinity potassium permanganate pre-processes corncob, comprises the following steps:
(1) corncob is crushed, crosses 80 mesh sieves after 90 DEG C of drying to constant weight.
(2) the corn core raw material of the size-reduced drying of 5.0g is taken, 100mL concentration is added molten for 1.5% (w/v) potassium permanganate Liquid, sodium hydroxide adjusts pH to be 11.5, and the triangular flask that will be equipped with the mixed liquor is placed in ultrasonic response device, and setting power is 300W, frequency 40kHz, 4h is handled at 65 DEG C.
(3) pretreated corncob is filtered, with distillation water washing until filtrate pH reaches neutrality, 90 DEG C of drying to perseverance Weight.
(4) the corncob residue (or not pretreated corn core raw material) after the above-mentioned pretreatments of 2.0g through drying is taken, plus Enter in the citrate buffer solution that 25mL 0.05mol/L, pH are 4.8, the commercial fibers of Trichoderma source are added into the mixed liquor Plain enzyme and zytase, the useful load of its cellulase is 30FPU/g substrates, and the useful load of zytase is 16000U/g bottoms Thing, it is 40mL to control hydrolyzation system cumulative volume.
(5) above-mentioned system is digested under conditions of 50 DEG C, shaking speed 180rpm, is determined respectively also after reaction 72h Raw sugar, glucose and xylose concentration.
By determining and calculating, cellulose retention rate is 94.26% after pretreatment, and hemicellulose retention rate is 85.83%, Lignin removing rate is 58.17%.The enzymolysis more untreated corncob of Reducing sugar improves 92.21%.

Claims (6)

1. a kind of method of ultrasonic assistant alkalinity potassium permanganate preprocessing lignocellulose, it is characterised in that including following step Suddenly:
(1) lignocellulosic material is crushed, dried, respectively control ultrasonic power, alkalinity potassium permanganate concentration, solid-to-liquid ratio, Pretreatment time and temperature are filtered in suitable scope, and washing obtains pretreated lignocellulosic residue after drying;
(2) carried out into residue obtained above in citrate buffer solution system using commercial cellulose enzyme and zytase Enzymolysis, determines concentration of reduced sugar in hydrolyzate.
2. according to the method described in claim 1, it is characterised in that described lignocellulosic is maize straw, corncob, small Any one of Wheat Straw, rice straw and bagasse or its combination.
3. according to the method described in claim 1, it is characterised in that after lignocellulosic material is crushed in step (1), cross 40~ 80 mesh sieves, 90 DEG C of dryings to constant weight.
4. according to the method described in claim 1, it is characterised in that ultrasonic power used is 150-800W in step (1), is surpassed Frequency of sound wave is 20-50kHz;The concentration of alkalinity potassium permanganate is 0.5~4% (w/v);Lignocellulosic material and SODIUM PERCARBONATE The solid-to-liquid ratio of solution mixing is controlled 1: 10~1: 30;Pretreatment temperature is controlled at 30~70 DEG C;Pretreatment time is controlled 0.5 ~8h;Lignocellulosic residue after pretreatment is filtered, with distillation water washing until filtrate pH reaches neutrality, 90 DEG C of dryings To constant weight.
5. according to the method described in claim 1, it is characterised in that citrate buffer solution described in step (2) is 0.05mol/ L, pH are 4.5~5.0;Cellulase and zytase are from trichoderma commercialization enzyme preparation.
6. according to the method described in claim 1, it is characterised in that in step (2) concentration of lignocellulosic residue be 2~ 10% (w/v);The useful load of lignocellulosic residue enzymatic hydrolysis system cellulase is 10~30FPU/g substrates, zytase Useful load be 8000~20000U/g substrates;Enzymolysis is anti-under conditions of 45~55 DEG C of temperature, 100~200rpm of shaking speed Answer 48~96h.
CN201710583320.8A 2017-07-12 2017-07-12 A kind of method of ultrasonic assistant alkalinity potassium permanganate preprocessing lignocellulose Pending CN107164433A (en)

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Cited By (5)

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CN110628844A (en) * 2019-09-23 2019-12-31 福建生物工程职业技术学院 Graded separation method for cord grass
CN110791540A (en) * 2019-11-08 2020-02-14 孟保奎 Method for quickly pretreating biomass by microwave alkaline baking
CN112111541A (en) * 2019-06-20 2020-12-22 南京理工大学 Alkali method for pretreating densified lignocellulose and biotransformation method
CN112844324A (en) * 2019-11-26 2021-05-28 南京理工大学 Lignin/manganese oxide composite adsorption material and preparation method and application thereof
CN114086411A (en) * 2021-11-25 2022-02-25 集美大学 Honey pomelo young fruit cellulose and preparation method thereof

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112111541A (en) * 2019-06-20 2020-12-22 南京理工大学 Alkali method for pretreating densified lignocellulose and biotransformation method
CN110628844A (en) * 2019-09-23 2019-12-31 福建生物工程职业技术学院 Graded separation method for cord grass
CN110791540A (en) * 2019-11-08 2020-02-14 孟保奎 Method for quickly pretreating biomass by microwave alkaline baking
CN112844324A (en) * 2019-11-26 2021-05-28 南京理工大学 Lignin/manganese oxide composite adsorption material and preparation method and application thereof
CN114086411A (en) * 2021-11-25 2022-02-25 集美大学 Honey pomelo young fruit cellulose and preparation method thereof

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Application publication date: 20170915