CN109880865A - A kind of high-efficiency separation and transformation method of corn stover - Google Patents

A kind of high-efficiency separation and transformation method of corn stover Download PDF

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CN109880865A
CN109880865A CN201910118218.XA CN201910118218A CN109880865A CN 109880865 A CN109880865 A CN 109880865A CN 201910118218 A CN201910118218 A CN 201910118218A CN 109880865 A CN109880865 A CN 109880865A
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separation
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lignin
corn stover
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孙润仓
孙少妮
李宜静
曹学飞
袁同琦
庞博
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Beijing Forestry University
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Abstract

本发明的目的在于提供一种玉米秸秆的高效分离与转化方法,其包括:(1)半纤维素的分离与转化;(2)纤维素的分离与转化;(3)木质素的分离。本发明提供了一种系统的玉米秸秆的高效分离和转化的方法,有效的利用玉米秸秆作为原料,生产高附加值的能源化学品、材料。其中,玉米秸秆当中的半纤维素被分离转化为糠醛,且糠醛得率较高;纤维素被分离转化为高浓度的葡萄糖液;分离得到的木质素,经过鉴定其结构较完整。本发明可以有效的提高三大组分的分离效率与利用率,对于玉米秸秆生物质资源利用和环境保护具有重要意义。The purpose of the present invention is to provide a high-efficiency separation and transformation method of corn stover, which comprises: (1) separation and transformation of hemicellulose; (2) separation and transformation of cellulose; (3) separation of lignin. The present invention provides a systematic method for efficient separation and transformation of corn stalks, which effectively utilizes the corn stalks as raw materials to produce high value-added energy chemicals and materials. Among them, the hemicellulose in the corn stover was separated and converted into furfural, and the yield of furfural was high; the cellulose was separated and converted into a high-concentration glucose solution; the isolated lignin was identified as having a relatively complete structure. The invention can effectively improve the separation efficiency and utilization rate of the three components, and is of great significance to the utilization of corn stover biomass resources and environmental protection.

Description

A kind of corn stover efficiently separate and method for transformation
Technical field
The invention belongs to the separation of biomass full constituent and trans-utilization field, and in particular to a kind of corn stover is efficiently divided From with method for transformation.
Background technique
China is corn planting economic development big country, while corn yield increasing, the total amount for the corn stover discarded every year Up to several hundred million tons.Byproduct of the corn stover as grain has many advantages, such as renewable, environmentally friendly, a large amount of supplies, is a kind of great The petroleum resources substitute of attraction.On the other hand, a large amount of corn stover is not effectively utilized, and does not pass through system Processing is just directly discharged in the ecosystem, is become agricultural straw refuse, is caused the waste of resource and the dirt of environment Dye, green, environmental-friendly corn stover cause negative effect to soil, atmosphere, microorganism etc. originally.Therefore, how to have Effect using corn stover as raw material, produce energy chemistry product, the material of high added value, for environmental protection have important meaning Justice.
Corn stover is one kind of wood fiber biomass, mainly contains three kinds of cellulose, hemicellulose and lignin groups Part.In general, the usually hydrolyzed fermentation of cellulose is bio-ethanol, and hemicellulose and lignin can be converted into high add The chemicals and product of value, such as furfural.Currently, the existing technology to corn stover separation conversion, is difficult to realize to cellulose, half Cellulose and the big component of lignin three carry out efficient separation and conversion.Wherein, to be produced using hemicellulose in corn stover Industrial process based on furfural, it is most of be use strong inorganic acid to carry out in the single_phase system of water as catalyst, such as Sulfuric acid or hydrochloric acid.However using inorganic acid as catalyst, there is shortcomings, lead to difficulty as cellulose decomposition degree is higher It is significant etc. to carry out later use, inorganic acid severe corrosion to equipment, safety problem.Meanwhile in the single_phase system of water, furfural Once being formed, it is particularly easy to degrade by resinification reaction and condensation reaction, catabolite is that the insoluble by-product corruption of black is planted Matter seriously affects furfural yield.Diphasic system is constituted using organic solvent and sodium chloride solution, biomass material is located in advance Reason, can effectively improve furfural yield, principle is after furfural is formed, by into organic phase, making to degrade furfural extraction Reaction is preferably minimized, and avoids subsequent adverse effect.Corn stover is in the two-phase formed by organic solvent and sodium chloride solution After system processing, the organic phase rich in furfural be easy to it is separated from the water open, allow the water phase rich in catalyst to carry out weight It is multiple to utilize, rich cellulose-containing solid residue is left for further fermenting.
The purpose of the present invention is developing a kind of method for efficiently separating and converting of the corn stover of system, to obtain compared with The lignin of high furfural yield and enzymolysis efficiency and structural integrity, reaches cellulose in corn stover, hemicellulose, wood The big component of quality three efficiently separating and converting.
Summary of the invention
The purpose of the present invention is to provide a kind of corn stover efficiently separate and method for transformation.This method is easy to operate, While obtaining furfural using the hemicellulose in corn stover, the cellulose in the first solid is largely retained in rear There is higher enzymolysis efficiency in the first continuous enzymolysis process, and still stays in the lignin knot in the second solid after enzymatic hydrolysis Structure is relatively complete.
The object of the invention to solve the technical problems adopts the following technical solutions to realize:
1, a kind of corn stover proposed according to the present invention efficiently separate and method for transformation, comprising the following steps:
The separation and conversion of hemicellulose: being broken to 20-80 mesh for corn stalk powder, with organic solvent and sodium chloride solution institute The diphasic system of composition is blended, and catalyst is added, and is rapidly heated and is carried out the first reaction to the first temperature, after reaction, First is carried out first to be separated by solid-liquid separation, and obtains the first solid and the first liquid, organic phase and water phase then are carried out to the first liquid Separation, obtains the first organic phase and the first water phase, wherein hemicellulose is converted into furfural and is present in the first organic phase, rich The first water phase containing catalyst may be repeated utilization;
The separation and conversion of cellulose: the first solid of gained being placed in acetic acid-sodium acetate buffer solution and carries out the first dipping, Then cellulase is added, carries out the first enzymatic hydrolysis, then carries out second and is separated by solid-liquid separation, obtain the second solid and second liquid, Middle cellulose is converted into glucose and is present in second liquid;
The separation of lignin: sufficiently cleaning the second solid using acetic acid-sodium acetate buffer solution, be then dried, In, lignin is present in solid form in the second solid.
The object of the invention to solve the technical problems also can be used following technical measures and further realize:
Preferably, preparation method above-mentioned, wherein hemicellulose separation is 160-180 DEG C with conversion temperature, it is described Reaction time is 30-60 minutes, and the catalyst concn is 0.05-0.50mol/L.
Preferably, preparation method above-mentioned, wherein the acetic acid-sodium acetate buffer solution concentration is 50mmol/L, pH is 4.7-4.9;Used dip time is 12-24 hours;The solid-to-liquid ratio of used solid residue and sodium acetate solution is 1:20- 50g/mL;The enzyme activity of used cellulase is to contain 15-20 filter paper enzyme activity unit in every gram of substrate;The enzymolysis time is 36-72 hours, temperature was 50-55 DEG C.
Also the following technical solution is employed for the object of the invention to solve the technical problems to realize:
A kind of corn stover proposed according to the present invention efficiently separate and method for transformation, the corn stover it is efficient Separation can be realized with conversion by method described in any of the above embodiments.
By above-mentioned technical proposal, the efficiently separating with method for transformation of corn stover of the invention at least has following excellent Point:
(1) compared with traditional acid catalyst dehydration prepares furfural, using there is bronsted acid and lewis acid simultaneously Property metal nitrate as catalyst, the destruction journey to cellulose and lignin can be reduced while improving furfural yield Degree.
(2) compared with the pretreatment of the single_phase system of traditional water, the diphasic system of organic solvent and water can be in furfural in water It while formation in phase, is extracted into the first organic phase, is effectively reduced the resinification reaction and condensation reaction of furfural, The a large amount of generations for avoiding humus, effectively raise the yield of furfural.
(3) it is compared with the traditional method, hemicellulose, which is converted into the solid waste after furfural, can obtain height by enzymatic hydrolysis The Glucose Liquid of concentration realizes the effective use to cellulose, and is still largely retained in the second solid after enzymatic hydrolysis Lignin, structure retain it is more complete.
The above description is only an overview of the technical scheme of the present invention, in order to better understand the technical means of the present invention, And can be implemented in accordance with the contents of the specification, with presently preferred embodiments of the present invention, detailed description is as follows below.
Specific embodiment
It is of the invention to reach the technical means and efficacy that predetermined goal of the invention is taken further to illustrate, below in conjunction with Preferred embodiment, to a kind of its specific embodiment of the method for comprehensive utilization of corn stover proposed according to the present invention, feature and Its performance, detailed description is as follows.In the following description, what different " embodiment " or " embodiment " referred to is not necessarily same reality Apply example.In addition, the special characteristic, structure or feature in one or more embodiments can be combined by any suitable form.
The embodiment of the present invention propose a kind of corn stover efficiently separate and method for transformation.
The preparation method the following steps are included:
The separation and conversion of hemicellulose: being broken to 20-80 mesh for corn stalk powder, methyl iso-butyl ketone (MIBK) or tetrahydrofuran and Concentration is ratio composition diphasic system of the 10-30wt% sodium chloride solution according to 1:0.5-2.0, by corn stover and diphasic system It is blended, the metal nitrate that 0.01-1.00mol/L is added makees catalyst, and being rapidly heated to 120-200 DEG C, it is anti-to carry out first It answers, reaction temperature is 120-200 DEG C, and the reaction time is 15-150 minutes.After reaction, first is carried out first to be separated by solid-liquid separation, Obtain the first solid and the first liquid, then to the first liquid carry out organic phase and water phase separation, obtain the first organic phase with First water phase, wherein hemicellulose is converted into furfural and is present in the first organic phase, and the first water phase rich in catalyst can be with It is reused;
The separation and conversion of cellulose: it is 50mmol/L that the first solid of gained, which is placed in concentration, and pH is the second of 4.6-5.0 12-24 hours the first dippings, the solid-to-liquid ratio of the first solid and acetic acid-sodium acetate buffer solution are carried out in acid-sodium acetate buffer For 1:20-50g/mL, cellulase is then added, the enzyme activity of cellulase is to contain 10-20 filter paper enzyme activity in every gram of substrate Unit, carries out the enzymatic hydrolysis of 3-72 hour first in 40-60 DEG C of environment, then carries out second and is separated by solid-liquid separation, obtains the second solid And second liquid, wherein cellulose is converted into glucose and is present in second liquid;
The separation of lignin: sufficiently cleaning the second solid using acetic acid-sodium acetate buffer solution, be then dried, In, lignin is present in solid form in the second solid.
With specific embodiment, the present invention will be further described below, but not as the limitation of the invention.
Embodiment 1
The separation and conversion of hemicellulose: corn stalk powder is broken to 20-80 mesh, methyl iso-butyl ketone (MIBK) and concentration are 20wt% sodium chloride solution forms diphasic system according to the ratio of 1:1, and corn stover is blended with diphasic system, is added The chromic nitrate of 0.05mol/L is rapidly heated as catalyst and carries out the first reaction to 160 DEG C, and reaction temperature is 160 DEG C, reaction Time is 30 minutes.After reaction, first is carried out first to be separated by solid-liquid separation, the first solid and the first liquid are obtained, then to the One liquid carries out the separation of organic phase and water phase, obtains the first organic phase and the first water phase, wherein hemicellulose is converted into furfural It is present in the first organic phase, the first water phase rich in catalyst may be repeated utilization;
The separation and conversion of cellulose: it is 50mmol/L, acetic acid-second that pH is 4.7 that the first solid of gained, which is placed in concentration, 12 hours the first dippings are carried out in sour sodium buffer, the solid-to-liquid ratio of the first solid and acetic acid-sodium acetate buffer solution is 1:50g/ Then cellulase is added in mL, the enzyme activity of cellulase is to contain 20 filter paper enzyme activity units in every gram of substrate, in 50 DEG C of ring It carries out 60 hours first digesting in border, then carries out second and be separated by solid-liquid separation, obtain the second solid and second liquid, wherein cellulose Glucose is converted into be present in second liquid;
The separation of lignin: sufficiently cleaning the second solid using acetic acid-sodium acetate buffer solution, be then dried, In, lignin is present in solid form in the second solid.
The furfural and Glucose Liquid obtained using the present embodiment carries out Concentration Testing, and obtaining its furfural yield is 34.2%, enzyme Solving saccharification efficiency is 84.9%, and the solid residue to gained rich in lignin carries out Structural Identification, as the result is shown the knot of lignin Structure retains more complete.
Embodiment 2
The separation and conversion of hemicellulose: corn stalk powder is broken to 20-80 mesh, methyl iso-butyl ketone (MIBK) and concentration are 10wt% sodium chloride solution forms diphasic system according to the ratio of 1:0.5, and corn stover is blended with diphasic system, is added The aluminum nitrate of 0.10mol/L is rapidly heated as catalyst and carries out the first reaction to 160 DEG C, and reaction temperature is 160 DEG C, reaction Time is 60 minutes.After reaction, first is carried out first to be separated by solid-liquid separation, the first solid and the first liquid are obtained, then to the One liquid carries out the separation of organic phase and water phase, obtains the first organic phase and the first water phase, wherein hemicellulose is converted into furfural It is present in the first organic phase, the first water phase rich in catalyst may be repeated utilization;
The separation and conversion of cellulose: it is 50mmol/L, acetic acid-second that pH is 4.8 that the first solid of gained, which is placed in concentration, 24 hours the first dippings are carried out in sour sodium buffer, the solid-to-liquid ratio of the first solid and acetic acid-sodium acetate buffer solution is 1:50g/ Then cellulase is added in mL, the enzyme activity of cellulase is to contain 15 filter paper enzyme activity units in every gram of substrate, in 55 DEG C of ring It carries out 36 hours first digesting in border, then carries out second and be separated by solid-liquid separation, obtain the second solid and second liquid, wherein cellulose Glucose is converted into be present in second liquid;
The separation of lignin: sufficiently cleaning the second solid using acetic acid-sodium acetate buffer solution, be then dried, In, lignin is present in solid form in the second solid.
The furfural and Glucose Liquid obtained using the present embodiment carries out Concentration Testing, and obtaining its furfural yield is 48.0%, enzyme Solving saccharification efficiency is 85.5%, and the solid residue to gained rich in lignin carries out Structural Identification, and fruit shows the structure of lignin Retain more complete.
Embodiment 3
The separation and conversion of hemicellulose: corn stalk powder is broken to 20-80 mesh, tetrahydrofuran and concentration are 30wt% chlorine Change sodium solution and form diphasic system according to the ratio of 1:1, corn stover is blended with diphasic system, 0.50mol/L is added Aluminum nitrate as catalyst, be rapidly heated to 160 DEG C carry out first reaction, reaction temperature be 160 DEG C, the reaction time be 60 points Clock.After reaction, first is carried out first to be separated by solid-liquid separation, obtain the first solid and the first liquid, then the first liquid is carried out The separation of organic phase and water phase obtains the first organic phase and the first water phase, wherein hemicellulose is converted into furfural and is present in first In organic phase, the first water phase rich in catalyst may be repeated utilization;
The separation and conversion of cellulose: it is 50mmol/L, acetic acid-second that pH is 4.9 that the first solid of gained, which is placed in concentration, 12 hours the first dippings are carried out in sour sodium buffer, the solid-to-liquid ratio of the first solid and acetic acid-sodium acetate buffer solution is 1:20g/ Then cellulase is added in mL, the enzyme activity of cellulase is to contain 15 filter paper enzyme activity units in every gram of substrate, in 55 DEG C of ring It carries out 72 hours first digesting in border, then carries out second and be separated by solid-liquid separation, obtain the second solid and second liquid, wherein cellulose Glucose is converted into be present in second liquid;
The separation of lignin: sufficiently cleaning the second solid using acetic acid-sodium acetate buffer solution, be then dried, In, lignin is present in solid form in the second solid.
The furfural and Glucose Liquid obtained using the present embodiment carries out Concentration Testing, and obtaining its furfural yield is 25.0%, enzyme Solving saccharification efficiency is 44.6%, and the solid residue to gained rich in lignin carries out Structural Identification, and fruit shows the structure of lignin Retain more complete.
Embodiment 4
The separation and conversion of hemicellulose: corn stalk powder is broken to 20-80 mesh, tetrahydrofuran and concentration are 10wt% chlorine Change sodium solution and form diphasic system according to the ratio of 1:0.5, corn stover is blended with diphasic system, 0.10mol/ is added The chromic nitrate of L is rapidly heated as catalyst and carries out the first reaction to 180 DEG C, and reaction temperature is 180 DEG C, the reaction time 30 Minute.After reaction, first carry out first be separated by solid-liquid separation, obtain the first solid and the first liquid, then to the first liquid into The separation of row organic phase and water phase obtains the first organic phase and the first water phase, wherein hemicellulose is converted into furfural and is present in In one organic phase, the first water phase rich in catalyst may be repeated utilization;
The separation and conversion of cellulose: it is 50mmol/L, acetic acid-second that pH is 4.8 that the first solid of gained, which is placed in concentration, 24 hours the first dippings are carried out in sour sodium buffer, the solid-to-liquid ratio of the first solid and acetic acid-sodium acetate buffer solution is 1:50g/ Then cellulase is added in mL, the enzyme activity of cellulase is to contain 20 filter paper enzyme activity units in every gram of substrate, in 50 DEG C of ring It carries out 60 hours first digesting in border, then carries out second and be separated by solid-liquid separation, obtain the second solid and second liquid, wherein cellulose Glucose is converted into be present in second liquid;
The separation of lignin: sufficiently cleaning the second solid using acetic acid-sodium acetate buffer solution, be then dried, In, lignin is present in solid form in the second solid.
The furfural and Glucose Liquid obtained using the present embodiment carries out Concentration Testing, and obtaining its furfural yield is 42.0%, enzyme Solving saccharification efficiency is 80.9%, and the solid residue to gained rich in lignin carries out Structural Identification, and fruit shows the structure of lignin Retain more complete.
The above described is only a preferred embodiment of the present invention, be not intended to limit the present invention in any form, according to According to technical spirit any simple modification, equivalent change and modification to the above embodiments of the invention, this hair is still fallen within In the range of bright technical solution.

Claims (5)

1.一种玉米秸秆的高效分离与转化方法,其特征在于,包括以下步骤:1. a high-efficiency separation and transformation method of corn stover, is characterized in that, comprises the following steps: 半纤维素的分离与转化:将玉米秸秆粉碎至20-80目,与有机溶剂和氯化钠溶液所组成的双相体系进行共混,加入催化剂,快速升温至第一温度进行第一反应,反应结束后,首先进行第一固液分离,得到第一固体和第一液体,然后对第一液体进行有机相和水相的分离,得到第一有机相与第一水相,其中,半纤维素转化为糠醛存在于第一有机相当中,富含催化剂的第一水相可以进行重复利用;Separation and conversion of hemicellulose: pulverize corn stalks to 20-80 mesh, blend with a two-phase system composed of organic solvent and sodium chloride solution, add catalyst, and quickly heat up to the first temperature to carry out the first reaction, After the reaction is completed, first solid-liquid separation is performed to obtain a first solid and a first liquid, and then the first liquid is separated from an organic phase and an aqueous phase to obtain a first organic phase and a first aqueous phase, wherein the hemifibers are The element is converted into furfural and exists in the first organic phase, and the first aqueous phase rich in catalyst can be reused; 纤维素的分离与转化:将所得第一固体置于乙酸-乙酸钠缓冲液中进行第一浸渍,然后加入纤维素酶,进行第一酶解,随后进行第二固液分离,得到第二固体和第二液体,其中纤维素转化为葡萄糖存在于第二液体中;Separation and conversion of cellulose: the first solid obtained is placed in an acetic acid-sodium acetate buffer for first dipping, then cellulase is added to carry out the first enzymatic hydrolysis, and then the second solid-liquid separation is carried out to obtain a second solid and a second liquid, wherein the conversion of cellulose to glucose is present in the second liquid; 木质素的分离:使用乙酸-乙酸钠缓冲液对第二固体充分清洗,然后进行干燥,其中,木质素以固体形式存在于第二固体中。Isolation of lignin: The second solid was washed thoroughly with acetic acid-sodium acetate buffer, and then dried, wherein the lignin was present in the second solid in solid form. 2.根据权利要求1所述的制备方法,其特征在于,2. preparation method according to claim 1, is characterized in that, 所述催化剂为金属硝酸盐,具体包括硝酸铁、硝酸镍、硝酸铬、硝酸铝中的任意一种;Described catalyzer is metal nitrate, specifically includes any one in ferric nitrate, nickel nitrate, chromium nitrate, aluminum nitrate; 所述催化剂浓度为0.01-1.00mol/L。The catalyst concentration is 0.01-1.00mol/L. 3.根据权利要求1所述的制备方法,其特征在于,3. preparation method according to claim 1, is characterized in that, 所述有机溶剂为甲基异丁基酮、四氢呋喃中的任意一种;Described organic solvent is any one in methyl isobutyl ketone, tetrahydrofuran; 所述氯化钠溶液浓度为10-30wt%;The concentration of the sodium chloride solution is 10-30wt%; 所述有机溶剂与氯化钠溶液的体积比为1:0.5-2.0。The volume ratio of the organic solvent to the sodium chloride solution is 1:0.5-2.0. 4.根据权利要求1所述的制备方法,其特征在于,4. preparation method according to claim 1, is characterized in that, 所述第一温度为120-200℃;the first temperature is 120-200°C; 所述第一反应的条件为:温度120-200℃,时间15-150分钟。The conditions of the first reaction are: temperature 120-200° C., time 15-150 minutes. 5.根据权利要求1所述的制备方法,其特征在于,5. preparation method according to claim 1, is characterized in that, 所述乙酸-乙酸钠缓冲液浓度为50mmol/L,pH为4.6-5.0;The acetic acid-sodium acetate buffer concentration is 50mmol/L, and the pH is 4.6-5.0; 所述第一浸渍时间为12-24小时;The first dipping time is 12-24 hours; 所述第一固体与乙酸-乙酸钠缓冲液的固液比为1:20-50g/mL;The solid-to-liquid ratio of the first solid to the acetic acid-sodium acetate buffer is 1:20-50g/mL; 所述纤维素酶的酶活为每克底物中含有10-20个滤纸酶活单位;The enzymatic activity of the cellulase is 10-20 filter paper enzymatic activity units per gram of substrate; 所述第一酶解的条件为:时间3-72小时,温度40-60℃。The conditions of the first enzymatic hydrolysis are: time 3-72 hours, temperature 40-60°C.
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CN114085252A (en) * 2021-10-21 2022-02-25 中国林业科学研究院林产化学工业研究所 A comprehensive utilization method of organic acid-catalyzed two-phase system for separating wood fiber

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