CN102936632B - A method for improving cellulose hydrolysis efficiency - Google Patents

A method for improving cellulose hydrolysis efficiency Download PDF

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CN102936632B
CN102936632B CN201210438249.1A CN201210438249A CN102936632B CN 102936632 B CN102936632 B CN 102936632B CN 201210438249 A CN201210438249 A CN 201210438249A CN 102936632 B CN102936632 B CN 102936632B
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蒋学
田秀枝
王树根
蒋静
翁佛全
顾坚
黄丹
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Gaomi Yinying New Material Co ltd
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Abstract

本发明涉及一种纤维素改性剂的制备方法及其应用,尤其是一种能提高纤维素水解效率的方法。本发明以三聚氯氰为活性组份,以苯酚或对羟基苯磺酸或1-氨基-8-萘酚-3、6-二磺酸钠为功能组份,合成三嗪衍生物的纤维素改性剂,通过红外光谱和质谱图表征其结构。然后用合成出来的三嗪衍生物对纤维进行修饰,并将修饰后的微晶纤维素在8%的H2SO4、130℃下水解5h,结果表明,当改性剂的相对摩尔含量(以葡萄糖环计)在16.67%时,纤维素水解成还原糖得率最大为23.54%;通过分析广角X射线衍射图发现改性使微晶纤维素的结晶结构发生变化,无定形区增加、结晶指数下降、晶粒尺寸减小。该方法在纤维素水解中具有广阔的应用前景。The invention relates to a preparation method and application of a cellulose modifier, in particular to a method capable of improving cellulose hydrolysis efficiency. The present invention uses cyanuric chloride as the active component and phenol or p-hydroxybenzenesulfonic acid or 1-amino-8-naphthol-3,6-sodium disulfonate as the functional component to synthesize the fiber of triazine derivatives prime modifier, and its structure was characterized by infrared and mass spectrograms. Then the fiber was modified with the synthesized triazine derivative, and the modified microcrystalline cellulose was hydrolyzed in 8% H 2 SO 4 at 130°C for 5 hours. The results showed that when the relative molar content of the modifier ( (based on glucose ring) at 16.67%, the maximum yield of cellulose hydrolyzed into reducing sugar is 23.54%. Through the analysis of wide-angle X-ray diffraction patterns, it is found that the modification changes the crystal structure of microcrystalline cellulose, increases the amorphous area, and crystallizes. The index decreases and the grain size decreases. This method has broad application prospects in cellulose hydrolysis.

Description

一种提高纤维素水解效率的方法A method for improving cellulose hydrolysis efficiency

技术领域 technical field

本发明涉及一种提高纤维素水解效率的方法,尤其是一种利用纤维素的化学改性提高纤维素水解效率的方法。The invention relates to a method for improving cellulose hydrolysis efficiency, in particular to a method for improving cellulose hydrolysis efficiency by chemical modification of cellulose.

背景技术 Background technique

乙醇(俗称酒精)是一种重要的工业原料,广泛应用于化工、食品、饮料工业、军工、日用化工和医药卫生等领域,还能作为能源工业的基础原料、燃料(燃烧值为26900KJ/Kg)。纤维素是自然界中含量最高的多糖资源之一,利用纤维素转化成乙醇作为生物质能源在化石能源代替研究领域倍受关注,然而纤维素转化为清洁燃料以及化学品乙醇的关键,是寻找有效途径将纤维素水解为葡萄糖等可溶性发酵糖。纤维素是β-D-葡萄糖残基彼此以1,4-糖甙键链接成的长链分子,长链分子进一步形成一种具有高度结晶区的超分子稳定结构,这使得纤维素很难水解。Ethanol (commonly known as alcohol) is an important industrial raw material, which is widely used in the fields of chemical industry, food, beverage industry, military industry, daily chemical industry, medicine and health, etc. Kg). Cellulose is one of the polysaccharide resources with the highest content in nature. The conversion of cellulose into ethanol as biomass energy has attracted much attention in the field of fossil energy replacement research. However, the key to converting cellulose into clean fuel and chemical ethanol is to find effective The pathway hydrolyzes cellulose to soluble fermentable sugars such as glucose. Cellulose is a long-chain molecule in which β-D-glucose residues are linked by 1,4-glycosidic bonds. The long-chain molecule further forms a supramolecular stable structure with highly crystalline regions, which makes cellulose difficult to hydrolyze. .

科学研究发现,对纤维素进行一定的预处理,可以提高其水解产生还原糖的得率,目前纤维素预处理的方法主要有物理方法(机械粉碎、蒸汽爆破、超临界水处理等)、化学方法(碱处理、酸处理、氧化剂处理等)、生物方法。但是,这些方法都有两面性,如蒸汽爆破法会产生抑制酶水解和发酵的物质,碱处理可以在除去一部分木质素的同时也带走部分半纤维素,影响总糖的得率等。而且针对纤维素原料的大部分预处理方法都不改变其链结构,对结晶结构的影响很小,导致酶催化水解只能在纤维素无定形区发生,酸催化剂对纤维素结晶区的可及度也很小。因此,寻找显著提高纤维素可及度的预处理方法仍然是目前纤维素-乙醇转化研究的重点。Scientific research has found that certain pretreatment of cellulose can increase the yield of reducing sugars produced by its hydrolysis. Currently, cellulose pretreatment methods mainly include physical methods (mechanical crushing, steam explosion, supercritical water treatment, etc.), chemical Methods (alkaline treatment, acid treatment, oxidant treatment, etc.), biological methods. However, these methods have two sides. For example, the steam explosion method will produce substances that inhibit enzymatic hydrolysis and fermentation. Alkali treatment can remove part of the lignin and also take away part of the hemicellulose, affecting the yield of total sugar. Moreover, most of the pretreatment methods for cellulose raw materials do not change its chain structure, and have little effect on the crystal structure, resulting in enzyme-catalyzed hydrolysis that can only occur in the amorphous region of cellulose, and the acid catalyst is accessible to the cellulose crystal region. The degree is also very small. Therefore, finding a pretreatment method that significantly improves the accessibility of cellulose is still the focus of current cellulose-ethanol conversion research.

泊萨等人报道了低取代度的羧甲基纤维素水解效率比纤维素高(J.Borsa,I.Tanczos,I.Rusznak.Acid hydrolysis of carboxymethylcellulsoe of low degree of substitution[J].ColloldPolymer Science,1990,268(7):649-657);戴维,喀斯特等人应用分子模拟方法研究了不同体积的基团改性的纤维素,预测出体积较大的取代基对提高纤维素水解效率有利(David T.Karst,Yiqi Yang.Effect of structure of large aromatic molecules grafted onto cellulsoe on hydrolysis ofthe glycosidic linkages[J].Macromolecular Chemistry and Physics,2007,208:784-791);蒋学等披露了带氨基、磺酸基的苯基取代的三聚氯氰改性纤维素的水解糖得率得到了显著增加(蒋学,田秀枝,顾坚,黄丹,王树根.申请号:201110154930.9)。Posa et al reported that the hydrolysis efficiency of carboxymethylcellulose with low degree of substitution is higher than that of cellulose (J.Borsa, I.Tanczos, I.Rusznak.Acid hydrolysis of carboxymethylcellulsoe of low degree of substitution[J]. 1990,268(7):649-657); David, Karst et al. used molecular simulation methods to study the cellulose modified by groups with different volumes, and predicted that the substituents with larger volumes are beneficial to improve the hydrolysis efficiency of cellulose (David T. Karst, Yiqi Yang. Effect of structure of large aromatic molecules grafted onto cellulose on hydrolysis of the glycosidic linkages [J]. Macromolecular Chemistry and Physics, 2007, 208:784-791); The hydrolysis sugar yield of cyanuric chloride-modified cellulose with phenyl-substituted sulfonic acid groups has been significantly increased (Jiang Xue, Tian Xiuzhi, Gu Jian, Huang Dan, Wang Shugen. Application number: 201110154930.9).

因此,本发明以三聚氯氰基为活性组份,以含有羟基的化合物苯酚、对羟基苯磺酸、1-氨基-8-萘酚-3、6-二磺酸钠为功能组份,利用羟基与三聚氯氰的反应合成出改性剂,并对纤维素进行改性,通过改性剂的反应改变纤维素的链结构,降低纤维素的结晶度进而提高纤维素水解效率。Therefore, the present invention uses cyanuric chloride as an active component, and compound phenol, p-hydroxybenzenesulfonic acid, 1-amino-8-naphthol-3,6-sodium disulfonate as a functional component, The modifier is synthesized by the reaction of hydroxyl and cyanuric chloride, and the cellulose is modified, the chain structure of the cellulose is changed through the reaction of the modifier, the crystallinity of the cellulose is reduced, and the hydrolysis efficiency of the cellulose is improved.

发明内容 Contents of the invention

本发明的目的是克服现有纤维素燃料乙醇制备技术中存在的不足,提供一种提高纤维素水解效率的方法,其特征包括以下步骤:The purpose of the invention is to overcome the deficiencies in the existing cellulose fuel ethanol preparation technology, and provide a method for improving cellulose hydrolysis efficiency, which is characterized in that it comprises the following steps:

1)在配有搅拌的反应器中加入活性组份溶液和还原剂,将功能组份溶液置于恒压滴液漏中并缓慢滴入反应器,历时1~2h滴毕,然后0~5℃下反应1~3h;沉淀后过滤,并用有机溶剂重结晶,固体于50℃真空干燥,改性剂产率60%~80%。1) Add the active component solution and reducing agent into the reactor equipped with stirring, put the functional component solution in the constant pressure dripping tank and slowly drop it into the reactor for 1~2h, then 0~5 React at ℃ for 1~3h; filter after precipitation, recrystallize with organic solvent, dry the solid in vacuum at 50℃, and the yield of modifier is 60%~80%.

2)将2份纤维素、10~40份溶剂、4份碱溶液置于反应器中,相对摩尔百分含量(以葡萄糖环计)为1/40~1份的改性剂溶液置于恒压漏斗中,缓慢滴加碱溶液到入反应器中,40℃下反应3h;反应结束后产物抽滤,用清水洗涤滤饼pH至中性,于50℃真空烘箱中干燥24h;将1~0.5份改性纤维素置于配有搅拌的反应器中,加入浓度为8%的硫酸10ml,130℃下水解5h,离心分离,得水解产物。2) Put 2 parts of cellulose, 10-40 parts of solvent, and 4 parts of alkali solution in the reactor, and place the modifier solution with a relative molar percentage (based on glucose ring) of 1/40-1 part in a constant In the pressure funnel, slowly drop the alkali solution into the reactor, and react at 40°C for 3h; after the reaction, the product was suction filtered, and the filter cake was washed with water until the pH was neutral, and dried in a vacuum oven at 50°C for 24h; Put 0.5 parts of modified cellulose in a stirred reactor, add 10 ml of 8% sulfuric acid, hydrolyze at 130°C for 5 hours, and centrifuge to obtain a hydrolyzate.

所述活性组分与功能组分的摩尔质量比为1:1~2。。The molar mass ratio of the active component to the functional component is 1:1-2. .

所述活性组份为三聚氯氰,The active component is cyanuric chloride,

所述活性组份溶液的溶剂为二氯甲烷或丙酮。The solvent of the active component solution is dichloromethane or acetone.

所述还原剂为无水亚硫酸钠。The reducing agent is anhydrous sodium sulfite.

所述功能组份为苯酚、对羟基苯磺酸、1-氨基-8-萘酚-3、6-二磺酸钠中的任一种或一种以上任意比例的混合。The functional component is any one of phenol, p-hydroxybenzenesulfonic acid, 1-amino-8-naphthol-3, 6-sodium disulfonate or a mixture of more than one in any proportion.

所述功能组份溶液的溶剂为无水碳酸钠的水溶液。The solvent of the functional component solution is an aqueous solution of anhydrous sodium carbonate.

所述重结晶溶剂为四氢呋喃和水的混合。The recrystallization solvent is a mixture of tetrahydrofuran and water.

所述碱溶液为10%氢氧化钠溶液。The alkaline solution is 10% sodium hydroxide solution.

本发明以含有羟基的化合物苯酚、对羟基苯磺酸、1-氨基-8-萘酚-3、6-二磺酸钠为功能组份,在活性组份三聚氯氰中仅引入含羟基的苯环和萘环,合成三嗪衍生物的纤维素改性剂,然后用合成出的含有不同比例的单苯氧基和萘环氧基三嗪环的三嗪衍生物改性纤维素,含有羟基的苯环和萘环的均三嗪基团对纤维素进行改性。实验表明,经三嗪衍生物改性的纤维素水解后的还原糖得率提高了,如当改性剂的相对摩尔含量(以葡萄糖环计)在16.67%时,纤维素水解成还原糖得率最大为23.54%;通过分析广角X射线衍射图发现改性使微晶纤维素的结晶结构发生变化,无定形区增加、结晶指数下降、晶粒尺寸减小。通过改变纤维素的链结构,降低纤维素的结晶度进而提高纤维素水解成可发酵糖的转化率,该方法在纤维素水解中具有广阔的应用前景。The present invention uses hydroxyl-containing compounds phenol, p-hydroxybenzenesulfonic acid, and 1-amino-8-naphthol-3,6-sodium disulfonate as functional components, and only introduces hydroxyl-containing compounds into the active component cyanuric chloride benzene ring and naphthalene ring, synthetic cellulose modifier of triazine derivatives, and then modified cellulose with the synthesized triazine derivatives containing different proportions of monophenoxy and naphthyl epoxy triazine rings, Cellulose is modified by s-triazine groups containing benzene rings and naphthalene rings. Experiments have shown that the yield of reducing sugar after hydrolysis of cellulose modified by triazine derivatives is increased. The maximum rate is 23.54%. By analyzing the wide-angle X-ray diffraction pattern, it is found that the modification changes the crystal structure of microcrystalline cellulose, increases the amorphous area, decreases the crystallization index, and reduces the grain size. By changing the chain structure of cellulose, reducing the crystallinity of cellulose and increasing the conversion rate of cellulose hydrolysis into fermentable sugar, this method has broad application prospects in cellulose hydrolysis.

说明书附图Instructions attached

图1改性剂的质谱图Figure 1 Mass Spectrum of Modifier

图2改性剂的红外光谱The infrared spectrum of Fig. 2 modifier

图3改性纤维素的红外光谱Figure 3 Infrared spectrum of modified cellulose

图4改性纤维素的X射线衍射图,(A)纤维素;(B)~(F):实施例1~5The X-ray diffraction figure of Fig. 4 modified cellulose, (A) cellulose; (B) ~ (F): embodiment 1 ~ 5

具体实施方式 Detailed ways

本发明主要包括三部分内容:The present invention mainly comprises three parts:

(1)合成含有活性组份和功能组份的改性剂;(1) Synthesis of modifiers containing active components and functional components;

(2)利用改性剂与纤维素反应制备改性纤维素;(2) Prepare modified cellulose by reacting modifier with cellulose;

(3)不同比例的改性纤维素的水解。(3) Hydrolysis of modified cellulose with different proportions.

下面结合具体实施例对本发明作进一步说明。The present invention will be further described below in conjunction with specific examples.

实施例1:Example 1:

(1)称取4份三聚氯氰于反应器中,加入40份二氯甲烷,然后置于冰水浴中搅拌;2份苯酚和2份无水碳酸钠及0.1份无水亚硫酸钠用30份水溶解后慢慢滴入上述体系,历时1h滴毕,继续反应2h,停止反应,倒入分液漏斗中,静置1h,待体系充分分层后,分出下层透明液,蒸出二氯甲烷得粗产品,粗产品用四氢呋喃-水重结晶得到白色固体,产率65.5%。(1) Weigh 4 parts of cyanuric chloride into the reactor, add 40 parts of dichloromethane, and then stir in an ice-water bath; use 30 parts of 2 parts of phenol, 2 parts of anhydrous sodium carbonate and 0.1 part of anhydrous sodium sulfite After the water is dissolved, it is slowly dripped into the above system, and it lasts for 1 hour. Continue to react for 2 hours, stop the reaction, pour it into a separatory funnel, and let it stand for 1 hour. The crude product was obtained from methane, and the crude product was recrystallized from THF-water to obtain a white solid with a yield of 65.5%.

(2)称取2份纤维素于反应器中,加入10份丙酮;称取相对摩尔含量(以葡萄糖环计)为1/40份改性剂,并加入30份丙酮搅拌下使之溶解,并慢慢地滴入上述体系中;以10wt%NaOH为催化剂,在温度为40℃下反应3h,产物经抽滤、去离子水洗涤至中性,所得固体在减压下烘燥24h;(2) Weigh 2 parts of cellulose into the reactor, add 10 parts of acetone; weigh the relative molar content (based on glucose ring) of 1/40 parts of modifier, and add 30 parts of acetone to dissolve it under stirring, And slowly drop it into the above system; use 10wt% NaOH as a catalyst, react at a temperature of 40°C for 3 hours, the product is filtered by suction and washed with deionized water until neutral, and the obtained solid is dried under reduced pressure for 24 hours;

(3)将0.5份改性纤维素置于反应器中,加入浓度为8%的硫酸10份,130℃下水解5h,离心分离,得水解产物待检测。(3) Put 0.5 parts of modified cellulose in a reactor, add 10 parts of sulfuric acid with a concentration of 8%, hydrolyze at 130°C for 5 hours, and centrifuge to obtain hydrolyzed products to be tested.

实施例2:Example 2:

(1)称取2份三聚氯氰于反应器中,加入20份二氯甲烷,然后置于冰水浴中搅拌;1份苯酚和1份无水碳酸钠及0.1份无水亚硫酸钠用30份水溶解后慢慢滴入上述体系,历时1h滴毕,继续反应2h,停止反应,倒入分液漏斗中,静置1h,待体系充分分层后,分出下层透明液,蒸出二氯甲烷得粗产品,粗产品用四氢呋喃-水重结晶得到白色固体,产率75.5%。(1) Weigh 2 parts of cyanuric chloride into the reactor, add 20 parts of dichloromethane, and then stir in an ice-water bath; use 30 parts of 1 part of phenol, 1 part of anhydrous sodium carbonate and 0.1 part of anhydrous sodium sulfite After the water is dissolved, it is slowly dripped into the above system, and it lasts for 1 hour. Continue to react for 2 hours, stop the reaction, pour it into a separatory funnel, and let it stand for 1 hour. The crude product was obtained from methane, and the crude product was recrystallized from THF-water to obtain a white solid with a yield of 75.5%.

(2)称取2份纤维素于反应器中,加入10份丙酮;称取相对摩尔含量(以葡萄糖环计)为1/20改性剂,并加入30份丙酮搅拌下使之溶解,并慢慢地滴入上述体系中;以10wt%NaOH为催化剂,在温度为40℃下反应3h,产物经抽滤、去离子水洗涤至中性,所得固体在减压下烘燥24h;(2) Weigh 2 parts of cellulose in the reactor, add 10 parts of acetone; weigh the relative molar content (based on glucose ring) as 1/20 modifier, add 30 parts of acetone to dissolve it under stirring, and Slowly drop into the above system; use 10wt% NaOH as a catalyst, react at a temperature of 40°C for 3 hours, the product is filtered by suction and washed with deionized water until neutral, and the obtained solid is dried under reduced pressure for 24 hours;

(3)将0.5份改性纤维素置于反应器中,加入浓度为8%的硫酸10份,130℃下水解5h,离心分离,得水解产物待检测。(3) Put 0.5 parts of modified cellulose in a reactor, add 10 parts of sulfuric acid with a concentration of 8%, hydrolyze at 130°C for 5 hours, and centrifuge to obtain hydrolyzed products to be tested.

实施例3:Example 3:

(1)称取1份三聚氯氰于反应器中,加入10份二氯甲烷,然后置于冰水浴中搅拌;1份苯酚和1份无水碳酸钠及0.1份无水亚硫酸钠用30份水溶解后慢慢滴入上述体系,历时1h滴毕,继续反应2h,停止反应,倒入分液漏斗中,静置1h,待体系充分分层后,分出下层透明液,蒸出二氯甲烷得粗产品,粗产品用四氢呋喃-水重结晶得到白色固体,产率60.5%。(1) Weigh 1 part of cyanuric chloride into the reactor, add 10 parts of dichloromethane, and then stir in an ice-water bath; use 30 parts of 1 part of phenol, 1 part of anhydrous sodium carbonate and 0.1 part of anhydrous sodium sulfite After the water is dissolved, it is slowly dripped into the above system, and it lasts for 1 hour. Continue to react for 2 hours, stop the reaction, pour it into a separatory funnel, and let it stand for 1 hour. The crude product was obtained from methane, and the crude product was recrystallized with tetrahydrofuran-water to obtain a white solid with a yield of 60.5%.

(2)称取2份纤维素于反应器中,加入10份丙酮;称取相对摩尔含量(以葡萄糖环计)为1/5份改性剂,并加入30份丙酮搅拌下使之溶解,并慢慢地滴入上述体系中;以10wt%NaOH为催化剂,在温度为40℃下反应3h,产物经抽滤、去离子水洗涤至中性,所得固体在减压下烘燥24h;(2) Weigh 2 parts of cellulose into the reactor, add 10 parts of acetone; weigh the relative molar content (based on glucose ring) of 1/5 parts of modifier, and add 30 parts of acetone to dissolve it under stirring, And slowly drop it into the above system; use 10wt% NaOH as a catalyst, react at a temperature of 40°C for 3 hours, the product is filtered by suction and washed with deionized water until neutral, and the obtained solid is dried under reduced pressure for 24 hours;

(3)将0.5份改性纤维素置于反应器中,加入浓度为8%的硫酸10份,130℃下水解5h,离心分离,得水解产物待检测。(3) Put 0.5 parts of modified cellulose in a reactor, add 10 parts of sulfuric acid with a concentration of 8%, hydrolyze at 130°C for 5 hours, and centrifuge to obtain hydrolyzed products to be tested.

实施例4:Example 4:

(1)称取4份三聚氯氰于反应器中,加入40份丙酮,然后置于冰水浴中搅拌;2份对羟基苯磺酸和2份无水碳酸钠及0.1份无水亚硫酸钠用30份水溶解后慢慢滴入上述体系,历时1h滴毕,继续反应2h,停止反应,倒入分液漏斗中,静置1h,待体系充分分层后,分出下层透明液,蒸出二氯甲烷得粗产品,粗产品用四氢呋喃-水重结晶得到白色固体,产率65.5%。(1) Weigh 4 parts of cyanuric chloride into the reactor, add 40 parts of acetone, and then stir in an ice-water bath; 2 parts of p-hydroxybenzenesulfonic acid, 2 parts of anhydrous sodium carbonate and 0.1 part of anhydrous sodium sulfite are used After dissolving 30 parts of water, slowly drop into the above system, after 1 hour, continue to react for 2 hours, stop the reaction, pour it into a separatory funnel, and let it stand for 1 hour. After the system is fully layered, separate the lower transparent liquid and evaporate The crude product was obtained from dichloromethane, and the crude product was recrystallized with tetrahydrofuran-water to obtain a white solid with a yield of 65.5%.

(2)称取2份纤维素于反应器中,加入10mL丙酮;称取相对摩尔含量(以葡萄糖环计)为1/3份改性剂,并加入30份丙酮搅拌下使之溶解,并慢慢地滴入上述体系中;以10wt%NaOH为催化剂,在温度为40℃下反应3h,产物经抽滤、去离子水洗涤至中性,所得固体在减压下烘燥24h;(2) Weigh 2 parts of cellulose into the reactor, add 10 mL of acetone; weigh the relative molar content (based on glucose rings) of 1/3 part of modifier, add 30 parts of acetone and stir to dissolve it, and Slowly drop into the above system; use 10wt% NaOH as a catalyst, react at a temperature of 40°C for 3 hours, the product is filtered by suction and washed with deionized water until neutral, and the obtained solid is dried under reduced pressure for 24 hours;

(3)将0.5份改性纤维素置于反应器中,加入浓度为8%的硫酸10份,130℃下水解5h,离心分离,得水解产物待检测。(3) Put 0.5 parts of modified cellulose in a reactor, add 10 parts of sulfuric acid with a concentration of 8%, hydrolyze at 130°C for 5 hours, and centrifuge to obtain hydrolyzed products to be tested.

实施例5:Example 5:

(1)称取4份三聚氯氰于反应器中,加入40份二氯甲烷,然后置于冰水浴中搅拌;2份1-氨基-8-萘酚-3、6-二磺酸钠和2份无水碳酸钠及0.1份无水亚硫酸钠用30份水溶解后慢慢滴入上述体系,历时1h滴毕,继续反应2h,停止反应,倒入分液漏斗中,静置1h,待体系充分分层后,分出下层透明液,蒸出二氯甲烷得粗产品,粗产品用四氢呋喃-水重结晶得到白色固体,产率65.5%。(1) Weigh 4 parts of cyanuric chloride in the reactor, add 40 parts of dichloromethane, and then stir in an ice-water bath; 2 parts of 1-amino-8-naphthol-3,6-sodium disulfonate Dissolve 2 parts of anhydrous sodium carbonate and 0.1 part of anhydrous sodium sulfite with 30 parts of water and slowly drop into the above system. After 1 hour of dripping, continue to react for 2 hours, stop the reaction, pour it into a separatory funnel, and let it stand for 1 hour. After the system was fully layered, the lower transparent liquid was separated, and dichloromethane was distilled off to obtain a crude product, which was recrystallized with tetrahydrofuran-water to obtain a white solid with a yield of 65.5%.

(2)称取2份纤维素于反应器中,加入10份丙酮;称取相对摩尔含量(以葡萄糖环计)为1/2份改性剂,并加入30份丙酮搅拌下使之溶解,并慢慢地滴入上述体系中;以10wt%NaOH为催化剂,在温度为40℃下反应3h,产物经抽滤、去离子水洗涤至中性,所得固体在减压下烘燥24h;(2) Weigh 2 parts of cellulose into the reactor, add 10 parts of acetone; weigh the relative molar content (based on glucose ring) as 1/2 part of modifier, and add 30 parts of acetone to dissolve it under stirring, And slowly drop it into the above system; use 10wt% NaOH as a catalyst, react at a temperature of 40°C for 3 hours, the product is filtered by suction and washed with deionized water until neutral, and the obtained solid is dried under reduced pressure for 24 hours;

(3)将0.5份改性纤维素置于反应器中,加入浓度为8%的硫酸10份,130℃下水解5h,离心分离,得水解产物待检测。(3) Put 0.5 parts of modified cellulose in a reactor, add 10 parts of sulfuric acid with a concentration of 8%, hydrolyze at 130°C for 5 hours, and centrifuge to obtain hydrolyzed products to be tested.

本发明所述的改性方法得到的改性纤维素的结构及水解性能等各项性能可采用以下指标进行检测:Various performances such as the structure of the modified cellulose that the modification method of the present invention obtains and hydrolysis performance can adopt following index to detect:

(1)还原糖含量:采用3,5-二硝基水杨酸比色法(DNS)测定水解液中还原糖含量。494nm处测得的葡萄糖标准曲线为Y=0.91412X-0.10154(R2=0.9985)。计算方法如下式:(1) Reducing sugar content: 3,5-dinitrosalicylic acid colorimetric method (DNS) was used to measure the reducing sugar content in the hydrolyzate. The glucose standard curve measured at 494nm is Y=0.91412X-0.10154 (R 2 =0.9985). The calculation method is as follows:

Figure BDA00002360560500051
Figure BDA00002360560500051

(2)结构分析测定:FTIR分析使用NICOLET NEXUS 470红外光谱仪,样品制备采用KBr压片法。光谱仪分辨率为4cm-1,扫描次数为30。样品的X-射线衍射分析在德国BrukerAXS公司的D8Advance型X-射线衍射仪上进行,采用铜靶Cu Kα(λ=0.15406nm),功率为1600W(40kV×40mA),采用NaI晶体闪烁计数器测量X-射线的强度,扫描范围为3°-60°,扫描速度4°/min,步长0.02°。(2) Structural analysis and determination: NICOLET NEXUS 470 infrared spectrometer was used for FTIR analysis, and KBr tablet method was used for sample preparation. The resolution of the spectrometer is 4 cm -1 , and the number of scans is 30. The X-ray diffraction analysis of the sample is carried out on the D8Advance type X-ray diffractometer of Germany BrukerAXS company, adopts copper target Cu Kα (λ=0.15406nm), power is 1600W (40kV * 40mA), adopts NaI crystal scintillation counter to measure X - The intensity of the ray, the scanning range is 3°-60°, the scanning speed is 4°/min, and the step size is 0.02°.

(3)晶粒尺寸计算:晶粒尺寸根据Scherrer公式

Figure BDA00002360560500052
计算,其中D为晶粒尺寸;k为Scherrer常数,取k=0.89;λ为X射线波长,对铜靶λ=0.15406nm;B为特征衍射峰的最大半高宽,以弧度表示;θ为Bragg角,文中计算002面的晶粒尺寸。采用公式CrI=(I002-Iam)/I002计算产物的结晶指数,式中I002为002晶面衍射强度的最大值,Iam指2θ=18.3°处的衍射强度。(3) Calculation of grain size: grain size according to Scherrer formula
Figure BDA00002360560500052
Calculation, where D is the grain size; k is the Scherrer constant, take k=0.89; λ is the wavelength of X-rays, λ=0.15406nm for the copper target; B is the maximum full width at half maximum of the characteristic diffraction peak, expressed in radians; θ is Bragg angle, the grain size of the 002 plane is calculated in this paper. The crystallization index of the product was calculated using the formula CrI=(I 002 -I am )/I 002 , where I 002 is the maximum value of the diffraction intensity of the 002 crystal plane, and I am refers to the diffraction intensity at 2θ=18.3°.

表1改性纤维素检测结果Table 1 Modified cellulose detection results

Figure BDA00002360560500061
Figure BDA00002360560500061

Claims (4)

1.一种提高纤维素水解效率的方法,其特征包括以下步骤:1. A method for improving cellulose hydrolysis efficiency, characterized in that it comprises the following steps: 1)在配有搅拌的反应器中加入活性组份溶液和还原剂,将功能组份溶液置于恒压滴液漏中并缓慢滴入反应器,历时1~2h滴毕,然后0~5℃下反应1~3h;沉淀后过滤,并用有机溶剂重结晶,固体于50℃真空干燥,改性剂产率60%~80%;2)将2份纤维素、10~40份溶剂、4份碱溶液置于反应器中,以葡萄糖环计的相对摩尔百分含量为1/40~1份的改性剂溶液置于恒压漏斗中,缓慢滴加碱溶液到入反应器中,40℃下反应3h;反应结束后产物抽滤,用清水洗涤滤饼pH至中性,于50℃真空烘箱中干燥24h;将1~0.5份改性纤维素置于配有搅拌的反应器中,加入浓度为8%的硫酸10ml,130℃下水解5h,离心分离,得水解产物;所述活性组分与功能组分的摩尔质量比为1:1~2;所述活性组份为三聚氯氰;所述活性组份溶液的溶剂为二氯甲烷或丙酮;所述还原剂为无水亚硫酸钠;所述功能组份为苯酚、对羟基苯磺酸、1-氨基-8-萘酚-3、6-二磺酸钠中的任一种或一种以上任意比例的混合。1) Add the active component solution and reducing agent into the reactor equipped with stirring, put the functional component solution in the constant pressure dripping tank and slowly drop it into the reactor for 1~2 hours, then 0~5 Reaction at ℃ for 1~3h; filter after precipitation, and recrystallize with organic solvent, dry the solid in vacuum at 50℃, the yield of modifier is 60%~80%; 2) Mix 2 parts of cellulose, 10~40 parts of solvent, 4 One part of alkaline solution is placed in the reactor, and the relative molar percentage based on the glucose ring is 1/40 to 1 part of the modifying agent solution is placed in a constant pressure funnel, and the alkaline solution is slowly added dropwise into the reactor, 40 React at ℃ for 3 hours; after the reaction, the product is suction filtered, the filter cake is washed with water until the pH is neutral, and dried in a vacuum oven at 50℃ for 24 hours; 1-0.5 parts of modified cellulose are placed in a reactor equipped with stirring, Add 10ml of sulfuric acid with a concentration of 8%, hydrolyze at 130°C for 5 hours, and centrifuge to obtain a hydrolyzate; the molar mass ratio of the active component to the functional component is 1:1-2; the active component is trimeric Cyanogen chloride; the solvent of the active component solution is dichloromethane or acetone; the reducing agent is anhydrous sodium sulfite; the functional component is phenol, p-hydroxybenzenesulfonic acid, 1-amino-8-naphthol- 3. Any one of 6-sodium disulfonate or a mixture of more than one in any proportion. 2.根据权利要求1所述的方法,其特征在于所述功能组份溶液的溶剂为无水碳酸钠的水溶液。2. The method according to claim 1, characterized in that the solvent of the functional component solution is an aqueous solution of anhydrous sodium carbonate. 3.根据权利要求1所述的方法,其特征在于所述重结晶溶剂为四氢呋喃和水的混合。3. The method according to claim 1, characterized in that the recrystallization solvent is a mixture of THF and water. 4.根据权利要求1所述的方法,其特征在于所述碱溶液为10%氢氧化钠溶液。4. The method according to claim 1, characterized in that the alkaline solution is 10% sodium hydroxide solution.
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CN102218306A (en) * 2011-04-27 2011-10-19 中国科学院西双版纳热带植物园 Solid nanometer catalyst and applications thereof in cellulose hydrolysis
CN102409113A (en) * 2011-06-07 2012-04-11 江南大学 Method for improving cellulose hydrolysis efficiency

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006086861A2 (en) * 2005-02-15 2006-08-24 Oxiteno S.A. Indústria E Comércio Acid hydrolysis process of cellulosic and lignocellulosic materials, digestion vessel and hydrolysis reactor
CN102218306A (en) * 2011-04-27 2011-10-19 中国科学院西双版纳热带植物园 Solid nanometer catalyst and applications thereof in cellulose hydrolysis
CN102409113A (en) * 2011-06-07 2012-04-11 江南大学 Method for improving cellulose hydrolysis efficiency

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
顾坚,等.2-氯-4,6-二苯氨基-1,3,5-三嗪改性纤维素的制备、结晶结构与水解性能.《化学学报》.2011,第69卷(第24期),第2975-2980页. *

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