CN113563604B - Method for regulating and controlling industrial alkali lignin molecules - Google Patents
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- 229920005610 lignin Polymers 0.000 title claims abstract description 124
- 239000003513 alkali Substances 0.000 title claims abstract description 113
- 230000001105 regulatory effect Effects 0.000 title claims abstract description 23
- 238000000034 method Methods 0.000 title claims abstract description 16
- 230000001276 controlling effect Effects 0.000 title abstract description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims abstract description 45
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims abstract description 26
- SGRHVVLXEBNBDV-UHFFFAOYSA-N 1,6-dibromohexane Chemical compound BrCCCCCCBr SGRHVVLXEBNBDV-UHFFFAOYSA-N 0.000 claims abstract description 25
- 229910000027 potassium carbonate Inorganic materials 0.000 claims abstract description 13
- 239000003960 organic solvent Substances 0.000 claims abstract description 12
- 238000003916 acid precipitation Methods 0.000 claims abstract description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 64
- 239000002244 precipitate Substances 0.000 claims description 45
- 239000002253 acid Substances 0.000 claims description 28
- 239000006228 supernatant Substances 0.000 claims description 24
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 claims description 22
- 239000000203 mixture Substances 0.000 claims description 21
- 239000007864 aqueous solution Substances 0.000 claims description 19
- 239000000243 solution Substances 0.000 claims description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 16
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 16
- 238000006243 chemical reaction Methods 0.000 claims description 16
- 238000000746 purification Methods 0.000 claims description 16
- 239000007787 solid Substances 0.000 claims description 16
- 238000005804 alkylation reaction Methods 0.000 claims description 11
- 239000000843 powder Substances 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 230000002378 acidificating effect Effects 0.000 claims description 8
- 239000011230 binding agent Substances 0.000 claims description 8
- 229910052757 nitrogen Inorganic materials 0.000 claims description 8
- 229910000030 sodium bicarbonate Inorganic materials 0.000 claims description 8
- 235000017557 sodium bicarbonate Nutrition 0.000 claims description 8
- 239000000126 substance Substances 0.000 claims description 7
- 239000012190 activator Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000011259 mixed solution Substances 0.000 claims description 5
- 239000006185 dispersion Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 239000011347 resin Substances 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- 238000004043 dyeing Methods 0.000 claims description 2
- 239000003337 fertilizer Substances 0.000 claims description 2
- 239000000575 pesticide Substances 0.000 claims description 2
- 238000007639 printing Methods 0.000 claims description 2
- 230000009467 reduction Effects 0.000 claims description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- DHXVGJBLRPWPCS-UHFFFAOYSA-N Tetrahydropyran Chemical compound C1CCOCC1 DHXVGJBLRPWPCS-UHFFFAOYSA-N 0.000 claims 1
- 229920002521 macromolecule Polymers 0.000 claims 1
- 238000001556 precipitation Methods 0.000 claims 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 abstract description 6
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 abstract description 6
- 238000004537 pulping Methods 0.000 abstract description 5
- 230000004048 modification Effects 0.000 abstract description 4
- 238000012986 modification Methods 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 2
- 230000035484 reaction time Effects 0.000 abstract description 2
- 230000029936 alkylation Effects 0.000 description 8
- 238000005119 centrifugation Methods 0.000 description 7
- 235000015320 potassium carbonate Nutrition 0.000 description 7
- 238000002390 rotary evaporation Methods 0.000 description 7
- 238000004458 analytical method Methods 0.000 description 5
- 230000008859 change Effects 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 230000004913 activation Effects 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 235000011181 potassium carbonates Nutrition 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 125000000524 functional group Chemical group 0.000 description 2
- 229920001002 functional polymer Polymers 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 241000592342 Tracheophyta Species 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08H—DERIVATIVES OF NATURAL MACROMOLECULAR COMPOUNDS
- C08H6/00—Macromolecular compounds derived from lignin, e.g. tannins, humic acids
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Abstract
Description
技术领域technical field
本发明属于制浆造纸工业碱木质素利用领域,具体涉及一种碱木质素分子量和主要官能团调控的方法。The invention belongs to the field of alkali lignin utilization in the pulp and paper industry, and in particular relates to a method for regulating the molecular weight and main functional groups of alkali lignin.
背景技术Background technique
木质素是存在于木本植物、草本植物和所有维管植物中的具有共同性质的一类物质的总称,是植物界中储量仅次于纤维素的第二大生物质资源。同时,木质素是唯一可再生的芳香族高分子化合物,可用于制备树脂材料、功能性高分子材料,并在石油开采、建筑混凝土减水、印染染料分散、农药缓释分散、肥料缓释等领域发挥重要作用。目前只有约2%的木质素用于生产高附加值产品,大多数仅用作廉价燃料。木质素主要来源于制浆造纸工业,作为制浆副产品,全世界每年的产生量约5000万吨,其中我国约1500万吨,95%的木质素未被分离或利用,而是以直接排放或燃烧的方式处理,造成严重的环境问题。当今,世界上多数制浆造纸厂使用碱法制浆,产生的木质素主要是碱木质素。因此,充分利用碱木质素资源生产高附加值的碱木质素基产品更具有经济、社会和生态意义。碱木质素的小分子量、高多分散性和低反应活性等严重限制了其应用。Lignin is a general term for a class of substances with common properties existing in woody plants, herbaceous plants and all vascular plants. It is the second largest biomass resource in the plant kingdom after cellulose. At the same time, lignin is the only renewable aromatic polymer compound, which can be used to prepare resin materials and functional polymer materials. areas play an important role. Currently only about 2% of lignin is used to produce high value-added products, and most of it is only used as cheap fuel. Lignin is mainly derived from the pulp and paper industry. As a by-product of pulping, the annual output of the world is about 50 million tons, of which about 15 million tons are in my country. 95% of the lignin is not separated or utilized, but is discharged directly or The way of burning will cause serious environmental problems. Today, most pulp and paper mills in the world use alkaline pulping, and the lignin produced is mainly alkali lignin. Therefore, it is of more economic, social and ecological significance to make full use of alkali lignin resources to produce high value-added alkali lignin-based products. The small molecular weight, high polydispersity and low reactivity of alkali lignin severely limit its application.
发明内容Contents of the invention
为克服上述问题,本发明以制浆造纸工业碱木质素为原料,采用1,6-二溴己烷/二甲基甲酰胺/碳酸钾新型烷基化体系,高效提高碱木质素分子量,调节多分散性,调控酚羟基等官能团。通过控制1,6-二溴己烷的加入量、反应时间和温度,碱木质素分子量可提高353%-1643%,降低部分级分的多分散性,调控酚羟基含量降低2%-80%,并能实现碱木质素颜色的改变。In order to overcome the above-mentioned problems, the present invention uses alkali lignin in the pulp and paper industry as a raw material, and adopts a novel alkylation system of 1,6-dibromohexane/dimethylformamide/potassium carbonate to efficiently increase the molecular weight of alkali lignin, regulate Polydispersity, regulation of functional groups such as phenolic hydroxyl groups. By controlling the addition of 1,6-dibromohexane, reaction time and temperature, the molecular weight of alkali lignin can be increased by 353%-1643%, the polydispersity of some fractions can be reduced, and the content of phenolic hydroxyl groups can be adjusted to reduce by 2%-80%. , and can change the color of alkali lignin.
为实现上述技术目的,本发明采用如下技术方案:In order to realize the above-mentioned technical purpose, the present invention adopts following technical scheme:
本发明的第一个方面,提供了一种工业碱木质素分子的调控方法,包括:The first aspect of the present invention provides a method for regulating industrial alkali lignin molecules, including:
对工业碱木质素进行纯化,得到纯化的碱木质素;Purify industrial alkali lignin to obtain purified alkali lignin;
将纯化碱木质素在1,6-二溴己烷/二甲基甲酰胺/碳酸钾体系进行烷基化反应,得到经分子调控的碱木质素。The purified alkali lignin is subjected to an alkylation reaction in a 1,6-dibromohexane/dimethylformamide/potassium carbonate system to obtain molecularly regulated alkali lignin.
本申请研发的新技术,提高了碱木质素分子量,降低了部分级分的多分散性,调控了酚羟基含量,改变了碱木质素颜色的深浅,为碱木质素的后续改性和应用奠定了基础。The new technology developed by this application increases the molecular weight of alkali lignin, reduces the polydispersity of some fractions, regulates the content of phenolic hydroxyl groups, changes the color depth of alkali lignin, and lays the foundation for the subsequent modification and application of alkali lignin. foundation.
本发明的第二个方面,提供了任一上述的方法制备的经分子调控的碱木质素。The second aspect of the present invention provides molecularly regulated alkali lignin prepared by any one of the above-mentioned methods.
本发明的第三个方面,提供了上述经分子调控的碱木质素在制备树脂材料、功能性高分子材料,以及石油开采、建筑混凝土减水、印染染料分散、农药缓释分散、肥料缓释领域中的应用。The third aspect of the present invention provides that the above-mentioned molecularly regulated alkali lignin can be used in the preparation of resin materials, functional polymer materials, and oil extraction, construction concrete water reduction, printing and dyeing dye dispersion, pesticide slow-release dispersion, fertilizer slow-release applications in the field.
本发明的有益效果在于:The beneficial effects of the present invention are:
(1)整个碱木质素分子调控过程,采用了有机溶剂和酸沉淀法纯化碱木质素、1,6-二溴己烷/二甲基甲酰胺/碳酸钾新型烷基化体系,能按照不同碱木质素的不同应用要求,调控其分子量,降低部分级分的多分散性,调控酚羟基含量,改变碱木质素颜色的深浅,对碱木质素的后续改性和应用有重要意义。(1) The entire alkali lignin molecular regulation process uses organic solvents and acid precipitation to purify alkali lignin, and a new alkylation system of 1,6-dibromohexane/dimethylformamide/potassium carbonate can be used according to different Different application requirements of alkali lignin, adjusting its molecular weight, reducing the polydispersity of some fractions, regulating the content of phenolic hydroxyl groups, and changing the color depth of alkali lignin are of great significance to the subsequent modification and application of alkali lignin.
(2)本申请的操作方法简单、成本较低、效率高、具有普适性,易于规模化生产。(2) The operation method of the present application is simple, low in cost, high in efficiency, universal in applicability, and easy for large-scale production.
附图说明Description of drawings
构成本发明的一部分的说明书附图用来提供对本发明的进一步理解,本发明的示意性实施例及其说明用于解释本发明,并不构成对本发明的不当限定。The accompanying drawings constituting a part of the present invention are used to provide a further understanding of the present invention, and the schematic embodiments of the present invention and their descriptions are used to explain the present invention and do not constitute improper limitations to the present invention.
图1为本发明实施例1中调控前后碱木质素颜色的变化。Figure 1 shows the color change of alkali lignin before and after regulation in Example 1 of the present invention.
图2为本发明实施例2中调控前后碱木质素颜色的变化。Fig. 2 shows the color change of alkali lignin before and after regulation in Example 2 of the present invention.
图3为本发明实施例3中调控前后碱木质素颜色的变化。Fig. 3 shows the color change of alkali lignin before and after regulation in Example 3 of the present invention.
图4为本发明实施例4中调控前后碱木质素颜色的变化。Figure 4 shows the color change of alkali lignin before and after regulation in Example 4 of the present invention.
具体实施方式Detailed ways
应该指出,以下详细说明都是示例性的,旨在对本发明提供进一步的说明。除非另有指明,本发明使用的所有技术和科学术语具有与本发明所属技术领域的普通技术人员通常理解的相同含义。It should be noted that the following detailed description is exemplary and intended to provide further explanation of the present invention. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs.
一种工业碱木质素分子的调控方法,以制浆造纸工业碱木质素为原料,包括以下步骤:A method for regulating industrial alkali lignin molecules, using the pulp and paper industry alkali lignin as a raw material, comprising the following steps:
将干燥的粗碱木质素加入酸性二氧六环水溶液中(二氧六环/水=9∶1,v∶v,pH=2)。混合物在87~90℃搅拌2~2.5小时,然后离心除去沉淀物。加入碳酸氢钠的上清液保持搅拌3~4小时以中和溶液中的酸。再次离心去除沉淀后,上清液在55℃下真空旋转蒸发以除去并回收二氧六环。将真空旋转蒸发后上清液加入到pH=2的盐酸溶液中,然后离心得到沉淀物。沉淀物经冷冻干燥得到固体粉末状纯化碱木质素(PAL)。将PAL以1∶20~25的比例溶解在二甲基甲酰胺中。在上述混合液中加入相当于纯化碱木质素质量0.6~08倍的K2CO3作为酸结合剂,以吸收反应中产生的酸,并加入痕量的KI作为1,6-二溴己烷的活化剂。在氮气保护下,加热上述混合物至规定温度(60~90℃)后,加入1,6-二溴己烷,保持温度反应1~4小时,然后加入2mol/L盐酸水溶液结束反应。用盐酸水溶液(pH=2)沉淀反应后的碱木质素。离心分离得到沉淀物,再用盐酸水溶液(pH=2)洗涤,冷冻干燥成得到固体粉末状物质即为经分子调控的碱木质素(CAL)。The dried crude alkali lignin was added to an acidic dioxane aqueous solution (dioxane/water=9:1, v:v, pH=2). The mixture was stirred at 87-90°C for 2-2.5 hours, and then centrifuged to remove the precipitate. The supernatant to which sodium bicarbonate was added was kept stirring for 3-4 hours to neutralize the acid in the solution. After centrifuging again to remove the precipitate, the supernatant was rotovapped under vacuum at 55 °C to remove and recover dioxane. The supernatant after vacuum rotary evaporation was added to a hydrochloric acid solution with pH=2, and then centrifuged to obtain a precipitate. The precipitate was freeze-dried to obtain purified alkali lignin (PAL) as a solid powder. Dissolve PAL in dimethylformamide at a ratio of 1:20-25. Add K2CO3 equivalent to 0.6-08 times the mass of purified alkali lignin to the above mixed solution as an acid binder to absorb the acid generated in the reaction , and add a trace amount of KI as 1,6-dibromohexane the activator. Under nitrogen protection, heat the above mixture to the specified temperature (60-90°C), add 1,6-dibromohexane, keep the temperature for 1-4 hours, and then add 2mol/L hydrochloric acid aqueous solution to end the reaction. The reacted alkali lignin was precipitated with aqueous hydrochloric acid (pH=2). The precipitate was obtained by centrifugation, washed with hydrochloric acid aqueous solution (pH=2), and freeze-dried to obtain a solid powdery substance, which is molecularly regulated alkali lignin (CAL).
在一些实施例中,所述碱木质素为从碱法制浆黑液中分离提取得到的粗碱木质素,粉末状或块状。In some embodiments, the alkali lignin is crude alkali lignin separated and extracted from alkaline pulping black liquor, in the form of powder or block.
本发明专利中所用化学试剂等级全部为化学纯。The grades of chemical reagents used in the patent of the present invention are all chemically pure.
本发明以制浆造纸工业碱木质素为原料,利用有机溶剂和酸沉淀法纯化碱木质素,采用新型烷基化体系1,6-二溴己烷/二甲基甲酰胺/碳酸钾对碱木质素分子进行调控,详细步骤如下:The invention uses alkali lignin in the pulp and paper industry as raw material, utilizes organic solvents and acid precipitation to purify alkali lignin, and adopts a novel alkylation system 1,6-dibromohexane/dimethylformamide/potassium carbonate Lignin molecules are regulated, and the detailed steps are as follows:
(1)粗碱木质素的有机溶剂纯化:将干燥的粗碱木质素加入酸性二氧六环水溶液中(二氧六环/水=9∶1,v∶v,pH=2)。混合物在87~90℃搅拌2~2.5小时,然后离心除去沉淀物。加入碳酸氢钠的上清液保持搅拌3~4小时以中和溶液中的酸。再次离心去除沉淀后,上清液在55℃下真空旋转蒸发以除去并回收二氧六环。(1) Organic solvent purification of crude alkali lignin: add dry crude alkali lignin into acidic dioxane aqueous solution (dioxane/water=9:1, v:v, pH=2). The mixture was stirred at 87-90°C for 2-2.5 hours, and then centrifuged to remove the precipitate. The supernatant to which sodium bicarbonate was added was kept stirring for 3-4 hours to neutralize the acid in the solution. After centrifuging again to remove the precipitate, the supernatant was rotovapped under vacuum at 55 °C to remove and recover dioxane.
(2)碱木质素的酸沉淀分离纯化:将真空旋转蒸发后上清液加入到pH=2的盐酸溶液中,然后离心得到沉淀物。沉淀物经冷冻干燥得到固体粉末状纯化的碱木质素(PAL)。(2) Separation and purification of alkali lignin by acid precipitation: adding the supernatant after vacuum rotary evaporation to a hydrochloric acid solution with pH=2, and then centrifuging to obtain a precipitate. The precipitate was freeze-dried to obtain purified alkali lignin (PAL) as a solid powder.
(3)PAL的烷基化:将PAL以1∶20~25的比例溶解在二甲基甲酰胺中。在上述混合液中加入相当于纯化碱木质素质量0.6~08倍的K2CO3作为酸结合剂,以吸收反应中产生的酸,并加入痕量的KI作为1,6-二溴己烷的活化剂。在氮气保护下,加热上述混合物至规定温度(60~90℃)后,加入1,6-二溴己烷,保持温度反应1~4小时,然后加入2mol/L盐酸水溶液结束反应。(3) Alkylation of PAL: Dissolve PAL in dimethylformamide at a ratio of 1:20-25. Add K2CO3 equivalent to 0.6-08 times the mass of purified alkali lignin to the above mixed solution as an acid binder to absorb the acid generated in the reaction , and add a trace amount of KI as 1,6-dibromohexane the activator. Under nitrogen protection, heat the above mixture to the specified temperature (60-90°C), add 1,6-dibromohexane, keep the temperature for 1-4 hours, and then add 2mol/L hydrochloric acid aqueous solution to end the reaction.
(4)CAL的酸析:用盐酸水溶液(pH=2)沉淀出反应后的碱木质素。离心分离得到沉淀物,再用盐酸水溶液(pH=2)洗涤,冷冻干燥成得到固体粉末状物质即为经分子调控的碱木质素(CAL)。(4) Acid analysis of CAL: Precipitate the reacted alkali lignin with aqueous hydrochloric acid (pH=2). The precipitate was obtained by centrifugation, washed with aqueous hydrochloric acid (pH=2), and freeze-dried to obtain a solid powder, which was molecularly regulated alkali lignin (CAL).
具体包括如下步骤:Specifically include the following steps:
(1)将干燥的粗碱木质素加入酸性二氧六环水溶液中(二氧六环/水=9∶1,v∶v,pH=2)。混合物在87~90℃搅拌2~2.5小时,然后离心除去沉淀物。加入碳酸氢钠的上清液保持搅拌3~4小时以中和溶液中的酸。再次离心去除沉淀后,上清液在55℃下真空旋转蒸发以除去并回收二氧六环。(1) Add dry crude alkali lignin into acidic dioxane aqueous solution (dioxane/water=9:1, v:v, pH=2). The mixture was stirred at 87-90°C for 2-2.5 hours, and then centrifuged to remove the precipitate. The supernatant to which sodium bicarbonate was added was kept stirring for 3-4 hours to neutralize the acid in the solution. After centrifuging again to remove the precipitate, the supernatant was rotovapped under vacuum at 55 °C to remove and recover dioxane.
(2)将步骤(1)中真空旋转蒸发后上清液加入到pH=2的盐酸溶液中,然后离心得到沉淀物。沉淀物经冷冻干燥得到固体粉末状纯化的碱木质素(PAL)。(2) Add the supernatant after the vacuum rotary evaporation in the step (1) to the hydrochloric acid solution with pH=2, and then centrifuge to obtain the precipitate. The precipitate was freeze-dried to obtain purified alkali lignin (PAL) as a solid powder.
(3)将步骤(2)中PAL以1∶20的比例溶解在二甲基甲酰胺中。在上述混合液中加入相当于纯化碱木质素质量0.6~08倍的K2CO3作为酸结合剂,以吸收反应中产生的酸,并加入痕量的KI作为1,6-二溴己烷的活化剂。在氮气保护下,加热上述混合物至规定温度(60~90℃)后,加入1,6-二溴己烷,保持温度反应1-4小时,然后加入2mol/L盐酸水溶液结束反应。(3) Dissolve PAL in step (2) in dimethylformamide at a ratio of 1:20. Add K2CO3 equivalent to 0.6-08 times the mass of purified alkali lignin to the above mixed solution as an acid binder to absorb the acid generated in the reaction , and add a trace amount of KI as 1,6-dibromohexane the activator. Under nitrogen protection, heat the above mixture to the specified temperature (60-90°C), add 1,6-dibromohexane, keep the temperature for reaction for 1-4 hours, then add 2mol/L hydrochloric acid aqueous solution to end the reaction.
(4)将步骤(3)中混合物用盐酸水溶液(pH=2)沉淀出反应后的碱木质素。离心分离得到沉淀物,再用盐酸水溶液(pH=2)洗涤,冷冻干燥成得到固体粉末状物质即为经分子调控的碱木质素(CAL)。(4) Precipitating the reacted alkali lignin from the mixture in step (3) with aqueous hydrochloric acid (pH=2). The precipitate was obtained by centrifugation, washed with aqueous hydrochloric acid (pH=2), and freeze-dried to obtain a solid powder, which was molecularly regulated alkali lignin (CAL).
下面结合具体的实施例,对本发明做进一步的详细说明,应该指出,所述具体实施例是对本发明的解释而不是限定。The present invention will be described in further detail below in conjunction with specific examples. It should be pointed out that the specific examples are to explain rather than limit the present invention.
实施例1:制浆造纸工业碱木质素分子调控,通过以下步骤制备得到。Example 1: Molecular regulation of alkali lignin in the pulp and paper industry, prepared through the following steps.
(1)粗碱木质素的有机溶剂纯化:在干燥的粗碱木质素中按照1:10(w:v)比例加入酸性二氧六环水溶液中(二氧六环/水=9∶1,v∶v,pH=2)。混合物在87℃搅拌2小时,然后离心除去沉淀物。加入碳酸氢钠的上清液保持搅拌3小时以中和溶液中的酸。再次离心去除沉淀后,上清液在55℃下真空旋转蒸发以除去并回收二氧六环。(1) Organic solvent purification of crude alkali lignin: add acidic dioxane aqueous solution (dioxane/water=9:1, v:v, pH=2). The mixture was stirred at 87°C for 2 hours, then centrifuged to remove the precipitate. The supernatant to which sodium bicarbonate was added was kept stirring for 3 hours to neutralize the acid in the solution. After centrifuging again to remove the precipitate, the supernatant was rotovapped under vacuum at 55 °C to remove and recover dioxane.
(2)碱木质素的酸沉淀分离纯化:将真空旋转蒸发后上清液加入到2000mL的盐酸溶液(pH=2)中,然后离心得到沉淀物。沉淀物经冷冻干燥得到固体粉末状纯化的碱木质素(PAL)。(2) Separation and purification of alkali lignin by acid precipitation: the supernatant after vacuum rotary evaporation was added to 2000 mL of hydrochloric acid solution (pH=2), and then centrifuged to obtain a precipitate. The precipitate was freeze-dried to obtain purified alkali lignin (PAL) as a solid powder.
(3)PAL的烷基化:将PAL以1∶20的比例溶解在二甲基甲酰胺中。在上述混合液中加入相当于纯化碱木质素质量0.6倍的K2CO3作为酸结合剂,以吸收反应中产生的酸,并加入痕量的KI作为1,6-二溴己烷的活化剂。在氮气保护下,加热上述混合物至70℃后,按照0.05g/g木质素加入1,6-二溴己烷,保持温度反应4小时,然后加入2mol/L盐酸水溶液结束反应。(3) Alkylation of PAL: Dissolve PAL in dimethylformamide at a ratio of 1:20. Add K2CO3 equivalent to 0.6 times the mass of purified alkali lignin to the above mixture as an acid binder to absorb the acid produced in the reaction , and add a trace amount of KI as an activation of 1,6-dibromohexane agent. Under the protection of nitrogen, after heating the above mixture to 70°C, add 1,6-dibromohexane according to 0.05g/g lignin , keep the temperature for 4 hours, and then add 2mol/L hydrochloric acid aqueous solution to end the reaction.
(4)CAL的酸析:用盐酸水溶液(pH=2)沉淀出反应后的碱木质素。离心分离得到沉淀物,再用盐酸水溶液(pH=2)洗涤,冷冻干燥成得到固体粉末状物质即为分子调控的碱木质素(CAL)。所得CAL分子量和酚羟基含量变化如表1,颜色变化见图1。(4) Acid analysis of CAL: Precipitate the reacted alkali lignin with aqueous hydrochloric acid (pH=2). The precipitate was obtained by centrifugation, washed with aqueous hydrochloric acid (pH=2), and freeze-dried to obtain a solid powdery substance, which is molecularly regulated alkali lignin (CAL). The changes in the molecular weight and phenolic hydroxyl content of the obtained CAL are shown in Table 1, and the color changes are shown in Figure 1.
表1调控前后碱木质素分子量和酚羟基含量变化Table 1 Changes of alkali lignin molecular weight and phenolic hydroxyl content before and after regulation
实施例2:制浆造纸工业碱木质素分子调控,通过以下步骤制备得到。Example 2: Molecular regulation of alkali lignin in the pulp and paper industry, prepared through the following steps.
(1)粗碱木质素的有机溶剂纯化:在干燥的粗碱木质素中按照1:10(w:v)比例加入酸性二氧六环水溶液中(二氧六环/水=9∶1,v∶v,pH=2)。混合物在87℃搅拌2小时,然后离心除去沉淀物。加入碳酸氢钠的上清液保持搅拌3小时以中和溶液中的酸。再次离心去除沉淀后,上清液在55℃下真空旋转蒸发以除去并回收二氧六环。(1) Organic solvent purification of crude alkali lignin: add acidic dioxane aqueous solution (dioxane/water=9:1, v:v, pH=2). The mixture was stirred at 87°C for 2 hours, then centrifuged to remove the precipitate. The supernatant to which sodium bicarbonate was added was kept stirring for 3 hours to neutralize the acid in the solution. After centrifuging again to remove the precipitate, the supernatant was rotovapped under vacuum at 55 °C to remove and recover dioxane.
(2)碱木质素的酸沉淀分离纯化:将真空旋转蒸发后上清液加入到2000mL的盐酸溶液(pH=2)中,然后离心得到沉淀物。沉淀物经冷冻干燥得到固体粉末状纯化的碱木质素(PAL)。(2) Separation and purification of alkali lignin by acid precipitation: the supernatant after vacuum rotary evaporation was added to 2000 mL of hydrochloric acid solution (pH=2), and then centrifuged to obtain a precipitate. The precipitate was freeze-dried to obtain purified alkali lignin (PAL) as a solid powder.
(3)PAL的烷基化:将PAL以1∶20的比例溶解在二甲基甲酰胺中。在上述混合液中加入相当于纯化碱木质素质量0.6倍的K2CO3作为酸结合剂,以吸收反应中产生的酸,并加入痕量的KI作为1,6-二溴己烷的活化剂。在氮气保护下,加热上述混合物至70℃后,按照0.60g/g木质素加入1,6-二溴己烷,保持温度反应4小时,然后加入2mol/L盐酸水溶液结束反应。(3) Alkylation of PAL: Dissolve PAL in dimethylformamide at a ratio of 1:20. Add K2CO3 equivalent to 0.6 times the mass of purified alkali lignin to the above mixture as an acid binder to absorb the acid produced in the reaction , and add a trace amount of KI as an activation of 1,6-dibromohexane agent. Under the protection of nitrogen, after heating the above mixture to 70°C, add 1,6-dibromohexane according to 0.60 g/g lignin , keep the temperature for 4 hours, and then add 2 mol/L hydrochloric acid aqueous solution to end the reaction.
(4)CAL的酸析:用盐酸水溶液(pH=2)沉淀出反应后的碱木质素。离心分离得到沉淀物,再用盐酸水溶液(pH=2)洗涤,冷冻干燥成得到固体粉末状物质即为分子调控的碱木质素(CAL)。所得CAL分子量和酚羟基含量变化如表2,颜色变化见图2。(4) Acid analysis of CAL: Precipitate the reacted alkali lignin with aqueous hydrochloric acid (pH=2). The precipitate was obtained by centrifugation, washed with aqueous hydrochloric acid (pH=2), and freeze-dried to obtain a solid powdery substance, which is molecularly regulated alkali lignin (CAL). The changes in the molecular weight and phenolic hydroxyl content of the obtained CAL are shown in Table 2, and the color changes are shown in Figure 2.
表2调控前后碱木质素分子量和酚羟基含量变化Table 2 Changes of alkali lignin molecular weight and phenolic hydroxyl content before and after regulation
实施例3:制浆造纸工业碱木质素分子调控,通过以下步骤制备得到。Example 3: Molecular regulation of alkali lignin in the pulp and paper industry, prepared through the following steps.
(1)粗碱木质素的有机溶剂纯化:在干燥的粗碱木质素中按照1:10(w:v)比例加入酸性二氧六环水溶液中(二氧六环/水=9∶1,v∶v,pH=2)。混合物在87℃搅拌2小时,然后离心除去沉淀物。加入碳酸氢钠的上清液保持搅拌3小时以中和溶液中的酸。再次离心去除沉淀后,上清液在55℃下真空旋转蒸发以除去并回收二氧六环。(1) Organic solvent purification of crude alkali lignin: add acidic dioxane aqueous solution (dioxane/water=9:1, v:v, pH=2). The mixture was stirred at 87°C for 2 hours, then centrifuged to remove the precipitate. The supernatant to which sodium bicarbonate was added was kept stirring for 3 hours to neutralize the acid in the solution. After centrifuging again to remove the precipitate, the supernatant was rotovapped under vacuum at 55 °C to remove and recover dioxane.
(2)碱木质素的酸沉淀分离纯化:将真空旋转蒸发后上清液加入到2000mL的盐酸溶液(pH=2)中,然后离心得到沉淀物。沉淀物经冷冻干燥得到固体粉末状纯化的碱木质素(PAL)。(2) Separation and purification of alkali lignin by acid precipitation: the supernatant after vacuum rotary evaporation was added to 2000 mL of hydrochloric acid solution (pH=2), and then centrifuged to obtain a precipitate. The precipitate was freeze-dried to obtain purified alkali lignin (PAL) as a solid powder.
(3)PAL的烷基化:将PAL以1∶20的比例溶解在二甲基甲酰胺中。在上述混合液中加入相当于纯化碱木质素质量0.6倍的K2CO3作为酸结合剂,以吸收反应中产生的酸,并加入痕量的KI作为1,6-二溴己烷的活化剂。在氮气保护下,加热上述混合物至70℃后,按照0.60g/g木质素加入1,6-二溴己烷,保持温度反应1小时,然后加入2mol/L盐酸水溶液结束反应。(3) Alkylation of PAL: Dissolve PAL in dimethylformamide at a ratio of 1:20. Add K2CO3 equivalent to 0.6 times the mass of purified alkali lignin to the above mixture as an acid binder to absorb the acid produced in the reaction , and add a trace amount of KI as an activation of 1,6-dibromohexane agent. Under the protection of nitrogen, after heating the above mixture to 70°C, add 1,6-dibromohexane according to 0.60 g/g lignin , keep the temperature for 1 hour, and then add 2 mol/L hydrochloric acid aqueous solution to end the reaction.
(4)CAL的酸析:用盐酸水溶液(pH=2)沉淀出反应后的碱木质素。离心分离得到沉淀物,再用盐酸水溶液(pH=2)洗涤,冷冻干燥成得到固体粉末状物质即为分子调控的碱木质素(CAL)。所得CAL分子量和酚羟基含量变化如表3,颜色变化见图3。(4) Acid analysis of CAL: Precipitate the reacted alkali lignin with aqueous hydrochloric acid (pH=2). The precipitate was obtained by centrifugation, washed with aqueous hydrochloric acid (pH=2), and freeze-dried to obtain a solid powdery substance, which is molecularly regulated alkali lignin (CAL). The changes in the molecular weight and phenolic hydroxyl content of the obtained CAL are shown in Table 3, and the color changes are shown in Figure 3.
表3调控前后碱木质素分子量和酚羟基含量变化Table 3 Changes in molecular weight and phenolic hydroxyl content of alkali lignin before and after regulation
实施例4:制浆造纸工业碱木质素分子调控,通过以下步骤制备得到。Example 4: Molecular regulation of alkali lignin in the pulp and paper industry, prepared through the following steps.
(1)粗碱木质素的有机溶剂纯化:在干燥的粗碱木质素中按照1:10(w:v)比例加入酸性二氧六环水溶液中(二氧六环/水=9∶1,v∶v,pH=2)。混合物在87℃搅拌2小时,然后离心除去沉淀物。加入碳酸氢钠的上清液保持搅拌3小时以中和溶液中的酸。再次离心去除沉淀后,上清液在55℃下真空旋转蒸发以除去并回收二氧六环。(1) Organic solvent purification of crude alkali lignin: add acidic dioxane aqueous solution (dioxane/water=9:1, v:v, pH=2). The mixture was stirred at 87°C for 2 hours, then centrifuged to remove the precipitate. The supernatant to which sodium bicarbonate was added was kept stirring for 3 hours to neutralize the acid in the solution. After centrifuging again to remove the precipitate, the supernatant was rotovapped under vacuum at 55 °C to remove and recover dioxane.
(2)碱木质素的酸沉淀分离纯化:将真空旋转蒸发后上清液加入到2000mL的盐酸溶液(pH=2)中,然后离心得到沉淀物。沉淀物经冷冻干燥得到固体粉末状纯化的碱木质素(PAL)。(2) Separation and purification of alkali lignin by acid precipitation: the supernatant after vacuum rotary evaporation was added to 2000 mL of hydrochloric acid solution (pH=2), and then centrifuged to obtain a precipitate. The precipitate was freeze-dried to obtain purified alkali lignin (PAL) as a solid powder.
(3)PAL的烷基化:将PAL以1∶20的比例溶解在二甲基甲酰胺中。在上述混合液中加入相当于纯化碱木质素质量0.6倍的K2CO3作为酸结合剂,以吸收反应中产生的酸,并加入痕量的KI作为1,6-二溴己烷的活化剂。在氮气保护下,加热上述混合物至90℃后,按照0.30g/g木质素加入1,6-二溴己烷,保持温度反应4小时,然后加入2mol/L盐酸水溶液结束反应。(3) Alkylation of PAL: Dissolve PAL in dimethylformamide at a ratio of 1:20. Add K2CO3 equivalent to 0.6 times the mass of purified alkali lignin to the above mixture as an acid binder to absorb the acid produced in the reaction , and add a trace amount of KI as an activation of 1,6-dibromohexane agent. Under the protection of nitrogen, after heating the above mixture to 90°C, add 1,6-dibromohexane according to 0.30 g/g lignin , keep the temperature for 4 hours, and then add 2 mol/L hydrochloric acid aqueous solution to end the reaction.
(4)CAL的酸析:用盐酸水溶液(pH=2)沉淀出反应后的碱木质素。离心分离得到沉淀物,再用盐酸水溶液(pH=2)洗涤,冷冻干燥成得到固体粉末状物质即为分子调控的碱木质素(CAL)。所得CAL分子量和酚羟基含量变化如表4,颜色变化见图4。(4) Acid analysis of CAL: Precipitate the reacted alkali lignin with aqueous hydrochloric acid (pH=2). The precipitate was obtained by centrifugation, washed with aqueous hydrochloric acid (pH=2), and freeze-dried to obtain a solid powdery substance, which is molecularly regulated alkali lignin (CAL). The molecular weight and phenolic hydroxyl content changes of the obtained CAL are shown in Table 4, and the color changes are shown in Figure 4.
表4调控前后碱木质素分子量和酚羟基含量变化Table 4 Changes in molecular weight and phenolic hydroxyl content of alkali lignin before and after regulation
最后应该说明的是,以上所述仅为本发明的优选实施例而已,并不用于限制本发明,尽管参照前述实施例对本发明进行了详细的说明,对于本领域的技术人员来说,其依然可以对前述实施例所记载的技术方案进行修改,或者对其中部分进行等同替换。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。Finally, it should be noted that the above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Although the present invention has been described in detail with reference to the foregoing embodiments, for those skilled in the art, it is still The technical solutions described in the foregoing embodiments may be modified, or part of them may be equivalently replaced. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included within the protection scope of the present invention.
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