[go: up one dir, main page]

CN116516706A - Organic alkali extraction method of bamboo cellulose - Google Patents

Organic alkali extraction method of bamboo cellulose Download PDF

Info

Publication number
CN116516706A
CN116516706A CN202210078667.8A CN202210078667A CN116516706A CN 116516706 A CN116516706 A CN 116516706A CN 202210078667 A CN202210078667 A CN 202210078667A CN 116516706 A CN116516706 A CN 116516706A
Authority
CN
China
Prior art keywords
bamboo
cellulose
mass concentration
solvent
lignin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202210078667.8A
Other languages
Chinese (zh)
Inventor
孟祥光
陈丽宇
张玉莲
余文旺
甘子玉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sichuan University
Original Assignee
Sichuan University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sichuan University filed Critical Sichuan University
Priority to CN202210078667.8A priority Critical patent/CN116516706A/en
Publication of CN116516706A publication Critical patent/CN116516706A/en
Pending legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C1/00Pretreatment of the finely-divided materials before digesting
    • D21C1/06Pretreatment of the finely-divided materials before digesting with alkaline reacting compounds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C11/00Regeneration of pulp liquors or effluent waste waters
    • D21C11/0007Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/18De-watering; Elimination of cooking or pulp-treating liquors from the pulp
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D5/00Purification of the pulp suspension by mechanical means; Apparatus therefor
    • D21D5/18Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Compounds Of Unknown Constitution (AREA)

Abstract

本发明提供了一种从竹子中提取纤维素的简易方法。所述方法通过有机碱处理竹材生物质,提取物可以达到95%以上的竹纤维素含量。同时可以得到竹木质素和半纤维素成分。本发明提供的方法过程简单、提取效果好、有机溶剂可回收重复使用、环境友好。The invention provides a simple method for extracting cellulose from bamboo. In the method, organic alkali is used to treat bamboo biomass, and the extract can reach a bamboo cellulose content of more than 95%. At the same time, bamboo lignin and hemicellulose components can be obtained. The method provided by the invention has the advantages of simple process, good extraction effect, recyclable and reusable organic solvent, and environmental friendliness.

Description

一种竹纤维素的有机碱提取方法A kind of organic alkali extraction method of bamboo cellulose

技术领域technical field

本发明属于生物质利用技术领域,具体涉及到一种从竹子中提取纤维素的有效方法。The invention belongs to the technical field of biomass utilization, and in particular relates to an effective method for extracting cellulose from bamboo.

背景技术Background technique

纤维素是自然界中分布最广、含量最多的可再生的多糖类有机高分子,可广泛应用于造纸、纺织、建材、胶黏剂、新材料、化学品等领域,因此从木质纤维素生物质中提取纤维素具有重要的应用价值。Cellulose is the most widely distributed and abundant renewable polysaccharide organic polymer in nature, which can be widely used in papermaking, textiles, building materials, adhesives, new materials, chemicals and other fields. Extracting cellulose from substances has important application value.

造纸制浆是生物质中纤维素提取的典型工业应用之一。目前从生物质(如木材、麦草和竹子等)中分离提取纤维素的方法主要有硫酸盐法、亚硫酸盐法、烧碱法、有机酸法和有机溶剂法等方法,然而这些方法具有对纤维素的提取效果差(一般小于85%含量)、纤维素损失大、操作复杂、污染严重、成本高等缺点。竹子是纤维素含量较高的一类生物质,它具有生长迅速、生长周期短、分布广泛、资源丰富等特点,在造纸制浆上也得到广泛应用。Paper pulping is one of the typical industrial applications for cellulose extraction from biomass. At present, the methods for separating and extracting cellulose from biomass (such as wood, wheat straw and bamboo, etc.) mainly include methods such as sulfate method, sulfite method, caustic soda method, organic acid method and organic solvent method. The extraction effect of cellulose is poor (generally less than 85% content), the loss of cellulose is large, the operation is complicated, the pollution is serious, and the cost is high. Bamboo is a type of biomass with high cellulose content. It has the characteristics of rapid growth, short growth cycle, wide distribution, and rich resources. It is also widely used in papermaking and pulping.

因此发明一种从竹材中提取纤维素,使得提取率高、工艺简单易行、绿色环保无污染、成本低的工艺路线,对造纸制浆、溶解浆制浆以及纺织等领域都具有重要工业应用价值。Therefore, a process route for extracting cellulose from bamboo is invented, which makes the extraction rate high, the process is simple and easy, green, environmentally friendly and pollution-free, and the cost is low. It has important industrial applications in the fields of paper pulping, dissolving pulp pulping, and textiles. value.

发明内容Contents of the invention

本发明目的在于提出了一种利用有机碱处理竹材来得到竹纤维素的方法,通过进一步漂白处理,可以得到高含量(95%)的纤维素。而且具有纤维素损失小、溶剂可回收重复利用、处理简单、绿色环保的优点。可完全用于造纸制浆、溶解浆制浆等技术领域。本发明中,竹子是指慈竹、毛竹和硬头黄等各类竹子。The purpose of the present invention is to propose a method for obtaining bamboo cellulose by treating bamboo with an organic alkali, and by further bleaching treatment, high-content (95%) cellulose can be obtained. Moreover, it has the advantages of small loss of cellulose, recyclable and reusable solvent, simple treatment, and environmental protection. It can be completely used in technical fields such as paper pulping and dissolving pulp pulping. In the present invention, bamboo refers to various kinds of bamboos such as Cizhu, moso bamboo and hard-headed yellow.

本发明提供的竹纤维素提取方法,包括以下步骤:Bamboo cellulose extraction method provided by the invention comprises the following steps:

(1)将竹子洗净并烘干,切成竹块;(1) bamboo is washed and dried, and cut into bamboo pieces;

(2)将步骤(1)得到的竹块放入反应器中进行有机碱液脱除竹材中的木质素和半纤维素;(2) the bamboo piece that step (1) is obtained is put into reactor and carries out lignin and hemicellulose in the bamboo wood that organic alkali solution removes;

(3)将步骤(2)得到的混合物挤压成浆、分离并洗涤得到粗纤维和滤液;(3) extruding the mixture obtained in step (2) into pulp, separating and washing to obtain crude fiber and filtrate;

(4)将步骤(3)得到的粗纤维进行漂白处理,然后分离得到竹纤维素;(4) the crude fiber obtained in step (3) is bleached, and then separated to obtain bamboo cellulose;

(5)将步骤(3)分离得到的滤液进行减压蒸馏和精馏可回收有机碱和溶剂。(5) The filtrate obtained by step (3) separation is subjected to vacuum distillation and rectification to reclaim the organic base and the solvent.

(6)将步骤(5)减压蒸馏得到的固体烘干后用水洗,然后离心,上层液体为溶解的半纤维素,下层沉积物即木质素。(6) Drying the solid obtained by distillation under reduced pressure in step (5), washing with water, and then centrifuging, the upper liquid is dissolved hemicellulose, and the lower sediment is lignin.

在本发明范围内,纤维素的损失率较低,而相应的木质素和半纤维素去除率较高,且有机碱和溶剂可回收重复利用、处理简单、绿色环保。在漂白前半纤维素和木质素的去除率可达到80%-90%;漂白后半纤维素和木质素去除率能达到90%以上,而纤维素的损失率基本小于5%,竹纤维素的提取率能达到95%以上。Within the scope of the invention, the loss rate of cellulose is low, while the corresponding removal rate of lignin and hemicellulose is high, and the organic base and solvent can be recycled and reused, the treatment is simple, and the method is environmentally friendly. Before bleaching, the removal rate of hemicellulose and lignin can reach 80%-90%; after bleaching, the removal rate of hemicellulose and lignin can reach more than 90%, while the loss rate of cellulose is basically less than 5%. The extraction rate can reach more than 95%.

本技术发明中,漂白过程简单有效,相对于目前传统的使用4-5段漂白过程而言,本方法只用一段漂白就能达到良好效果,且用料少、过程方便、成本低。In the technical invention, the bleaching process is simple and effective. Compared with the current traditional bleaching process of 4-5 stages, this method only needs one stage of bleaching to achieve good results, and uses less material, and the process is convenient and low in cost.

本技术发明中,由于木质素和半纤维素可以分离回收,一方面极大地减少了污染物排放,在制浆过程中可以达到全回收和无污染;另一方面还可以将回收的木质素和半纤维素进一步改性加工,生产高附加值产品。In the invention of this technology, since lignin and hemicellulose can be separated and recovered, on the one hand, the discharge of pollutants is greatly reduced, and full recovery and pollution-free can be achieved in the pulping process; on the other hand, the recovered lignin and hemicellulose can also be recovered Hemicellulose is further modified and processed to produce high value-added products.

以上详细描述了本发明优选实施方式,但是本发明并不局限于上述实施案例,本发明的各种不同的实施方式之间也可以进行任意组合,只要不违背本发明的思想,其均应视为本发明所公开的内容。The preferred embodiments of the present invention have been described in detail above, but the present invention is not limited to the above-mentioned examples, and any combination of various embodiments of the present invention is also possible, as long as they do not violate the idea of the present invention, they should be regarded as It is the disclosed content of the present invention.

附图说明Description of drawings

图1是本发明最终提取的竹纤维素。Fig. 1 is the bamboo cellulose finally extracted of the present invention.

具体实施方式Detailed ways

为了更好理解本发明的技术方案和优点,下面结合具体实施例对本发明做出更详细的说明。In order to better understand the technical solutions and advantages of the present invention, the present invention will be described in more detail below in conjunction with specific examples.

实施例1:将竹子洗净并烘干,切成竹块,将5g竹块放入密闭容器中,分别加入25mlN-甲基甲酰胺和25ml水,在150℃高温下反应3h,得到混合物,将反应后的混合液搅拌过滤并洗涤。过滤后的固体放入含有50ml质量浓度分别为0.3%过氧化氢、0.4%氢氧化钠、0.04%硫酸镁和0.3%硅酸钠的水溶液中,在50℃下漂白6h。然后分离得到竹纤维素,收率为45.4%,提取的固体纤维素含量为93.6%。滤液(有机碱液)经减压蒸馏可回收有机碱和溶剂而重复利用,减压蒸馏得到的固体烘干,用30ml水分三次洗涤,离心,上层液体为溶解的半纤维素,沉淀为木质素,然后分离木质素,烘干后得到的木质素回收率为30.4%。Example 1: Wash and dry the bamboo, cut into bamboo pieces, put 5g of bamboo pieces into an airtight container, add 25ml of N-methylformamide and 25ml of water respectively, and react at a high temperature of 150°C for 3h to obtain a mixture, The reacted mixture was stirred, filtered and washed. The filtered solids were put into 50ml aqueous solution containing 0.3% hydrogen peroxide, 0.4% sodium hydroxide, 0.04% magnesium sulfate and 0.3% sodium silicate, and bleached at 50°C for 6h. Then the bamboo cellulose is separated and obtained, the yield is 45.4%, and the extracted solid cellulose content is 93.6%. The filtrate (organic lye) can be recycled by vacuum distillation to recycle the organic base and solvent, and the solid obtained by vacuum distillation is dried, washed three times with 30ml of water, centrifuged, the upper liquid is dissolved hemicellulose, and the precipitate is lignin , and then separate the lignin, and the recovery rate of the lignin obtained after drying is 30.4%.

实施例2:将竹子洗净并烘干,切成竹块,将5g竹块放入密闭容器中分别加入35ml四甲基胍、20ml N,N-二甲基甲酰胺和20ml水,在170℃高温下反应2h,得到混合物,将反应后的混合液搅拌过滤并洗涤。过滤后的固体放入含有50ml质量浓度分别为0.6%过氧化氢、0.3%氢氧化钠、0.05%硫酸镁和0.3%硅酸钠的水溶液中,在60℃下漂白5h,然后分离得到竹纤维素,收率为47.2%,提取的固体纤维素含量为97.3%。滤液(有机碱液)经减压蒸馏和精馏可回收有机碱和溶剂而重复利用。减压蒸馏得到的固体烘干,用30ml水分三次洗涤,离心,上层液体为溶解的半纤维素,沉淀为木质素,然后分离木质素,烘干后得到的木质素回收率为82.3%。Embodiment 2: Bamboo is cleaned and dried, cut into bamboo pieces, 5g bamboo pieces are put into airtight container, add 35ml tetramethylguanidine, 20ml N,N-dimethylformamide and 20ml water respectively, at 170 The mixture was reacted at high temperature for 2 h, and the reacted mixture was stirred, filtered and washed. The solid after filtration is put into the aqueous solution that contains 50ml mass concentration and is respectively 0.6% hydrogen peroxide, 0.3% sodium hydroxide, 0.05% magnesium sulfate and 0.3% sodium silicate, bleaches 5h at 60 ℃, then separates to obtain bamboo fiber The yield is 47.2%, and the extracted solid cellulose content is 97.3%. The filtrate (organic lye) can be recycled by vacuum distillation and rectification, and the organic base and solvent can be reused. The solid obtained by distillation under reduced pressure was dried, washed three times with 30ml of water, and centrifuged. The upper liquid was dissolved hemicellulose, which was precipitated as lignin, and then the lignin was separated. The recovery rate of lignin obtained after drying was 82.3%.

实施例3:将竹子洗净并烘干,切成竹块,将5g竹块放入密闭容器中分别加入35ml二丁胺和15ml水,在150℃高温下反应5h,得到混合物,将反应后的混合液搅拌过滤并洗涤。过滤后的固体放入含有50ml质量浓度分别为0.5%过氧化氢、0.5%氢氧化钠、0.03%硫酸镁和0.1%硅酸钠的水溶液中,在60℃下漂白5h,然后分离得到竹纤维素,收率为45.5%,提取的固体纤维素含量为93.7%。滤液(有机碱液)经减压蒸馏和精馏可回收有机碱重复利用。减压蒸馏得到的固体烘干,用30ml水分三次洗涤,离心,上层液体为溶解的半纤维素,沉淀为木质素,然后分离木质素,烘干后得到的木质素回收率为25.3%。Example 3: Wash and dry the bamboo, cut into bamboo pieces, put 5g of bamboo pieces into an airtight container, add 35ml of dibutylamine and 15ml of water respectively, and react at a high temperature of 150°C for 5h to obtain a mixture. After the reaction, The mixture was stirred, filtered and washed. The solid after filtration is put into the aqueous solution that contains 50ml mass concentration and is respectively 0.5% hydrogen peroxide, 0.5% sodium hydroxide, 0.03% magnesium sulfate and 0.1% sodium silicate, bleaches 5h at 60 ℃, then separates to obtain bamboo fiber The yield is 45.5%, and the extracted solid cellulose content is 93.7%. The filtrate (organic lye) can be recovered and reused through vacuum distillation and rectification. The solid obtained by vacuum distillation was dried, washed three times with 30ml of water, and centrifuged. The upper liquid was dissolved hemicellulose, which was precipitated as lignin, and then the lignin was separated. The recovery rate of lignin obtained after drying was 25.3%.

实施例4将竹子洗净并烘干,切成竹块,将3g竹块放入密闭容器中,分别加入10g吡咯烷酮、10ml四氢呋喃和30ml水,在160℃高温下反应2h,得到混合物,将反应后的混合液搅拌过滤并洗涤。过滤后的固体放入含有30ml质量浓度分别为0.5%过氧化氢、0.5%氢氧化钠、0.02%硫酸镁和0.2%硅酸钠水溶液中,在50℃下漂白7h,然后分离得到竹纤维素,产率为46.1%,提取的固体纤维素含为量为95.1%。滤液(有机碱液)经减压蒸馏和精馏可回收有机碱和溶剂而重复利用。减压蒸馏得到的固体烘干,用30ml水分三次洗涤,离心,上层液体为溶解的半纤维素,沉淀为木质素,然后分离木质素,烘干后得到的木质素回收率为4.9%。Example 4 Wash and dry the bamboo, cut into bamboo pieces, put 3g of bamboo pieces into an airtight container, add 10g of pyrrolidone, 10ml of tetrahydrofuran and 30ml of water respectively, and react at a high temperature of 160°C for 2h to obtain a mixture. The resulting mixture was stirred, filtered and washed. The solid after filtration is put into the aqueous solution containing 30ml mass concentration of 0.5% hydrogen peroxide, 0.5% sodium hydroxide, 0.02% magnesium sulfate and 0.2% sodium silicate, bleached at 50°C for 7h, and then separated to obtain bamboo cellulose , the yield was 46.1%, and the extracted solid cellulose content was 95.1%. The filtrate (organic lye) can be recycled by vacuum distillation and rectification, and the organic base and solvent can be reused. The solid obtained by distillation under reduced pressure was dried, washed three times with 30ml of water, and centrifuged. The upper liquid was dissolved hemicellulose, which was precipitated as lignin, and then the lignin was separated. The recovery rate of lignin obtained after drying was 4.9%.

实施例5将竹子洗净并烘干,切成竹块,将2g竹块放入密闭容器中,分别加入7g乙基脲、5ml丙酮和30ml水,在140℃高温下反应4h,得到混合物,将反应后的混合液搅拌过滤并洗涤。过滤后的固体放入含有20ml质量浓度分别为0.4%过氧化氢、0.3%氢氧化钠、0.05%硫酸镁和0.3%硅酸钠的水溶液中,在60℃下漂白5h,然后分离得到竹纤维素,收率为47.0%,提取的固体纤维素含量为96.9%。滤液(有机碱液)经减压蒸馏和精馏可回收有机碱和溶剂重复利用。减压蒸馏得到的固体烘干,用30ml水分三次洗涤,离心,上层液体为溶解的半纤维素,沉淀为木质素,然后分离木质素,烘干后得到的木质素回收率为26.3%。Example 5 Wash and dry the bamboo, cut it into bamboo pieces, put 2g of bamboo pieces into a closed container, add 7g of ethyl urea, 5ml of acetone and 30ml of water respectively, and react at a high temperature of 140°C for 4h to obtain a mixture, The reacted mixture was stirred, filtered and washed. The solid after filtration is put into the aqueous solution that contains 20ml mass concentration and is respectively 0.4% hydrogen peroxide, 0.3% sodium hydroxide, 0.05% magnesium sulfate and 0.3% sodium silicate, bleaches 5h at 60 ℃, then separates to obtain bamboo fiber The yield is 47.0%, and the extracted solid cellulose content is 96.9%. The filtrate (organic lye) can reclaim the organic base and solvent for reuse through vacuum distillation and rectification. The solid obtained by vacuum distillation was dried, washed three times with 30ml of water, and centrifuged. The upper liquid was dissolved hemicellulose, which was precipitated as lignin, and then the lignin was separated. The recovery rate of lignin obtained after drying was 26.3%.

Claims (5)

1. A method for extracting cellulose from bamboo, the method comprising the steps of:
(1) Cleaning bamboo, oven drying, and cutting into bamboo blocks;
(2) Placing bamboo blocks into a closed container, respectively adding organic alkali A and solvent B, and reacting at high temperature to obtain a mixture;
(3) Pulping, separating and washing the mixture obtained in the step (2) to obtain crude fibers and filtrate;
(4) Bleaching the crude fiber obtained in the step (3), and then separating to obtain bamboo cellulose;
(5) And (3) carrying out reduced pressure distillation and rectification on the filtrate obtained in the step (3) to recover organic alkali and solvent, and simultaneously obtaining lignin and hemicellulose.
2. The method according to claim 1, wherein the organic base a is at least one of dipropylamine, dibutylamine, diethanolamine, tetramethylguanidine, N-methylamide, ethylurea, pyrrolidone.
3. The method according to claim 1, characterized in that the solvent B is at least one of toluene, ethanol, acetone, dioxane, tetrahydrofuran, N-dimethylformamide and water.
4. The process according to claim 1, wherein the reaction temperature is 130-170 ℃ and the reaction time is 1-5 hours.
5. The method according to claim 1, wherein the bleaching treatment method comprises: adding the crude fiber obtained in the step (3) into an aqueous solution containing sodium hydroxide with the mass concentration of 0.2-0.5%, hydrogen peroxide with the mass concentration of 0.3-1%, magnesium sulfate with the mass concentration of 0.02-0.05% and sodium silicate with the mass concentration of 0.05-0.3%, and keeping the temperature at 50-70 ℃ for 3-8 hours.
CN202210078667.8A 2022-01-24 2022-01-24 Organic alkali extraction method of bamboo cellulose Pending CN116516706A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202210078667.8A CN116516706A (en) 2022-01-24 2022-01-24 Organic alkali extraction method of bamboo cellulose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202210078667.8A CN116516706A (en) 2022-01-24 2022-01-24 Organic alkali extraction method of bamboo cellulose

Publications (1)

Publication Number Publication Date
CN116516706A true CN116516706A (en) 2023-08-01

Family

ID=87394564

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202210078667.8A Pending CN116516706A (en) 2022-01-24 2022-01-24 Organic alkali extraction method of bamboo cellulose

Country Status (1)

Country Link
CN (1) CN116516706A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102449232A (en) * 2009-04-09 2012-05-09 齐卢姆有限公司专利第二两合公司 Process for obtaining pulp from lignocellulose-containing biomass
CN102605667A (en) * 2012-03-13 2012-07-25 山东海龙股份有限公司 Chinese yew pulp and preparation method thereof
CN102898547A (en) * 2012-08-06 2013-01-30 南京林业大学 Method for separating non-wood lignocellulosic biomass hemicellulose by complex solvent
CN105568729A (en) * 2015-12-22 2016-05-11 齐鲁工业大学 Method for extracting celluloses, hemicelluloses and lignins from pennisetum hydridum
JP2017057368A (en) * 2016-03-28 2017-03-23 王子ホールディングス株式会社 Fine fibrous cellulose content
US20210230375A1 (en) * 2018-11-07 2021-07-29 Earthrecycle Co., Ltd. Method for separating cellulose

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102449232A (en) * 2009-04-09 2012-05-09 齐卢姆有限公司专利第二两合公司 Process for obtaining pulp from lignocellulose-containing biomass
CN102605667A (en) * 2012-03-13 2012-07-25 山东海龙股份有限公司 Chinese yew pulp and preparation method thereof
CN102898547A (en) * 2012-08-06 2013-01-30 南京林业大学 Method for separating non-wood lignocellulosic biomass hemicellulose by complex solvent
CN105568729A (en) * 2015-12-22 2016-05-11 齐鲁工业大学 Method for extracting celluloses, hemicelluloses and lignins from pennisetum hydridum
JP2017057368A (en) * 2016-03-28 2017-03-23 王子ホールディングス株式会社 Fine fibrous cellulose content
US20210230375A1 (en) * 2018-11-07 2021-07-29 Earthrecycle Co., Ltd. Method for separating cellulose

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
LIYU CHEN等: "Efficient separation of cellulose from bamboo by organic alkali", CELLULOSE, vol. 30, 5 December 2022 (2022-12-05), pages 1369 *
ZHUQUN SHI等: "Effects of lignin and hemicellulose contents on dissolution of wood pulp in aqueous NaOH/urea solution", CELLULOSE, vol. 21, 7 March 2014 (2014-03-07), pages 1205 *

Similar Documents

Publication Publication Date Title
CN104532641B (en) The energy-saving and environmental protection of Plant fiber, resource pulping process
CN103898784B (en) A kind of comprehensive utilization process of biomass material
CN112482069B (en) Method for preparing high-yield dissolving slurry from deep eutectic solvent
CN108660837A (en) The separation method of three component of cellulose, hemicellulose and lignin in one plant fiber raw material
CN102677510A (en) Method for separating cellulose and lignin from plant fiber raw material by utilizing ion liquid
CN109706769A (en) A method for separating lignocellulose by blending organic acid with small molecular aldehydes
CN108179644A (en) A kind of method that lignin is extracted from biomass
CN105839449B (en) A kind of clean method for preparing of viscose grade bamboo pulp
CN108797176A (en) A kind of method that whole-cotton stalk prepares dissolving pulp
US2308564A (en) Recovery of cellulose and lignin from wood
CN103526623B (en) A kind of xylanase pretr eatment improves the method for soda-oxygen pulping effect
CN103556517B (en) A kind of laccase pretreatment improves the method for oxygen alkali pulping effect
CN103074790B (en) Comprehensive utilization process of biomass raw material
CN111848976B (en) Method for preparing lignosulfonate by using dissolving pulp precooking waste liquid and application
CN105672016B (en) A kind of washing of organic solvent method paper pulp and method for recovering solvents
CN116516706A (en) Organic alkali extraction method of bamboo cellulose
CN108623817A (en) A kind of green convenient method of the purifying lignin from raw alkaline lignin
CN113372572B (en) A method for recycling solid organic acid to separate lignin
CN114105739B (en) Green alkali lignin micromolecule separation method and product
CN115075032B (en) A method for removing lignin by boiling in water at low temperature
CN109776697A (en) A method for separating cellulose, hemicellulose and lignin from sawdust and straw
CN113831549B (en) Method for purifying lignin from agriculture and forestry biomass raw materials
CN109518507A (en) The method of lignin and the preparation method of lignin particle in a kind of hydrotropes removal sawdust
CN115819796B (en) Method for efficiently separating organic acid lignin
CN103321075B (en) A kind of method reclaiming low alcohol legal system pulp waste component of boiling

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination