CN111576069A - Ramie bone microfibrillated cellulose and preparation method and application thereof - Google Patents
Ramie bone microfibrillated cellulose and preparation method and application thereof Download PDFInfo
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- 240000008564 Boehmeria nivea Species 0.000 title claims abstract description 158
- 210000000988 bone and bone Anatomy 0.000 title claims abstract description 146
- 239000001913 cellulose Substances 0.000 title claims abstract description 125
- 229920002678 cellulose Polymers 0.000 title claims abstract description 125
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 98
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims abstract description 75
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000000243 solution Substances 0.000 claims abstract description 34
- 239000003513 alkali Substances 0.000 claims abstract description 29
- 238000004061 bleaching Methods 0.000 claims abstract description 28
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- 238000000265 homogenisation Methods 0.000 claims abstract description 26
- 238000002156 mixing Methods 0.000 claims abstract description 26
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000000843 powder Substances 0.000 claims abstract description 21
- 239000000725 suspension Substances 0.000 claims abstract description 18
- 238000004880 explosion Methods 0.000 claims abstract description 17
- 239000007864 aqueous solution Substances 0.000 claims abstract description 14
- 239000011343 solid material Substances 0.000 claims abstract description 13
- 239000003463 adsorbent Substances 0.000 claims abstract description 10
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- 238000004043 dyeing Methods 0.000 claims description 10
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- 238000007711 solidification Methods 0.000 claims description 3
- 230000008023 solidification Effects 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 21
- 238000001179 sorption measurement Methods 0.000 abstract description 15
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- MCPLVIGCWWTHFH-UHFFFAOYSA-L methyl blue Chemical compound [Na+].[Na+].C1=CC(S(=O)(=O)[O-])=CC=C1NC1=CC=C(C(=C2C=CC(C=C2)=[NH+]C=2C=CC(=CC=2)S([O-])(=O)=O)C=2C=CC(NC=3C=CC(=CC=3)S([O-])(=O)=O)=CC=2)C=C1 MCPLVIGCWWTHFH-UHFFFAOYSA-L 0.000 description 5
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- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
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- 238000004438 BET method Methods 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- 229920001410 Microfiber Polymers 0.000 description 1
- 239000002585 base Substances 0.000 description 1
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- 239000008103 glucose Substances 0.000 description 1
- -1 glucose β-glycosides Chemical class 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000003658 microfiber Substances 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28023—Fibres or filaments
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/286—Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
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- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/30—Defibrating by other means
- D21B1/36—Explosive disintegration by sudden pressure reduction
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- D21C9/00—After-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
- D21C9/001—Modification of pulp properties
- D21C9/007—Modification of pulp properties by mechanical or physical means
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- D21C9/00—After-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
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- D21C9/00—After-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
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/12—Bleaching ; Apparatus therefor with halogens or halogen-containing compounds
- D21C9/14—Bleaching ; Apparatus therefor with halogens or halogen-containing compounds with ClO2 or chlorites
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/308—Dyes; Colorants; Fluorescent agents
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Abstract
Description
技术领域technical field
本发明涉及吸附材料技术领域,尤其涉及一种苎麻骨微纤化纤维素及其制备方法和应用。The invention relates to the technical field of adsorption materials, in particular to a ramie bone microfibrillated cellulose and a preparation method and application thereof.
背景技术Background technique
随着工业的快速发展,由废水引起的环境污染问题日益突出。其中,染料的化学稳定性强,不易生物降解,因此印染废水处理是一项棘手的工作。传统的印染废水处理方法,主要包括絮凝沉淀法、化学氧化法、膜分离法和生物降解法。这些方法虽然可以在一定程度上降低印染废水中染料的含量,但仍然存在着各式各样的缺陷,例如,实际应用中局限性较大、成本高、可操作性差、容易造成二次污染等。With the rapid development of industry, the problem of environmental pollution caused by wastewater has become increasingly prominent. Among them, dyes have strong chemical stability and are not easy to biodegrade, so the treatment of printing and dyeing wastewater is a difficult task. Traditional printing and dyeing wastewater treatment methods mainly include flocculation sedimentation method, chemical oxidation method, membrane separation method and biodegradation method. Although these methods can reduce the content of dyes in printing and dyeing wastewater to a certain extent, they still have various defects, such as large limitations in practical application, high cost, poor operability, and easy to cause secondary pollution, etc. .
近年来,吸附法由于具有成本低、安全无毒且操作简单等优点而备受青睐。在使用吸附法进行印染废水处理的过程中,主要是利用吸附剂吸附分离水中的染料污染物,通过吸附剂与染料污染物之间的物理吸附、化学吸附和离子交换吸附等相互作用,实现对印染废水的净化处理,在此过程中,吸附剂的选择对最终的印染废水处理效果至关重要。因此,开发新型高效、低成本的吸附剂在印染废水处理领域具有十分重要的现实意义。In recent years, the adsorption method has been favored due to its advantages of low cost, safety, non-toxicity, and simple operation. In the process of printing and dyeing wastewater treatment using the adsorption method, the dye pollutants in the water are mainly adsorbed and separated by the adsorbent. In the purification and treatment of printing and dyeing wastewater, in this process, the selection of adsorbents is crucial to the final treatment effect of printing and dyeing wastewater. Therefore, the development of new high-efficiency and low-cost adsorbents is of great practical significance in the field of printing and dyeing wastewater treatment.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种苎麻骨微纤化纤维素及其制备方法和应用,采用本发明提供的方法制备得到的苎麻骨微纤化纤维素具有疏松多孔网状结构,其作为吸附剂对于染料具有较好的吸附效果,且原料资源丰富,工艺简单,生产成本较低。The purpose of the present invention is to provide a ramie bone microfibrillated cellulose and a preparation method and application thereof. The ramie bone microfibrillated cellulose prepared by the method provided by the present invention has a loose porous network structure, which is used as an adsorbent for The dye has good adsorption effect, rich raw material resources, simple process and low production cost.
为了实现上述发明目的,本发明提供以下技术方案:In order to achieve the above-mentioned purpose of the invention, the present invention provides the following technical solutions:
一种苎麻骨微纤化纤维素的制备方法,包括以下步骤:A preparation method of ramie bone microfibrillated cellulose, comprising the following steps:
(1)将苎麻骨粉与水混合后进行蒸汽爆破预处理,得到预处理苎麻骨粉;(1) carrying out steam explosion pretreatment after mixing the ramie bone meal with water to obtain the pretreated ramie bone meal;
(2)将所述步骤(1)中预处理苎麻骨粉与氢氧化钠溶液混合后进行碱处理,得到苎麻骨粗纤维素;(2) carrying out alkali treatment after mixing the pretreated ramie bone powder and sodium hydroxide solution in the described step (1) to obtain the crude ramie bone cellulose;
(3)将所述步骤(2)中苎麻骨粗纤维素、醋酸缓冲液和次氯酸钠水溶液混合后进行漂白处理,得到苎麻骨纤维素;(3) performing bleaching after mixing the crude ramie bone cellulose, acetic acid buffer and sodium hypochlorite aqueous solution in the step (2) to obtain the ramie bone cellulose;
(4)将所述步骤(3)中苎麻骨纤维素与水混合,得到苎麻骨纤维素悬浮液,将所述苎麻骨纤维素悬浮液进行匀浆处理,将匀浆处理后所得体系进行固液分离,所得固体物料经冷冻干燥,得到苎麻骨微纤化纤维素。(4) mixing the ramie bone cellulose and water in the step (3) to obtain a ramie bone cellulose suspension, subjecting the ramie bone cellulose suspension to a homogenization treatment, and subjecting the obtained system to solidification after the homogenization treatment. The liquid is separated, and the obtained solid material is freeze-dried to obtain ramie bone microfibrillated cellulose.
优选地,所述步骤(1)中苎麻骨粉与水的质量比为1:4~6,所述蒸汽爆破预处理的温度为110~130℃,时间为20~30min。Preferably, in the step (1), the mass ratio of ramie bone meal to water is 1:4-6, the temperature of the steam explosion pretreatment is 110-130°C, and the time is 20-30min.
优选地,所述步骤(2)中碱处理的次数为2~3次。Preferably, the number of times of alkali treatment in the step (2) is 2 to 3 times.
优选地,所述氢氧化钠溶液的浓度为5~8wt.%,进行碱处理时体系中固体物料与氢氧化钠溶液的用量比为1g:10~15mL;Preferably, the concentration of the sodium hydroxide solution is 5-8 wt.%, and the dosage ratio of the solid material and the sodium hydroxide solution in the system during the alkali treatment is 1 g: 10-15 mL;
所述碱处理的温度为75~85℃,单次碱处理的时间为1.5~2.5h。The temperature of the alkali treatment is 75-85°C, and the time of a single alkali treatment is 1.5-2.5h.
优选地,所述步骤(3)中漂白处理的次数为2~3次。Preferably, the number of times of bleaching treatment in the step (3) is 2 to 3 times.
优选地,所述醋酸缓冲液由氢氧化钠、冰醋酸和水混合配制而成,所述醋酸缓冲液中氢氧化钠的用量为30g/L,冰醋酸的用量为70mL/L;所述次氯酸钠水溶液的浓度为1~2wt.%;进行漂白处理时体系中固体物料与醋酸缓冲液、次氯酸钠水溶液的用量比为1g:5~10mL:5~10mL;Preferably, the acetate buffer is prepared by mixing sodium hydroxide, glacial acetic acid and water, the amount of sodium hydroxide in the acetate buffer is 30g/L, and the amount of glacial acetic acid is 70mL/L; the sodium hypochlorite The concentration of the aqueous solution is 1-2 wt.%; the dosage ratio of the solid material in the system to the acetic acid buffer solution and the aqueous sodium hypochlorite solution is 1 g: 5-10 mL: 5-10 mL during the bleaching treatment;
所述漂白处理的温度为75~85℃,单次漂白处理的时间为0.5~1.5h。The temperature of the bleaching treatment is 75-85° C., and the time of a single bleaching treatment is 0.5-1.5 h.
优选地,所述步骤(4)中匀浆处理的次数为8~10次。Preferably, the number of times of homogenization in the step (4) is 8 to 10 times.
优选地,进行匀浆处理时体系的固含量为4~6wt.%;Preferably, the solid content of the system is 4-6 wt.% during the homogenization treatment;
所述匀浆处理的转速为20000~25000rpm,单次匀浆处理的时间为5~8min。The rotating speed of the homogenizing treatment is 20000-25000 rpm, and the time of a single homogenizing treatment is 5-8 min.
本发明提供了上述技术方案所述制备方法制备得到的苎麻骨微纤化纤维素。The present invention provides the ramie bone microfibrillated cellulose prepared by the preparation method described in the above technical solution.
本发明提供了上述技术方案所述苎麻骨微纤化纤维素作为吸附剂在印染废水处理领域中的应用。The present invention provides the application of the ramie bone microfibrillated cellulose described in the above technical solution as an adsorbent in the field of printing and dyeing wastewater treatment.
本发明提供了一种苎麻骨微纤化纤维素的制备方法,包括以下步骤:(1)将苎麻骨粉与水混合后进行蒸汽爆破预处理,得到预处理苎麻骨粉;(2)将所述步骤(1)中预处理苎麻骨粉与氢氧化钠溶液混合后进行碱处理,得到苎麻骨粗纤维素;(3)将所述步骤(2)中苎麻骨粗纤维素、醋酸缓冲液和次氯酸钠水溶液混合后进行漂白处理,得到苎麻骨纤维素;(4)将所述步骤(3)中苎麻骨纤维素与水混合,得到苎麻骨纤维素悬浮液,将所述苎麻骨纤维素悬浮液进行匀浆处理,将匀浆处理后所得体系进行固液分离,所得固体物料经冷冻干燥,得到苎麻骨微纤化纤维素。本发明利用蒸汽爆破预处理和碱处理得到苎麻骨粗纤维素,之后在漂白处理过程中,次氯酸钠可以去除残留的木质素和附着在苎麻骨纤维素上的其它成分,具体的,残留的木质素与次氯酸钠发生氧化反应,碎裂形成可溶性成分溶解在溶剂中被除去,而且次氯酸钠同时也会对苎麻骨纤维素产生氧化作用,从而一定程度降低苎麻骨纤维素强度,有利于使其经后续匀浆处理形成具有疏松多孔网状结构的苎麻骨微纤化纤维素。采用本发明提供的方法制备的苎麻骨微纤化纤维素具有较高的比表面积和较大的微孔结构,未经化学修饰和改性即能对染料具有较高的吸附量。此外,本发明以苎麻骨为原料制备苎麻骨微纤化纤维素作为吸附剂,原料资源丰富,工艺简单,生产成本较低。The invention provides a preparation method of ramie bone microfibrillated cellulose, comprising the following steps: (1) mixing ramie bone powder with water and then performing steam explosion pretreatment to obtain pretreated ramie bone powder; (2) mixing the step (1) Alkaline treatment is carried out after mixing the pretreated ramie bone powder with the sodium hydroxide solution to obtain the crude ramie bone cellulose; (3) the crude ramie bone cellulose, the acetic acid buffer and the aqueous sodium hypochlorite solution in the step (2) are mixed and then performing bleaching treatment to obtain ramie bone cellulose; (4) mixing the ramie bone cellulose with water in the step (3) to obtain a ramie bone cellulose suspension, and homogenizing the ramie bone cellulose suspension treatment, the system obtained after homogenization treatment is subjected to solid-liquid separation, and the obtained solid material is freeze-dried to obtain ramie bone microfibrillated cellulose. The invention utilizes steam explosion pretreatment and alkali treatment to obtain crude ramie bone cellulose, and then in the bleaching process, sodium hypochlorite can remove residual lignin and other components attached to the ramie bone cellulose, specifically, residual lignin Oxidation reaction occurs with sodium hypochlorite, and the soluble components formed by fragmentation are dissolved in the solvent and removed, and sodium hypochlorite will also oxidize the ramie bone cellulose, thereby reducing the strength of the ramie bone cellulose to a certain extent, which is conducive to making it through subsequent homogenization. Treatment to form ramie bone microfibrillated cellulose with loose porous network structure. The ramie bone microfibrillated cellulose prepared by the method provided by the invention has higher specific surface area and larger microporous structure, and can have higher adsorption capacity for dyes without chemical modification and modification. In addition, the invention uses ramie bone as a raw material to prepare ramie bone microfibrillated cellulose as an adsorbent, and has rich raw material resources, simple process and low production cost.
附图说明Description of drawings
图1为实施例1制备的苎麻骨微纤化纤维素的SEM图;Fig. 1 is the SEM image of the ramie bone microfibrillated cellulose prepared in Example 1;
图2为实施例1制备的苎麻骨纤维素和苎麻骨微纤化纤维素的FT-IR吸收光谱图。2 is the FT-IR absorption spectrum of ramie bone cellulose and ramie bone microfibrillated cellulose prepared in Example 1.
具体实施方式Detailed ways
本发明提供了一种苎麻骨微纤化纤维素的制备方法,包括以下步骤:The invention provides a preparation method of ramie bone microfibrillated cellulose, comprising the following steps:
(1)将苎麻骨粉与水混合后进行蒸汽爆破预处理,得到预处理苎麻骨粉;(1) carrying out steam explosion pretreatment after mixing the ramie bone meal with water to obtain the pretreated ramie bone meal;
(2)将所述步骤(1)中预处理苎麻骨粉与氢氧化钠溶液混合后进行碱处理,得到苎麻骨粗纤维素;(2) carrying out alkali treatment after mixing the pretreated ramie bone powder and sodium hydroxide solution in the described step (1) to obtain the crude ramie bone cellulose;
(3)将所述步骤(2)中苎麻骨粗纤维素、醋酸缓冲液和次氯酸钠水溶液混合后进行漂白处理,得到苎麻骨纤维素;(3) performing bleaching after mixing the crude ramie bone cellulose, acetic acid buffer and sodium hypochlorite aqueous solution in the step (2) to obtain the ramie bone cellulose;
(4)将所述步骤(3)中苎麻骨纤维素与水混合,得到苎麻骨纤维素悬浮液,将所述苎麻骨纤维素悬浮液进行匀浆处理,将匀浆处理后所得体系进行固液分离,所得固体物料经冷冻干燥,得到苎麻骨微纤化纤维素。(4) mixing the ramie bone cellulose and water in the step (3) to obtain a ramie bone cellulose suspension, subjecting the ramie bone cellulose suspension to a homogenization treatment, and subjecting the obtained system to solidification after the homogenization treatment. The liquid is separated, and the obtained solid material is freeze-dried to obtain ramie bone microfibrillated cellulose.
本发明将苎麻骨粉与水混合后进行蒸汽爆破预处理,得到预处理苎麻骨粉。在本发明中,所述苎麻骨粉的粒度优选为20~40目,所述苎麻骨粉优选由苎麻骨经粉碎得到。本发明以苎麻骨为原料制备苎麻骨微纤化纤维素作为吸附剂,原料资源丰富、成本廉价,既解决了苎麻骨焚烧污染环境问题,又提高了苎麻资源综合利用价值。In the invention, the ramie bone powder is mixed with water and then subjected to steam explosion pretreatment to obtain the pretreated ramie bone powder. In the present invention, the particle size of the ramie bone powder is preferably 20-40 meshes, and the ramie bone powder is preferably obtained by crushing the ramie bone. The invention uses the ramie bone as the raw material to prepare the ramie bone microfibrillated cellulose as the adsorbent, has rich raw material resources and low cost, not only solves the problem of environmental pollution by burning the ramie bone, but also improves the comprehensive utilization value of the ramie resource.
在本发明中,所述苎麻骨粉与水的质量比优选为1:4~6,更优选为1:5;所述蒸汽爆破预处理的温度优选为110~130℃,更优选为115~125℃,进一步优选为121℃;蒸汽爆破预处理的时间优选为20~30min。本发明利用蒸汽爆破预处理使苎麻骨粉中纤维素角质化和结构重排,可使苎麻骨中的半纤维素和木质素部分降解,并使纤维软化,有利于经后续匀浆处理崩解成微纤化纤维。在本发明中,所述蒸汽爆破预处理完成后,本发明优选将所得体系过滤,所得固体物料(即预处理苎麻骨粉)直接与氢氧化钠溶液混合进行后续碱处理即可。In the present invention, the mass ratio of the ramie bone meal to water is preferably 1:4-6, more preferably 1:5; the temperature of the steam explosion pretreatment is preferably 110-130°C, more preferably 115-125°C °C, more preferably 121 °C; the time of steam explosion pretreatment is preferably 20-30 min. The invention utilizes steam explosion pretreatment to keratinize and rearrange the cellulose in the ramie bone powder, partially degrade the hemicellulose and lignin in the ramie bone, and soften the fibers, which is favorable for disintegrating into microfibers after subsequent homogenization treatment. chemical fiber. In the present invention, after the steam explosion pretreatment is completed, the present invention preferably filters the obtained system, and the obtained solid material (ie, pretreated ramie bone powder) is directly mixed with sodium hydroxide solution for subsequent alkali treatment.
得到预处理苎麻骨粉后,本发明将所述预处理苎麻骨粉与氢氧化钠溶液混合后进行碱处理,得到苎麻骨粗纤维素。在本发明中,所述碱处理的次数优选为2~3次,所述氢氧化钠溶液的浓度优选为5~8wt.%,进行碱处理时体系中固体物料与氢氧化钠溶液的用量比优选为1g:10~15mL;所述碱处理的温度优选为75~85℃,单次碱处理的时间优选为1.5~2.5h。在本发明中,所述碱处理优选在搅拌条件下进行,所述搅拌的转速优选为100~150rpm。在本发明中,优选地,将所述预处理苎麻骨粉与氢氧化钠溶液混合后进行碱处理和过滤,所得滤渣与氢氧化钠溶液混合,再次进行碱处理和过滤,其中,与氢氧化钠溶液混合-碱处理-过滤的操作共进行2~3次;每次碱处理完成后,本发明优选将所得体系静置50~70min,更优选静置60min,然后再进行过滤,以增加预处理苎麻骨粉与氢氧化钠溶液的接触时间,使其中的木质素充分降解并溶解在氢氧化钠溶液中。最后一次过滤完成后,本发明优选将所得滤渣干燥,得到苎麻骨粗纤维素。After the pretreated ramie bone powder is obtained, in the present invention, the pretreated ramie bone powder is mixed with a sodium hydroxide solution and then subjected to alkali treatment to obtain crude ramie bone cellulose. In the present invention, the number of times of the alkali treatment is preferably 2 to 3 times, the concentration of the sodium hydroxide solution is preferably 5 to 8 wt.%, and the ratio of the amount of solid material to the sodium hydroxide solution in the system when the alkali treatment is performed Preferably, it is 1 g: 10-15 mL; the temperature of the alkali treatment is preferably 75-85° C., and the time of a single alkali treatment is preferably 1.5-2.5 h. In the present invention, the alkali treatment is preferably performed under stirring conditions, and the rotational speed of the stirring is preferably 100 to 150 rpm. In the present invention, preferably, alkali treatment and filtration are carried out after mixing the pretreated ramie bone powder with sodium hydroxide solution, the obtained filter residue is mixed with sodium hydroxide solution, and alkali treatment and filtration are carried out again, wherein, with sodium hydroxide The operation of solution mixing-alkali treatment-filtration is carried out 2 to 3 times in total; after each alkali treatment is completed, the present invention preferably allows the obtained system to stand for 50 to 70 minutes, more preferably for 60 minutes, and then filter to increase the pretreatment The contact time between the ramie bone meal and the sodium hydroxide solution makes the lignin in it fully degrade and dissolve in the sodium hydroxide solution. After the last filtration is completed, in the present invention, the obtained filter residue is preferably dried to obtain crude ramie bone cellulose.
本发明通过碱处理破坏纤维的初生壁,使纤维素大分子发生降聚,同时使低聚合度的纤维素发生部分溶解;利用NaOH与木质素相作用,使呈三维交联网络结构的木质素的化学键发生断裂,使木质素大分子降解后形成若干碎片甚至低分子物而溶于碱液中,从而得到苎麻骨粗纤维素。The invention destroys the primary wall of fibers by alkali treatment, depolymerizes cellulose macromolecules, and at the same time partially dissolves cellulose with a low degree of polymerization; uses NaOH to interact with lignin to make lignin in a three-dimensional cross-linked network structure The chemical bonds of ramie are broken, and the lignin macromolecules are degraded to form a number of fragments or even low-molecular substances, which are dissolved in the lye, thereby obtaining crude ramie bone cellulose.
得到苎麻骨粗纤维素后,本发明将所述苎麻骨粗纤维素、醋酸缓冲液和次氯酸钠水溶液混合后进行漂白处理,得到苎麻骨纤维素。在本发明中,所述醋酸缓冲液优选由氢氧化钠、冰醋酸和水混合配制而成,所述醋酸缓冲液中氢氧化钠的用量优选为30g/L,冰醋酸的用量优选为70mL/L,具体是将30g氢氧化钠与70mL冰醋酸混合,用水稀释至1L;所述次氯酸钠水溶液的浓度优选为1~2wt.%;进行漂白处理时体系中固体物料与醋酸缓冲液、次氯酸钠水溶液的用量比优选为1g:5~10mL:5~10mL;所述漂白处理的温度优选为75~85℃,更优选为80℃;单次漂白处理的时间优选为0.5~1.5h,更优选为1h。在本发明中,所述漂白处理优选在搅拌条件下进行,所述搅拌的转速优选为100~150rpm。在本发明中,优选地,将所述苎麻骨粗纤维素、醋酸缓冲液和次氯酸钠水溶液混合后依次进行漂白处理和过滤,所得滤渣与醋酸缓冲液和次氯酸钠水溶液混合,再次进行漂白处理和过滤,其中,与醋酸缓冲液和次氯酸钠水溶液混合-漂白处理-过滤的操作共进行2~3次;最后一次过滤完成后,本发明优选将所得滤渣用水洗涤,之后进行干燥,得到苎麻骨纤维素。在本发明中,所述洗涤的用水量优选为滤渣质量的8~10倍,洗涤的次数优选为3~5次。After the crude ramie bone cellulose is obtained, the present invention mixes the crude ramie bone cellulose, an acetic acid buffer and an aqueous sodium hypochlorite solution, and then performs bleaching treatment to obtain the ramie bone cellulose. In the present invention, the acetate buffer is preferably prepared by mixing sodium hydroxide, glacial acetic acid and water, the dosage of sodium hydroxide in the acetate buffer is preferably 30 g/L, and the dosage of glacial acetic acid is preferably 70 mL/L L, specifically mix 30g sodium hydroxide with 70mL glacial acetic acid, and dilute to 1L with water; the concentration of the sodium hypochlorite aqueous solution is preferably 1~2wt.%; the solid material in the system, the acetic acid buffer, and the sodium hypochlorite aqueous solution during bleaching treatment The dosage ratio is preferably 1g:5-10mL:5-10mL; the temperature of the bleaching treatment is preferably 75-85°C, more preferably 80°C; the time of a single bleaching treatment is preferably 0.5-1.5h, more preferably 1h . In the present invention, the bleaching treatment is preferably performed under stirring conditions, and the rotational speed of the stirring is preferably 100-150 rpm. In the present invention, preferably, the crude ramie bone cellulose, acetic acid buffer and sodium hypochlorite aqueous solution are mixed and then subjected to bleaching treatment and filtration in turn, the obtained filter residue is mixed with acetic acid buffer and sodium hypochlorite aqueous solution, and bleaching treatment and filtration are performed again, Wherein, the operations of mixing with acetate buffer and sodium hypochlorite aqueous solution-bleaching-filtering are carried out 2 to 3 times in total; after the last filtration is completed, the present invention preferably washes the obtained filter residue with water, and then performs drying to obtain ramie bone cellulose. In the present invention, the water consumption for the washing is preferably 8 to 10 times the mass of the filter residue, and the number of washings is preferably 3 to 5 times.
在本发明的漂白处理过程中,次氯酸钠可以去除残留的木质素和附着在苎麻骨纤维素上的其它成分,具体的,残留的木质素与次氯酸钠发生氧化反应,碎裂形成可溶性成分溶解在溶剂中被除去,而且次氯酸钠同时也会对苎麻骨纤维素产生氧化作用,从而一定程度降低苎麻骨纤维素强度,醋酸缓冲液的作用是使体系pH值变化缓和,防止漂白处理过程中pH值剧烈变化而导致对苎麻骨纤维素性能产生影响;本发明采用相对温和的漂白体系(即次氯酸钠水溶液和醋酸缓冲液)有利于使所得苎麻骨纤维素经后续匀浆处理形成具有疏松多孔网状结构的苎麻骨微纤化纤维素。In the bleaching treatment process of the present invention, sodium hypochlorite can remove residual lignin and other components attached to the ramie bone cellulose. Specifically, the residual lignin undergoes oxidation reaction with sodium hypochlorite, and is fragmented to form soluble components that dissolve in the solvent It is removed, and sodium hypochlorite will also oxidize the ramie bone cellulose, thereby reducing the strength of the ramie bone cellulose to a certain extent. The function of the acetic acid buffer is to soften the pH value of the system and prevent the pH value during the bleaching process. Lead to an impact on the properties of ramie bone cellulose; the present invention adopts a relatively mild bleaching system (ie sodium hypochlorite aqueous solution and acetic acid buffer), which is conducive to the subsequent homogenization of the obtained ramie bone cellulose to form ramie bone with a loose porous network structure. Microfibrillated cellulose.
得到苎麻骨纤维素后,本发明将所述苎麻骨纤维素与水混合,得到苎麻骨纤维素悬浮液,将所述苎麻骨纤维素悬浮液进行匀浆处理,将匀浆处理后所得体系进行固液分离,所得固体物料经冷冻干燥,得到苎麻骨微纤化纤维素。在本发明中,进行匀浆处理时体系的固含量优选为4~6wt.%,所述匀浆处理的转速优选为20000~25000rpm,单次匀浆处理的时间优选为5~8min。在本发明中,优选地,将所述苎麻骨纤维素与水混合,得到苎麻骨纤维素悬浮液,将所述苎麻骨纤维素悬浮液进行匀浆处理和过滤,所得滤渣与水混合,再次进行匀浆处理和过滤,其中,与水混合-匀浆处理和过滤的操作共进行8~10次,最后所得滤渣经冷冻干燥,得到苎麻骨微纤化纤维素。本发明对于所述冷冻干燥没有特殊的限定,采用本领域技术人员熟知的方法即可。After the ramie bone cellulose is obtained, the present invention mixes the ramie bone cellulose with water to obtain a ramie bone cellulose suspension, the ramie bone cellulose suspension is subjected to homogenization treatment, and the obtained system after the homogenization treatment is subjected to homogenization treatment. Solid-liquid separation, the obtained solid material is freeze-dried to obtain ramie bone microfibrillated cellulose. In the present invention, the solid content of the system is preferably 4-6 wt.% during the homogenization treatment, the rotation speed of the homogenization treatment is preferably 20000-25000 rpm, and the time of a single homogenization treatment is preferably 5-8 min. In the present invention, preferably, the ramie bone cellulose is mixed with water to obtain a ramie bone cellulose suspension, the ramie bone cellulose suspension is subjected to homogenization treatment and filtration, the obtained filter residue is mixed with water, and the Homogenization treatment and filtration are carried out, wherein the operations of mixing with water - homogenization treatment and filtration are carried out for 8 to 10 times, and finally the obtained filter residue is freeze-dried to obtain ramie bone microfibrillated cellulose. The present invention has no special limitation on the freeze-drying, and a method well known to those skilled in the art can be used.
本发明中苎麻骨纤维素通过匀浆处理,纤维断裂分解形成具有疏松多孔网状结构的苎麻骨微纤化纤维素,其比表面积大,表面裸露出大量的极性羟基,具有较强的吸附染料能力;且不使用化学试剂,避免了环境污染问题,简化了生产过程,效率高,生产成本低。In the present invention, the ramie bone cellulose is treated by homogenization, and the fibers are broken and decomposed to form the ramie bone microfibrillated cellulose with a loose porous network structure, which has a large specific surface area, a large number of polar hydroxyl groups exposed on the surface, and has strong adsorption. dye ability; and no chemical reagents are used, the problem of environmental pollution is avoided, the production process is simplified, the efficiency is high, and the production cost is low.
本发明提供了上述技术方案所述制备方法制备得到的苎麻骨微纤化纤维素,所述苎麻骨微纤化纤维素具有疏松多孔的网状结构,其比表面积优选为20~100m2/g,直径优选为100~1000nm,孔隙率优选为90~95%。The present invention provides the ramie bone microfibrillated cellulose prepared by the preparation method of the above technical solution, the ramie bone microfibrillated cellulose has a loose and porous network structure, and its specific surface area is preferably 20-100 m 2 /g , the diameter is preferably 100-1000 nm, and the porosity is preferably 90-95%.
本发明提供了上述技术方案所述苎麻骨微纤化纤维素作为吸附剂在印染废水处理领域中的应用。本发明提供的苎麻骨微纤化纤维素具有较高的比表面积和较大的微孔结构,未经化学修饰和改性即能对染料具有较高的吸附量。本发明对于所述苎麻骨微纤化纤维素的具体使用方法没有特殊限定,根据实际需要选择合适的用量即可;在本发明的实施例中,以处理甲基蓝溶液为例,所述甲基蓝溶液浓度为50~300mg/L,所述苎麻骨微纤化纤维素的加入量为200~400mg/L,在体系pH值为6.5~7.5(优选采用1mol/L的盐酸调节pH值)、室温、100~150rpm条件下进行吸附60~90min,苎麻骨微纤化纤维素对甲基蓝的吸附量为110~150mg/g。The present invention provides the application of the ramie bone microfibrillated cellulose described in the above technical solution as an adsorbent in the field of printing and dyeing wastewater treatment. The ramie bone microfibrillated cellulose provided by the invention has higher specific surface area and larger microporous structure, and can have higher adsorption capacity for dyes without chemical modification and modification. The present invention does not specifically limit the specific use method of the ramie bone microfibrillated cellulose, and an appropriate amount can be selected according to actual needs; in the embodiments of the present invention, taking the treatment of methyl blue solution as an example, the methyl The concentration of the base blue solution is 50-300mg/L, the addition amount of the ramie bone microfibrillated cellulose is 200-400mg/L, and the pH value of the system is 6.5-7.5 (preferably using 1mol/L hydrochloric acid to adjust the pH value) , room temperature, and 100-150 rpm for 60-90 min of adsorption, and the adsorption capacity of ramie bone microfibrillated cellulose to methyl blue is 110-150 mg/g.
下面将结合本发明中的实施例,对本发明中的技术方案进行清楚、完整地描述。显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions of the present invention will be clearly and completely described below with reference to the embodiments of the present invention. Obviously, the described embodiments are only some, but not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
实施例1Example 1
将100g苎麻骨粉(粒度为20~40目)与500mL水混合,于121℃条件下进行蒸汽爆破处理20min,取50g经蒸汽爆破处理后的苎麻骨粉,加入500mL浓度为5wt.%的NaOH溶液,于80℃、100rpm条件下进行碱处理2h,之后静置1h,将所得体系抽滤,将所得滤渣重复进行与氢氧化钠溶液混合-碱处理-静置-抽滤操作2次,将最终所得滤渣烘干,得到19.62g苎麻骨粗纤维素;Mix 100 g of ramie bone powder (granularity of 20-40 mesh) with 500 mL of water, carry out steam explosion treatment at 121 ° C for 20 min, take 50 g of ramie bone powder after steam explosion treatment, add 500 mL of NaOH solution with a concentration of 5wt.%, Alkali treatment was carried out at 80 ° C and 100 rpm for 2 hours, and then allowed to stand for 1 hour. The obtained system was suction filtered, and the obtained filter residue was repeatedly mixed with sodium hydroxide solution - alkali treatment - standing - suction filtration operation 2 times, the final obtained The filter residue was dried to obtain 19.62g of ramie bone crude cellulose;
将30g的NaOH与70mL冰醋酸混合,用水稀释至1L,得到醋酸缓冲液;将10g苎麻骨粗纤维素、50mL醋酸缓冲液和50mL浓度为2wt.%的次氯酸钠水溶液混合,于80℃、100rpm条件下进行漂白处理1h,将所得体系抽滤,将所得滤渣重复进行与醋酸缓冲液和次氯酸钠水溶液混合-漂白处理-抽滤操作2次,将最终所得滤渣用10倍质量的水洗涤3次,烘干后得到8.62g苎麻骨纤维素;Mix 30 g of NaOH with 70 mL of glacial acetic acid, and dilute to 1 L with water to obtain acetate buffer; 10 g of ramie bone crude cellulose, 50 mL of acetic acid buffer and 50 mL of sodium hypochlorite aqueous solution with a concentration of 2 wt.% are mixed at 80 ° C and 100 rpm. Bleaching treatment was carried out for 1 h, the obtained system was subjected to suction filtration, and the obtained filter residue was repeatedly mixed with acetic acid buffer and sodium hypochlorite aqueous solution-bleaching treatment-suction filtration operation 2 times, and the final obtained filter residue was washed 3 times with 10 times the mass of water, and dried. After drying, 8.62g of ramie bone cellulose was obtained;
将所述苎麻骨纤维素与水混合,配制成浓度为4wt.%的苎麻骨纤维素悬浮液,将所述苎麻骨纤维素悬浮液于20000rpm条件下进行匀浆处理5min,将所得体系过滤,所得滤渣重复进行与水混合-匀浆处理-过滤操作9次,最后所得滤渣(白色凝胶状物质)经真空冷冻干燥后,得到粉末状的苎麻骨微纤化纤维素。The ramie bone cellulose is mixed with water to prepare a ramie bone cellulose suspension with a concentration of 4 wt.%, the ramie bone cellulose suspension is subjected to homogenization treatment at 20,000 rpm for 5 minutes, and the obtained system is filtered, The obtained filter residue was mixed with water - homogenized treatment - filtration operation was repeated 9 times, and finally the obtained filter residue (white gelatinous substance) was vacuum freeze-dried to obtain powdered ramie bone microfibrillated cellulose.
实施例2Example 2
将100g苎麻骨粉(粒度为20~40目)与500mL水混合,于121℃条件下进行蒸汽爆破处理30min,取50g经蒸汽爆破处理后的苎麻骨粉,加入750mL浓度为8wt.%的NaOH溶液,于80℃、150rpm条件下进行碱处理2h,之后静置1h,将所得体系抽滤,将所得滤渣重复进行与氢氧化钠溶液混合-碱处理-静置-抽滤操作2次,将最终所得滤渣烘干,得到18.65g苎麻骨粗纤维素;Mix 100g of ramie bone powder (granularity of 20-40 mesh) with 500mL of water, carry out steam explosion treatment at 121°C for 30min, take 50g of ramie bone powder after steam explosion treatment, add 750mL of NaOH solution with a concentration of 8wt.%, Alkali treatment was carried out at 80 ° C and 150 rpm for 2 h, then left standing for 1 h, the obtained system was suction filtered, and the obtained filter residue was repeatedly mixed with sodium hydroxide solution - alkali treatment - standing - suction filtration operation 2 times, the final obtained The filter residue was dried to obtain 18.65g of ramie bone crude cellulose;
将30g的NaOH与70mL冰醋酸混合,用水稀释至1L,得到醋酸缓冲液;将10g苎麻骨粗纤维素、100mL醋酸缓冲液和100mL浓度为1.5wt.%的次氯酸钠水溶液混合,于80℃、150rpm条件下进行漂白处理1h,将所得体系抽滤,将所得滤渣重复进行与醋酸缓冲液和次氯酸钠水溶液混合-漂白处理-抽滤操作2次,将最终所得滤渣用10倍质量的水洗涤5次,烘干后得到8.45g苎麻骨纤维素;Mix 30 g of NaOH with 70 mL of glacial acetic acid, and dilute with water to 1 L to obtain acetate buffer; 10 g of ramie bone crude cellulose, 100 mL of acetic acid buffer and 100 mL of sodium hypochlorite aqueous solution with a concentration of 1.5 wt. Bleaching treatment was carried out for 1 h under the conditions, the obtained system was suction filtered, the obtained filter residue was repeatedly mixed with acetic acid buffer and sodium hypochlorite aqueous solution-bleaching treatment-suction filtration operation twice, and the final obtained filter residue was washed 5 times with 10 times the mass of water, After drying, 8.45g of ramie bone cellulose was obtained;
将所述苎麻骨纤维素与水混合,配制成浓度为6wt.%的苎麻骨纤维素悬浮液,将所述苎麻骨纤维素悬浮液于25000rpm条件下进行匀浆处理8min,将所得体系过滤,所得滤渣重复进行与水混合-匀浆处理-过滤操作7次,最后所得滤渣(白色凝胶状物质)经真空冷冻干燥后,得到粉末状的苎麻骨微纤化纤维素。The ramie bone cellulose is mixed with water to prepare a ramie bone cellulose suspension with a concentration of 6 wt.%, the ramie bone cellulose suspension is subjected to homogenization treatment at 25000 rpm for 8 minutes, and the obtained system is filtered, The obtained filter residue is mixed with water - homogenized treatment - filtration operation is repeated 7 times, and finally the obtained filter residue (white gelatinous substance) is vacuum freeze-dried to obtain powdery ramie bone microfibrillated cellulose.
表征和性能测试:Characterization and Performance Testing:
图1为实施例1制备的苎麻骨微纤化纤维素的SEM图,由图1可知,所述苎麻骨微纤化纤维素呈现疏松多孔的网状结构。利用Nano Measurer测得苎麻骨微纤化纤维素的平均直径为112nm;利用BET法测得苎麻骨微纤化纤维素的平均比表面积为32m2/g,平均孔隙率为92.32%。FIG. 1 is a SEM image of the ramie bone microfibrillated cellulose prepared in Example 1. It can be seen from FIG. 1 that the ramie bone microfibrillated cellulose has a loose and porous network structure. The average diameter of ramie bone microfibrillated cellulose measured by Nano Measurer was 112 nm; the average specific surface area of ramie bone microfibrillated cellulose measured by BET method was 32 m 2 /g, and the average porosity was 92.32%.
图2为实施例1制备的苎麻骨纤维素和苎麻骨微纤化纤维素的FT-IR吸收光谱图,由图2可知,苎麻骨纤维素和苎麻骨微纤化纤维素的出峰位置基本一致,但苎麻骨微纤化纤维素的特征峰更明显一些,其中1048cm-1和896cm-1吸收峰来自环振动和O-H弯曲振动引起的糖苷键C-H变形,这是纤维素中葡萄糖β-糖苷键连接的特征吸收峰;且图谱中未见到木质素苯环骨架的特征峰(1509cm-1和1426cm-1),说明木质素在纤维素分离过程中被脱除。Figure 2 is the FT-IR absorption spectrum of the ramie bone cellulose and the ramie bone microfibrillated cellulose prepared in Example 1. It can be seen from Figure 2 that the peak positions of the ramie bone cellulose and the ramie bone microfibrillated cellulose are basically Consistent, but the characteristic peaks of ramie bone microfibrillated cellulose are more obvious, in which the absorption peaks at 1048 cm -1 and 896 cm -1 are derived from the CH deformation of the glycosidic bond caused by ring vibration and OH bending vibration, which are the glucose β-glycosides in cellulose. Bonded characteristic absorption peaks; and no characteristic peaks (1509 cm -1 and 1426 cm -1 ) of lignin benzene ring skeleton were seen in the spectrum, indicating that lignin was removed during cellulose separation.
实施例2制备的苎麻骨微纤化纤维素的表征结果与实施例1制备的苎麻骨微纤化纤维素类似,均为疏松多孔的网状结构。The characterization results of the ramie bone microfibrillated cellulose prepared in Example 2 are similar to those of the ramie bone microfibrillated cellulose prepared in Example 1, both of which are loose and porous network structures.
将实施例1制备的苎麻骨微纤化纤维素20g加入到100mL浓度为50mg/L的甲基蓝溶液中,采用1mol/L的盐酸调节体系的pH值为7,在室温、100rpm条件下搅拌吸附60min;之后经分光光度法测试计算得到苎麻骨微纤化纤维素对甲基蓝的吸附量为124.38mg/g。20g of ramie bone microfibrillated cellulose prepared in Example 1 was added to 100mL of methyl blue solution with a concentration of 50mg/L, the pH value of the system using 1mol/L hydrochloric acid was adjusted to 7, and stirred at room temperature and 100rpm. Adsorption was carried out for 60min; after that, the adsorption amount of ramie bone microfibrillated cellulose to methyl blue was calculated to be 124.38mg/g by spectrophotometry.
按照上述方法对实施例2制备的苎麻骨微纤化纤维素的吸附性能进行测试,结果显示,实施例2制备的苎麻骨微纤化纤维素对甲基蓝的吸附量为135.62mg/g。The adsorption performance of the ramie bone microfibrillated cellulose prepared in Example 2 was tested according to the above method, and the results showed that the adsorption capacity of the ramie bone microfibrillated cellulose prepared in Example 2 to methyl blue was 135.62 mg/g.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above are only the preferred embodiments of the present invention. It should be pointed out that for those skilled in the art, without departing from the principles of the present invention, several improvements and modifications can be made. It should be regarded as the protection scope of the present invention.
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