CN101280532B - Preparation process of textile paper thread base paper - Google Patents
Preparation process of textile paper thread base paper Download PDFInfo
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- CN101280532B CN101280532B CN200810018062XA CN200810018062A CN101280532B CN 101280532 B CN101280532 B CN 101280532B CN 200810018062X A CN200810018062X A CN 200810018062XA CN 200810018062 A CN200810018062 A CN 200810018062A CN 101280532 B CN101280532 B CN 101280532B
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- 239000004753 textile Substances 0.000 title claims abstract description 13
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 238000010009 beating Methods 0.000 claims abstract description 57
- 239000000835 fiber Substances 0.000 claims abstract description 54
- 239000012209 synthetic fiber Substances 0.000 claims abstract description 38
- 229920002994 synthetic fiber Polymers 0.000 claims abstract description 38
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 33
- 229920001131 Pulp (paper) Polymers 0.000 claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 230000001580 bacterial effect Effects 0.000 claims abstract description 14
- 229920002749 Bacterial cellulose Polymers 0.000 claims abstract description 11
- 239000005016 bacterial cellulose Substances 0.000 claims abstract description 11
- 238000007796 conventional method Methods 0.000 claims abstract description 9
- 239000000203 mixture Substances 0.000 claims description 45
- 238000001035 drying Methods 0.000 claims description 12
- 239000002002 slurry Substances 0.000 claims description 9
- 238000004537 pulping Methods 0.000 claims description 8
- 230000007935 neutral effect Effects 0.000 claims description 7
- 238000000034 method Methods 0.000 abstract description 5
- 239000000654 additive Substances 0.000 abstract description 2
- 230000002195 synergetic effect Effects 0.000 abstract description 2
- 238000011282 treatment Methods 0.000 abstract description 2
- 238000006386 neutralization reaction Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000009941 weaving Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
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Abstract
纺织用纸线原纸的制备工艺,首先将水溶性PVA合成纤维在水中浸泡;然后将细菌纤维素湿膜浸泡于NaOH溶液中,再将木浆纤维用Valley打浆机疏解切断,然后将其与经过预处理的水溶性PVA合成纤维混合,在PFI磨浆机中进行精浆,最后加入细菌纤维、PEO、CMC、PAE混合均匀,经过流送系统,采用常规方式抄造成纸。本发明采用非植物纤维即细菌纤维、水溶性PVA纤维与木浆植物纤维按比例混合抄造。采用打浆方法对各种纤维进行了不同的打浆处理来提高纤维的抄造性能,增强纤维间结合力;并通过在抄造过程中助剂的协同效应,使原纸的物理强度大大提高。 The preparation process of textile paper thread base paper, first soak the water-soluble PVA synthetic fiber in water; then soak the bacterial cellulose wet film in NaOH solution, and then loosen and cut the wood pulp fiber with a Valley beater, and then mix it with the The pretreated water-soluble PVA synthetic fibers are mixed, refined in a PFI refiner, and finally bacterial fiber, PEO, CMC, and PAE are added to mix evenly, and then passed through the flow delivery system and made into paper by conventional methods. The invention adopts non-plant fiber, that is, bacterial fiber, water-soluble PVA fiber and wood pulp plant fiber to mix and make in proportion. The beating method is used to perform different beating treatments on various fibers to improve the papermaking performance of the fibers and enhance the bonding force between fibers; and through the synergistic effect of the additives in the papermaking process, the physical strength of the base paper is greatly improved.
Description
技术领域technical field
本发明属纺织工业和造纸工业的交叉领域,具体涉及一种纺织用纸线原纸的制备工艺。The invention belongs to the intersecting field of the textile industry and the papermaking industry, and in particular relates to a preparation process of a textile thread base paper.
背景技术Background technique
纸线原纸是纸制纤维产品,是以安全环保和韧性好的植物纤维为主要原料,经过特定条件生产加工为纸张纸条,纸条经过染色、并捻等加工工艺,形成粗细不等的纸线,成功用于生产纺织品。Paper thread base paper is a paper fiber product. It is made of safe, environmentally friendly and tough plant fibers as the main raw material. It is produced and processed into paper strips under specific conditions. The paper strips are processed by dyeing and twisting to form paper of various thicknesses. thread, successfully used in the production of textiles.
目前,国内市场纸线的产品主要用于编织各种款式的凉帽、时装包、一次性拖鞋、榻榻米、健康席等的彩色工艺编织纸,以及纸辫、纸草包、多彩绳等纸绳纸带产品。用于生产湿毛巾、高档T恤衫等纺织的产品因生产难度大、技术含量高国内未见相关研究报道。At present, the paper thread products in the domestic market are mainly used for weaving various styles of color craft weaving paper for sandal hats, fashion bags, disposable slippers, tatami mats, health mats, etc. product. There are no relevant research reports in China for the production of textile products such as wet towels and high-end T-shirts due to the difficulty of production and high technical content.
纸线原纸的使用要求决定了它的质量要求,原纸不仅定量低(16g/m2左右),而且由于抄造后在分切成窄幅系列盘纸、卷成纸线的过程中,纸条受到拉伸、扭转等复合力的作用,这就要求原纸应具有组织均匀、干强度高、伸长率大的特点;同时纸线还要经得起水力的作用,耐搓洗,即还要有较高的湿强度;在保证成纸干强度和湿强度的同时,又要求具有较佳的吸水性和柔软性。The requirements for the use of paper base paper determine its quality requirements. The base paper is not only low in basis weight (about 16g/m 2 ), but also due to the Stretching, torsion and other compound forces, which require the base paper should have the characteristics of uniform structure, high dry strength, and high elongation; at the same time, the paper thread must also withstand the action of water force and wash resistance, that is, it must have a relatively strong High wet strength; while ensuring the dry strength and wet strength of the paper, it also requires better water absorption and softness.
发明内容Contents of the invention
本发明的目的在于提供一种不仅制备工艺简单,而且在满足纸张强度性能的同时又能够赋予纸张较好环保性能的纺织用纸线原纸的制备工艺。The object of the present invention is to provide a preparation process of textile thread base paper which not only has a simple preparation process, but also can give the paper better environmental protection performance while satisfying the strength performance of the paper.
为达到上述目的,本发明采用的技术方案是:首先将3-4mm的水溶性PVA合成纤维在50℃~60℃的水温下保温15min~20min;然后将细菌纤维素湿膜浸泡于80℃的0.1mol/L的NaOH溶液中保温2h,用水冲洗至中性后在标准浆样疏解器中疏解8000转~12000转;再将质量浓度为2%的木浆纤维用Valley打浆机疏解切断,控制打浆度35°SR~45°SR,湿重16g~20g,然后将其与经过预处理的水溶性PVA合成纤维以97~98∶3~2的质量比混合均匀,在PFI磨浆机中进行精浆,打浆间隙为0.3mm~0.5mm,打浆质量浓度为8%~10%,成浆打浆度为60°SR~70°SR;最后加入合成纤维和木浆纤维混合物质量0.05%~0.07%的细菌纤维,加入总混合物质量0.05%~0.09%的PEO,0.1%~0.5%的CMC,1.6%~2.0%的PAE,混合均匀,调节浆料的质量浓度为0.4%~0.8%,经过流送系统,在70℃~80℃的干燥温度下,采用常规方式抄造成纸。In order to achieve the above-mentioned purpose, the technical scheme adopted in the present invention is: first, heat the 3-4mm water-soluble PVA synthetic fiber at a water temperature of 50°C-60°C for 15min-20min; then soak the bacterial cellulose wet film in an 80°C Incubate in 0.1mol/L NaOH solution for 2 hours, rinse with water until neutral, and then decompose in a standard pulp decomposer at 8000 to 12000 revolutions; then decompose and cut wood pulp fibers with a mass concentration of 2% with a Valley beater, and The beating degree is 35°SR~45°SR, the wet weight is 16g~20g, and then it is mixed evenly with the pretreated water-soluble PVA synthetic fiber at a mass ratio of 97~98:3~2, and it is processed in a PFI refiner. Fine pulp, the beating gap is 0.3mm-0.5mm, the beating mass concentration is 8%-10%, the beating degree of pulping is 60°SR-70°SR; finally, the mixture of synthetic fiber and wood pulp fiber is added in a mass of 0.05%-0.07% 0.05% to 0.09% PEO, 0.1% to 0.5% CMC and 1.6% to 2.0% PAE were added to the total mixture mass, mixed evenly, and the mass concentration of the slurry was adjusted to 0.4% to 0.8%. Sending system, under the drying temperature of 70 ℃ ~ 80 ℃, adopt conventional method to make paper.
本发明采用非植物纤维即细菌纤维、水溶性PVA纤维与木浆植物纤维按比例混合抄造。由于非植物纤维抄造性能较差,原纸定量又较低(16g/m2左右),因此纸张强度不理想;而本发明首先采用打浆方法对各种纤维进行了不同的打浆处理来提高纤维的抄造性能,增强纤维间结合力;并通过在抄造过程中助剂的协同效应,使原纸的物理强度大大提高。按本发明的制备工艺得到的产品其干强抗张指数为71.10N·m/g,湿强抗张指数为30.03N.m.g-1,撕裂指数为8.01mN.m2.g-1,耐折度为460次,伸长率为2.46%。The invention adopts non-plant fiber, that is, bacterial fiber, water-soluble PVA fiber and wood pulp plant fiber to mix in proportion for papermaking. Due to poor papermaking performance of non-plant fibers and low weight of base paper (about 16g/ m2 ), the paper strength is not ideal; and the present invention first adopts beating method to carry out different beating treatments on various fibers to improve fiber papermaking performance, enhance the bonding force between fibers; and through the synergistic effect of additives in the papermaking process, the physical strength of the base paper is greatly improved. The dry strength tensile index of the product obtained by the preparation process of the present invention is 71.10N·m/g, the wet strength tensile index is 30.03Nmg -1 , the tear index is 8.01mN.m 2 .g-1, and the folding resistance The degree is 460 times and the elongation is 2.46%.
具体实施方式Detailed ways
实施例1,首先将3-4mm的水溶性PVA合成纤维在50℃的水温下保温15min;然后将细菌纤维素湿膜浸泡于80℃的0.1mol/L的NaOH溶液中保温2h,用水冲洗至中性后在标准浆样疏解器中疏解10000转;再将质量浓度为2%的木浆纤维用Valley打浆机疏解切断,控制打浆度45°SR,湿重18g,然后将其与经过预处理的水溶性PVA合成纤维以97∶3的质量比混合均匀,在PFI磨浆机中进行精浆,打浆间隙为0.3mm,打浆质量浓度为8%,成浆打浆度为70°SR;最后加入合成纤维和木浆纤维混合物质量0.05%的细菌纤维,加入总混合物质量0.05%的PEO,0.4%的CMC,2.0%的PAE,混合均匀,调节浆料的质量浓度为0.4%,经过流送系统,在70℃的干燥温度下,采用常规方式抄造成纸。Example 1, firstly, the water-soluble PVA synthetic fiber of 3-4 mm was incubated at a water temperature of 50° C. for 15 minutes; then the bacterial cellulose wet film was soaked in a 0.1mol/L NaOH solution of 80° C. After neutralization, decompose 10,000 revolutions in a standard pulp decomposer; then decompose and cut wood pulp fibers with a mass concentration of 2% with a Valley beater, control the degree of beating to 45°SR, and wet weight 18g, and then mix it with the pretreated The water-soluble PVA synthetic fiber is mixed evenly with the mass ratio of 97:3, and refined in the PFI refiner, the beating gap is 0.3mm, the beating mass concentration is 8%, and the beating degree of beating is 70 ° SR; finally add Synthetic fiber and wood pulp fiber mixture mass 0.05% bacterial fiber, add total mixture mass 0.05% PEO, 0.4% CMC, 2.0% PAE, mix well, adjust the mass concentration of the pulp to 0.4%, and pass through the flow delivery system , at a drying temperature of 70°C, paper was made in a conventional manner.
实施例2,首先将3-4mm的水溶性PVA合成纤维在60℃的水温下保温18min;然后将细菌纤维素湿膜浸泡于80℃的0.1mol/L的NaOH溶液中保温2h,用水冲洗至中性后在标准浆样疏解器中疏解8000转;再将质量浓度为2%的木浆纤维用Valley打浆机疏解切断,控制打浆度40°SR,湿重16g,然后将其与经过预处理的水溶性PVA合成纤维以98∶2的质量比混合均匀,在PFI磨浆机中进行精浆,打浆间隙为0.4mm,打浆质量浓度为9%,成浆打浆度为65SR;最后加入合成纤维和木浆纤维混合物质量0.06%的细菌纤维,加入总混合物质量0.07%的PEO,0.1%的CMC,1.8%的PAE,混合均匀,调节浆料的质量浓度为0.6%,经过流送系统,在73℃的干燥温度下,采用常规方式抄造成纸。Example 2, firstly, the water-soluble PVA synthetic fiber of 3-4mm was incubated at a water temperature of 60°C for 18min; After neutralization, decompose 8000 revolutions in a standard pulp decomposer; then decompose and cut wood pulp fibers with a mass concentration of 2% with a Valley beater, control the degree of beating to 40°SR, and wet weight 16g, and then mix it with the pretreated The water-soluble PVA synthetic fiber is mixed evenly with the mass ratio of 98:2, and refined in the PFI refiner, the beating gap is 0.4mm, the beating mass concentration is 9%, and the beating degree of beating is 65SR; finally add the synthetic fiber With the bacterial fiber of wood pulp fiber mixture quality 0.06%, add the PEO of total mixture quality 0.07%, the CMC of 0.1%, the PAE of 1.8%, mix homogeneously, the mass concentration of adjusting slurry is 0.6%, through flow delivery system, in At a drying temperature of 73°C, the conventional method was used to make paper.
实施例3,首先将3-4mm的水溶性PVA合成纤维在53℃的水温下保温20min;然后将细菌纤维素湿膜浸泡于80℃的0.1mol/L的NaOH溶液中保温2h,用水冲洗至中性后在标准浆样疏解器中疏解11000转;再将质量浓度为2%的木浆纤维用Valley打浆机疏解切断,控制打浆度42°SR,湿重19g,然后将其与经过预处理的水溶性PVA合成纤维以97.3∶2.7的质量比混合均匀,在PFI磨浆机中进行精浆,打浆间隙为0.5mm,打浆质量浓度为10%,成浆打浆度为68°SR;最后加入合成纤维和木浆纤维混合物质量0.07%的细菌纤维,加入总混合物质量0.09%的PEO,0.32%的CMC,1.6%的PAE,混合均匀,调节浆料的质量浓度为0.8%,经过流送系统,在77℃的干燥温度下,采用常规方式抄造成纸。Example 3, firstly, the water-soluble PVA synthetic fiber of 3-4 mm was incubated at a water temperature of 53° C. for 20 minutes; then the bacterial cellulose wet film was soaked in 0.1 mol/L NaOH solution of 80° C. After neutralization, decompose 11,000 rpm in a standard pulp decomposer; then decompose and cut wood pulp fibers with a mass concentration of 2% with a Valley beater, control the degree of beating to 42°SR, and wet weight 19g, and then mix it with the pretreated The water-soluble PVA synthetic fiber is mixed evenly with the mass ratio of 97.3:2.7, and is refined in the PFI refiner, the beating gap is 0.5mm, the beating mass concentration is 10%, and the beating degree of beating is 68 ° SR; Synthetic fiber and wood pulp fiber mixture quality 0.07% bacterial fiber, add total mixture quality 0.09% PEO, 0.32% CMC, 1.6% PAE, mix well, adjust the mass concentration of the pulp to be 0.8%, and pass through the flow delivery system , at a drying temperature of 77°C, paper was made in a conventional manner.
实施例4,首先将3-4mm的水溶性PVA合成纤维在55℃的水温下保温17min;然后将细菌纤维素湿膜浸泡于80℃的0.1mol/L的NaOH溶液中保温2h,用水冲洗至中性后在标准浆样疏解器中疏解9000转;再将质量浓度为2%的木浆纤维用Valley打浆机疏解切断,控制打浆度38°SR,湿重17g,然后将其与经过预处理的水溶性PVA合成纤维以97.5∶2.5的质量比混合均匀,在PFI磨浆机中进行精浆,打浆间隙为0.4mm,打浆质量浓度为8.5%,成浆打浆度为63°SR;最后加入合成纤维和木浆纤维混合物质量0.06%的细菌纤维,加入总混合物质量0.06%的PEO,0.5%的CMC,1.9%的PAE,混合均匀,调节浆料的质量浓度为0.5%,经过流送系统,在75℃的干燥温度下,采用常规方式抄造成纸。Example 4, firstly, the water-soluble PVA synthetic fiber of 3-4mm was incubated at a water temperature of 55°C for 17min; After neutralization, decompose 9000 revolutions in a standard pulp decomposer; then decompose and cut wood pulp fibers with a mass concentration of 2% with a Valley beater, control the degree of beating to 38°SR, and wet weight 17g, and then mix it with the pretreated The water-soluble PVA synthetic fiber is mixed evenly with the mass ratio of 97.5: 2.5, and is refined in the PFI refiner, the beating gap is 0.4mm, the beating mass concentration is 8.5%, and the beating degree of beating is 63 ° SR; Synthetic fiber and wood pulp fiber mixture mass 0.06% bacterial fiber, add total mixture mass 0.06% PEO, 0.5% CMC, 1.9% PAE, mix evenly, adjust the mass concentration of the pulp to 0.5%, and pass through the flow delivery system , at a drying temperature of 75°C, paper was made in a conventional manner.
实施例5,首先将3-4mm的水溶性PVA合成纤维在58℃的水温下保温19min;然后将细菌纤维素湿膜浸泡于80℃的0.1mol/L的NaOH溶液中保温2h,用水冲洗至中性后在标准浆样疏解器中疏解12000转;再将质量浓度为2%的木浆纤维用Valley打浆机疏解切断,控制打浆度35°SR,湿重20g,然后将其与经过预处理的水溶性PVA合成纤维以97.7∶2.3的质量比混合均匀,在PFI磨浆机中进行精浆,打浆间隙为0.3mm,打浆质量浓度为9.5%,成浆打浆度为60°SR;最后加入合成纤维和木浆纤维混合物质量0.07%的细菌纤维,加入总混合物质量0.08%的PEO,0.2%的CMC,1.7%的PAE,混合均匀,调节浆料的质量浓度为0.7%,经过流送系统,在80℃的干燥温度下,采用常规方式抄造成纸。Example 5, first, the 3-4mm water-soluble PVA synthetic fiber was incubated at a water temperature of 58°C for 19min; then the bacterial cellulose wet film was soaked in a 0.1mol/L NaOH solution of 80°C for 2h, and rinsed with water until After neutralization, decompose 12,000 rpm in a standard pulp decomposer; then decompose and cut wood pulp fibers with a mass concentration of 2% with a Valley beater, control the degree of beating to 35°SR, and wet weight 20g, and then mix it with the pretreated The water-soluble PVA synthetic fiber is mixed evenly with the mass ratio of 97.7: 2.3, is refined in the PFI refiner, the beating gap is 0.3mm, the beating mass concentration is 9.5%, and the beating degree of beating is 60 ° SR; Synthetic fiber and wood pulp fiber mixture quality 0.07% bacterial fiber, add total mixture quality 0.08% PEO, 0.2% CMC, 1.7% PAE, mix evenly, adjust the mass concentration of the pulp to be 0.7%, and pass through the flow delivery system , at a drying temperature of 80°C, paper was made in a conventional manner.
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| CN102251431A (en) * | 2011-07-22 | 2011-11-23 | 浙江舜浦纸业有限公司 | Method for producing colored knitting paper for handicraft articles by using mixed bamboo and wood pulp |
| CN102582132A (en) * | 2012-03-02 | 2012-07-18 | 中国航空工业集团公司北京航空材料研究院 | Flame-retardant vegetable fiber paper honeycomb core and preparation method thereof |
| CN104389228B (en) * | 2014-09-29 | 2016-06-08 | 长沙理工大学 | Preparation method of raw paper for firecracker lead |
| CN104611994A (en) * | 2015-02-05 | 2015-05-13 | 温岭市得利纸业工艺有限公司 | Process for processing allochroic craft paper |
| CN106757456A (en) * | 2017-01-18 | 2017-05-31 | 山东纳美德生物科技有限公司 | A kind of preparation method of bacteria cellulose microfibre |
| CN115652691A (en) * | 2022-09-06 | 2023-01-31 | 广东轻工职业技术学院 | High-performance bacterial cellulose/plant fiber composite colored paper and preparation method thereof |
| CN115478452A (en) * | 2022-10-14 | 2022-12-16 | 中国制浆造纸研究院有限公司 | Filtering material for detecting trace heavy metal elements and preparation method thereof |
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