CN101089257B - Stabilizing agent for cellulose fibre prepared by solvent method - Google Patents
Stabilizing agent for cellulose fibre prepared by solvent method Download PDFInfo
- Publication number
- CN101089257B CN101089257B CN2006100277221A CN200610027722A CN101089257B CN 101089257 B CN101089257 B CN 101089257B CN 2006100277221 A CN2006100277221 A CN 2006100277221A CN 200610027722 A CN200610027722 A CN 200610027722A CN 101089257 B CN101089257 B CN 101089257B
- Authority
- CN
- China
- Prior art keywords
- propyl
- solvent
- solution
- nmmo
- cellulose
- 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.)
- Expired - Fee Related
Links
- 239000002904 solvent Substances 0.000 title claims abstract description 38
- 239000003381 stabilizer Substances 0.000 title claims abstract description 17
- 229920003043 Cellulose fiber Polymers 0.000 title claims abstract description 14
- 238000000034 method Methods 0.000 title claims abstract description 13
- LFTLOKWAGJYHHR-UHFFFAOYSA-N N-methylmorpholine N-oxide Chemical compound CN1(=O)CCOCC1 LFTLOKWAGJYHHR-UHFFFAOYSA-N 0.000 claims abstract description 30
- UHOPWFKONJYLCF-UHFFFAOYSA-N 2-(2-sulfanylethyl)isoindole-1,3-dione Chemical compound C1=CC=C2C(=O)N(CCS)C(=O)C2=C1 UHOPWFKONJYLCF-UHFFFAOYSA-N 0.000 claims 2
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 abstract description 30
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 239000002002 slurry Substances 0.000 abstract description 8
- 238000002425 crystallisation Methods 0.000 abstract description 6
- 230000008025 crystallization Effects 0.000 abstract description 6
- 238000002360 preparation method Methods 0.000 abstract description 2
- 229920002678 cellulose Polymers 0.000 description 16
- 239000001913 cellulose Substances 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000009987 spinning Methods 0.000 description 9
- 239000004033 plastic Substances 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- SJRJJKPEHAURKC-UHFFFAOYSA-N N-Methylmorpholine Chemical compound CN1CCOCC1 SJRJJKPEHAURKC-UHFFFAOYSA-N 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- YNAVUWVOSKDBBP-UHFFFAOYSA-N Morpholine Chemical compound C1COCCN1 YNAVUWVOSKDBBP-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- ZTHYODDOHIVTJV-UHFFFAOYSA-N Propyl gallate Chemical compound CCCOC(=O)C1=CC(O)=C(O)C(O)=C1 ZTHYODDOHIVTJV-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- -1 amine compounds Chemical class 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 235000010388 propyl gallate Nutrition 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
Abstract
一种溶剂法制备纤维素纤维用稳定剂,蓓酸丙酯的重量百分比为0.3~1%,NMMO溶剂蓓酸丙酯的重量百分比为99~99.7%,其中NMMO溶剂的浓度为40~50%。采用本发明所制成的蓓酸丙酯溶液为稳定剂,在纤维素纤维浆液制备的生产过程中,可以解决该稳定剂溶液在低温下容易出现结晶等缺点,便于控制,简单精确。A stabilizer for preparing cellulose fiber by a solvent method, the weight percentage of propyl benoate is 0.3-1%, the weight percentage of NMMO solvent propyl benoate is 99-99.7%, and the concentration of NMMO solvent is 40-50% . Using the propyl benicate solution prepared by the present invention as a stabilizer can solve the shortcomings of the stabilizer solution, such as easy crystallization at low temperature, during the production process of cellulose fiber slurry preparation, and is easy to control, simple and accurate.
Description
技术领域technical field
本发明涉及一种溶剂法制备纤维素纤维用稳定剂,更具体的说,本发明涉及一种应用于纤维素纤维生产中所使用的蓓酸丙酯(Propyl-3,4,5-trihydroxybenzoate for synthesis)溶液。The present invention relates to a kind of stabilizer that solvent method prepares cellulose fiber, more specifically, the present invention relates to a kind of propyl benoate (Propyl-3,4,5-trihydroxybenzoate for used in the production of cellulose fiber) synthesis) solution.
背景技术Background technique
纤维素纤维被称为21世纪的绿色纤维。将主原料浆粕、溶剂NMMO(N-甲基吗啉N氧化物)按一定比例加入至设备中,经混合均化、脱水直至溶解和匀质化成为纺丝浆液,通过纺丝和一系列后处理,得到成品纤维。但是,当纤维素浆粕在一定温度下溶解于NMMO溶液中时,纤维素的聚合度会下降,特别是有金属离子存在时会导致纤维素大分子链断裂,纤维素发生降解。另一方面,NMMO的热稳定性有限,且其热稳定性随结构而变,当纤维素与溶剂混合并加热时,溶剂NMMO会发生降解放出胺类化合物,如N甲基吗啉和吗啉,随着降解的进行,溶液粘度下降,颜色变深。为防止纤维素和溶剂在溶解过程中氧化降解,在溶解过程中通常加入适量稳定剂,目前国际上使用最多的是,用抗氧化剂蓓酸丙酯作为稳定剂,这样经溶解得到的纤维素溶液具有较好的稳定性和较高的粘度和热塑性。Cellulose fiber is known as the green fiber of the 21st century. The main raw material pulp and solvent NMMO (N-methylmorpholine N oxide) are added to the equipment in a certain proportion, mixed and homogenized, dehydrated until dissolved and homogenized to become a spinning slurry, through spinning and a series of After processing, the finished fiber is obtained. However, when cellulose pulp is dissolved in NMMO solution at a certain temperature, the degree of polymerization of cellulose will decrease, especially in the presence of metal ions, which will cause cellulose macromolecular chains to break and cellulose to degrade. On the other hand, the thermal stability of NMMO is limited, and its thermal stability varies with the structure. When cellulose is mixed with a solvent and heated, the solvent NMMO will degrade and release amine compounds, such as N-methylmorpholine and morpholine , as the degradation proceeds, the solution viscosity decreases and the color becomes darker. In order to prevent oxidative degradation of cellulose and solvents during the dissolution process, an appropriate amount of stabilizer is usually added during the dissolution process. At present, the most widely used in the world is to use the antioxidant propyl bedecate as a stabilizer, so that the cellulose solution obtained after dissolution It has good stability and high viscosity and thermoplasticity.
由于蓓酸丙酯为固体颗粒状,加入量微小,且需与纤维素和溶剂按比例同步加入,控制起来相当的困难,所以一般是用溶剂将其溶解、调配成蓓酸丙酯溶液再与纤维素和溶剂按一定的比例加到溶解系统中。例如:德国东图林根纺织及塑料研究所(TITK)的技术,采用蓓酸丙酯作为稳定剂。用浓度为60%以上的NMMO为溶剂溶解蓓酸丙酯制成溶液。但是这样调配出来的溶液需配套上热水保温系统来精确控制溶液的温度,否则在室温低于19℃时就会结晶,这样就需要在技术上有较高的温度控制能力,特别是在冬春季节必须使用配套的保温系统才能保证生产的需要,增加了生产的成本。Since propyl berionate is in the form of solid particles, the amount of addition is small, and it needs to be added synchronously with cellulose and solvent in proportion, which is quite difficult to control. Therefore, it is generally dissolved with a solvent, prepared into a propyl benoate solution, and then mixed with Cellulose and solvent are added to the dissolving system in a certain proportion. For example: the technology of East Thuringia Institute of Textile and Plastics (TITK) in Germany uses propyl benicate as a stabilizer. A solution is prepared by dissolving the propyl bedecate in a solvent with a concentration of more than 60% NMMO. However, the solution prepared in this way needs to be equipped with a hot water insulation system to accurately control the temperature of the solution, otherwise it will crystallize when the room temperature is lower than 19°C, which requires a high temperature control capability in technology, especially in winter. In the spring season, a matching thermal insulation system must be used to ensure the production needs, which increases the production cost.
在制备作为稳定剂的蓓酸丙酯溶液中,使用浓度越低的NMMO作为溶剂来调配蓓酸丙酯溶液就越不容易产生结晶,但是如果作为溶剂NMMO的浓度偏低,就会给纤维素溶解系统带进较多的水分,这样会加重后续工段溶解的负荷,进而影响整个纺丝工序正常运行。In preparing the propyl benoate solution as a stabilizer, the lower the concentration of NMMO is used as a solvent to prepare the propyl benoate solution, the less likely it is to produce crystallization, but if the concentration of NMMO as a solvent is low, it will give cellulose The dissolving system brings in more water, which will increase the dissolving load of the subsequent section, thereby affecting the normal operation of the entire spinning process.
发明内容Contents of the invention
为解决上述生产中的问题,本发明的目是提供一种溶剂法制备纤维素纤维溶解过程中所使用的不易结晶、又便于控制、有效而经济的稳定剂---蓓酸丙酯溶液。In order to solve the problems in the above-mentioned production, the object of this invention is to provide a kind of solvent method to prepare used in the cellulose fiber dissolving process, which is difficult to crystallize, easy to control, effective and economical stabilizer --- propyl benicate solution.
本发明的纤维素纤维溶解过程中用的蓓酸丙酯溶液为:The propyl benicate solution used in the cellulose fiber dissolving process of the present invention is:
蓓酸丙酯的重量百分比为0.3~1%The weight percentage of propyl bembinoate is 0.3~1%
NMMO溶剂的重量百分比为99~99.7%The weight percentage of NMMO solvent is 99~99.7%
上述NMMO溶剂的浓度为40-50%。The concentration of the above-mentioned NMMO solvent is 40-50%.
本发明中蓓酸丙酯在溶液中的重量百分比含量最好为0.5~0.7%,NMMO溶剂的优选浓度为:45~47%。In the present invention, the weight percent content of propyl benicate in the solution is preferably 0.5-0.7%, and the preferred concentration of NMMO solvent is: 45-47%.
本发明蓓酸丙酯溶液的配制方法为:The preparation method of propyl benicate solution of the present invention is:
首先配制浓度为40~50%的NMMO溶剂,然后将蓓酸丙酯溶解于40~50%的NMMO溶剂中。First prepare the NMMO solvent with a concentration of 40-50%, and then dissolve the propyl becinoate in the 40-50% NMMO solvent.
采用本发明制备的蓓酸丙酯溶液作为稳定剂,在溶剂法纤维素纤维的生产中,能有效的避免该溶液在低温下产生结晶,特别是在冬春气温较低的季节,可以不使用任何保温设备应用于溶剂法纤维素纤维的生产中。同时使用本发明的蓓酸丙酯溶液作为稳定剂,也可以避免作为溶剂NMMO的浓度在低于40%以下时,会给纤维素溶解系统带进较多水分的问题,能有效地控制系统的稳定性。Adopt the propyl benicate solution prepared by the present invention as stabilizer, in the production of solvent method cellulose fiber, can effectively avoid this solution to produce crystallization at low temperature, especially in winter and spring season when air temperature is low, can not use Any insulation equipment used in the production of solvent-processed cellulose fibers. Simultaneously using the propyl betinate solution of the present invention as a stabilizing agent can also avoid the problem that more water will be brought into the cellulose dissolving system when the concentration of NMMO as a solvent is lower than 40%, and the system can be effectively controlled. stability.
使用本发明作为稳定剂生产出来的纤维素纤维纺丝浆液,采用德国TITK的检验标准进行检测,各项指标均符合国际相关标准。The cellulose fiber spinning slurry produced by using the present invention as a stabilizer is tested by the inspection standard of TITK in Germany, and all indexes are in compliance with relevant international standards.
采用不同浓度的NMMO溶液为溶剂,制备的蓓酸丙酯溶液的结晶温度可见表1。Using different concentrations of NMMO solutions as solvents, the crystallization temperature of the prepared propyl benoate solution can be seen in Table 1.
表1Table 1
从表1中可以清楚的看出,当使用浓度高于50%的NMMO作溶剂制备蓓酸丙酯溶液时,其结晶温度明显高于采用50%以下浓度的NMMO作溶剂,也就是说使用本发明的蓓酸丙酯溶液作稳定剂能够很好地解决蓓酸丙酯溶液在低温时容易产生结晶的问题,而且在生产应用中又不会给系统带进更多的水分。As can be clearly seen from Table 1, when using NMMO with a concentration higher than 50% as a solvent to prepare propyl becinoate solution, its crystallization temperature is significantly higher than using NMMO with a concentration below 50% as a solvent, that is to say using this The inventive propyl benoate solution as a stabilizer can well solve the problem that the propyl benoate solution is prone to crystallization at low temperature, and will not bring more water into the system during production and application.
具体实施方式Detailed ways
制备本发明的蓓酸丙酯溶液的方法依次由以下步骤:The method for preparing propyl benicate solution of the present invention is followed by the following steps successively:
1)将市售浓度为50%左右NMMO溶液,用无离子水稀释至10%~40%左右,然后通过阴阳树脂净化,去色去杂;1) Dilute the commercially available NMMO solution with a concentration of about 50% to about 10% to 40% with deionized water, and then purify it with anion and yang resins to remove color and impurities;
2)将净化后的溶液在10~15kpa和50~70℃的条件下蒸浓至浓度为40~50%;2) Concentrating the purified solution under the conditions of 10-15kpa and 50-70°C to a concentration of 40-50%;
3)取出该浓度NMMO溶液,加入要求量的蓓酸丙酯,通过搅拌器搅拌使其混合均匀。3) Take out the NMMO solution of this concentration, add the required amount of propyl bedecate, and stir it with a stirrer to mix it evenly.
实施例中所用的蓓酸丙酯为MERCK生产的;所用的水纤维素为SAPPI公司浆粕通过用水浸渍脱水至20~55%,粉碎所得,或者用SAPPI公司浆粕通过活化,再脱水至20~55%,粉碎所得。The propyl berconate used in the examples is produced by MERCK; the water cellulose used is that the SAPPI company's pulp is dehydrated to 20-55% by soaking in water, and pulverized, or is dehydrated to 20% by activation with the SAPPI company's pulp. ~55%, obtained by crushing.
实施例1Example 1
在带低速搅拌器的槽罐中加入重量百分比为99.1%的浓度为43%的NMMO溶剂,再加入重量百分比0.9%的蓓酸丙酯,用搅拌器搅拌均匀使之成为均一的溶液。In a tank with a low-speed stirrer, add 99.1% by weight of NMMO solvent with a concentration of 43%, then add 0.9% by weight of propyl becate, and stir with a stirrer to make it a uniform solution.
将上述制得的溶液与200kg水纤维素和682kg的88%NMMO溶剂同步按比例加入溶解机中,在1~10kpa和75~115℃条件下进行溶解得到纺丝浆液,采用德国东图林根纺织及塑料研究所(TITK)的浆液检验标准进行检测,其结果见表1。Add the solution prepared above, 200kg of water cellulose and 682kg of 88% NMMO solvent into the dissolving machine synchronously in proportion, and dissolve under the conditions of 1-10kpa and 75-115°C to obtain spinning slurry. The size test standard of the Institute of Textile and Plastics (TITK) was tested, and the results are shown in Table 1.
实施例2Example 2
在带低速搅拌器的槽罐中加入重量百分比为99.3%的浓度为45%的NMMO溶剂,再加入重量百分比为0.7%蓓酸丙酯,用搅拌器搅拌均匀使之成为均一的溶液。In a tank with a low-speed stirrer, add 99.3% by weight of NMMO solvent with a concentration of 45%, then add 0.7% by weight of propyl bedecate, and stir with a stirrer to make it a uniform solution.
将上述制得的溶液与200kg水纤维素和711kg的84%NMMO溶剂同步按比例加入溶解机中,在1~10kpa和75~115℃条件下进行溶解得到纺丝浆液,采用德国东图林根纺织及塑料研究所(TITK)的浆液检验标准进行检测,其结果见表1。Add the solution prepared above, 200kg of water cellulose and 711kg of 84% NMMO solvent into the dissolving machine synchronously in proportion, and dissolve under the conditions of 1-10kpa and 75-115°C to obtain spinning slurry. The size test standard of the Institute of Textile and Plastics (TITK) was tested, and the results are shown in Table 1.
实施例3Example 3
在带低速搅拌器的槽罐中加入重量百分比为99.5%的浓度为47%的NMMO溶剂,再加入重量百分比为0.5%蓓酸丙酯,用搅拌器搅拌均匀使之成为均一的溶液。In a tank with a low-speed stirrer, add 99.5% by weight of NMMO solvent with a concentration of 47%, then add 0.5% by weight of propyl bedecate, and stir with a stirrer to make it a uniform solution.
将上述制得的溶液与200kg水纤维素和732kg的81%NMMO溶剂同步按比例加入溶解机中,在1~10kpa和75~115℃条件下进行溶解得到纺丝浆液,采用德国东图林根纺织及塑料研究所(TITK)的浆液检验标准进行检测,其结果见表1。Add the solution prepared above, 200kg of water cellulose and 732kg of 81% NMMO solvent into the dissolving machine synchronously in proportion, and dissolve under the conditions of 1-10kpa and 75-115°C to obtain spinning slurry. The size test standard of the Institute of Textile and Plastics (TITK) was tested, and the results are shown in Table 1.
实施例4Example 4
在带低速搅拌器的槽罐中加入重量百分比为99.6%的浓度为49%NMM0溶剂,再加入重量百分比为0.4%蓓酸丙酯,用搅拌器搅拌均匀使之成为均一的溶液。Adding the concentration of 99.6% by weight in a tank with a low-speed stirrer is a 49% NMM0 solvent, and then adding 0.4% by weight of propyl bedecate, stirring with a stirrer to make it a uniform solution.
将上述制得的溶液与200kg水纤维素和755kg的78%NMMO溶剂同步按比例加入溶解机中,在1~10kpa和75~115℃条件下进行溶解得到纺丝浆液,采用德国东图林根纺织及塑料研究所(TITK)的浆液检验标准进行检测,其结果见表2。Add the solution prepared above, 200kg of water cellulose and 755kg of 78% NMMO solvent into the dissolving machine synchronously in proportion, and dissolve under the conditions of 1-10kpa and 75-115°C to obtain spinning slurry. The size test standard of the Institute of Textile and Plastics (TITK) was tested, and the results are shown in Table 2.
表2Table 2
表2中各实施例的测试数据说明,所得的浆液其质量符合国际目前纤维素纤维纺丝的工艺要求,也就是本发明的蓓酸丙酯溶液很好的发挥了稳定剂的作用。The test data of each embodiment in Table 2 shows that the quality of the resulting slurry meets the current international cellulose fiber spinning process requirements, that is, the propyl benoate solution of the present invention has played the role of a stabilizer well.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2006100277221A CN101089257B (en) | 2006-06-13 | 2006-06-13 | Stabilizing agent for cellulose fibre prepared by solvent method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2006100277221A CN101089257B (en) | 2006-06-13 | 2006-06-13 | Stabilizing agent for cellulose fibre prepared by solvent method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101089257A CN101089257A (en) | 2007-12-19 |
| CN101089257B true CN101089257B (en) | 2011-01-05 |
Family
ID=38942753
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2006100277221A Expired - Fee Related CN101089257B (en) | 2006-06-13 | 2006-06-13 | Stabilizing agent for cellulose fibre prepared by solvent method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101089257B (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5556452A (en) * | 1993-09-14 | 1996-09-17 | Lenzing Aktiengesellschaft | Moulding materials and spinning materials containing cellulose |
| US5702515A (en) * | 1994-10-20 | 1997-12-30 | Courtaulds Fibres (Holdings) Limited | Stabilised solutions of polysaccharide |
-
2006
- 2006-06-13 CN CN2006100277221A patent/CN101089257B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5556452A (en) * | 1993-09-14 | 1996-09-17 | Lenzing Aktiengesellschaft | Moulding materials and spinning materials containing cellulose |
| US5702515A (en) * | 1994-10-20 | 1997-12-30 | Courtaulds Fibres (Holdings) Limited | Stabilised solutions of polysaccharide |
Non-Patent Citations (2)
| Title |
|---|
| Enrico Marsano,et al..Wet spinning of Bombyx mori silk fibroin dissolved in N-methyl morpholine N-oxide and properties of regenerated fibres.International Journal of Biological Macromolecules.2005,(37),179-188. * |
| 吴翠玲等.纤维素溶剂研究现状及应用前景.中国造纸学报.2004,19(2),171-175. * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101089257A (en) | 2007-12-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP6205351B2 (en) | Process for the production of lignin-containing precursor fibers and also carbon fibers | |
| JP5820688B2 (en) | Solvent used for dissolving polysaccharide, molded product using the solvent, and method for producing polysaccharide derivative | |
| CN106012103B (en) | A kind of preparation method of high intensity alginate fibre | |
| CN101476166A (en) | Improved preparation of cellulose spinning solution with ion liquid as solvent | |
| CN106591992B (en) | A kind of modified gelatin fiber | |
| CN103541034B (en) | A kind of flame-retardant Lyocell fiber and preparation method thereof | |
| JP6504161B2 (en) | Method for producing cellulose solution | |
| CN106521668B (en) | Spinning process of regenerated cellulose staple fiber | |
| CN109575369B (en) | Method for preparing thermoplastic chitosan by melting lactic acid | |
| CN106591993B (en) | A kind of gelatin fiber spinning process | |
| CN102516418A (en) | Method for mixing natural rubber by wet process | |
| CN101089257B (en) | Stabilizing agent for cellulose fibre prepared by solvent method | |
| CN107502982A (en) | A kind of preparation method of feather keratin viscose rayon | |
| CN103938469A (en) | Method for preparing reactive dyeing and printing paste of linen fabric | |
| CN103757891A (en) | Formaldehyde catching agent for fabrics and preparation method thereof | |
| CN115537955B (en) | A kind of NMMO solvent method Juncao regenerated cellulose fiber and its preparation method | |
| CN107574491B (en) | Hemp high-strength regenerated cellulose fiber and production method thereof | |
| CN114534865B (en) | Ball milling process of sanitary ceramic glaze slip | |
| TWI547609B (en) | Preparation method of high cellulose concentratlon spinning dope and manufacturing method of non-woven fabric | |
| CN103586601B (en) | The preparation method of alginate for a kind of welding material | |
| CN101440132A (en) | Preparation of technology level sodium carboxymethylcellulose | |
| CN103911881A (en) | Printing paste applicable to ramie cotton fabrics | |
| CN115976875B (en) | Continuous production method of solvent-method functional regenerated cellulose membrane | |
| CN115873313B (en) | A kind of preparation method of maleic acid plasticized thermoplastic chitosan | |
| CN115785534B (en) | A method for preparing formamide plasticized thermoplastic chitosan |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C53 | Correction of patent for invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Wang Xin Inventor after: Xuan Jianxin Inventor after: Jiang Kun Inventor after: Wang Xiaoliang Inventor after: Xiao Nianyu Inventor after: Zhang Yihua Inventor after: Yang Danrong Inventor before: Xiao Nianyu Inventor before: Wang Xin Inventor before: Xuan Jianxin Inventor before: Zhang Yihua Inventor before: Yang Danrong |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: XIAO NIANYU WANG XIN XUAN JIANXIN ZHANG YIHUA YANG DANRONG TO: WANG XIN XUAN JIANXIN JIANG KUN WANG XIAOLIANG XIAO NIANYU ZHANG YIHUA YANG DANRONG |
|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110105 Termination date: 20180613 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |