CN103102459B - Preparation method of gelatin grafted acrylamide cation polymeric flocculant - Google Patents
Preparation method of gelatin grafted acrylamide cation polymeric flocculant Download PDFInfo
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- 108010010803 Gelatin Proteins 0.000 title claims abstract description 39
- 229920000159 gelatin Polymers 0.000 title claims abstract description 39
- 239000008273 gelatin Substances 0.000 title claims abstract description 39
- 235000019322 gelatine Nutrition 0.000 title claims abstract description 39
- 235000011852 gelatine desserts Nutrition 0.000 title claims abstract description 39
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- -1 acrylamide cation Chemical class 0.000 title claims abstract description 10
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 claims abstract description 40
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims abstract description 22
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 20
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000003756 stirring Methods 0.000 claims abstract description 17
- 239000008367 deionised water Substances 0.000 claims abstract description 12
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 10
- 238000000034 method Methods 0.000 claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims abstract description 5
- 238000001816 cooling Methods 0.000 claims abstract description 3
- 238000007599 discharging Methods 0.000 claims abstract description 3
- 229920000578 graft copolymer Polymers 0.000 claims description 20
- 238000007334 copolymerization reaction Methods 0.000 claims description 10
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 8
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 claims description 6
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 claims description 6
- JRKICGRDRMAZLK-UHFFFAOYSA-L persulfate group Chemical group S(=O)(=O)([O-])OOS(=O)(=O)[O-] JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 claims description 5
- CHQMHPLRPQMAMX-UHFFFAOYSA-L sodium persulfate Chemical compound [Na+].[Na+].[O-]S(=O)(=O)OOS([O-])(=O)=O CHQMHPLRPQMAMX-UHFFFAOYSA-L 0.000 claims description 4
- XMPZTFVPEKAKFH-UHFFFAOYSA-P ceric ammonium nitrate Chemical compound [NH4+].[NH4+].[Ce+4].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O XMPZTFVPEKAKFH-UHFFFAOYSA-P 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 150000003926 acrylamides Chemical class 0.000 claims 1
- 239000010985 leather Substances 0.000 abstract description 6
- 239000003054 catalyst Substances 0.000 abstract description 5
- 229920001577 copolymer Polymers 0.000 abstract description 3
- 238000004062 sedimentation Methods 0.000 abstract description 2
- 230000003311 flocculating effect Effects 0.000 abstract 1
- 238000004065 wastewater treatment Methods 0.000 abstract 1
- 229920006317 cationic polymer Polymers 0.000 description 11
- 238000005576 amination reaction Methods 0.000 description 8
- 239000008394 flocculating agent Substances 0.000 description 8
- 238000005189 flocculation Methods 0.000 description 5
- 230000016615 flocculation Effects 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- LCPVQAHEFVXVKT-UHFFFAOYSA-N 2-(2,4-difluorophenoxy)pyridin-3-amine Chemical compound NC1=CC=CN=C1OC1=CC=C(F)C=C1F LCPVQAHEFVXVKT-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229920002401 polyacrylamide Polymers 0.000 description 3
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 229920001807 Urea-formaldehyde Polymers 0.000 description 2
- GZCGUPFRVQAUEE-SLPGGIOYSA-N aldehydo-D-glucose Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C=O GZCGUPFRVQAUEE-SLPGGIOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 229920005615 natural polymer Polymers 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 229920001059 synthetic polymer Polymers 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- HKVFISRIUUGTIB-UHFFFAOYSA-O azanium;cerium;nitrate Chemical compound [NH4+].[Ce].[O-][N+]([O-])=O HKVFISRIUUGTIB-UHFFFAOYSA-O 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 description 1
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229920005613 synthetic organic polymer Polymers 0.000 description 1
- 238000009966 trimming Methods 0.000 description 1
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
技术领域 technical field
本发明属于污水处理技术领域,涉及一种絮凝剂的制备方法,具体是一种明胶接枝丙烯酰胺阳离子高分子絮凝剂的制备方法。 The invention belongs to the technical field of sewage treatment, and relates to a preparation method of a flocculant, in particular to a preparation method of a gelatin-grafted acrylamide cationic polymer flocculant.
背景技术 Background technique
皮革工业在产生巨大经济和社会效益的同时,也对环境造成了一定的污染。制革过程中,仅有原料皮重20%的物质转化为成品革,其余部分在制革过程中作为剖、削、磨和修边屑等固体废弃物被丢弃掉。同时皮革企业排放的污水中含有大量的COD、铬和悬浮物等物质。这些均是造成皮革工业污染严重的重要因素。 While the leather industry produces huge economic and social benefits, it also causes certain pollution to the environment. During the tanning process, only 20% of the skin weight of the raw material is converted into finished leather, and the rest is discarded as solid waste such as cutting, cutting, grinding and trimming scraps during the tanning process. At the same time, the sewage discharged by leather enterprises contains a large amount of COD, chromium and suspended solids. These are all important factors that cause serious pollution in the leather industry.
制革废水处理中使用的合成类有机高分子絮凝剂,主要包括阴离子型的和非离子型的有机高分子絮凝剂有聚丙烯酰胺及其衍生物、聚丙烯酸钠、聚磺基苯乙烯、聚氧化乙烯、脲醛树脂和聚乙烯醇等。 Synthetic organic polymer flocculants used in the treatment of tannery wastewater mainly include anionic and nonionic organic polymer flocculants such as polyacrylamide and its derivatives, sodium polyacrylate, polysulfostyrene, poly Ethylene oxide, urea-formaldehyde resin and polyvinyl alcohol, etc.
聚丙烯酰胺类高分子絮凝剂的残余毒性单体问题,目前仍未得到有效解决。类似的情况也存在于脲醛树脂及聚乙烯醇的制备中,这两类絮凝剂属于低相对分子质量的高聚物,絮凝性能相对差一些。 The problem of residual toxic monomers in polyacrylamide polymer flocculants has not yet been effectively resolved. A similar situation also exists in the preparation of urea-formaldehyde resin and polyvinyl alcohol. These two types of flocculants are high polymers with low relative molecular weight, and their flocculation performance is relatively poor.
目前处理制革废水所采用的絮凝剂多为有机合成高分子絮凝剂,其中使用最广泛地为聚丙烯酰胺类高分子絮凝剂。这类絮凝剂虽然具有相对分子质量较大,分子链活性官能团多的结构特点,但其存在着致命的弱点,它们大多数呈微毒,影响人体健康,其残留物不易被生物降解,对环境造成二次污染,反而制约着制革业的持续健康发展。因此,在接枝共聚物的基础上,利用天然高分子原料自身的优势条件合成接枝型高分子絮凝剂,是一条值得探索的思路。 At present, most of the flocculants used in the treatment of tannery wastewater are organic synthetic polymer flocculants, among which polyacrylamide polymer flocculants are the most widely used. Although this type of flocculant has the structural characteristics of relatively large molecular weight and many active functional groups in the molecular chain, it has a fatal weakness. Most of them are slightly toxic and affect human health, and their residues are not easy to be biodegraded. Cause secondary pollution, but restrict the sustainable and healthy development of the leather industry. Therefore, on the basis of graft copolymers, using the advantages of natural polymer raw materials to synthesize grafted polymer flocculants is an idea worth exploring.
发明内容 Contents of the invention
本发明的目的针对现有技术的不足,提供一种明胶接枝丙烯酰胺阳离子高分子絮凝剂的制备方法。 The object of the present invention is to provide a preparation method of gelatin-grafted acrylamide cationic polymer flocculant against the deficiencies of the prior art.
本发明方法的具体步骤如下: The concrete steps of the inventive method are as follows:
步骤(1).接枝共聚反应:将干燥明胶加入去离子水中,搅拌均匀,然后加入催化剂,在氮气保护条件下,35℃~55℃反应40~60分钟,再加入丙烯酰胺,45℃~70℃下反应3~6小时,制得接枝共聚物;每升去离子水中加入50~150克干燥明胶、2~20克催化剂、150~500克丙烯酰胺; Step (1). Graft copolymerization reaction: Add dry gelatin to deionized water, stir evenly, then add catalyst, under nitrogen protection condition, 35℃~55℃ for 40~60 minutes, then add acrylamide, 45℃~ React at 70°C for 3 to 6 hours to obtain a graft copolymer; add 50 to 150 grams of dry gelatin, 2 to 20 grams of catalyst, and 150 to 500 grams of acrylamide per liter of deionized water;
所述的明胶为100~280 bloom的明胶; Described gelatin is the gelatin of 100~280 bloom;
作为优选,所述的明胶为250 bloom的明胶; As preferably, described gelatin is the gelatin of 250 bloom;
所述的催化剂为硝酸铈铵、过氧化氢、亚硫酸氢钠、过硫酸盐中的一种或多种;当为多种时,比例为任意比; The catalyst is one or more of cerium ammonium nitrate, hydrogen peroxide, sodium bisulfite, and persulfate; when multiple, the ratio is any ratio;
所述的催化剂为亚硫酸氢钠和过硫酸盐按任意比混合而成的混合物; Described catalyst is the mixture that sodium bisulfite and persulfate are mixed in any ratio;
所述的过硫酸盐为所有过硫酸盐; Described persulfate is all persulfates;
步骤(2).胺基化反应:将戊二醛溶液和二甲胺溶液加入制得的接枝共聚物中,45~65℃下搅拌反应2~4.5小时,冷却出料,制得明胶接枝丙烯酰胺阳离子高分子絮凝剂; Step (2). Amination reaction: Add glutaraldehyde solution and dimethylamine solution to the prepared graft copolymer, stir and react at 45-65°C for 2-4.5 hours, cool and discharge, and obtain gelatin grafted copolymer. Branched acrylamide cationic polymer flocculant;
反应体系中加入的戊二醛溶液与干燥明胶的质量比为0.13~1:1,二甲胺溶液与干燥明胶的质量比为0.13~1:1; The mass ratio of glutaraldehyde solution to dry gelatin added to the reaction system is 0.13-1:1, and the mass ratio of dimethylamine solution to dry gelatin is 0.13-1:1;
所述的戊二醛溶液中戊二醛的质量含量为35~50%; The mass content of glutaraldehyde in the described glutaraldehyde solution is 35~50%;
所述的二甲胺溶液中二甲胺的质量含量为33~40%。 The mass content of dimethylamine in the dimethylamine solution is 33-40%.
作为优选,所述的戊二醛溶液中戊二醛的质量含量为45%,所述的二甲胺溶液中二甲胺的质量含量为40%。 As a preference, the mass content of glutaraldehyde in the glutaraldehyde solution is 45%, and the mass content of dimethylamine in the dimethylamine solution is 40%.
本发明所具有的有益效果: The beneficial effects that the present invention has:
1.本发明明胶接枝丙烯酰胺阳离子高分子絮凝剂具备以下优点:(1)用量少,在絮凝剂加入量为1.5~4mg/L时,絮凝效果较佳;(2)絮凝效果好,絮体形成快,颗粒大,沉降速率较快;(3)成本低;(4)污染少。 1. The gelatin-grafted acrylamide cationic polymer flocculant of the present invention has the following advantages: (1) the dosage is small, and when the flocculant addition is 1.5-4 mg/L, the flocculation effect is better; (2) the flocculation effect is good, The flocs are formed quickly, the particles are large, and the sedimentation rate is fast; (3) low cost; (4) less pollution.
2.接枝共聚型高分子絮凝剂兼具天然高分子化合物和合成高分子化合物的某些优良特性,这主要表现在絮凝能力增强,分子链稳定性增加,阳离子化更容易进行等方面。其分子链上具有大量的极性基团和表面活性点,故能通过高分子的吸附架桥或电中和作用而产生絮凝效果。同时其自身可完全生物降解,具有良好的“环境可接受性”,因此正符合目前国家提倡绿色环保工程的要求。 2. The graft copolymerization polymer flocculant has some excellent characteristics of both natural polymer compounds and synthetic polymer compounds, which are mainly reflected in the enhanced flocculation ability, increased molecular chain stability, and easier cationization. There are a large number of polar groups and surface active points on its molecular chain, so it can produce flocculation effect through adsorption bridging or electrical neutralization of polymers. At the same time, it is completely biodegradable and has good "environmental acceptability", so it is in line with the current national requirements for promoting green environmental protection projects.
具体实施方式 Detailed ways
实施例1: Example 1:
步骤(1).接枝共聚反应:将50.0克干燥的100bloom明胶加入到1L去离子水中,搅拌均匀,然后加入2克硝酸铈铵,在氮气保护条件下,35℃反应60分钟,再加入150克丙烯酰胺,45℃下反应6小时,制得接枝共聚物; Step (1). Graft copolymerization reaction: Add 50.0 grams of dry 100 bloom gelatin to 1L of deionized water, stir evenly, then add 2 grams of ammonium cerium nitrate, react at 35°C for 60 minutes under nitrogen protection, and then add 150 gram of acrylamide, reacted for 6 hours at 45°C to obtain a graft copolymer;
步骤(2).胺基化反应:将50.0克质量含量为35%的戊二醛溶液和50.0克质量含量为33%的二甲胺溶液加入制得的接枝共聚物中,45℃下搅拌反应4.5小时,冷却出料,制得明胶接枝丙烯酰胺阳离子高分子絮凝剂。 Step (2). Amination reaction: 50.0 grams of 35% glutaraldehyde solution and 50.0 grams of 33% dimethylamine solution were added to the prepared graft copolymer and stirred at 45°C After reacting for 4.5 hours, cooling and discharging, the gelatin-grafted acrylamide cationic polymer flocculant was prepared.
实施例2: Example 2:
步骤(1).接枝共聚反应:将100克干燥的250bloom明胶加入到1L去离子水中,搅拌均匀,然后加入10克过氧化氢,在氮气保护条件下,50℃反应45分钟,再加入300克丙烯酰胺,57℃下反应4.5小时,制得接枝共聚物; Step (1). Graft copolymerization reaction: Add 100 grams of dry 250 bloom gelatin to 1L deionized water, stir evenly, then add 10 grams of hydrogen peroxide, react at 50°C for 45 minutes under nitrogen protection, and then add 300 gram of acrylamide, reacted for 4.5 hours at 57°C to obtain a graft copolymer;
步骤(2).胺基化反应:将13克质量含量为50%的戊二醛溶液和13克质量含量为40%的二甲胺溶液加入制得的接枝共聚物中,55℃下搅拌反应3.5小时,冷却出料,制得明胶接枝丙烯酰胺阳离子高分子絮凝剂。 Step (2). Amination reaction: 13 grams of glutaraldehyde solution with a mass content of 50% and 13 grams of dimethylamine solution with a mass content of 40% are added to the prepared graft copolymer, stirred at 55°C React for 3.5 hours, cool and discharge to prepare gelatin grafted acrylamide cationic polymer flocculant.
实施例3: Example 3:
步骤(1).接枝共聚反应:将150克干燥的280bloom明胶加入到1L去离子水中,搅拌均匀,然后加入20克亚硫酸氢钠,在氮气保护条件下,55℃反应40分钟,再加入500克丙烯酰胺,70℃下反应3小时,制得接枝共聚物; Step (1). Graft copolymerization reaction: Add 150 grams of dry 280 bloom gelatin to 1L deionized water, stir evenly, then add 20 grams of sodium bisulfite, react at 55°C for 40 minutes under nitrogen protection, and then add 500 grams of acrylamide were reacted for 3 hours at 70° C. to obtain a graft copolymer;
步骤(2).胺基化反应:将75克质量含量为45%的戊二醛溶液和75克质量含量为37%的二甲胺溶液加入制得的接枝共聚物中,65℃下搅拌反应2小时,冷却出料,制得明胶接枝丙烯酰胺阳离子高分子絮凝剂。 Step (2). Amination reaction: adding 75 grams of glutaraldehyde solution with a mass content of 45% and 75 grams of dimethylamine solution with a mass content of 37% into the prepared graft copolymer, stirring at 65°C React for 2 hours, cool and discharge to prepare gelatin-grafted acrylamide cationic polymer flocculant.
实施例4: Example 4:
步骤(1).接枝共聚反应:将60克干燥的150bloom明胶加入到1L去离子水中,搅拌均匀,然后加入6克过硫酸钠,在氮气保护条件下,40℃反应55分钟,再加入200克丙烯酰胺,50℃下反应5.5小时,制得接枝共聚物; Step (1). Graft copolymerization reaction: Add 60 grams of dry 150 bloom gelatin to 1L deionized water, stir evenly, then add 6 grams of sodium persulfate, react at 40°C for 55 minutes under nitrogen protection, and then add 200 gram of acrylamide, reacted for 5.5 hours at 50°C to obtain a graft copolymer;
步骤(2).胺基化反应:将48克质量含量为40%的戊二醛溶液和48克质量含量为35%的二甲胺溶液加入制得的接枝共聚物中,50℃下搅拌反应4小时,冷却出料,制得明胶接枝丙烯酰胺阳离子高分子絮凝剂。 Step (2). Amination reaction: adding 48 grams of glutaraldehyde solution with a mass content of 40% and 48 grams of dimethylamine solution with a mass content of 35% into the prepared graft copolymer, stirring at 50°C React for 4 hours, cool and discharge to prepare gelatin grafted acrylamide cationic polymer flocculant.
实施例5: Example 5:
步骤(1).接枝共聚反应:将80克干燥的200bloom明胶加入到1L去离子水中,搅拌均匀,然后加入15克过硫酸钾,在氮气保护条件下,45℃反应50分钟,再加入250克丙烯酰胺,60℃下反应5小时,制得接枝共聚物; Step (1). Graft copolymerization reaction: Add 80 grams of dry 200 bloom gelatin to 1L deionized water, stir evenly, then add 15 grams of potassium persulfate, react at 45°C for 50 minutes under nitrogen protection, and then add 250 gram of acrylamide, reacted for 5 hours at 60°C to obtain a graft copolymer;
步骤(2).胺基化反应:将48克质量含量为40%的戊二醛溶液和48克质量含量为35%的二甲胺溶液加入制得的接枝共聚物中,60℃下搅拌反应3小时,冷却出料,制得明胶接枝丙烯酰胺阳离子高分子絮凝剂。 Step (2). Amination reaction: adding 48 grams of glutaraldehyde solution with a mass content of 40% and 48 grams of dimethylamine solution with a mass content of 35% into the prepared graft copolymer, stirring at 60°C React for 3 hours, cool and discharge to prepare gelatin grafted acrylamide cationic polymer flocculant.
实施例6: Embodiment 6:
步骤(1).接枝共聚反应:将120克干燥的250bloom明胶加入到1L去离子水中,搅拌均匀,然后加入6克亚硫酸氢钠和6克过硫酸钠,在氮气保护条件下,48℃反应50分钟,再加入350克丙烯酰胺,65℃下反应4小时,制得接枝共聚物; Step (1). Graft copolymerization reaction: add 120 grams of dry 250 bloom gelatin to 1L deionized water, stir evenly, then add 6 grams of sodium bisulfite and 6 grams of sodium persulfate, under nitrogen protection conditions, 48 ° C React for 50 minutes, then add 350 grams of acrylamide, and react for 4 hours at 65°C to obtain a graft copolymer;
步骤(2).胺基化反应:将48克质量含量为45%的戊二醛溶液和48克质量含量为40%的二甲胺溶液加入制得的接枝共聚物中,60℃下搅拌反应3小时,冷却出料,制得明胶接枝丙烯酰胺阳离子高分子絮凝剂。 Step (2). Amination reaction: 48 grams of glutaraldehyde solution with a mass content of 45% and 48 grams of dimethylamine solution with a mass content of 40% are added to the prepared graft copolymer, stirred at 60°C React for 3 hours, cool and discharge to prepare gelatin grafted acrylamide cationic polymer flocculant.
实施例7: Embodiment 7:
步骤(1).接枝共聚反应:将140克干燥的230bloom明胶加入到1L去离子水中,搅拌均匀,然后加入8克过氧化氢和8克过硫酸钠,在氮气保护条件下,52℃反应43分钟,再加入450克丙烯酰胺,65℃下反应3.5小时,制得接枝共聚物; Step (1). Graft copolymerization reaction: add 140 grams of dry 230 bloom gelatin to 1L deionized water, stir evenly, then add 8 grams of hydrogen peroxide and 8 grams of sodium persulfate, and react at 52 ° C under nitrogen protection conditions After 43 minutes, add 450 grams of acrylamide and react at 65°C for 3.5 hours to obtain a graft copolymer;
步骤(2).胺基化反应:将28克质量含量为48%的戊二醛溶液和28克质量含量为38%的二甲胺溶液加入制得的接枝共聚物中,63℃下搅拌反应2.5小时,冷却出料,制得明胶接枝丙烯酰胺阳离子高分子絮凝剂。 Step (2). Amination reaction: adding 28 grams of glutaraldehyde solution with a mass content of 48% and 28 grams of dimethylamine solution with a mass content of 38% into the prepared graft copolymer, stirring at 63°C React for 2.5 hours, cool and discharge to prepare gelatin grafted acrylamide cationic polymer flocculant.
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1247838A (en) * | 1998-09-17 | 2000-03-22 | 吕广明 | Cationic high-molecular flocculant and its preparation |
| CN1519645A (en) * | 2003-02-06 | 2004-08-11 | ���Ῠ���ܴ�ع���ʽ���� | Silver-halide emulsion, its prepn. method, and silver-halide photograph material |
| EP1555997A1 (en) * | 2002-11-01 | 2005-07-27 | The Procter & Gamble Company | Polymeric assisted benefit agent delivery systems |
| CN102020775A (en) * | 2010-11-26 | 2011-04-20 | 浙江工业大学 | Preparation method of modified gelatin |
| CN102329843A (en) * | 2011-08-05 | 2012-01-25 | 蚌埠丰原明胶有限公司 | Enzyme method for preparing gelatin |
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Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1247838A (en) * | 1998-09-17 | 2000-03-22 | 吕广明 | Cationic high-molecular flocculant and its preparation |
| EP1555997A1 (en) * | 2002-11-01 | 2005-07-27 | The Procter & Gamble Company | Polymeric assisted benefit agent delivery systems |
| CN1519645A (en) * | 2003-02-06 | 2004-08-11 | ���Ῠ���ܴ�ع���ʽ���� | Silver-halide emulsion, its prepn. method, and silver-halide photograph material |
| CN102020775A (en) * | 2010-11-26 | 2011-04-20 | 浙江工业大学 | Preparation method of modified gelatin |
| CN102329843A (en) * | 2011-08-05 | 2012-01-25 | 蚌埠丰原明胶有限公司 | Enzyme method for preparing gelatin |
Non-Patent Citations (1)
| Title |
|---|
| 明胶接枝丙烯酰胺的研究;冷延国等;《高分子材料科学与工程》;20020128;第18卷(第01期);第1和2部分 * |
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