CN102603970B - Preparation method of cationic polyacrylamide - Google Patents
Preparation method of cationic polyacrylamide Download PDFInfo
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- CN102603970B CN102603970B CN201210010428.5A CN201210010428A CN102603970B CN 102603970 B CN102603970 B CN 102603970B CN 201210010428 A CN201210010428 A CN 201210010428A CN 102603970 B CN102603970 B CN 102603970B
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- 125000002091 cationic group Chemical group 0.000 title claims abstract description 46
- 229920002401 polyacrylamide Polymers 0.000 title claims abstract description 39
- 238000002360 preparation method Methods 0.000 title claims abstract description 9
- 239000000178 monomer Substances 0.000 claims abstract description 83
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000003999 initiator Substances 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims abstract description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 32
- 239000000084 colloidal system Substances 0.000 claims description 16
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 15
- 229910052757 nitrogen Inorganic materials 0.000 claims description 15
- 239000001301 oxygen Substances 0.000 claims description 15
- 229910052760 oxygen Inorganic materials 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 15
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims description 9
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 claims description 8
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 8
- 239000004202 carbamide Substances 0.000 claims description 8
- 239000012153 distilled water Substances 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 8
- 239000000843 powder Substances 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 8
- GQOKIYDTHHZSCJ-UHFFFAOYSA-M dimethyl-bis(prop-2-enyl)azanium;chloride Chemical compound [Cl-].C=CC[N+](C)(C)CC=C GQOKIYDTHHZSCJ-UHFFFAOYSA-M 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 2
- 239000002253 acid Substances 0.000 claims description 2
- -1 acrylyl Chemical group 0.000 claims description 2
- 238000007670 refining Methods 0.000 claims description 2
- 230000002829 reductive effect Effects 0.000 claims 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims 1
- 239000004160 Ammonium persulphate Substances 0.000 claims 1
- 239000004159 Potassium persulphate Substances 0.000 claims 1
- YXYZMHGSOKYZAF-UHFFFAOYSA-M [Cl-].C(C(=C)C)(=O)OCC[N+](C(C)(C)C)(C)C Chemical compound [Cl-].C(C(=C)C)(=O)OCC[N+](C(C)(C)C)(C)C YXYZMHGSOKYZAF-UHFFFAOYSA-M 0.000 claims 1
- 235000019270 ammonium chloride Nutrition 0.000 claims 1
- 235000019395 ammonium persulphate Nutrition 0.000 claims 1
- 229960000935 dehydrated alcohol Drugs 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 238000005469 granulation Methods 0.000 claims 1
- 230000003179 granulation Effects 0.000 claims 1
- 238000000227 grinding Methods 0.000 claims 1
- 235000019394 potassium persulphate Nutrition 0.000 claims 1
- 238000007789 sealing Methods 0.000 claims 1
- 229920001897 terpolymer Polymers 0.000 claims 1
- 238000009281 ultraviolet germicidal irradiation Methods 0.000 claims 1
- 239000010802 sludge Substances 0.000 abstract description 15
- 208000005156 Dehydration Diseases 0.000 abstract description 10
- 239000000654 additive Substances 0.000 abstract description 10
- 239000007864 aqueous solution Substances 0.000 abstract description 10
- 230000018044 dehydration Effects 0.000 abstract description 10
- 238000006297 dehydration reaction Methods 0.000 abstract description 10
- 239000003651 drinking water Substances 0.000 abstract description 10
- 235000020188 drinking water Nutrition 0.000 abstract description 10
- 238000006116 polymerization reaction Methods 0.000 abstract description 10
- 239000008139 complexing agent Substances 0.000 abstract description 8
- 239000002904 solvent Substances 0.000 abstract description 7
- 239000010865 sewage Substances 0.000 abstract description 5
- 231100000252 nontoxic Toxicity 0.000 abstract description 3
- 230000003000 nontoxic effect Effects 0.000 abstract description 3
- 230000035484 reaction time Effects 0.000 abstract description 3
- 239000000047 product Substances 0.000 description 16
- 239000000243 solution Substances 0.000 description 7
- 150000001408 amides Chemical class 0.000 description 6
- 239000012895 dilution Substances 0.000 description 6
- 238000010790 dilution Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 235000010265 sodium sulphite Nutrition 0.000 description 6
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- RRHXZLALVWBDKH-UHFFFAOYSA-M trimethyl-[2-(2-methylprop-2-enoyloxy)ethyl]azanium;chloride Chemical compound [Cl-].CC(=C)C(=O)OCC[N+](C)(C)C RRHXZLALVWBDKH-UHFFFAOYSA-M 0.000 description 4
- 239000012752 auxiliary agent Substances 0.000 description 3
- 239000008394 flocculating agent Substances 0.000 description 3
- 230000000977 initiatory effect Effects 0.000 description 3
- 230000001678 irradiating effect Effects 0.000 description 3
- FZGFBJMPSHGTRQ-UHFFFAOYSA-M trimethyl(2-prop-2-enoyloxyethyl)azanium;chloride Chemical compound [Cl-].C[N+](C)(C)CCOC(=O)C=C FZGFBJMPSHGTRQ-UHFFFAOYSA-M 0.000 description 3
- 239000004970 Chain extender Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000007879 VA-044 Substances 0.000 description 2
- LXEKPEMOWBOYRF-UHFFFAOYSA-N [2-[(1-azaniumyl-1-imino-2-methylpropan-2-yl)diazenyl]-2-methylpropanimidoyl]azanium;dichloride Chemical compound Cl.Cl.NC(=N)C(C)(C)N=NC(C)(C)C(N)=N LXEKPEMOWBOYRF-UHFFFAOYSA-N 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- LBSPZZSGTIBOFG-UHFFFAOYSA-N bis[2-(4,5-dihydro-1h-imidazol-2-yl)propan-2-yl]diazene;dihydrochloride Chemical compound Cl.Cl.N=1CCNC=1C(C)(C)N=NC(C)(C)C1=NCCN1 LBSPZZSGTIBOFG-UHFFFAOYSA-N 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229920000620 organic polymer Polymers 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- IMNIMPAHZVJRPE-UHFFFAOYSA-N triethylenediamine Chemical compound C1CN2CCN1CC2 IMNIMPAHZVJRPE-UHFFFAOYSA-N 0.000 description 2
- 208000004998 Abdominal Pain Diseases 0.000 description 1
- 206010012735 Diarrhoea Diseases 0.000 description 1
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 description 1
- 206010028813 Nausea Diseases 0.000 description 1
- 206010047700 Vomiting Diseases 0.000 description 1
- 231100000570 acute poisoning Toxicity 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 239000012986 chain transfer agent Substances 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000002496 gastric effect Effects 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 210000004400 mucous membrane Anatomy 0.000 description 1
- 230000008693 nausea Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 230000008733 trauma Effects 0.000 description 1
- 230000008673 vomiting Effects 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Treatment Of Sludge (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
本发明涉及一种阳离子型聚丙烯酰胺的制备方法。本发明是在丙烯酰胺(AM)和两种阳离子单体水溶液中,加入一定量的增溶剂及络合剂,调节反应体系的pH值,再加入一定量的引发剂,在一定波长的紫外光下经聚合反应而成。本发明的优点是聚合反应时间短,加入助剂种类少,制备的产品纯度高、无毒无害。本发明所获得的阳离子聚丙烯酰胺具有多功能性,分子量可达100万~1200万,残留丙烯酰胺单体浓度极低,适用于饮用水、污水处理和污泥脱水处理,具有良好的应用前景。The invention relates to a preparation method of cationic polyacrylamide. In the present invention, a certain amount of solubilizer and complexing agent are added to acrylamide (AM) and two cationic monomer aqueous solutions to adjust the pH value of the reaction system, and then a certain amount of initiator is added. It is formed by polymerization reaction. The invention has the advantages that the polymerization reaction time is short, the types of additives are few, and the prepared product has high purity and is non-toxic and harmless. The cationic polyacrylamide obtained in the present invention has multi-functionality, the molecular weight can reach 1 million to 12 million, and the residual acrylamide monomer concentration is extremely low. It is suitable for drinking water, sewage treatment and sludge dehydration treatment, and has a good application prospect .
Description
技术领域technical field
本发明涉及一种水溶液高分子聚合物的制备方法,具体涉及一种阳离子聚丙烯酰胺的制备方法。The invention relates to a method for preparing an aqueous solution polymer, in particular to a method for preparing a cationic polyacrylamide.
背景技术Background technique
目前,用于污水处理厂絮凝剂主要有无机絮凝剂和有机高分子絮凝剂两大类。聚丙烯酰胺絮凝剂是一种重要的有机高分子絮凝剂,包括阳离子聚丙烯酰胺(CPAM)、阴离子聚丙烯酰胺(APAM)、非离子聚丙烯酰胺(NPAM)和两性离子聚丙烯酰胺;其中,阳离子聚丙烯酰胺(CPAM)是其高端产品,它具有优良的除浊、脱色性能等优点,现行制备方法的产品大多由于助剂使用过多,影响产物纯度且合成反应不充分,丙烯酰胺残留单体含量较大,精制后丙烯酰胺残留单体含量仍大于0.05%不适用于生活饮用水处理,仅适合于工业污水、城市生活污水处理及城镇污水处理厂污泥脱水处理。At present, the flocculants used in sewage treatment plants mainly include inorganic flocculants and organic polymer flocculants. Polyacrylamide flocculant is an important organic polymer flocculant, including cationic polyacrylamide (CPAM), anionic polyacrylamide (APAM), nonionic polyacrylamide (NPAM) and zwitterionic polyacrylamide; among them, Cationic polyacrylamide (CPAM) is its high-end product. It has the advantages of excellent turbidity removal and decolorization performance. Most of the products produced by the current preparation method are affected by the use of too many additives, which affects the purity of the product and the synthesis reaction is insufficient. The monomer content is relatively large, and the residual monomer content of acrylamide after refining is still greater than 0.05%. It is not suitable for drinking water treatment, but only suitable for industrial sewage, urban domestic sewage treatment and sludge dehydration treatment of urban sewage treatment plants.
现有阳离子聚丙烯酰胺的制备方法,是以丙烯酰胺为原料,通过与阳离子单体的共聚或改性反应获得。如公开号为CN101353392A的专利“高分子量速溶阳离子聚丙烯酰胺的制备方法”中,该专利是以丙烯酰胺和共聚单体溶解于去离子水中;加入一定的添加剂,将物料混合均匀呈粘稠态,倾倒在一平面上铺摊为薄片状,通入高纯氮气,再对铺摊为薄片状的物料进行紫外光照射。该方法的不足是:1、反应聚合时间长,优选时间为3~6小时;2、反应水溶液中添加剂中除引发剂外,还加入六种助剂如螯合剂、链增长剂、链转移剂、表面活化剂等,而且每种助剂还包括一种或几种物质,各种助剂的投加量总和可高达总单体质量的1.95%。各种助剂最终将残留在合成产物之中,不易除去严重影响产物纯度;3、助剂中还有部分物质毒性较大,不合适生产及应用,如链增长剂硼酸本身可作为一种外伤消毒剂,口服可引起急性中毒,主要表现为胃肠道症状,有恶心、呕吐、腹痛、腹泻等,是不能用作水处理剂的原料和在水处理中应用,对水体可造成污染具有潜在的毒性;链调节剂二乙烯三胺,三乙烯二胺其蒸气或雾对鼻、喉和粘膜有腐蚀性,生产人员需佩戴防毒面具。The existing cationic polyacrylamide is prepared by using acrylamide as raw material through copolymerization or modification reaction with cationic monomers. For example, in the patent "Preparation Method of High Molecular Weight Instant Cationic Polyacrylamide" whose publication number is CN101353392A, the patent is to dissolve acrylamide and comonomer in deionized water; , poured on a flat surface and spread into flakes, and high-purity nitrogen gas is passed through, and then ultraviolet light is irradiated on the spread into flakes. The disadvantages of this method are: 1. The reaction polymerization time is long, preferably 3 to 6 hours; 2. In addition to the initiator, six kinds of auxiliary agents such as chelating agent, chain extender and chain transfer agent are added in the additive in the reaction aqueous solution. , surfactants, etc., and each additive also includes one or several substances, and the total dosage of various additives can be as high as 1.95% of the total monomer mass. Various additives will eventually remain in the synthetic product, which is not easy to remove and seriously affect the purity of the product; 3. Some substances in the additives are highly toxic and not suitable for production and application, such as the chain extender boric acid itself can be used as a trauma Disinfectant, oral administration can cause acute poisoning, mainly manifested as gastrointestinal symptoms, such as nausea, vomiting, abdominal pain, diarrhea, etc. It cannot be used as a raw material for water treatment agents and is used in water treatment. It has the potential to cause pollution to water bodies Toxicity; chain regulator diethylenetriamine, triethylenediamine, its vapor or mist are corrosive to the nose, throat and mucous membranes, production personnel need to wear gas masks.
发明内容Contents of the invention
本发明所要解决的技术问题就是提供一种阳离子聚丙烯酰胺的方法,该方法的制备过程中聚合反应时间短,加入助剂种类少、用量低,制备的产品纯度高、无毒无害。The technical problem to be solved by the present invention is to provide a method of cationic polyacrylamide, the polymerization reaction time is short in the preparation process of the method, the types of additives are added and the dosage is low, and the prepared product is high in purity, non-toxic and harmless.
本发明所要解决的技术问题是通过这样的技术方案实现的,它包括以下步骤:The technical problem to be solved by the present invention is realized by such technical scheme, and it comprises the following steps:
第一步,按单体总质量百分比称取单体丙烯酰胺20%~80%,两种阳离子单体20%~80%;加入蒸馏水,并搅拌均匀至完全溶解,配制出总单体的质量浓度为20%~50%的单体水溶液;The first step is to weigh 20% to 80% of the monomer acrylamide and 20% to 80% of the two cationic monomers according to the total mass percentage of the monomer; add distilled water and stir until it is completely dissolved to prepare the mass of the total monomer Monomer aqueous solution with a concentration of 20% to 50%;
第二步,在上述配制的单体水溶液中,加入以单体总质量0.05%~0.5%的尿素,再加入以单体总质量0.01%~0.2%的乙二胺四乙酸络合剂,用弱碱或弱酸调节体系的pH值8~9,充入高纯氮除氧气,快速加入以单体总质量0.1%~3%的引发剂,该引发剂包括氧化剂过硫酸钾或过硫酸铵和还原剂亚硫酸钠,氧化剂与还原剂的质量比范围为0.5~2,同时搅拌均匀,再充入高纯氮除氧气后密封;In the second step, add 0.05% to 0.5% of urea with the total mass of the monomers to the aqueous monomer solution prepared above, and then add 0.01% to 0.2% of the ethylenediaminetetraacetic acid complexing agent with the total mass of the monomers. Weak base or weak acid adjusts the pH value of the system to 8-9, fills high-purity nitrogen to remove oxygen, and quickly adds 0.1% to 3% of the total mass of the monomer Initiator, the initiator includes the oxidizing agent potassium persulfate or ammonium persulfate and The reducing agent is sodium sulfite, the mass ratio of the oxidizing agent to the reducing agent is in the range of 0.5 to 2, and at the same time, it is stirred evenly, and then filled with high-purity nitrogen to remove oxygen and then sealed;
第三步,在室内环境温度下,将上述配制的混合物放入到紫外光反应装置中,在紫外光照射下进行引发,照射10min~90min后,静置熟化1小时以上,制得无色透明的阳离子聚丙烯酰胺胶体;The third step is to put the above-mentioned prepared mixture into the ultraviolet light reaction device at the indoor ambient temperature, and initiate it under ultraviolet light irradiation. After irradiating for 10 minutes to 90 minutes, let it stand and mature for more than 1 hour to obtain a colorless and transparent cationic polyacrylamide colloid;
第四步,将所述的阳离子聚丙烯酰胺粘稠胶体,经过剪碎造粒、无水乙醇多次洗涤精制、烘干、研磨后制得阳离子聚丙烯酰胺白色固体粉末。In the fourth step, the cationic polyacrylamide viscous colloid is shredded and granulated, repeatedly washed and refined with absolute ethanol, dried and ground to obtain a white solid powder of cationic polyacrylamide.
本发明采用的引发剂还可以是有机引发剂或无机有机复配引发剂。The initiator used in the present invention can also be an organic initiator or an inorganic-organic composite initiator.
本发明所用材料均为市售,价格低廉,可直接购买。The materials used in the present invention are all commercially available with low price and can be purchased directly.
由于本发明选用的引发体系为波长较短的紫外光,其能量大于单体的化学键能,可以在较长时间内引发单体聚合,加入引发剂、助剂后反应速率大幅提升,且所需引发剂、助剂用量低,就可得到纯度高、分子量分布均匀的产物。本发明具有以下的优点:Since the initiating system selected by the present invention is ultraviolet light with a shorter wavelength, its energy is greater than the chemical bond energy of the monomer, which can initiate monomer polymerization in a long period of time, and the reaction rate is greatly improved after adding initiator and auxiliary agent, and the required With low dosage of initiator and auxiliary agent, a product with high purity and uniform molecular weight distribution can be obtained. The present invention has the following advantages:
1、聚合反应时间短。由于本发明采用的是紫外光引发聚合,紫外光能够加快化学键的断裂,通过自由基聚合,所以能够大大缩短引发聚合时间,其引发聚合时间最低10min。1. The polymerization reaction time is short. Since the present invention uses ultraviolet light to initiate polymerization, ultraviolet light can accelerate the breaking of chemical bonds through free radical polymerization, so the initiation polymerization time can be greatly shortened, and the initiation polymerization time is at least 10 minutes.
2、合成所需引发剂、助剂种类少、用量低,产品中的残留物少,产品纯度高;所用助剂无毒无害,产品使用安全,适合饮用水的处理。2. The initiators and additives required for the synthesis are few in type and low in dosage, with few residues in the product and high purity of the product; the additives used are non-toxic and harmless, and the product is safe to use and suitable for drinking water treatment.
具体实施方式Detailed ways
下面结合实施例对本发明作进一步说明:The present invention will be further described below in conjunction with embodiment:
实施例1:Example 1:
第一步,称取单体丙烯酰胺7g、二甲基二烯丙基氯化铵2g、丙烯酰氧乙基三甲基氯化铵1g放入广口瓶中,加蒸馏水23.3ml,搅拌均匀,配制出总单体的质量浓度为30%的单体水溶液;In the first step, weigh 7g of monomer acrylamide, 2g of dimethyldiallyl ammonium chloride, and 1g of acryloyloxyethyltrimethylammonium chloride into a jar, add 23.3ml of distilled water, and stir well , prepare the monomer aqueous solution that the mass concentration of total monomer is 30%;
第二步,在上述配制的单体水溶液中,加入0.02g尿素作为增溶剂(用量为单体总质量的0.2%),再加入乙二胺四乙酸络合剂0.004g(用量为单体总质量的0.04%),调节pH=9;通入氮气除氧,加入无机引发剂0.144g(过硫酸钾与亚硫酸钠质量比为1:2),用量为单体总质量的1.44%,搅拌均匀,再通入氮气除氧,之后密闭。In the second step, add 0.02 g of urea as a solubilizer (0.2% of the total mass of the monomer) to the aqueous monomer solution prepared above, and then add 0.004 g of ethylenediaminetetraacetic acid complexing agent (0.2% of the total mass of the monomer) 0.04% of the mass), adjust the pH=9; pass nitrogen to remove oxygen, add 0.144g of inorganic initiator (the mass ratio of potassium persulfate to sodium sulfite is 1:2), the dosage is 1.44% of the total mass of the monomer, stir evenly, Nitrogen was added to remove oxygen, and then airtight.
第三步,在室内环境温度下,将上述配制的混合物放入到紫外光反应装置中,紫外光照射15分钟后,得到无色透明的阳离子聚丙烯酰胺胶体;丙烯酰胺残留单体含量为0.1870%,稀释后可直接用于污泥脱水处理。The third step is to put the above-prepared mixture into the ultraviolet light reaction device at the ambient temperature of the room. After irradiating ultraviolet light for 15 minutes, a colorless and transparent cationic polyacrylamide colloid is obtained; the residual monomer content of acrylamide is 0.1870 %, it can be directly used for sludge dewatering after dilution.
第四步,将所述的阳离子聚丙烯酰胺胶体,经过剪碎造粒、精制、烘干、研磨后制得阳离子聚丙烯酰胺白色固体粉末;测得分子量为4747241,阳离子度为10.86%,丙烯酰胺残留单体含量为0.0153%的高纯度产品。适用于饮用水处理和污泥脱水处理。In the fourth step, the cationic polyacrylamide colloid is crushed and granulated, refined, dried, and ground to obtain a white solid powder of cationic polyacrylamide; the measured molecular weight is 4747241, and the cationic degree is 10.86%. High-purity product with amide residual monomer content of 0.0153%. It is suitable for drinking water treatment and sludge dehydration treatment.
实施例2Example 2
第一步,称取单体丙烯酰胺8g、甲基丙烯酰氧乙基三甲基氯化铵1g、二甲基二烯丙基氯化铵1g放入广口瓶中,加蒸馏水10ml,搅拌均匀,配制出总单体的质量浓度为50%的单体水溶液;In the first step, weigh 8g of monomer acrylamide, 1g of methacryloyloxyethyltrimethylammonium chloride, and 1g of dimethyldiallylammonium chloride into a jar, add 10ml of distilled water, and stir Uniform, prepare the monomer aqueous solution whose mass concentration of total monomer is 50%;
第二步,在上述配制的单体水溶液中,加入0.05g尿素作为增溶剂(用量为单体总质量的0.5%),再加入乙二胺四乙酸络合剂0.02g(用量为单体总质量的0.2%),调节pH=8;通入氮气除氧,加入无机引发剂0.015g(过硫酸铵与亚硫酸钠质量比为2:1,用量为单体总质量的0.15%),搅拌均匀,再通入氮气除氧,之后密闭;In the second step, add 0.05g of urea as a solubilizer (0.5% of the total mass of the monomer) to the aqueous monomer solution prepared above, and then add 0.02g of ethylenediaminetetraacetic acid complexing agent (0.5% of the total mass of the monomer) 0.2% of the mass), adjust the pH=8; pass nitrogen to remove oxygen, add 0.015g of inorganic initiator (the mass ratio of ammonium persulfate to sodium sulfite is 2:1, the dosage is 0.15% of the total mass of the monomer), stir evenly, Then pass nitrogen gas to remove oxygen, and then airtight;
第三步,在室内环境温度下,将上述配制的混合物放入到紫外光反应装置中,紫外光照射10分钟后,得到无色透明的阳离子聚丙烯酰胺胶体;丙烯酰胺残留单体含量为0.2262%,稀释后可直接用于污泥脱水处理。The third step is to put the above-prepared mixture into the ultraviolet light reaction device at the indoor ambient temperature. After 10 minutes of ultraviolet light irradiation, a colorless and transparent cationic polyacrylamide colloid is obtained; the residual monomer content of acrylamide is 0.2262 %, it can be directly used for sludge dewatering after dilution.
第四步,将所述的阳离子聚丙烯酰胺胶体,经过剪碎造粒、精制、烘干、研磨后制得阳离子聚丙烯酰胺白色固体粉末;测得分子量为1280500,阳离子度为3.37%,丙烯酰胺残留单体含量为0.0197%的高纯度产品,适用于饮用水处理和污泥脱水处理。In the fourth step, the cationic polyacrylamide colloid is crushed and granulated, refined, dried, and ground to obtain a white solid powder of cationic polyacrylamide; the measured molecular weight is 1280500, and the cationic degree is 3.37%. It is a high-purity product with amide residual monomer content of 0.0197%, suitable for drinking water treatment and sludge dehydration treatment.
实施例3Example 3
第一步,称取单体丙烯酰胺7g、甲基丙烯酰氧乙基三甲基氯化铵1.5g、二甲基二烯丙基氯化铵1.5g放入广口瓶中,加蒸馏水30ml,搅拌均匀,配制出总单体的质量浓度为25%的单体水溶液;In the first step, weigh 7g of monomer acrylamide, 1.5g of methacryloxyethyltrimethylammonium chloride, and 1.5g of dimethyldiallylammonium chloride into a jar, add 30ml of distilled water , stir evenly, prepare the monomer aqueous solution that the mass concentration of total monomer is 25%;
第二步,在上述配制的单体水溶液中,加入0.005g尿素作为增溶剂(用量为单体总质量的0.05%),再加入乙二胺四乙酸络合剂0.001g(用量为单体总质量的0.01%),调节pH=6;通入氮气除氧,加入0.12g有机引发剂偶氮二异丁脒盐酸盐V50(用量为单体总质量的1.2%),搅拌均匀,再通入氮气除氧,之后密闭;In the second step, add 0.005g of urea as a solubilizer (0.05% of the total mass of the monomer) to the aqueous monomer solution prepared above, and then add 0.001g of ethylenediaminetetraacetic acid complexing agent (0.05% of the total mass of the monomer) 0.01% of the mass of the monomer), adjust the pH=6; pass through nitrogen to remove oxygen, add 0.12g of organic initiator azobisisobutylamidine hydrochloride V50 (the amount is 1.2% of the total mass of the monomer), stir evenly, and pass through Into nitrogen to remove oxygen, then airtight;
第三步,在室内环境温度下,将上述配制的混合物放入到紫外光反应装置中,紫外光照射60分钟后,得到无色透明的阳离子聚丙烯酰胺胶体;丙烯酰胺残留单体含量为0.1221%;稀释后可直接用于污泥脱水处理。The third step is to put the above-prepared mixture into the ultraviolet light reaction device at the indoor ambient temperature. After irradiating with ultraviolet light for 60 minutes, a colorless and transparent cationic polyacrylamide colloid is obtained; the residual monomer content of acrylamide is 0.1221 %; It can be directly used for sludge dehydration after dilution.
第四步,将所述的阳离子聚丙烯酰胺胶体,经过剪碎造粒、精制、烘干、研磨后制得阳离子聚丙烯酰胺白色固体粉末;测得分子量为4051330,阳离子度为10.98%,丙烯酰胺残留单体含量为0.0107%的高纯度产品,适用于饮用水处理和污泥脱水处理。In the fourth step, the cationic polyacrylamide colloid is crushed, granulated, refined, dried, and ground to obtain a white solid powder of cationic polyacrylamide; the measured molecular weight is 4051330, and the cationic degree is 10.98%. It is a high-purity product with amide residual monomer content of 0.0107%, suitable for drinking water treatment and sludge dehydration treatment.
实施例4Example 4
第一步,称取单体丙烯酰胺2g、二甲基二烯丙基氯化铵4g、丙烯酰氧乙基三甲基氯化铵4g放入广口瓶中,加蒸馏水30ml,搅拌均匀,配制出总单体的质量浓度为25%的单体水溶液;In the first step, weigh 2g of monomer acrylamide, 4g of dimethyldiallyl ammonium chloride, and 4g of acryloyloxyethyltrimethylammonium chloride into a jar, add 30ml of distilled water, and stir evenly. Prepare the monomer aqueous solution that the mass concentration of total monomer is 25%;
第二步,在上述配制的单体水溶液中,加入0.024g尿素作为增溶剂(用量为单体总质量的0.24%),再加入乙二胺四乙酸络合剂0.02g(用量为单体总质量的0.2%),调节pH=8;通入氮气除氧,加入无机有机复配引发剂0.12g(过硫酸钾、亚硫酸钠与v50质量比为1:1:8,用量为单体总质量的1.2%),搅拌均匀,再通入氮气除氧,之后密闭;In the second step, add 0.024g of urea as a solubilizer (0.24% of the total mass of the monomer) to the aqueous monomer solution prepared above, and then add 0.02g of ethylenediaminetetraacetic acid complexing agent (0.24% of the total mass of the monomer) 0.2% of the mass), adjust the pH=8; pass through nitrogen to remove oxygen, add 0.12g of inorganic-organic compound initiator (the mass ratio of potassium persulfate, sodium sulfite and v50 is 1:1:8, and the dosage is 1% of the total mass of the monomer 1.2%), stir evenly, then pass in nitrogen to remove oxygen, and then airtight;
第三步,在室内环境温度下,将上述配制的混合物放入到紫外光反应装置中,紫外光照射60分钟后,得到无色透明的阳离子聚丙烯酰胺胶体;丙烯酰胺残留单体含量为0.1416%,稀释后可直接用于污泥脱水处理。The third step is to put the above-prepared mixture into the ultraviolet light reaction device at the indoor ambient temperature. After 60 minutes of ultraviolet light irradiation, a colorless and transparent cationic polyacrylamide colloid is obtained; the residual monomer content of acrylamide is 0.1416 %, it can be directly used for sludge dewatering after dilution.
第四步,将所述的阳离子聚丙烯酰胺胶体,经过剪碎造粒、精制、烘干、研磨后制得阳离子聚丙烯酰胺白色固体粉末;测得分子量为7051330,阳离子度为51.86%,丙烯酰胺残留单体含量为0.0113%的高纯度产品,适用于饮用水处理和污泥脱水处理。In the fourth step, the cationic polyacrylamide colloid is crushed, granulated, refined, dried, and ground to obtain a white solid powder of cationic polyacrylamide; the measured molecular weight is 7051330, and the cationic degree is 51.86%. It is a high-purity product with amide residual monomer content of 0.0113%, suitable for drinking water treatment and sludge dehydration treatment.
实施例5Example 5
第一步,称取单体丙烯酰胺6g、甲基丙烯酰氧乙基三甲基氯化铵2g、丙烯酰氧乙基三甲基氯化铵2g放入广口瓶中,加蒸馏水40ml,搅拌均匀,配制出总单体的质量浓度为20%的单体水溶液;In the first step, weigh 6g of monomer acrylamide, 2g of methacryloyloxyethyltrimethylammonium chloride, and 2g of acryloyloxyethyltrimethylammonium chloride into a jar, add 40ml of distilled water, Stir evenly, prepare the monomer aqueous solution that the mass concentration of total monomer is 20%;
第二步,在上述配制的单体水溶液中,加入0.005g尿素作为增溶剂(用量为单体总质量的0.05%),再加入乙二胺四乙酸络合剂0.001g(用量为单体总质量的0.01%),调节pH=8;通入氮气除氧,加入无机有机复配引发剂0.25g(过硫酸铵、亚硫酸钠与V-50质量比为2:2:1,用量为单体总质量的2.5%),搅拌均匀,再通入氮气除氧,之后密闭;In the second step, add 0.005g of urea as a solubilizer (0.05% of the total mass of the monomer) to the aqueous monomer solution prepared above, and then add 0.001g of ethylenediaminetetraacetic acid complexing agent (0.05% of the total mass of the monomer) 0.01% of the mass), adjust the pH=8; pass through nitrogen to remove oxygen, add 0.25g of inorganic-organic compound initiator (the mass ratio of ammonium persulfate, sodium sulfite and V-50 is 2:2:1, and the dosage is the total monomer 2.5% of the mass), stir evenly, then pass in nitrogen to deoxygenate, and then airtight;
第三步,在室内环境温度下,将上述配制的混合物放入到紫外光反应装置中,紫外光照射60分钟后,得到无色透明的阳离子聚丙烯酰胺胶体;丙烯酰胺残留单体含量为0.0866%,稀释后可直接用于污泥脱水处理。The third step is to put the above-mentioned prepared mixture into the ultraviolet light reaction device at the indoor ambient temperature, and after 60 minutes of ultraviolet light irradiation, a colorless and transparent cationic polyacrylamide colloid is obtained; the residual monomer content of acrylamide is 0.0866 %, it can be directly used for sludge dewatering after dilution.
第四步,将所述的阳离子聚丙烯酰胺胶体,经过剪碎造粒、精制、烘干、研磨后制得阳离子聚丙烯酰胺白色固体粉末;测得分子量为6378830,阳离子度为16.0%,丙烯酰胺残留单体含量为0.0087%的高纯度产品,适用于饮用水处理和污泥脱水处理。In the fourth step, the cationic polyacrylamide colloid is crushed and granulated, refined, dried, and ground to obtain a white solid powder of cationic polyacrylamide; the measured molecular weight is 6378830, and the cationic degree is 16.0%. It is a high-purity product with amide residual monomer content of 0.0087%, suitable for drinking water treatment and sludge dehydration treatment.
实施例6Example 6
第一步,称取单体丙烯酰胺4g、甲基丙烯酰氧乙基三甲基氯化铵3g、二甲基二烯丙基氯化铵3g放入广口瓶中,加蒸馏水10ml,搅拌均匀,配制出总单体的质量浓度为50%的单体水溶液;The first step, weigh 4g of monomer acrylamide, 3g of methacryloxyethyltrimethylammonium chloride, 3g of dimethyldiallylammonium chloride into a jar, add 10ml of distilled water, stir Uniform, prepare the monomer aqueous solution whose mass concentration of total monomer is 50%;
第二步,在上述配制的单体水溶液中,加入0.05g尿素作为增溶剂(用量为单体总质量的0.5%),再加入乙二胺四乙酸络合剂0.001g(用量为单体总质量的0.01%),调节pH=8;通入氮气除氧,加入无机有机复配引发剂0.3g(过硫酸铵、亚硫酸钠与VA-044质量比为1:1:8,用量为单体总质量的3%),搅拌均匀,再通入氮气除氧,之后密闭;In the second step, add 0.05g of urea as a solubilizer (0.5% of the total mass of the monomer) to the aqueous monomer solution prepared above, and then add 0.001g of ethylenediaminetetraacetic acid complexing agent (0.5% of the total mass of the monomer) 0.01% of the mass), adjust the pH=8; pass through nitrogen to remove oxygen, add 0.3g of inorganic-organic compound initiator (the mass ratio of ammonium persulfate, sodium sulfite and VA-044 is 1:1:8, and the dosage is the total monomer 3% of the mass), stir evenly, then pass in nitrogen to remove oxygen, and then seal it;
第三步,在室内环境温度下,将上述配制的混合物放入到紫外光反应装置中,紫外光照射90分钟后,得到无色透明的阳离子聚丙烯酰胺胶体;丙烯酰胺残留单体含量为0.0582%,稀释后可直接用于污泥脱水处理。The third step is to put the above-prepared mixture into the ultraviolet light reaction device at the indoor ambient temperature. After 90 minutes of ultraviolet light irradiation, a colorless and transparent cationic polyacrylamide colloid is obtained; the residual monomer content of acrylamide is 0.0582 %, it can be directly used for sludge dewatering after dilution.
第四步,将所述的阳离子聚丙烯酰胺胶体,经过剪碎造粒、精制、烘干、研磨后制得阳离子聚丙烯酰胺白色固体粉末;测得分子量为11200730,阳离子度为29.85%,丙烯酰胺残留单体含量为0.0068%的高纯度产品,适用于饮用水处理和污泥脱水处理。In the fourth step, the cationic polyacrylamide colloid is crushed and granulated, refined, dried, and ground to obtain a white solid powder of cationic polyacrylamide; the measured molecular weight is 11200730, and the cationic degree is 29.85%. It is a high-purity product with amide residual monomer content of 0.0068%, suitable for drinking water treatment and sludge dehydration treatment.
实施例7Example 7
与实施例3相同,但加入0.25g有机引发剂偶氮二异丙基咪唑啉盐酸盐VA-044(用量为单体总质量的2.5%),得到分子量为6378830,阳离子度为11.85%,丙烯酰胺残留单体含量为0.0087%的高纯度产品,适用于饮用水处理和污泥脱水处理。Same as Example 3, but adding 0.25g of organic initiator azodiisopropylimidazoline hydrochloride VA-044 (the amount is 2.5% of the total mass of monomers), the obtained molecular weight is 6378830, and the cationic degree is 11.85%. It is a high-purity product with acrylamide residual monomer content of 0.0087%, suitable for drinking water treatment and sludge dehydration treatment.
上述实施例中,聚合反应使用的室内环境温度为5℃~45℃室内温度,上述的紫外光由高压汞灯产生,其紫外光波长在220nm~2000nm,主波长365nm。In the above examples, the indoor ambient temperature used for the polymerization reaction is 5° C. to 45° C., and the above-mentioned ultraviolet light is generated by a high-pressure mercury lamp. The ultraviolet light has a wavelength of 220 nm to 2000 nm and a dominant wavelength of 365 nm.
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| CN103059219B (en) * | 2013-01-28 | 2015-06-24 | 重庆大学 | Preparation method for hydrophobic-association cationic polyacrylamide |
| CN103819692A (en) * | 2014-02-28 | 2014-05-28 | 重庆大学 | Simplified processing method of polyacrylamide by template copolymerization |
| CN103833117B (en) * | 2014-03-07 | 2015-07-15 | 重庆大学 | Organic-inorganic composite coagulant for processing printing and dyeing wastewater and preparation method thereof |
| CN106317298B (en) * | 2015-06-16 | 2020-07-31 | 中石化石油工程技术服务有限公司 | Cation-coated flocculant and preparation method thereof |
| CN104910321B (en) * | 2015-06-16 | 2019-02-12 | 河南弘康环保科技有限公司 | A kind of ternary polymerization cationic-type polyacrylamide |
| CN105273130A (en) * | 2015-11-06 | 2016-01-27 | 东营市诺尔化工有限责任公司 | Preparing method for degradability-resisting enhancement-type cationic polyacrylamide |
| CN106046248B (en) * | 2016-07-19 | 2019-04-16 | 四川科尔瑞环保科技有限责任公司 | Cationic flocculant and preparation method thereof |
| CN108440710B (en) * | 2018-03-15 | 2021-03-09 | 重庆大学 | A kind of synthetic method of cationic polyacrylamide water treatment agent |
| CN110563865B (en) * | 2019-09-05 | 2021-11-09 | 江苏富淼科技股份有限公司 | High molecular weight low-residual-monomer polyacrylamide inverse emulsion and preparation method thereof |
| CN111748057A (en) * | 2020-07-09 | 2020-10-09 | 重庆工商大学 | A kind of method for synthesizing gum arabic high polymer by composite initiation system |
| CN112409534A (en) * | 2020-11-27 | 2021-02-26 | 大庆石油管理局有限公司 | Cation auxiliary agent for treating oilfield produced water and preparation method thereof |
| CN112759705A (en) * | 2020-12-14 | 2021-05-07 | 中船重工(邯郸)派瑞特种气体有限公司 | Ternary polymerization cationic polymer and application thereof |
| CN113024719A (en) * | 2021-02-07 | 2021-06-25 | 青州金昊工贸有限公司 | Preparation method of dry strength agent for food-grade paper |
| CN113698530B (en) * | 2021-10-28 | 2022-02-18 | 江苏富淼科技股份有限公司 | High-steric-hindrance series cationic solid polyacrylamide and preparation method thereof |
-
2012
- 2012-01-13 CN CN201210010428.5A patent/CN102603970B/en not_active Expired - Fee Related
Non-Patent Citations (8)
| Title |
|---|
| "AM /DMC /DMDAAC三元共聚物粉剂的制备及应用";芦晓然等;《现代化工》;20100531;第30卷(第5期);44-46及48 * |
| "AM-DAC-DMDAAC共聚物制备及其絮凝性能研究";徐世莹等;《环境科学与技术》;20110630;第34卷(第6G期);92-95 * |
| "超高分子量高阳离子度AM-DMC-DAC三元共聚物的合成及其絮凝性能";李振泉等;《功能高分子学报》;20090930;第22卷(第3期);289-292及312 * |
| 刘晓平等."三元共聚阳离子聚丙烯酰胺的合成及性能评价".《山东大学学报(工学版)》.2009,第39卷(第3期),71-76. |
| 刘晓平等."三元共聚阳离子聚丙烯酰胺的合成及性能评价".《山东大学学报(工学版)》.2009,第39卷(第3期),71-76. * |
| 徐世莹等."AM-DAC-DMDAAC共聚物制备及其絮凝性能研究".《环境科学与技术》.2011,第34卷(第6G期),92-95. |
| 李振泉等."超高分子量高阳离子度AM-DMC-DAC三元共聚物的合成及其絮凝性能".《功能高分子学报》.2009,第22卷(第3期),289-292及312. |
| 芦晓然等."AM /DMC /DMDAAC三元共聚物粉剂的制备及应用".《现代化工》.2010,第30卷(第5期),44-46及48. |
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