CN102153183A - Nano ferric oxide-cationic polyelectrolyte coupled multielement composite flocculant - Google Patents
Nano ferric oxide-cationic polyelectrolyte coupled multielement composite flocculant Download PDFInfo
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- 239000002131 composite material Substances 0.000 title claims abstract description 35
- 229920000867 polyelectrolyte Polymers 0.000 title claims abstract description 29
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 125000002091 cationic group Chemical group 0.000 claims abstract description 16
- 230000000694 effects Effects 0.000 claims abstract description 15
- QJZYHAIUNVAGQP-UHFFFAOYSA-N 3-nitrobicyclo[2.2.1]hept-5-ene-2,3-dicarboxylic acid Chemical compound C1C2C=CC1C(C(=O)O)C2(C(O)=O)[N+]([O-])=O QJZYHAIUNVAGQP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000004021 humic acid Substances 0.000 claims abstract description 8
- 229920001661 Chitosan Polymers 0.000 claims abstract description 4
- 229920002401 polyacrylamide Polymers 0.000 claims abstract description 4
- 229920000768 polyamine Polymers 0.000 claims abstract description 3
- 238000004062 sedimentation Methods 0.000 claims abstract description 3
- 238000005345 coagulation Methods 0.000 claims description 16
- 230000015271 coagulation Effects 0.000 claims description 16
- 238000005189 flocculation Methods 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 15
- 230000016615 flocculation Effects 0.000 claims description 13
- 239000003795 chemical substances by application Substances 0.000 claims description 12
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 9
- 239000002105 nanoparticle Substances 0.000 claims description 7
- 238000002360 preparation method Methods 0.000 claims description 6
- 230000008878 coupling Effects 0.000 claims description 5
- 238000010168 coupling process Methods 0.000 claims description 5
- 238000005859 coupling reaction Methods 0.000 claims description 5
- 229910001566 austenite Inorganic materials 0.000 claims description 4
- 238000005516 engineering process Methods 0.000 claims description 4
- 229910000859 α-Fe Inorganic materials 0.000 claims description 4
- 239000002086 nanomaterial Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims description 2
- 238000000227 grinding Methods 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 239000000356 contaminant Substances 0.000 claims 1
- 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 1
- 231100001261 hazardous Toxicity 0.000 claims 1
- 229910006540 α-FeOOH Inorganic materials 0.000 abstract description 6
- 231100000331 toxic Toxicity 0.000 abstract description 4
- 230000002588 toxic effect Effects 0.000 abstract description 4
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 3
- 229920000371 poly(diallyldimethylammonium chloride) polymer Polymers 0.000 abstract description 3
- 239000003344 environmental pollutant Substances 0.000 abstract description 2
- 231100000719 pollutant Toxicity 0.000 abstract description 2
- SZVJSHCCFOBDDC-UHFFFAOYSA-N ferrosoferric oxide Chemical compound O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 abstract 2
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 abstract 2
- 238000005728 strengthening Methods 0.000 abstract 1
- 229910003145 α-Fe2O3 Inorganic materials 0.000 abstract 1
- 229910006297 γ-Fe2O3 Inorganic materials 0.000 abstract 1
- 239000008394 flocculating agent Substances 0.000 description 7
- 239000005416 organic matter Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 239000006228 supernatant Substances 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 239000003651 drinking water Substances 0.000 description 2
- 235000020188 drinking water Nutrition 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- -1 nano α-FeOOH Chemical compound 0.000 description 2
- YFSUTJLHUFNCNZ-UHFFFAOYSA-N perfluorooctane-1-sulfonic acid Chemical compound OS(=O)(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F YFSUTJLHUFNCNZ-UHFFFAOYSA-N 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- RGKMZNDDOBAZGW-UHFFFAOYSA-N aluminum calcium Chemical compound [Al].[Ca] RGKMZNDDOBAZGW-UHFFFAOYSA-N 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000010668 complexation reaction Methods 0.000 description 1
- 239000005446 dissolved organic matter Substances 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 159000000014 iron salts Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001021 polysulfide Polymers 0.000 description 1
- 239000005077 polysulfide Substances 0.000 description 1
- 150000008117 polysulfides Polymers 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
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- 230000005476 size effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 231100001234 toxic pollutant Toxicity 0.000 description 1
- 230000005641 tunneling Effects 0.000 description 1
- 239000011882 ultra-fine particle Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种无机-有机复合絮凝剂,特别涉及一种用于饮用水中有机物、浊度、色度去除效果较好的复合絮凝剂。The invention relates to an inorganic-organic composite flocculant, in particular to a composite flocculant with good removal effect for organic matters, turbidity and chroma in drinking water.
背景技术Background technique
面对水源水质的变化和对水质要求的提高,常规的混凝工艺已不能满足要求。国内外的试验研究和实际生产结果表明常规的混凝、沉淀及过滤只能去除水中有机物的20%~30%,且由于溶解性有机物的存在,不利于破坏胶体的稳定性除浊效果显著下降,因此,对复合絮凝剂的研究越来越受到关注,如专利CN1821114A公开了一种硫酸铝、熟石灰等复合絮凝剂的制备方法;专利CN1393410A通过水解反应、聚合反应及缩聚反应将二氰二胺与甲醛的聚合物、聚硫氯化铝和/或聚硫氯化铝钙制成一种有机无机复合型絮凝剂;专利CN101327977A将铝盐、铁盐、聚丙烯酰胺及淀粉复合成双层或多层絮凝剂,经多层缓释的结构增加了药剂的作用效率,提高了药剂的效能;专利CN101717144A将聚硅酸铝铁与壳聚糖按适当比例混合之后得到性能稳定、储存性能好、使用方便等优点。目前制备复合絮凝剂使用的为铁盐、铝盐及聚合铝盐与高分子有机物复合成絮凝剂,增强混凝效果;或者用增加混凝剂投加量的方法来改善混凝效果不仅增加处理成本,也可能使出水中的金属离子浓度增加。纳米材料具有独特的纳米效应:小尺寸效应、界面效应、量子效应、宏观量子隧道效应,将其应用于环境领域的研究越水越多。氧化铁具有储量大,提取简单,治污设备简易,治理效果好,作为环保材料前景十分看好。阳离子聚电解质作为有机絮凝剂,与无机絮凝剂相比,它用量少,絮凝速度快,受共存盐类、pH值及温度影响小,生成污泥量少而易处理,对节约用水、废水处理和回用有重要作用。而强化混凝通过对药剂的匹配改善和混凝工艺的优化,增大絮体对水中超微颗粒的碰撞、吸附、和脱除作用,降低出水浊度,提高对有机物的去除率。这种不需大量资金投入便可解决水源水微污染问题的处理技术,可为保护人类饮水安全,解决水质型缺水问题,促进社会经济的进步发挥作用。In the face of changes in water quality and the improvement of water quality requirements, the conventional coagulation process can no longer meet the requirements. Experimental research and actual production results at home and abroad show that conventional coagulation, sedimentation and filtration can only remove 20% to 30% of organic matter in water, and due to the presence of dissolved organic matter, it is not conducive to destroying the stability of the colloid and the turbidity removal effect is significantly reduced. , Therefore, more and more attention is paid to the research on composite flocculants, as patent CN1821114A discloses a kind of preparation method of composite flocculants such as aluminum sulfate, slaked lime; Formaldehyde polymer, polyaluminum sulfide and/or polysulfide aluminum calcium to make an organic-inorganic composite flocculant; patent CN101327977A composites aluminum salt, iron salt, polyacrylamide and starch into double-layer or Multi-layer flocculant, the multi-layer slow-release structure increases the efficiency of the agent and improves the efficacy of the agent; patent CN101717144A mixes polyaluminum iron silicate and chitosan in an appropriate proportion to obtain stable performance, good storage performance, Easy to use and other advantages. At present, the preparation of composite flocculants is made of iron salts, aluminum salts and polyaluminum salts combined with high-molecular organic matter to form flocculants to enhance the coagulation effect; or to improve the coagulation effect by increasing the dosage of coagulants. cost, and may also increase the concentration of metal ions in the effluent. Nanomaterials have unique nanoeffects: small size effect, interface effect, quantum effect, and macroscopic quantum tunneling effect. There are more and more researches on its application in the field of environment. Iron oxide has large reserves, simple extraction, simple pollution control equipment, and good treatment effect. It has a very promising prospect as an environmental protection material. Cationic polyelectrolyte is used as an organic flocculant. Compared with inorganic flocculants, it has less dosage and faster flocculation speed. It is less affected by coexisting salts, pH value and temperature. It generates less sludge and is easy to handle. Disposal and reuse play an important role. The enhanced coagulation improves the matching of chemicals and optimizes the coagulation process to increase the impact, adsorption, and removal of ultrafine particles in the water by flocs, reduce the turbidity of the effluent, and increase the removal rate of organic matter. This kind of treatment technology that can solve the problem of micro-pollution of water source water without a large amount of capital investment can play a role in protecting human drinking water safety, solving water quality-related water shortage problems, and promoting social and economic progress.
发明内容Contents of the invention
本发明的目的是通过纳米氧化铁-阳离子聚电解质耦合形成的多元复合絮凝剂,纳米氧化铁具有专属吸附作用,但由于纳米材料独特的效应,在水中不易分散,会团聚成大颗粒,形成稳定的胶体,使絮凝作用受影响。将纳米氧化铁与阳离子聚电解质耦合,利用阳离子聚电解质使纳米颗粒能更好的分散,同时发挥阳离子聚电解质的“聚电络合效应”,形成易于沉降的絮体,同时能对水中有机质、重金属和有毒污染物很好的去除。本发明的制备方法,具体说明如下:The purpose of the present invention is to form a multi-component composite flocculant through the coupling of nano-iron oxide-cationic polyelectrolyte. Nano-iron oxide has exclusive adsorption, but due to the unique effect of nano-materials, it is not easy to disperse in water, and will agglomerate into large particles, forming a stable Colloids affect flocculation. Coupling nano-iron oxide with cationic polyelectrolyte, using cationic polyelectrolyte to better disperse nanoparticles, and at the same time exerting the "polyelectric complexation effect" of cationic polyelectrolyte to form flocs that are easy to settle, and at the same time can remove organic matter, Very good removal of heavy metals and toxic pollutants. The preparation method of the present invention is specifically described as follows:
1、一种高效的纳米材料-阳离子聚电解质耦合多元复合絮凝剂,以纳米氧化铁和阳离子聚电解质耦合而成多元复合絮凝剂按重量百分比进行制备,纳米氧化铁:5-60%、聚合有机物:0.1-2%,余量为水。1. An efficient nano-material-cation polyelectrolyte coupled multi-element composite flocculant, which is prepared by coupling nano-iron oxide and cationic poly-electrolyte. The multi-element composite flocculant is prepared by weight percentage, nano-iron oxide: 5-60%, polymerized organic matter : 0.1-2%, the balance is water.
2、所述的一种高效的纳米材料-阳离子聚电解质耦合多元复合絮凝剂,其特征是:在纳米氧化铁如纳米α-FeOOH、Fe3O4、α-Fe2O3、γ-Fe2O3等制备过程中加入阳离子聚电解质,反应完毕后经洗涤、精制等工艺制得多元复合絮凝剂(或再经干燥、研磨等工艺制得多元复合絮凝剂干粉)。2. The high-efficiency nano-material-cation polyelectrolyte coupled multi-element composite flocculant is characterized in that: in nano iron oxide such as nano α-FeOOH, Fe 3 O 4 , α-Fe 2 O 3 , γ-Fe Cationic polyelectrolyte is added in the preparation process of 2 O 3 etc. After the reaction is completed, the multi-component composite flocculant is obtained through washing and refining processes (or the multi-component composite flocculant dry powder is obtained through drying and grinding processes).
3、所述的一种高效的纳米材料-阳离子聚电解质耦合多元复合絮凝剂,其特征是:水处理絮凝过程为将纳米氧化铁与阳离子聚电解质分别加入,纳米氧化铁加入后,进行混凝搅拌,混凝条件为:快搅:100-1000r/min,0.5-30min。慢搅:20-120r/min,5-60min。快搅0.2-10min后加入阳离子聚电解质,混凝温度:4-60℃。3. The high-efficiency nano-material-cation polyelectrolyte coupling multi-element composite flocculant is characterized in that: the water treatment flocculation process is to add nano-iron oxide and cationic polyelectrolyte respectively, and coagulate after adding nano-iron oxide Stirring and coagulation conditions: fast stirring: 100-1000r/min, 0.5-30min. Slow stirring: 20-120r/min, 5-60min. After stirring quickly for 0.2-10min, add cationic polyelectrolyte, coagulation temperature: 4-60℃.
4、所述的一种高效的纳米材料-阳离子聚电解质耦合多元复合絮凝剂,其特征是:纳米氧化铁:α-FeOOH、Fe3O4、α-Fe2O3、γ-Fe2O3等;阳离子聚电解质:聚胺、聚丙烯酰胺、聚二甲基二烯丙基氯化铵、壳聚糖等。4. The high-efficiency nano-material-cation polyelectrolyte coupled multi-element composite flocculant is characterized by: nano-iron oxide: α-FeOOH, Fe 3 O 4 , α-Fe 2 O 3 , γ-Fe 2 O 3 , etc.; cationic polyelectrolyte: polyamine, polyacrylamide, polydimethyldiallylammonium chloride, chitosan, etc.
本发明制备的纳米氧化铁-阳离子聚电解质耦合多元复合絮凝剂的特点是:The characteristics of the nano-iron oxide-cation polyelectrolyte coupled multi-element composite flocculant prepared by the present invention are:
1、采用的原材料方便易得,无任何有机化合物,在常温常压下进行制备,可以降低生产成本且绿色环保。1. The raw materials used are convenient and easy to obtain, without any organic compound, and the preparation is carried out under normal temperature and pressure, which can reduce production costs and is environmentally friendly.
2、该新型高效复合絮凝剂对水中的有机物质、浊度、色度的去除受水质pH影响较小,相对于传统絮凝剂和聚铁更具有优势。2. The removal of organic matter, turbidity, and chromaticity in water by this new type of high-efficiency composite flocculant is less affected by the pH of the water quality, and it has more advantages than traditional flocculants and polyferrons.
3、该新型高效复合絮凝剂,适用于微污染水源强化处理,对有毒有害污染物(重金属、毒害有机物等),腐殖酸,色度具有较高的处理效果,且具有分离效果好、沉降快、出水浊度小、pH适用范围广等优点。3. This new type of high-efficiency composite flocculant is suitable for intensive treatment of micro-polluted water sources. It has a high treatment effect on toxic and harmful pollutants (heavy metals, toxic organic substances, etc.), humic acid, and chroma, and has good separation effect and settlement Fast, low water turbidity, wide pH range and other advantages.
4、工艺操作简单可进行工业化的应用。4. The process operation is simple and can be applied industrially.
具体实施方式Detailed ways
下面给出本发明的几个具体实施例,以对本发明进行更加详细的说明Provide several specific embodiments of the present invention below, to describe the present invention in more detail
实施例1Example 1
将侧田水库原水水样1000mL加入到一系列250mL烧杯中,分别加入50mg/L、100mg/L、200mg/L、300mg/L、400mg/L、600mg/L纳米Fe3O4絮凝剂进行混凝搅拌,快搅1分钟后加入1mg/LPDADMAC,取混凝搅拌后,静置沉降后的上清液,过0.45μm的滤膜于50mL离心管中,腐殖酸的去除用TOC仪测定其总有机碳含量表示,并测定处理前后水浊度、色度的变化,结果表明:腐殖酸的去除率:49%;浊度去除率:77%;色度去除率:88%。Add 1000mL of raw water samples from the Jiantian Reservoir into a series of 250mL beakers, add 50mg/L, 100mg/L, 200mg/L, 300mg/L, 400mg/L, 600mg/L nano-Fe 3 O 4 flocculants for mixing Coagulate and stir, add 1mg/LPDADMAC after fast stirring for 1 minute, take the supernatant after coagulation and stirring, let it settle down, pass through a 0.45μm filter membrane in a 50mL centrifuge tube, and measure the removal of humic acid with a TOC instrument The total organic carbon content is expressed, and the changes of water turbidity and color before and after treatment are measured. The results show that the removal rate of humic acid is 49%, the removal rate of turbidity is 77%, and the removal rate of color is 88%.
实施例2Example 2
在1000mL烧杯中,将浓度分别为50mg/L、100mg/L、200mg/L、300mg/L、400mg/L、600mg/L纳米α-FeOOH絮凝剂于一系列1000mL烧杯中,将事先调节好的pH值分别为5、6、7、8,初始浓度为10mg/L的腐殖酸溶液1000mL加入到烧杯中,进行混凝搅拌,快搅1分钟后加入5mL浓度为400mg/LPDADMAC溶液。混凝温度为25℃。取静置沉降后的溶液上清液,过0.45um滤膜过滤到50mL样品管中,腐殖酸的去除用TOC仪测定其总有机碳含量表示,并测定处理前后水浊度、色度的变化,结果表明:投加阳离子后结果表明在不同的pH值条件下,对腐殖酸的去除率不断增加,在75%-95%;浊度去除率:60%-90%;色度去除率:80%-95%。In a 1000mL beaker, put the concentration of 50mg/L, 100mg/L, 200mg/L, 300mg/L, 400mg/L, 600mg/L nanometer α-FeOOH flocculant in a series of 1000mL beakers, the pre-adjusted The pH values were 5, 6, 7, 8 respectively, and 1000mL of humic acid solution with an initial concentration of 10mg/L was added to the beaker for coagulation and stirring. After stirring for 1 minute, 5mL of 400mg/LPDADMAC solution was added. The coagulation temperature is 25°C. Take the solution supernatant after standing and settling, and filter it into a 50mL sample tube through a 0.45um filter membrane. The removal of humic acid is indicated by measuring its total organic carbon content with a TOC instrument, and measuring the water turbidity and chromaticity before and after treatment. Changes, the results show that: after adding cations, the results show that under different pH conditions, the removal rate of humic acid continues to increase, at 75%-95%; turbidity removal rate: 60%-90%; chromaticity removal Rate: 80%-95%.
实施例3Example 3
称取纳米α-FeOOH与PDADMAC的复合絮凝剂样品分别为5.0、10.0、15.0、20.0、30.0和50mg/L,PFOS初始浓度为2mg/L,pH值为3.0,在25℃的恒温条件下振荡,取上清液,测定PFOS的浓度,结果表明,去除率:70%-93%。The composite flocculant samples of nano-α-FeOOH and PDADMAC were weighed to be 5.0, 10.0, 15.0, 20.0, 30.0 and 50 mg/L respectively, the initial concentration of PFOS was 2 mg/L, and the pH value was 3.0. Shake at a constant temperature of 25 °C , take the supernatant, measure the concentration of PFOS, the results show that the removal rate: 70%-93%.
实施例4Example 4
取400mL水样加入到一系列500mL烧杯中,分别投加质量浓度为50、100、200、300、400和600mg/L的α-FeOOH与PDADMAC的复合絮凝剂样品进行混凝搅拌,混凝温度为25℃,混凝搅拌后取静置沉降后的溶液的上清液,测定水中Mn2+变化,结果表明,Mn2+去除率:65%-83%。Take 400mL water samples and add them to a series of 500mL beakers, and add α-FeOOH and PDADMAC composite flocculant samples with mass concentrations of 50, 100, 200, 300, 400 and 600mg/L respectively for coagulation and stirring. After coagulation and stirring, take the supernatant of the solution after standing and settling, and measure the change of Mn 2+ in the water. The results show that the removal rate of Mn 2+ is 65%-83%.
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