CN118307112B - Sewage treatment flocculant and preparation method thereof - Google Patents
Sewage treatment flocculant and preparation method thereof Download PDFInfo
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- 239000010865 sewage Substances 0.000 title claims abstract description 25
- 238000002360 preparation method Methods 0.000 title claims abstract description 9
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims abstract description 67
- 238000003756 stirring Methods 0.000 claims abstract description 42
- 229920001577 copolymer Polymers 0.000 claims abstract description 25
- 239000000440 bentonite Substances 0.000 claims abstract description 23
- 229910000278 bentonite Inorganic materials 0.000 claims abstract description 23
- 229920001661 Chitosan Polymers 0.000 claims abstract description 17
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 63
- 239000002904 solvent Substances 0.000 claims description 35
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims description 28
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 27
- 238000006243 chemical reaction Methods 0.000 claims description 26
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 21
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 21
- -1 bentonite modified phenolic resin Chemical class 0.000 claims description 17
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 14
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 14
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims description 14
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 14
- MXMOTZIXVICDSD-UHFFFAOYSA-N anisoyl chloride Chemical compound COC1=CC=C(C(Cl)=O)C=C1 MXMOTZIXVICDSD-UHFFFAOYSA-N 0.000 claims description 14
- ILAHWRKJUDSMFH-UHFFFAOYSA-N boron tribromide Chemical compound BrB(Br)Br ILAHWRKJUDSMFH-UHFFFAOYSA-N 0.000 claims description 14
- 239000003054 catalyst Substances 0.000 claims description 14
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims description 14
- 238000001914 filtration Methods 0.000 claims description 9
- 239000003999 initiator Substances 0.000 claims description 9
- 238000010992 reflux Methods 0.000 claims description 9
- 238000005406 washing Methods 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 8
- 230000018044 dehydration Effects 0.000 claims description 7
- 238000006297 dehydration reaction Methods 0.000 claims description 7
- 239000005457 ice water Substances 0.000 claims description 7
- 238000006116 polymerization reaction Methods 0.000 claims description 7
- TZYULTYGSBAILI-UHFFFAOYSA-M trimethyl(prop-2-enyl)azanium;chloride Chemical compound [Cl-].C[N+](C)(C)CC=C TZYULTYGSBAILI-UHFFFAOYSA-M 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 2
- JHUUPUMBZGWODW-UHFFFAOYSA-N 3,6-dihydro-1,2-dioxine Chemical compound C1OOCC=C1 JHUUPUMBZGWODW-UHFFFAOYSA-N 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 239000002244 precipitate Substances 0.000 claims 1
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical class [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 abstract description 22
- 150000002500 ions Chemical class 0.000 abstract description 14
- 230000000694 effects Effects 0.000 abstract description 10
- 239000002351 wastewater Substances 0.000 abstract description 10
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 9
- 238000001179 sorption measurement Methods 0.000 abstract description 9
- 238000005189 flocculation Methods 0.000 abstract description 8
- 230000016615 flocculation Effects 0.000 abstract description 7
- 229910001430 chromium ion Inorganic materials 0.000 abstract description 5
- 125000000542 sulfonic acid group Chemical group 0.000 abstract description 4
- 150000001768 cations Chemical class 0.000 abstract description 2
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052901 montmorillonite Inorganic materials 0.000 abstract description 2
- 238000001556 precipitation Methods 0.000 abstract description 2
- 150000003242 quaternary ammonium salts Chemical group 0.000 abstract description 2
- 125000004434 sulfur atom Chemical group 0.000 abstract description 2
- 238000006386 neutralization reaction Methods 0.000 abstract 1
- 239000008394 flocculating agent Substances 0.000 description 11
- 239000000203 mixture Substances 0.000 description 8
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 6
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 6
- 239000012141 concentrate Substances 0.000 description 6
- 229910052708 sodium Inorganic materials 0.000 description 6
- 239000011734 sodium Substances 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- 125000003277 amino group Chemical group 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000005011 phenolic resin Substances 0.000 description 2
- 229920001568 phenolic resin Polymers 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 238000005292 vacuum distillation Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008827 biological function Effects 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 229920000592 inorganic polymer Polymers 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 229920005613 synthetic organic polymer Polymers 0.000 description 1
- FAGUFWYHJQFNRV-UHFFFAOYSA-N tetraethylenepentamine Chemical compound NCCNCCNCCNCCN FAGUFWYHJQFNRV-UHFFFAOYSA-N 0.000 description 1
- BPSIOYPQMFLKFR-UHFFFAOYSA-N trimethoxy-[3-(oxiran-2-ylmethoxy)propyl]silane Chemical compound CO[Si](OC)(OC)CCCOCC1CO1 BPSIOYPQMFLKFR-UHFFFAOYSA-N 0.000 description 1
- 238000001132 ultrasonic dispersion Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/285—Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5263—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using natural chemical compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/22—Chromium or chromium compounds, e.g. chromates
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
本发明涉及污水处理技术领域,且公开了一种污水处理絮凝剂及其制备方法,本发明通过将磺酸‑季铵盐共聚物、膨润土改性酚醛树脂、壳聚糖加入到搅拌器中,搅拌,结束后得到污水处理絮凝剂;其中膨润土改性酚醛树脂中的膨润土具有较大的比表面积和良好的吸附能力,其中的蒙脱石层间的阳离子能够很好的和废水中的铬离子、铅离子发生交换,进行吸附达到絮凝的效果;磺酸‑季铵盐共聚物中的磺酸基中有电子云密度较高的硫原子,使其易和废水中的铬离子、铅离子发生络合,形成微小絮体与季铵盐基团电中和作用形成沉淀,有效去除重金属离子,达到絮凝的作用。The invention relates to the technical field of sewage treatment, and discloses a sewage treatment flocculant and a preparation method thereof. The invention comprises the following steps: adding a sulfonic acid-quaternary ammonium salt copolymer, a bentonite-modified phenolic resin and chitosan into a stirrer, stirring, and obtaining the sewage treatment flocculant after stirring. The bentonite in the bentonite-modified phenolic resin has a large specific surface area and good adsorption capacity, and cations between montmorillonite layers can be well exchanged with chromium ions and lead ions in wastewater to achieve the effect of flocculation through adsorption. The sulfonic acid groups in the sulfonic acid-quaternary ammonium salt copolymer contain sulfur atoms with high electron cloud density, so that the sulfonic acid groups are easily complexed with chromium ions and lead ions in wastewater to form micro-flocculations and form precipitation through electrical neutralization with quaternary ammonium salt groups, thereby effectively removing heavy metal ions and achieving the effect of flocculation.
Description
技术领域Technical Field
本发明涉及污水处理技术领域,具体为一种污水处理絮凝剂及其制备方法。The invention relates to the technical field of sewage treatment, in particular to a sewage treatment flocculant and a preparation method thereof.
背景技术Background Art
絮凝剂可以分为无机絮凝剂和有机絮凝剂两类。其中无机絮凝剂又包括无机凝聚剂和无机高分子絮凝剂;有机絮凝剂又包括合成有机高分子絮凝剂、天然有机高分子絮凝剂和微生物絮凝剂,絮凝剂广泛应用于污水处理领域。随着工业化的发展,各种生活和工业污水越来越多,排入到环境中最终会危害到身体健康,因此如何避免这一现象,是解决问题的关键。Flocculants can be divided into two categories: inorganic flocculants and organic flocculants. Inorganic flocculants include inorganic coagulants and inorganic polymer flocculants; organic flocculants include synthetic organic polymer flocculants, natural organic polymer flocculants and microbial flocculants. Flocculants are widely used in sewage treatment. With the development of industrialization, various domestic and industrial sewage are increasing, and discharge into the environment will eventually endanger human health. Therefore, how to avoid this phenomenon is the key to solving the problem.
壳聚糖是一天然碱性多糖物质,具有优异的生物学功能和化学修饰反应的活性,广泛应用于多个领域,在絮凝剂方面,壳聚糖被用作阳离子絮凝剂,主要用于去除悬浮颗粒、提高液体产品的回收,本发明将其和磺酸-季铵盐共聚物、膨润土改性酚醛树脂进行复配,制备出一种高效处理水中重金属离子的絮凝剂。Chitosan is a natural alkaline polysaccharide substance with excellent biological functions and chemical modification reaction activity. It is widely used in many fields. In terms of flocculants, chitosan is used as a cationic flocculant, mainly used to remove suspended particles and improve the recovery of liquid products. The present invention compounded chitosan with sulfonic acid-quaternary ammonium salt copolymer and bentonite-modified phenolic resin to prepare a flocculant that can efficiently treat heavy metal ions in water.
发明内容Summary of the invention
(一)解决的技术问题1. Technical issues to be resolved
针对现有技术的不足,本发明提供了一种污水处理絮凝剂及其制备方法,解决了水中重金属离子污染的问题。In view of the deficiencies of the prior art, the present invention provides a sewage treatment flocculant and a preparation method thereof, which solves the problem of heavy metal ion pollution in water.
(二)技术方案(II) Technical solution
为实现上述目的,本发明提供以下技术方案:一种污水处理絮凝剂,包括以下重量组分:4-10重量份的磺酸-季铵盐共聚物、8-12重量份的膨润土改性酚醛树脂、15-25重量份的壳聚糖;To achieve the above object, the present invention provides the following technical solution: a sewage treatment flocculant, comprising the following weight components: 4-10 weight parts of sulfonic acid-quaternary ammonium salt copolymer, 8-12 weight parts of bentonite-modified phenolic resin, and 15-25 weight parts of chitosan;
所述磺酸-季铵盐共聚物的制备方法为:The preparation method of the sulfonic acid-quaternary ammonium salt copolymer is:
S1.向N,N-二甲基甲酰胺溶剂中加入5-8重量份的羟基化膨润土、2-5重量份的2-氯-4,6-双烯丙基三嗪,搅拌混合,在90-110℃下反应10-15h,结束后减压蒸馏,过滤并干燥,得到烯基化膨润土;S1. Add 5-8 parts by weight of hydroxylated bentonite and 2-5 parts by weight of 2-chloro-4,6-diallyl triazine to N,N-dimethylformamide solvent, stir and mix, react at 90-110 ° C for 10-15h, and then distill under reduced pressure, filter and dry to obtain olefinated bentonite;
S2.将4-7重量份的烯丙基三甲基氯化铵、3-6重量份的2-丙烯酰胺-2-甲基丙磺酸钠进行溶解、5-10重量份的烯基化膨润土加入到N,N-二甲基甲酰胺溶剂中,进行溶解,然后再加入0.5-1重量份的引发剂,进行聚合反应,在90-120℃下反应10-15h,得到磺酸-季铵盐共聚物。S2. Dissolve 4-7 parts by weight of allyltrimethylammonium chloride and 3-6 parts by weight of sodium 2-acrylamide-2-methylpropane sulfonate, add 5-10 parts by weight of olefinated bentonite into N,N-dimethylformamide solvent, dissolve them, then add 0.5-1 parts by weight of initiator, carry out polymerization reaction, react at 90-120°C for 10-15h, and obtain sulfonic acid-quaternary ammonium salt copolymer.
优选的,所述膨润土改性酚醛树脂的制备方法为:Preferably, the preparation method of the bentonite-modified phenolic resin is:
(1)将8-12重量份的γ-缩水甘油醚氧丙基三甲氧基硅烷改性膨润土加入到质量分数为2-3%的硫酸溶液中,在50-75℃下搅拌反应15-22h,结束后,过滤,洗涤并干燥,得到羟基化膨润土;(1) adding 8-12 parts by weight of γ-glycidyloxypropyltrimethoxysilane modified bentonite to a 2-3% by mass sulfuric acid solution, stirring and reacting at 50-75° C. for 15-22 hours, filtering, washing and drying after the reaction, to obtain hydroxylated bentonite;
(2)将羟基化膨润土加入到1,4-二氧六环溶剂中,搅拌均匀,然后继续加入对甲氧基苯甲酰氯和吡啶催化剂,在30-40℃下反应8-15h,反应后浓缩溶剂,丙酮洗涤,得到中间体;(2) Add hydroxylated bentonite to 1,4-dioxane solvent, stir evenly, then continue to add p-methoxybenzoyl chloride and pyridine catalyst, react at 30-40°C for 8-15h, concentrate the solvent after the reaction, wash with acetone, and obtain an intermediate;
(3)向N,N-二甲基甲酰胺溶剂中加入5-10重量份的中间体,搅拌,然后滴加1-2重量份的三溴化硼,在-15℃至-10℃下反应15-20h,然后继续加入甲醇终止反应,将溶液倒入冰水中析出沉淀,过滤并洗涤,乙酸乙酯重结晶,得到苯酚改性膨润土;(3) Add 5-10 parts by weight of the intermediate to N,N-dimethylformamide solvent, stir, then dropwise add 1-2 parts by weight of boron tribromide, react at -15°C to -10°C for 15-20 hours, then continue to add methanol to terminate the reaction, pour the solution into ice water to precipitate, filter and wash, and recrystallize from ethyl acetate to obtain phenol-modified bentonite;
(4)将苯酚改性膨润土、甲醛加入到搅拌器中,在70-90℃下反应45-55min,然后再滴加乙二胺,升温至95-100℃,回流脱水,冷却至室温,得到膨润土改性酚醛树脂。(4) Add phenol-modified bentonite and formaldehyde into a stirrer, react at 70-90°C for 45-55 minutes, then add ethylenediamine dropwise, raise the temperature to 95-100°C, reflux for dehydration, and cool to room temperature to obtain bentonite-modified phenolic resin.
优选的,所述(2)中羟基化膨润土、对甲氧基苯甲酰氯、吡啶催化剂的质量比为1.1-1.3:1:0.01-0.03。Preferably, the mass ratio of hydroxylated bentonite, p-methoxybenzoyl chloride and pyridine catalyst in (2) is 1.1-1.3:1:0.01-0.03.
优选的,所述(3)中搅拌时间为10-20min。Preferably, the stirring time in (3) is 10-20 min.
优选的,所述(4)中苯酚改性膨润土、甲醛、乙二胺的质量比为1:1.1-1.2:0.4-0.8。Preferably, the mass ratio of phenol-modified bentonite, formaldehyde and ethylenediamine in (4) is 1:1.1-1.2:0.4-0.8.
优选的,所述S2中引发剂为偶氮二异丁腈。Preferably, the initiator in S2 is azobisisobutyronitrile.
优选的,所述污水处理絮凝剂的制备方法为:将磺酸-季铵盐共聚物、膨润土改性酚醛树脂、壳聚糖加入到搅拌器中,搅拌20-30min,结束后得到污水处理絮凝剂。Preferably, the preparation method of the sewage treatment flocculant is: adding sulfonic acid-quaternary ammonium salt copolymer, bentonite-modified phenolic resin and chitosan into a stirrer, stirring for 20-30 minutes, and obtaining the sewage treatment flocculant after stirring.
(三)有益的技术效果3. Beneficial technical effects
本发明通过将磺酸-季铵盐共聚物、膨润土改性酚醛树脂、壳聚糖加入到搅拌器中,搅拌,结束后得到污水处理絮凝剂。The invention provides a sewage treatment flocculant by adding sulfonic acid-quaternary ammonium salt copolymer, bentonite modified phenolic resin and chitosan into a stirrer and stirring the mixture.
其中膨润土改性酚醛树脂中的膨润土具有较大的比表面积和良好的吸附能力,其中的蒙脱石层间的阳离子能够很好的和废水中的铬离子、铅离子发生交换,进行吸附达到絮凝的效果;酚醛树脂的酚羟基含量较高,亲水性强,对废水中的铬离子、铅离子具有较好的吸附效果,并且酚醛树脂中胺基的配位与氢键作用使其对重金属离子具有良好的吸附能,协效达到絮凝;磺酸-季铵盐共聚物中的磺酸基中有电子云密度较高的硫原子,使其易和废水中的铬离子、铅离子发生络合,形成微小絮体与季铵盐基团电中和作用形成沉淀,有效去除重金属离子,达到絮凝的作用;并且磺酸-季铵盐共聚物中的磺酸基和膨润土改性酚醛树脂中的酚羟基、氨基和壳聚糖中的氨基、羟基,形成氢键,构成了交联网,在废水中能更有效吸附重金属离子,达到絮凝的效果。The bentonite in the bentonite-modified phenolic resin has a large specific surface area and good adsorption capacity, and the cations between the montmorillonite layers can be well exchanged with the chromium ions and lead ions in the wastewater to achieve the effect of flocculation through adsorption; the phenolic resin has a high phenolic hydroxyl content and strong hydrophilicity, and has a good adsorption effect on the chromium ions and lead ions in the wastewater, and the coordination and hydrogen bonding of the amine groups in the phenolic resin make it have good adsorption energy for heavy metal ions, and synergistically achieve flocculation; the sulfonic acid group in the sulfonic acid-quaternary ammonium salt copolymer has a sulfur atom with a high electron cloud density, which makes it easy to complex with the chromium ions and lead ions in the wastewater to form tiny flocs, which are electrically neutralized with the quaternary ammonium salt group to form precipitation, effectively remove heavy metal ions, and achieve the effect of flocculation; and the sulfonic acid group in the sulfonic acid-quaternary ammonium salt copolymer, the phenolic hydroxyl group and the amino group in the bentonite-modified phenolic resin, and the amino group and the hydroxyl group in the chitosan form hydrogen bonds to form a cross-linked network, which can more effectively adsorb heavy metal ions in the wastewater to achieve the effect of flocculation.
具体实施方式DETAILED DESCRIPTION
γ-缩水甘油醚氧丙基三甲氧基硅烷改性膨润土参照文献《四乙烯五胺接枝膨润土对酸性大红GR的吸附性能》(《化工进展》,2021年第40卷第5期)进行制备:γ-Glycidyloxypropyltrimethoxysilane modified bentonite was prepared according to the literature "Adsorption performance of tetraethylenepentamine grafted bentonite on acid red GR" (Chemical Industry Progress, Vol. 40, No. 5, 2021):
向100 mL的7%的盐酸溶液中加入2g膨润土,在80℃中加热回流进行酸化,过滤,去离子水洗涤并干燥得到酸改性膨润土。将2g的酸改性膨润土分散到150mL的乙醇中,加入8g的γ-缩水甘油醚氧丙基三甲氧基硅烷,氮气气氛中90℃下,搅拌回流反应24h,过滤,乙醇洗涤并干燥,得到γ-缩水甘油醚氧丙基三甲氧基硅烷改性膨润土。Add 2 g of bentonite to 100 mL of 7% hydrochloric acid solution, heat and reflux at 80 ° C for acidification, filter, wash with deionized water and dry to obtain acid-modified bentonite. Disperse 2 g of acid-modified bentonite in 150 mL of ethanol, add 8 g of γ-glycidyloxypropyltrimethoxysilane, stir and reflux at 90 ° C in a nitrogen atmosphere for 24 hours, filter, wash with ethanol and dry to obtain γ-glycidyloxypropyltrimethoxysilane-modified bentonite.
实施例1Example 1
(1)将8重量份的γ-缩水甘油醚氧丙基三甲氧基硅烷改性膨润土加入到质量分数为2%的硫酸溶液中,在50℃下搅拌反应15h,结束后,过滤,洗涤并干燥,得到羟基化膨润土;(1) adding 8 parts by weight of γ-glycidyloxypropyltrimethoxysilane modified bentonite to a 2% sulfuric acid solution, stirring and reacting at 50° C. for 15 hours, filtering, washing and drying after the reaction, to obtain hydroxylated bentonite;
(2)将羟基化膨润土加入到1,4-二氧六环溶剂中,搅拌均匀,然后继续加入对甲氧基苯甲酰氯和吡啶催化剂,其中羟基化膨润土、对甲氧基苯甲酰氯、吡啶催化剂的质量比为1.1:1:0.01,在30℃下反应8h,反应后浓缩溶剂,丙酮洗涤,得到中间体;(2) Add hydroxylated bentonite to 1,4-dioxane solvent, stir evenly, then continue to add p-methoxybenzoyl chloride and pyridine catalyst, wherein the mass ratio of hydroxylated bentonite, p-methoxybenzoyl chloride and pyridine catalyst is 1.1:1:0.01, react at 30°C for 8h, concentrate the solvent after the reaction, wash with acetone, and obtain an intermediate;
(3)向N,N-二甲基甲酰胺溶剂中加入5重量份的中间体,搅拌10min,然后滴加1重量份的三溴化硼,在-15℃下反应15h,然后继续加入甲醇终止反应,将溶液倒入冰水中析出沉淀,过滤并洗涤,乙酸乙酯重结晶,得到苯酚改性膨润土;(3) Add 5 parts by weight of the intermediate to N,N-dimethylformamide solvent, stir for 10 minutes, then dropwise add 1 part by weight of boron tribromide, react at -15°C for 15 hours, then continue to add methanol to terminate the reaction, pour the solution into ice water to precipitate, filter and wash, and recrystallize from ethyl acetate to obtain phenol-modified bentonite;
(4)将苯酚改性膨润土、甲醛加入到搅拌器中,在70℃下反应45min,然后再滴加乙二胺,其中苯酚改性膨润土、甲醛、乙二胺的质量比为1:1.1:0.4,升温至95℃,回流脱水,冷却至室温,得到膨润土改性酚醛树脂;(4) adding phenol-modified bentonite and formaldehyde into a stirrer, reacting at 70° C. for 45 min, then adding ethylenediamine dropwise, wherein the mass ratio of phenol-modified bentonite, formaldehyde, and ethylenediamine is 1:1.1:0.4, heating to 95° C., reflux dehydration, and cooling to room temperature to obtain bentonite-modified phenolic resin;
(5)向N,N-二甲基甲酰胺溶剂中加入5重量份的羟基化膨润土、2重量份的2-氯-4,6-双烯丙基三嗪,搅拌混合,在90℃下反应10h,结束后减压蒸馏,过滤并干燥,得到烯基化膨润土;(5) Add 5 parts by weight of hydroxylated bentonite and 2 parts by weight of 2-chloro-4,6-diallyl triazine to N,N-dimethylformamide solvent, stir and mix, react at 90° C. for 10 h, and then distill under reduced pressure, filter and dry to obtain olefinated bentonite;
(6)将4重量份的烯丙基三甲基氯化铵、3重量份的2-丙烯酰胺-2-甲基丙磺酸钠进行溶解、5重量份的烯基化膨润土加入到N,N-二甲基甲酰胺溶剂中,进行溶解,然后再加入0.5重量份的偶氮二异丁腈引发剂,进行聚合反应,在90℃下反应10h,得到磺酸-季铵盐共聚物;(6) 4 parts by weight of allyltrimethylammonium chloride and 3 parts by weight of sodium 2-acrylamide-2-methylpropanesulfonate are dissolved, and 5 parts by weight of olefinated bentonite are added into N,N-dimethylformamide solvent to dissolve, and then 0.5 parts by weight of azobisisobutyronitrile initiator is added to carry out polymerization reaction, and the reaction is carried out at 90° C. for 10 hours to obtain a sulfonic acid-quaternary ammonium salt copolymer;
(7)将4重量份的磺酸-季铵盐共聚物、8重量份的膨润土改性酚醛树脂、15重量份的壳聚糖加入到搅拌器中,搅拌20min,结束后得到污水处理絮凝剂。(7) 4 parts by weight of sulfonic acid-quaternary ammonium salt copolymer, 8 parts by weight of bentonite-modified phenolic resin, and 15 parts by weight of chitosan were added into a stirrer and stirred for 20 minutes to obtain a wastewater treatment flocculant.
实施例2Example 2
(1)将12重量份的γ-缩水甘油醚氧丙基三甲氧基硅烷改性膨润土加入到质量分数为3%的硫酸溶液中,在75℃下搅拌反应22h,结束后,过滤,洗涤并干燥,得到羟基化膨润土;(1) adding 12 parts by weight of γ-glycidyloxypropyltrimethoxysilane modified bentonite to a 3% sulfuric acid solution, stirring and reacting at 75° C. for 22 hours, filtering, washing and drying after the reaction, to obtain hydroxylated bentonite;
(2)将羟基化膨润土加入到1,4-二氧六环溶剂中,搅拌均匀,然后继续加入对甲氧基苯甲酰氯和吡啶催化剂,其中羟基化膨润土、对甲氧基苯甲酰氯、吡啶催化剂的质量比为1.3:1:0.03,在40℃下反应15h,反应后浓缩溶剂,丙酮洗涤,得到中间体;(2) Add hydroxylated bentonite to 1,4-dioxane solvent, stir evenly, then continue to add p-methoxybenzoyl chloride and pyridine catalyst, wherein the mass ratio of hydroxylated bentonite, p-methoxybenzoyl chloride and pyridine catalyst is 1.3:1:0.03, react at 40°C for 15h, concentrate the solvent after the reaction, wash with acetone, and obtain an intermediate;
(3)向N,N-二甲基甲酰胺溶剂中加入10重量份的中间体,搅拌20min,然后滴加1-2重量份的三溴化硼,在-10℃下反应20h,然后继续加入甲醇终止反应,将溶液倒入冰水中析出沉淀,过滤并洗涤,乙酸乙酯重结晶,得到苯酚改性膨润土;(3) Add 10 parts by weight of the intermediate to N,N-dimethylformamide solvent, stir for 20 minutes, then dropwise add 1-2 parts by weight of boron tribromide, react at -10°C for 20 hours, then continue to add methanol to terminate the reaction, pour the solution into ice water to precipitate, filter and wash, and recrystallize from ethyl acetate to obtain phenol-modified bentonite;
(4)将苯酚改性膨润土、甲醛加入到搅拌器中,在90℃下反应55min,然后再滴加乙二胺,其中苯酚改性膨润土、甲醛、乙二胺的质量比为1:1.2:0.8,升温至100℃,回流脱水,冷却至室温,得到膨润土改性酚醛树脂;(4) adding phenol-modified bentonite and formaldehyde into a stirrer, reacting at 90° C. for 55 min, then adding ethylenediamine dropwise, wherein the mass ratio of phenol-modified bentonite, formaldehyde, and ethylenediamine is 1:1.2:0.8, heating to 100° C., reflux dehydration, and cooling to room temperature to obtain bentonite-modified phenolic resin;
(5)向N,N-二甲基甲酰胺溶剂中加入8重量份的羟基化膨润土、5重量份的2-氯-4,6-双烯丙基三嗪,搅拌混合,在110℃下反应15h,结束后减压蒸馏,过滤并干燥,得到烯基化膨润土;(5) Add 8 parts by weight of hydroxylated bentonite and 5 parts by weight of 2-chloro-4,6-diallyl triazine to N,N-dimethylformamide solvent, stir and mix, react at 110° C. for 15 h, and then distill under reduced pressure, filter and dry to obtain olefinated bentonite;
(6)将7重量份的烯丙基三甲基氯化铵、6重量份的2-丙烯酰胺-2-甲基丙磺酸钠进行溶解、10重量份的烯基化膨润土加入到N,N-二甲基甲酰胺溶剂中,进行溶解,然后再加入1重量份的偶氮二异丁腈引发剂,进行聚合反应,在120℃下反应15h,得到磺酸-季铵盐共聚物;(6) dissolving 7 parts by weight of allyltrimethylammonium chloride and 6 parts by weight of sodium 2-acrylamide-2-methylpropanesulfonate, adding 10 parts by weight of olefinated bentonite into N,N-dimethylformamide solvent, dissolving them, and then adding 1 part by weight of azobisisobutyronitrile initiator to carry out polymerization reaction at 120° C. for 15 hours to obtain a sulfonic acid-quaternary ammonium salt copolymer;
(7)将10重量份的磺酸-季铵盐共聚物、12重量份的膨润土改性酚醛树脂、25重量份的壳聚糖加入到搅拌器中,搅拌30min,结束后得到污水处理絮凝剂。(7) Add 10 parts by weight of sulfonic acid-quaternary ammonium salt copolymer, 12 parts by weight of bentonite-modified phenolic resin, and 25 parts by weight of chitosan into a stirrer and stir for 30 minutes to obtain a wastewater treatment flocculant.
实施例3Example 3
(1)将10重量份的γ-缩水甘油醚氧丙基三甲氧基硅烷改性膨润土加入到质量分数为2.5%的硫酸溶液中,在62.5℃下搅拌反应18.5h,结束后,过滤,洗涤并干燥,得到羟基化膨润土;(1) adding 10 parts by weight of γ-glycidyloxypropyltrimethoxysilane modified bentonite to a 2.5% sulfuric acid solution, stirring and reacting at 62.5° C. for 18.5 hours, filtering, washing and drying after the reaction, to obtain hydroxylated bentonite;
(2)将羟基化膨润土加入到1,4-二氧六环溶剂中,搅拌均匀,然后继续加入对甲氧基苯甲酰氯和吡啶催化剂,其中羟基化膨润土、对甲氧基苯甲酰氯、吡啶催化剂的质量比为1.2:1:0.02,在35℃下反应11.5h,反应后浓缩溶剂,丙酮洗涤,得到中间体;(2) Add hydroxylated bentonite to 1,4-dioxane solvent, stir evenly, then continue to add p-methoxybenzoyl chloride and pyridine catalyst, wherein the mass ratio of hydroxylated bentonite, p-methoxybenzoyl chloride and pyridine catalyst is 1.2:1:0.02, react at 35°C for 11.5h, concentrate the solvent after the reaction, wash with acetone, and obtain an intermediate;
(3)向N,N-二甲基甲酰胺溶剂中加入7.5重量份的中间体,搅拌15min,然后滴加1.5重量份的三溴化硼,在-12.5℃下反应17.5h,然后继续加入甲醇终止反应,将溶液倒入冰水中析出沉淀,过滤并洗涤,乙酸乙酯重结晶,得到苯酚改性膨润土;(3) Add 7.5 parts by weight of the intermediate to N,N-dimethylformamide solvent, stir for 15 minutes, then dropwise add 1.5 parts by weight of boron tribromide, react at -12.5°C for 17.5 hours, then continue to add methanol to terminate the reaction, pour the solution into ice water to precipitate, filter and wash, and recrystallize from ethyl acetate to obtain phenol-modified bentonite;
(4)将苯酚改性膨润土、甲醛加入到搅拌器中,在80℃下反应50min,然后再滴加乙二胺,其中苯酚改性膨润土、甲醛、乙二胺的质量比为1:1.15:0.6,升温至97.5℃,回流脱水,冷却至室温,得到膨润土改性酚醛树脂;(4) adding phenol-modified bentonite and formaldehyde into a stirrer, reacting at 80° C. for 50 min, then adding ethylenediamine dropwise, wherein the mass ratio of phenol-modified bentonite, formaldehyde, and ethylenediamine is 1:1.15:0.6, heating to 97.5° C., reflux dehydration, and cooling to room temperature to obtain bentonite-modified phenolic resin;
(5)向N,N-二甲基甲酰胺溶剂中加入6.5重量份的羟基化膨润土、3.5重量份的2-氯-4,6-双烯丙基三嗪,搅拌混合,在100℃下反应12.5h,结束后减压蒸馏,过滤并干燥,得到烯基化膨润土;(5) Add 6.5 parts by weight of hydroxylated bentonite and 3.5 parts by weight of 2-chloro-4,6-diallyl triazine to N,N-dimethylformamide solvent, stir and mix, react at 100° C. for 12.5 hours, and then perform vacuum distillation, filter and dry to obtain olefinated bentonite;
(6)将5.5重量份的烯丙基三甲基氯化铵、4.5重量份的2-丙烯酰胺-2-甲基丙磺酸钠进行溶解、7.5重量份的烯基化膨润土加入到N,N-二甲基甲酰胺溶剂中,进行溶解,然后再加入0.75重量份的偶氮二异丁腈引发剂,进行聚合反应,在105℃下反应12.5h,得到磺酸-季铵盐共聚物;(6) 5.5 parts by weight of allyltrimethylammonium chloride and 4.5 parts by weight of sodium 2-acrylamide-2-methylpropanesulfonate were dissolved, and 7.5 parts by weight of olefinated bentonite was added into N,N-dimethylformamide solvent to dissolve, and then 0.75 parts by weight of azobisisobutyronitrile initiator was added to carry out polymerization reaction, and the reaction was carried out at 105° C. for 12.5 hours to obtain a sulfonic acid-quaternary ammonium salt copolymer;
(7)将7重量份的磺酸-季铵盐共聚物、10重量份的膨润土改性酚醛树脂、20重量份的壳聚糖加入到搅拌器中,搅拌25min,结束后得到污水处理絮凝剂。(7) Add 7 parts by weight of sulfonic acid-quaternary ammonium salt copolymer, 10 parts by weight of bentonite-modified phenolic resin, and 20 parts by weight of chitosan into a stirrer and stir for 25 minutes to obtain a sewage treatment flocculant.
实施例4Example 4
(1)将8重量份的γ-缩水甘油醚氧丙基三甲氧基硅烷改性膨润土加入到质量分数为2%的硫酸溶液中,在50℃下搅拌反应15h,结束后,过滤,洗涤并干燥,得到羟基化膨润土;(1) adding 8 parts by weight of γ-glycidyloxypropyltrimethoxysilane modified bentonite to a 2% sulfuric acid solution, stirring and reacting at 50° C. for 15 hours, filtering, washing and drying after the reaction, to obtain hydroxylated bentonite;
(2)将羟基化膨润土加入到1,4-二氧六环溶剂中,搅拌均匀,然后继续加入对甲氧基苯甲酰氯和吡啶催化剂,其中羟基化膨润土、对甲氧基苯甲酰氯、吡啶催化剂的质量比为1.1:1:0.01,在30℃下反应8h,反应后浓缩溶剂,丙酮洗涤,得到中间体;(2) Add hydroxylated bentonite to 1,4-dioxane solvent, stir evenly, then continue to add p-methoxybenzoyl chloride and pyridine catalyst, wherein the mass ratio of hydroxylated bentonite, p-methoxybenzoyl chloride and pyridine catalyst is 1.1:1:0.01, react at 30°C for 8h, concentrate the solvent after the reaction, wash with acetone, and obtain an intermediate;
(3)向N,N-二甲基甲酰胺溶剂中加入5重量份的中间体,搅拌10min,然后滴加1重量份的三溴化硼,在-15℃下反应15h,然后继续加入甲醇终止反应,将溶液倒入冰水中析出沉淀,过滤并洗涤,乙酸乙酯重结晶,得到苯酚改性膨润土;(3) Add 5 parts by weight of the intermediate to N,N-dimethylformamide solvent, stir for 10 minutes, then dropwise add 1 part by weight of boron tribromide, react at -15°C for 15 hours, then continue to add methanol to terminate the reaction, pour the solution into ice water to precipitate, filter and wash, and recrystallize from ethyl acetate to obtain phenol-modified bentonite;
(4)将苯酚改性膨润土、甲醛加入到搅拌器中,在90℃下反应55min,然后再滴加乙二胺,其中苯酚改性膨润土、甲醛、乙二胺的质量比为1:1.2:0.8,升温至100℃,回流脱水,冷却至室温,得到膨润土改性酚醛树脂;(4) adding phenol-modified bentonite and formaldehyde into a stirrer, reacting at 90° C. for 55 min, then adding ethylenediamine dropwise, wherein the mass ratio of phenol-modified bentonite, formaldehyde, and ethylenediamine is 1:1.2:0.8, heating to 100° C., reflux dehydration, and cooling to room temperature to obtain bentonite-modified phenolic resin;
(5)向N,N-二甲基甲酰胺溶剂中加入8重量份的羟基化膨润土、5重量份的2-氯-4,6-双烯丙基三嗪,搅拌混合,在110℃下反应15h,结束后减压蒸馏,过滤并干燥,得到烯基化膨润土;(5) Add 8 parts by weight of hydroxylated bentonite and 5 parts by weight of 2-chloro-4,6-diallyl triazine to N,N-dimethylformamide solvent, stir and mix, react at 110° C. for 15 h, and then distill under reduced pressure, filter and dry to obtain olefinated bentonite;
(6)将5.5重量份的烯丙基三甲基氯化铵、4.5重量份的2-丙烯酰胺-2-甲基丙磺酸钠进行溶解、7.5重量份的烯基化膨润土加入到N,N-二甲基甲酰胺溶剂中,进行溶解,然后再加入0.75重量份的偶氮二异丁腈引发剂,进行聚合反应,在105℃下反应12.5h,得到磺酸-季铵盐共聚物;(6) 5.5 parts by weight of allyltrimethylammonium chloride and 4.5 parts by weight of sodium 2-acrylamide-2-methylpropanesulfonate were dissolved, and 7.5 parts by weight of olefinated bentonite was added into N,N-dimethylformamide solvent to dissolve, and then 0.75 parts by weight of azobisisobutyronitrile initiator was added to carry out polymerization reaction, and the reaction was carried out at 105° C. for 12.5 hours to obtain a sulfonic acid-quaternary ammonium salt copolymer;
(7)将7重量份的磺酸-季铵盐共聚物、10重量份的膨润土改性酚醛树脂、20重量份的壳聚糖加入到搅拌器中,搅拌25min,结束后得到污水处理絮凝剂。(7) Add 7 parts by weight of sulfonic acid-quaternary ammonium salt copolymer, 10 parts by weight of bentonite-modified phenolic resin, and 20 parts by weight of chitosan into a stirrer and stir for 25 minutes to obtain a sewage treatment flocculant.
实施例5Example 5
(1)将12重量份的γ-缩水甘油醚氧丙基三甲氧基硅烷改性膨润土加入到质量分数为3%的硫酸溶液中,在75℃下搅拌反应22h,结束后,过滤,洗涤并干燥,得到羟基化膨润土;(1) adding 12 parts by weight of γ-glycidyloxypropyltrimethoxysilane modified bentonite to a 3% sulfuric acid solution, stirring and reacting at 75° C. for 22 hours, filtering, washing and drying after the reaction, to obtain hydroxylated bentonite;
(2)将羟基化膨润土加入到1,4-二氧六环溶剂中,搅拌均匀,然后继续加入对甲氧基苯甲酰氯和吡啶催化剂,其中羟基化膨润土、对甲氧基苯甲酰氯、吡啶催化剂的质量比为1.3:1:0.03,在40℃下反应15h,反应后浓缩溶剂,丙酮洗涤,得到中间体;(2) Add hydroxylated bentonite to 1,4-dioxane solvent, stir evenly, then continue to add p-methoxybenzoyl chloride and pyridine catalyst, wherein the mass ratio of hydroxylated bentonite, p-methoxybenzoyl chloride and pyridine catalyst is 1.3:1:0.03, react at 40°C for 15h, concentrate the solvent after the reaction, wash with acetone, and obtain an intermediate;
(3)向N,N-二甲基甲酰胺溶剂中加入10重量份的中间体,搅拌20min,然后滴加1-2重量份的三溴化硼,在-10℃下反应20h,然后继续加入甲醇终止反应,将溶液倒入冰水中析出沉淀,过滤并洗涤,乙酸乙酯重结晶,得到苯酚改性膨润土;(3) Add 10 parts by weight of the intermediate to N,N-dimethylformamide solvent, stir for 20 minutes, then dropwise add 1-2 parts by weight of boron tribromide, react at -10°C for 20 hours, then continue to add methanol to terminate the reaction, pour the solution into ice water to precipitate, filter and wash, and recrystallize from ethyl acetate to obtain phenol-modified bentonite;
(4)将苯酚改性膨润土、甲醛加入到搅拌器中,在80℃下反应50min,然后再滴加乙二胺,其中苯酚改性膨润土、甲醛、乙二胺的质量比为1:1.15:0.6,升温至97.5℃,回流脱水,冷却至室温,得到膨润土改性酚醛树脂;(4) adding phenol-modified bentonite and formaldehyde into a stirrer, reacting at 80° C. for 50 min, then adding ethylenediamine dropwise, wherein the mass ratio of phenol-modified bentonite, formaldehyde, and ethylenediamine is 1:1.15:0.6, heating to 97.5° C., reflux dehydration, and cooling to room temperature to obtain bentonite-modified phenolic resin;
(5)向N,N-二甲基甲酰胺溶剂中加入6.5重量份的羟基化膨润土、3.5重量份的2-氯-4,6-双烯丙基三嗪,搅拌混合,在100℃下反应12.5h,结束后减压蒸馏,过滤并干燥,得到烯基化膨润土;(5) Add 6.5 parts by weight of hydroxylated bentonite and 3.5 parts by weight of 2-chloro-4,6-diallyl triazine to N,N-dimethylformamide solvent, stir and mix, react at 100° C. for 12.5 hours, and then perform vacuum distillation, filter and dry to obtain olefinated bentonite;
(6)将4重量份的烯丙基三甲基氯化铵、3重量份的2-丙烯酰胺-2-甲基丙磺酸钠进行溶解、5重量份的烯基化膨润土加入到N,N-二甲基甲酰胺溶剂中,进行溶解,然后再加入0.5重量份的偶氮二异丁腈引发剂,进行聚合反应,在90℃下反应10h,得到磺酸-季铵盐共聚物;(6) 4 parts by weight of allyltrimethylammonium chloride and 3 parts by weight of sodium 2-acrylamide-2-methylpropanesulfonate are dissolved, and 5 parts by weight of olefinated bentonite are added into N,N-dimethylformamide solvent to dissolve, and then 0.5 parts by weight of azobisisobutyronitrile initiator is added to carry out polymerization reaction, and the reaction is carried out at 90° C. for 10 hours to obtain a sulfonic acid-quaternary ammonium salt copolymer;
(7)将4重量份的磺酸-季铵盐共聚物、8重量份的膨润土改性酚醛树脂、15重量份的壳聚糖加入到搅拌器中,搅拌20min,结束后得到污水处理絮凝剂。(7) 4 parts by weight of sulfonic acid-quaternary ammonium salt copolymer, 8 parts by weight of bentonite-modified phenolic resin, and 15 parts by weight of chitosan were added into a stirrer and stirred for 20 minutes to obtain a wastewater treatment flocculant.
对比例1Comparative Example 1
将8重量份的膨润土改性酚醛树脂、15重量份的壳聚糖加入到搅拌器中,搅拌20min,结束后得到污水处理絮凝剂。8 parts by weight of bentonite-modified phenolic resin and 15 parts by weight of chitosan were added into a stirrer and stirred for 20 minutes to obtain a sewage treatment flocculant.
对比例2Comparative Example 2
将4重量份的磺酸-季铵盐共聚物、15重量份的壳聚糖加入到搅拌器中,搅拌20min,结束后得到污水处理絮凝剂。4 parts by weight of sulfonic acid-quaternary ammonium salt copolymer and 15 parts by weight of chitosan were added into a stirrer and stirred for 20 minutes. After stirring, a sewage treatment flocculant was obtained.
取200mL废水至烧杯中,废水中Cd2+、和Pb2+的初始浓度均为100mg/L,向废水中加入废水吸附剂,超声分散5min后置于摇床震荡12h后,取上清液,用ICP测定上清液中Cd2+和Pb2+的吸附后浓度,重金属离子的去除率w=(初始浓度-吸附后浓度)/初始浓度,检测结果如表1所示。200 mL of wastewater was taken into a beaker. The initial concentrations of Cd 2+ and Pb 2+ in the wastewater were both 100 mg/L. Wastewater adsorbent was added to the wastewater. After ultrasonic dispersion for 5 minutes, the mixture was placed on a shaker for 12 hours. The supernatant was taken and the post-adsorption concentrations of Cd 2+ and Pb 2+ in the supernatant were determined by ICP. The removal rate of heavy metal ions w = (initial concentration - post-adsorption concentration) / initial concentration. The test results are shown in Table 1.
表1:重金属离子去除率测试。Table 1: Heavy metal ion removal rate test.
由表1可知,本发明实施例1-5相较于对比例1-2对重金属离子具有较好的去除效果,说明絮凝效果较好。It can be seen from Table 1 that Examples 1-5 of the present invention have better removal effects on heavy metal ions than Comparative Examples 1-2, indicating that the flocculation effect is better.
以上公开的本发明优选实施例只是用于帮助阐述本发明。优选实施例并没有详尽叙述所有的细节,也不限制该发明仅为所述的具体实施方式。显然,根据本说明书的内容,可作很多的修改和变化。本说明书选取并具体描述这些实施例,是为了更好地解释本发明的原理和实际应用,从而使所属技术领域技术人员能很好地理解和利用本发明。本发明仅受权利要求书及其全部范围和等效物的限制。The preferred embodiments of the present invention disclosed above are only used to help illustrate the present invention. The preferred embodiments do not describe all the details in detail, nor do they limit the invention to the specific implementation methods described. Obviously, many modifications and changes can be made according to the content of this specification. This specification selects and specifically describes these embodiments in order to better explain the principles and practical applications of the present invention, so that those skilled in the art can understand and use the present invention well. The present invention is limited only by the claims and their full scope and equivalents.
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