CN101967209A - N-acetylethylenediamine chelate resin and preparation method thereof - Google Patents
N-acetylethylenediamine chelate resin and preparation method thereof Download PDFInfo
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- 229920005989 resin Polymers 0.000 title claims abstract description 73
- 239000011347 resin Substances 0.000 title claims abstract description 73
- DAKZISABEDGGSV-UHFFFAOYSA-N n-(2-aminoethyl)acetamide Chemical compound CC(=O)NCCN DAKZISABEDGGSV-UHFFFAOYSA-N 0.000 title claims abstract description 23
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 239000013522 chelant Substances 0.000 title abstract description 8
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000000460 chlorine Substances 0.000 claims abstract description 20
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 20
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims abstract description 17
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims abstract description 15
- 238000006243 chemical reaction Methods 0.000 claims abstract description 14
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims abstract description 10
- XEKOWRVHYACXOJ-UHFFFAOYSA-N ethyl acetate Substances CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims abstract description 9
- 229910000027 potassium carbonate Inorganic materials 0.000 claims abstract description 8
- 125000000524 functional group Chemical group 0.000 claims abstract description 6
- 238000005406 washing Methods 0.000 claims abstract description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 30
- 229920001429 chelating resin Polymers 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 17
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 15
- 239000000178 monomer Substances 0.000 claims description 15
- 239000003361 porogen Substances 0.000 claims description 15
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 claims description 14
- 239000003431 cross linking reagent Substances 0.000 claims description 14
- 238000004132 cross linking Methods 0.000 claims description 13
- 229920003053 polystyrene-divinylbenzene Polymers 0.000 claims description 13
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 12
- 238000007265 chloromethylation reaction Methods 0.000 claims description 9
- 239000002904 solvent Substances 0.000 claims description 8
- 239000004342 Benzoyl peroxide Substances 0.000 claims description 6
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 claims description 6
- 235000019400 benzoyl peroxide Nutrition 0.000 claims description 6
- HRQGCQVOJVTVLU-UHFFFAOYSA-N bis(chloromethyl) ether Chemical compound ClCOCCl HRQGCQVOJVTVLU-UHFFFAOYSA-N 0.000 claims description 6
- 239000003999 initiator Substances 0.000 claims description 6
- 239000012452 mother liquor Substances 0.000 claims description 6
- 239000011592 zinc chloride Substances 0.000 claims description 6
- 235000005074 zinc chloride Nutrition 0.000 claims description 6
- 239000004793 Polystyrene Substances 0.000 claims description 5
- 239000003054 catalyst Substances 0.000 claims description 5
- 239000002270 dispersing agent Substances 0.000 claims description 5
- 229920002223 polystyrene Polymers 0.000 claims description 5
- 230000035484 reaction time Effects 0.000 claims description 5
- 108010010803 Gelatin Proteins 0.000 claims description 4
- 229920000159 gelatin Polymers 0.000 claims description 4
- 239000008273 gelatin Substances 0.000 claims description 4
- 235000019322 gelatine Nutrition 0.000 claims description 4
- 235000011852 gelatine desserts Nutrition 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 claims description 3
- 239000001095 magnesium carbonate Substances 0.000 claims description 3
- 229910000021 magnesium carbonate Inorganic materials 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 3
- 238000000638 solvent extraction Methods 0.000 claims description 3
- 238000001256 steam distillation Methods 0.000 claims description 3
- 238000010558 suspension polymerization method Methods 0.000 claims description 3
- 230000008961 swelling Effects 0.000 claims description 3
- 229920001577 copolymer Polymers 0.000 claims description 2
- 239000011148 porous material Substances 0.000 claims description 2
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 11
- 238000003756 stirring Methods 0.000 abstract description 10
- -1 Cu<2+> and the like Chemical class 0.000 abstract description 8
- 150000002500 ions Chemical class 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000001035 drying Methods 0.000 abstract description 2
- 238000003891 environmental analysis Methods 0.000 abstract description 2
- 238000005272 metallurgy Methods 0.000 abstract description 2
- 238000005065 mining Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 abstract description 2
- 238000000605 extraction Methods 0.000 abstract 1
- 238000001914 filtration Methods 0.000 abstract 1
- 239000010413 mother solution Substances 0.000 abstract 1
- 239000000243 solution Substances 0.000 abstract 1
- 238000001179 sorption measurement Methods 0.000 description 11
- 238000010534 nucleophilic substitution reaction Methods 0.000 description 8
- 238000010557 suspension polymerization reaction Methods 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 238000010992 reflux Methods 0.000 description 4
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- SHQNGLYXRFCPGZ-UHFFFAOYSA-N ethyl 2-(2-amino-1,3-thiazol-4-yl)acetate Chemical compound CCOC(=O)CC1=CSC(N)=N1 SHQNGLYXRFCPGZ-UHFFFAOYSA-N 0.000 description 3
- 229910021645 metal ion Inorganic materials 0.000 description 3
- 125000004430 oxygen atom Chemical group O* 0.000 description 3
- 229920000768 polyamine Polymers 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 239000001993 wax Substances 0.000 description 3
- FZWLAAWBMGSTSO-UHFFFAOYSA-N Thiazole Chemical group C1=CSC=N1 FZWLAAWBMGSTSO-UHFFFAOYSA-N 0.000 description 2
- 229910001431 copper ion Inorganic materials 0.000 description 2
- 125000004185 ester group Chemical group 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 125000004433 nitrogen atom Chemical group N* 0.000 description 2
- 238000010189 synthetic method Methods 0.000 description 2
- VILCJCGEZXAXTO-UHFFFAOYSA-N 2,2,2-tetramine Chemical compound NCCNCCNCCN VILCJCGEZXAXTO-UHFFFAOYSA-N 0.000 description 1
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 1
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 229920003180 amino resin Polymers 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000009920 chelation Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 229940057995 liquid paraffin Drugs 0.000 description 1
- 229960000907 methylthioninium chloride Drugs 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 125000004434 sulfur atom Chemical group 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
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Abstract
Description
技术领域technical field
本发明涉及一种螯合树脂及其合成方法,具体地说,是指一种N-乙酰基乙二胺螯合树脂及其制备方法。The present invention relates to a kind of chelate resin and its synthetic method, specifically, refer to a kind of N-acetyl ethylenediamine chelate resin and its preparation method.
背景技术Background technique
多乙烯多胺类螯合树脂是一类氮原子配位的高聚物,通过氮上的孤对电子与金属离子作用,可与多种重金属离子形成络合物,尤其对过渡族重金属离子具有优越的吸附性能及吸附选择性。目前报道的多乙烯多胺类树脂对金属离子的吸附容量较大,但对于多组分溶液中特定金属离子的吸附选择性不足。国内孙向荣等采用环氧氯丙烷对三乙烯四胺化交联聚苯乙烯进行后交联反应,所得树脂对铜离子的选择性明显提高。文献报道,以聚乙二醇为链单元的乙二胺树脂吸附性能优于以聚乙二胺为单元的氨基树脂;增加乙氧基链节数量和将氧原子替换为硫原子,树脂对金的吸附容量显著提高。可见,对于多乙烯多胺类螯合树脂,取代基与母体间的链节长度和链节种类对于树脂的吸附性能有明显影响,因此可以通过调节链长度及链单元的类别来改善重金属的吸附性能,富集目标重金属,提高树脂的吸附选择性。Polyethylene polyamine chelating resin is a kind of high polymer coordinated by nitrogen atom. Through the interaction of lone pair electrons on nitrogen and metal ions, it can form complexes with various heavy metal ions, especially for transition group heavy metal ions. Superior adsorption performance and adsorption selectivity. The currently reported polyethylene polyamine resins have a large adsorption capacity for metal ions, but the adsorption selectivity for specific metal ions in multi-component solutions is insufficient. In China, Sun Xiangrong and others used epichlorohydrin to perform post-crosslinking reaction on triethylenetetraamine crosslinked polystyrene, and the selectivity of the obtained resin to copper ions was significantly improved. It has been reported in the literature that the adsorption performance of ethylenediamine resins with polyethylene glycol as chain units is better than that of amino resins with polyethylenediamine as units; increasing the number of ethoxy chain units and replacing oxygen atoms with sulfur atoms, the resin has a greater effect on gold The adsorption capacity was significantly increased. It can be seen that for polyethylene polyamine chelating resins, the length of the chain link between the substituent and the parent and the type of chain link have a significant impact on the adsorption performance of the resin, so the adsorption of heavy metals can be improved by adjusting the chain length and the type of chain unit performance, enrich the target heavy metals, and improve the adsorption selectivity of the resin.
文献检索表明,以氯球为基质,通过噻唑环上的酯基键合乙二胺的螯合树脂的合成方法未见报道。Document search shows, take chlorine ball as substrate, the synthetic method of the chelating resin of bonding ethylenediamine by the ester group on the thiazole ring has not been reported.
发明内容Contents of the invention
本发明的目的是提供一种N-乙酰基乙二胺螯合树脂及其制备方法,通过本发明可以合成具有N-乙酰基乙二胺结构、对铜离子具有特殊吸附选择性的螯合树脂。The purpose of the present invention is to provide a kind of N-acetylethylenediamine chelating resin and preparation method thereof, can synthesize the chelating resin that has N-acetylethylenediamine structure, has special adsorption selectivity to copper ion by the present invention .
本发明的技术方案如下:Technical scheme of the present invention is as follows:
一种N-乙酰基乙二胺螯合树脂,其结构单元如下:A kind of N-acetyl ethylenediamine chelating resin, its structural unit is as follows:
从结构单元中可以看出树脂中含有功能基团:N-乙酰基乙二胺和噻唑环,并通过氮、氧原子的螯合作用吸附重金属离子。该树脂可能通过基团上的氮原子及氧原子形成环状螯合结构:It can be seen from the structural units that the resin contains functional groups: N-acetylethylenediamine and thiazole rings, and absorbs heavy metal ions through the chelation of nitrogen and oxygen atoms. The resin may form a cyclic chelate structure through the nitrogen atom and oxygen atom on the group:
所述N-乙酰基乙二胺螯合树脂化学功能基团含量为0.71~1.39mmol/g。The chemical functional group content of the N-acetylethylenediamine chelating resin is 0.71-1.39 mmol/g.
一种N-乙酰基乙二胺螯合树脂的制备方法,包括以下几个步骤:A kind of preparation method of N-acetyl ethylenediamine chelate resin, comprises the following steps:
(a)利用苯乙烯作单体,二乙烯苯作交联剂,利用液蜡或200号溶剂油中的一种或两种混和作致孔剂,用碳酸镁、明胶、聚乙烯醇中的一种或几种混和作分散剂,用过氧化苯甲酰作引发剂,采用悬浮聚合法,制备低交联度大孔苯乙烯-二乙烯苯共聚物,选用水蒸汽蒸馏或乙醇、丙酮、工业酒精、低沸点溶剂汽油作溶剂抽提,去除树脂孔道中残留的致孔剂,再经过气流干燥得到低交联大孔聚苯乙烯-二乙烯苯树脂,以下简称白球;(a) Styrene is used as a monomer, divinylbenzene is used as a crosslinking agent, one or both of liquid wax or No. 200 solvent oil is used as a porogen, and magnesium carbonate, gelatin, and polyvinyl alcohol are used. One or several kinds of mixtures are used as dispersant, benzoyl peroxide is used as initiator, and low-crosslinking macroporous styrene-divinylbenzene copolymer is prepared by suspension polymerization method. Steam distillation or ethanol, acetone, Industrial alcohol and low-boiling-point solvent gasoline are used as solvent extraction to remove the porogen remaining in the resin pores, and then air-dried to obtain low-crosslinked macroporous polystyrene-divinylbenzene resin, hereinafter referred to as white ball;
(b)将白球浸泡于其重量4~7倍的氯甲醚中,加入白球重量的20~50%的氯化锌作催化剂,在25~55℃温度下进行氯甲基化反应,直到氯含量达到10%以上停止反应,滤出树脂球体,用水或乙醇、丙酮洗尽树脂中残余的氯化母液,气流干燥得到氯甲基化低交联大孔聚苯乙烯-二乙烯苯树脂,以下简称氯球;(b) Soak the white ball in chloromethyl ether 4 to 7 times its weight, add 20 to 50% of the weight of the white ball as zinc chloride as a catalyst, and carry out chloromethylation reaction at a temperature of 25 to 55°C until the chlorine When the content reaches more than 10%, the reaction is stopped, the resin spheres are filtered out, the remaining chlorinated mother liquor in the resin is washed with water or ethanol, and acetone, and air-dried to obtain chloromethylated low-crosslinked macroporous polystyrene-divinylbenzene resin, as follows Referred to as chlorine ball;
(c)步骤(b)后,一般经索氏抽提器抽提4~8小时,然后以N,N-二甲基甲酰胺为溶胀剂,在85℃下,加入2-氨基噻唑-4-乙酸乙酯和碳酸钾反应,入2-氨基噻唑-4-乙酸乙酯用量均为树脂重量的2~5倍,碳酸钾用量为树脂重量的1~2倍,搅拌反应6~24h,可得淡黄色螯合树脂。(c) After step (b), it is generally extracted by Soxhlet extractor for 4 to 8 hours, and then N, N-dimethylformamide is used as a swelling agent, and 2-aminothiazole-4 - Ethyl acetate and potassium carbonate are reacted, the amount of 2-aminothiazole-4-ethyl acetate is 2 to 5 times the weight of the resin, the amount of potassium carbonate is 1 to 2 times the weight of the resin, and the reaction is stirred for 6 to 24 hours. A light yellow chelating resin was obtained.
(d)将步骤(c)中得到的树脂洗涤烘干后,加入15~30倍树脂重量的乙二胺溶液,在125℃反应24~30h,抽滤并洗涤干燥得N-乙酰基乙二胺螯合树脂。(d) After washing and drying the resin obtained in step (c), add ethylenediamine solution 15 to 30 times the weight of the resin, react at 125°C for 24 to 30 hours, filter with suction, wash and dry to obtain N-acetylethylenediamine Amine Chelating Resin.
所述树脂的制备方法中,其特征在于步骤(c)反应时间反应温度控制在85℃步骤、(d)反应时间在24~30h,反应温度控制在125℃。通过控制反应中加入试剂的用量和反应时间,可制得系列螯合树脂。通常确定其他条件,反应时间愈长,则表面基团数目愈大;试剂的用量愈大,所得的树脂的表面基团愈多。In the preparation method of the resin, it is characterized in that step (c) the reaction time is controlled at 85°C, and (d) the reaction time is 24-30h, and the reaction temperature is controlled at 125°C. A series of chelating resins can be prepared by controlling the amount of reagents added in the reaction and the reaction time. Usually other conditions are determined, the longer the reaction time, the larger the number of surface groups; the larger the amount of reagent used, the more surface groups of the resin obtained.
有益效果Beneficial effect
本发明公开了一种N-乙酰基乙二胺螯合树脂及其制备方法,本发明提供的树脂可对Cu2+等重金属离子进行选择性性吸附分离。所含N、O等原子对重金属发挥螯合配位作用。本发明采用2-氨基噻唑-4-乙酸乙酯及乙二胺修饰得到的N-乙酰基乙二胺螯合树脂,所含基团可与某些重金属形成稳定常数较高的络合物,具有较高的吸附选择性,在矿冶生产母液提纯及生产废水治理以及环境分析中重金属的分离与预富集等领域具有广泛用途。The invention discloses an N-acetylethylenediamine chelating resin and a preparation method thereof. The resin provided by the invention can selectively adsorb and separate heavy metal ions such as Cu2+. The contained N, O and other atoms play a chelating and coordinating role on heavy metals. The N-acetylethylenediamine chelating resin obtained by modifying 2-aminothiazole-4-ethyl acetate and ethylenediamine in the present invention contains groups that can form complexes with higher stability constants with certain heavy metals. With high adsorption selectivity, it is widely used in the fields of purification of mother liquor in mining and metallurgy production, treatment of production wastewater, and separation and pre-enrichment of heavy metals in environmental analysis.
具体实施方式Detailed ways
以下通过实施例进一步说明本发明。The present invention is further illustrated by the following examples.
实施例1Example 1
(a)悬浮聚合(a) suspension polymerization
苯乙烯单体加入一定量的稀氢氧化钠溶液或将单体直接经过装有强碱阴离子交换树脂的树脂柱过滤以去除阻聚剂。Add a certain amount of dilute sodium hydroxide solution to the styrene monomer or directly filter the monomer through a resin column equipped with a strong base anion exchange resin to remove the polymerization inhibitor.
1000mL烧杯中,加入210g苯乙烯,26g二乙烯苯,140g液体石蜡,搅拌均匀后备用。In a 1000mL beaker, add 210g styrene, 26g divinylbenzene, and 140g liquid paraffin, stir well and set aside.
1000mL三口烧瓶中,加入600g蒸馏水并升温至40℃,再加入6g明胶,搅拌至完全溶解,同时升温至50℃,加入2mL次甲基蓝,搅拌均匀,加入上述苯乙烯、二乙烯苯及液蜡的混和液,加入引发剂过氧化苯甲酰4.0g;调整适当的搅拌速度使油珠大小合适,以1℃/6min的速度逐步升温至80℃,并保温4h,再逐步升温至85℃保温3h,90℃保温2h,95℃保温4h,反应完毕,滤出树脂,先用热水洗涤,滤出树脂,晾干,装入索氏抽提器,用丙酮抽提干净,气流干燥,过筛,取合适粒度的树脂备用。In a 1000mL three-neck flask, add 600g of distilled water and raise the temperature to 40°C, then add 6g of gelatin, stir until completely dissolved, and at the same time raise the temperature to 50°C, add 2mL of methylene blue, stir well, add the above-mentioned styrene, divinylbenzene and liquid Add the initiator benzoyl peroxide 4.0g to the wax mixture; adjust the stirring speed to make the oil droplet size appropriate, gradually raise the temperature to 80°C at a speed of 1°C/6min, keep it warm for 4 hours, and then gradually raise the temperature to 85°C Keep warm for 3 hours, keep warm at 90°C for 2 hours, keep warm at 95°C for 4 hours, after the reaction is completed, filter out the resin, wash it with hot water first, filter out the resin, dry it, put it into a Soxhlet extractor, extract it with acetone, and air-dry it. Sieve, and take the resin with suitable particle size for later use.
(b)氯甲基化(b) Chloromethylation
2000mL三口烧瓶中,加入300g白球,1200g氯甲醚,于20~25℃下浸泡2h以上,搅拌下,加入150g氯化锌,控制温度不高于25℃,搅拌1h后,升温至38℃,保温8~12h,控制氯含量在10%以上,即可结束反应。In a 2000mL three-neck flask, add 300g of white balls and 1200g of chloromethyl ether, soak at 20-25°C for more than 2 hours, add 150g of zinc chloride under stirring, control the temperature not higher than 25°C, stir for 1 hour, then raise the temperature to 38°C, Insulate for 8-12 hours and control the chlorine content above 10%, then the reaction can be ended.
反应结束后,滤出树脂球体,水洗后抽提树脂,再用水洗至中性,气流干燥得到氯球。After the reaction, filter out the resin spheres, wash with water and extract the resin, then wash with water until neutral, and air-dry to obtain chlorine spheres.
(c)亲核取代反应(c) Nucleophilic substitution reaction
250mL三口烧瓶中,加入步骤(b)所制备的氯甲基化树脂8g,用150ml的DMF溶胀4h;加入2-氨基噻唑-4-乙酸乙酯20g,无水碳酸钾10g,然后升温至65℃,搅拌,反应20h,滤出树脂,依次用水、丙酮、水洗涤,烘干即可制得含酯基结构的树脂。In a 250mL three-necked flask, add 8g of chloromethylated resin prepared in step (b), and swell with 150ml of DMF for 4h; add 20g of ethyl 2-aminothiazole-4-acetate, 10g of anhydrous potassium carbonate, and then heat up to 65 ℃, stirred, reacted for 20 hours, filtered out the resin, washed with water, acetone and water in turn, and dried to obtain the resin with ester group structure.
(d)亲核取代反应(d) Nucleophilic substitution reaction
250mL三口烧瓶中,加入步骤(c)所制备的树脂8g,乙二胺150mL,在115℃条件下冷凝回流反应30h,抽滤并水洗、丙酮洗涤、水洗,干燥后得N-乙酰基乙二胺螯合树脂。Into a 250mL three-neck flask, add 8g of the resin prepared in step (c), 150mL of ethylenediamine, condense and reflux for 30h at 115°C, filter with suction and wash with water, acetone, and water, and dry to obtain N-acetylethylenediamine Amine Chelating Resin.
实施例2Example 2
本发明另一实施例的合成步骤如下:The synthetic steps of another embodiment of the present invention are as follows:
(a)悬浮聚合(a) suspension polymerization
利用苯乙烯作单体,二乙烯苯作交联剂,利用200号溶剂油作致孔剂,用明胶作分散剂,用过氧化苯甲酰作引发剂,采用悬浮聚合法,合成低交联度大孔聚苯乙烯-二乙烯苯共聚物,选用乙醇(或丙酮、工业酒精、低沸点溶剂汽油)作溶剂抽提,去除树脂孔道中残留的致孔剂,再经过气流干燥得到低交联大孔聚苯乙烯-二乙烯苯树脂,即白球。Using styrene as a monomer, divinylbenzene as a crosslinking agent, using No. 200 solvent oil as a porogen, using gelatin as a dispersant, using benzoyl peroxide as an initiator, and adopting a suspension polymerization method to synthesize low crosslinking Macroporous polystyrene-divinylbenzene copolymer, using ethanol (or acetone, industrial alcohol, low boiling point solvent gasoline) as solvent extraction to remove the residual porogen in the resin channels, and then air drying to obtain low crosslinking Macroporous polystyrene-divinylbenzene resin, that is, white balls.
其中交联剂用量为单体和交联剂总量的7%,致孔剂用量为单体重量的100%,低交联大孔聚苯乙烯的交联度为10%。Wherein the dosage of the crosslinking agent is 7% of the total amount of the monomer and the crosslinking agent, the dosage of the porogen is 100% of the weight of the monomer, and the crosslinking degree of the low crosslinking macroporous polystyrene is 10%.
(b)氯甲基化(b) Chloromethylation
将白球浸泡于其重量4倍的氯甲醚中,加入白球重量的20%的氯化锌作催化剂,在35℃温度时进行氯甲基化反应,直到氯含量达到10%以上停止反应,滤出树脂球体,用水洗尽树脂中残余的氯化母液,气流干燥得到氯甲基化低交联大孔聚苯乙烯-二乙烯苯树脂,即氯球。Soak the white ball in chloromethyl ether that is 4 times its weight, add 20% of the weight of the white ball to zinc chloride as a catalyst, and carry out chloromethylation reaction at a temperature of 35°C until the chlorine content reaches more than 10% to stop the reaction, filter The resin spheres are taken out, the remaining chlorinated mother liquor in the resin is washed with water, and air-dried to obtain chloromethylated low-crosslinked macroporous polystyrene-divinylbenzene resin, namely chlorine spheres.
(c)亲核取代反应(c) Nucleophilic substitution reaction
用300ml的DMF溶胀步骤(b)所制备的氯球15g;4h后加入42g 2-氨基噻唑-4-乙酸乙酯,15g无水碳酸钾,升温至85℃,搅拌,反应8h,滤出树脂,依次用水、丙酮、水洗涤。Swell 15g of chlorine balls prepared in step (b) with 300ml of DMF; add 42g of ethyl 2-aminothiazole-4-acetate and 15g of anhydrous potassium carbonate after 4h, heat up to 85°C, stir, react for 8h, and filter out the resin , washed with water, acetone, and water successively.
(d)亲核取代反应(d) Nucleophilic substitution reaction
向500mL三口烧瓶中加入步骤(c)所制备的树脂15g、乙二胺溶液300mL,然后升温至125℃并冷凝回流24h,抽滤、水洗、丙酮洗涤、水洗,干燥后得N-乙酰基乙二胺螯合树脂。Add 15g of the resin prepared in step (c) and 300mL of ethylenediamine solution to a 500mL three-neck flask, then raise the temperature to 125°C and condense and reflux for 24h, filter with suction, wash with water, wash with acetone, wash with water, and dry to obtain N-acetyl ethyl Diamine chelating resin.
实施例3:Example 3:
本发明另一实施例的合成步骤如下:The synthetic steps of another embodiment of the present invention are as follows:
(a)悬浮聚合(a) suspension polymerization
利用苯乙烯作单体,二乙烯苯作交联剂,利用200号溶剂油作致孔剂,用碳酸镁作分散剂,用过氧化苯甲酰作引发剂,采用悬浮聚合法,合成低交联度大孔聚苯乙烯-二乙烯苯共聚物,选用水蒸气蒸馏,去除树脂孔道中残留的致孔剂,再经过气流干燥得到低交联大孔聚苯乙烯-二乙烯苯树脂,即白球。Using styrene as a monomer, divinylbenzene as a cross-linking agent, using No. 200 solvent oil as a porogen, magnesium carbonate as a dispersant, and benzoyl peroxide as an initiator, a low cross-linking agent was synthesized by suspension polymerization. Linked macroporous polystyrene-divinylbenzene copolymer, steam distillation is used to remove the porogen remaining in the resin channels, and then air-dried to obtain low-crosslinked macroporous polystyrene-divinylbenzene resin, that is, white ball .
其中交联剂用量为单体和交联剂总量的8%,致孔剂用量为单体重量的40%,低交联大孔聚苯乙烯的交联度为2%。Wherein the dosage of the crosslinking agent is 8% of the total amount of the monomer and the crosslinking agent, the dosage of the porogen is 40% of the weight of the monomer, and the crosslinking degree of the low crosslinking macroporous polystyrene is 2%.
(b)氯甲基化(b) Chloromethylation
将白球浸泡于其重量7倍的氯甲醚中,加入白球重量的50%的氯化锌作催化剂,在40℃温度中进行氯甲基化反应,直到氯含量达到10%以上停止反应,滤出树脂球体,用丙酮洗尽树脂中残余的氯化母液,气流干燥得到氯甲基化低交联大孔聚苯乙烯-二乙烯苯树脂,即氯球。Soak the white ball in chloromethyl ether which is 7 times its weight, add 50% of the weight of the white ball with zinc chloride as a catalyst, and carry out chloromethylation reaction at a temperature of 40°C until the chlorine content reaches more than 10% to stop the reaction, filter The resin spheres were taken out, the remaining chlorinated mother liquor in the resin was washed with acetone, and air-dried to obtain chloromethylated low-crosslinked macroporous polystyrene-divinylbenzene resin, namely chlorine spheres.
(c)亲核取代反应(c) Nucleophilic substitution reaction
500mL三口烧瓶中,加入氯球10g,并以250mlDMF溶胀4h;加入2-氨基噻唑-4-乙酸乙酯20g,无水碳酸钾12g,然后升温至80℃,搅拌,反应6h,滤出树脂,依次用水、丙酮、水洗涤。In a 500mL three-neck flask, add 10g of chlorine balls, and swell with 250ml of DMF for 4h; add 20g of ethyl 2-aminothiazole-4-acetate, 12g of anhydrous potassium carbonate, then heat up to 80°C, stir, react for 6h, and filter out the resin. Wash with water, acetone, and water successively.
(d)亲核取代反应(d) Nucleophilic substitution reaction
250mL三口烧瓶中,加入步骤(c)所制备的树脂10g,乙二胺200mL,在120℃条件下冷凝回流反应30h,抽滤、水洗、丙酮洗涤、水洗,干燥后得N-乙酰基乙二胺螯合树脂。Into a 250mL three-necked flask, add 10g of the resin prepared in step (c), 200mL of ethylenediamine, condense and reflux for 30h at 120°C, filter with suction, wash with water, wash with acetone, wash with water, and dry to obtain N-acetylethylenediamine Amine Chelating Resin.
本工艺合成的N-乙酰基乙二胺螯合树脂的结构特征如下表:The structural characteristics of the N-acetylethylenediamine chelating resin synthesized by this process are as follows:
主要技术指标如下:(树脂A,B和C分别对应实施案例1,2,3所制得的树脂)The main technical indicators are as follows: (resins A, B and C correspond to the resins prepared in cases 1, 2 and 3 respectively)
实施例4:Example 4:
本发明另一实施例的合成步骤如下:The synthetic steps of another embodiment of the present invention are as follows:
(b)悬浮聚合(b) suspension polymerization
利用苯乙烯作单体,二乙烯苯作交联剂,利用液蜡作致孔剂,用聚乙烯醇作分散剂,用过氧化苯甲酰作引发剂,采用悬浮聚合法,合成低交联度大孔聚苯乙烯-二乙烯苯共聚物,选用乙醇做溶剂抽提,去除树脂孔道中残留的致孔剂,再经过气流干燥得到低交联大孔聚苯乙烯-二乙烯苯树脂,即白球。Using styrene as a monomer, divinylbenzene as a crosslinking agent, liquid wax as a porogen, polyvinyl alcohol as a dispersant, benzoyl peroxide as an initiator, and suspension polymerization to synthesize low crosslinking The macroporous polystyrene-divinylbenzene copolymer is extracted with ethanol as a solvent to remove the porogen remaining in the resin channels, and then air-dried to obtain a low-crosslinked macroporous polystyrene-divinylbenzene resin, namely White ball.
其中交联剂用量为单体和交联剂总量的4%,致孔剂用量为单体重量的40%,低交联大孔聚苯乙烯的交联度为2%。Wherein the dosage of the crosslinking agent is 4% of the total amount of the monomer and the crosslinking agent, the dosage of the porogen is 40% of the weight of the monomer, and the crosslinking degree of the low crosslinking macroporous polystyrene is 2%.
(b)氯甲基化(b) Chloromethylation
将白球浸泡于其重量4倍的氯甲醚中,加入白球重量的20%的氯化锌作催化剂,在35℃温度中进行氯甲基化反应,直到氯含量达到10%以上停止反应,滤出树脂球体,用乙醇洗尽树脂中残余的氯化母液,气流干燥得到氯甲基化低交联大孔聚苯乙烯-二乙烯苯树脂,即氯球。Soak the white ball in chloromethyl ether that is 4 times its weight, add 20% of the weight of the white ball to zinc chloride as a catalyst, and carry out chloromethylation reaction at a temperature of 35°C until the chlorine content reaches more than 10% to stop the reaction, filter The resin spheres are taken out, the remaining chlorinated mother liquor in the resin is washed with ethanol, and air-dried to obtain chloromethylated low-crosslinked macroporous polystyrene-divinylbenzene resin, namely chlorine spheres.
(c)亲核取代反应(c) Nucleophilic substitution reaction
向装有25g氯球的三口烧瓶中加入600ml溶胀剂DMF,6h后加入试剂2-氨基噻唑-4-乙酸乙酯,用量为树脂重量的2倍,无水碳酸钾25g,70℃条件下搅拌反应12h,滤出树脂,依次用水、丙酮、水洗涤。Add 600ml of swelling agent DMF to a three-necked flask with 25g of chlorine balls, add reagent 2-aminothiazole-4-ethyl acetate 6h later, the dosage is twice the weight of the resin, 25g of anhydrous potassium carbonate, stir at 70°C After reacting for 12 hours, the resin was filtered out and washed with water, acetone and water successively.
(d)亲核取代反应(d) Nucleophilic substitution reaction
1000mL三口烧瓶中,加入步骤(c)所制备的树脂20g,乙二胺700mL,升温至110℃并冷凝回流20h,抽滤、水洗、丙酮洗涤、水洗,干燥后得N-乙酰基乙二胺螯合树脂。Into a 1000mL three-neck flask, add 20g of the resin prepared in step (c), 700mL of ethylenediamine, heat up to 110°C and condense and reflux for 20h, filter with suction, wash with water, wash with acetone, wash with water, and dry to obtain N-acetylethylenediamine Chelating resin.
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CN115960291A (en) * | 2023-02-09 | 2023-04-14 | 南京大学 | Preparation method of long-chain haloalkyl styrene polymer |
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