CN104448288A - Method for synthesizing polyepichlorohydrin - Google Patents
Method for synthesizing polyepichlorohydrin Download PDFInfo
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- 229920002755 poly(epichlorohydrin) Polymers 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title claims abstract description 10
- 230000002194 synthesizing effect Effects 0.000 title claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 21
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 21
- 238000003756 stirring Methods 0.000 claims abstract description 21
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000006243 chemical reaction Methods 0.000 claims abstract description 17
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 14
- SNMVRZFUUCLYTO-UHFFFAOYSA-N n-propyl chloride Chemical compound CCCCl SNMVRZFUUCLYTO-UHFFFAOYSA-N 0.000 claims abstract description 13
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000003054 catalyst Substances 0.000 claims abstract description 7
- YNLAOSYQHBDIKW-UHFFFAOYSA-M diethylaluminium chloride Chemical compound CC[Al](Cl)CC YNLAOSYQHBDIKW-UHFFFAOYSA-M 0.000 claims abstract description 7
- 239000012153 distilled water Substances 0.000 claims abstract description 7
- 230000007935 neutral effect Effects 0.000 claims abstract description 7
- 239000011541 reaction mixture Substances 0.000 claims abstract description 7
- 239000000243 solution Substances 0.000 claims description 18
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims description 15
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 12
- 239000010410 layer Substances 0.000 claims description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- -1 diamine hydrogen phosphate Chemical class 0.000 claims description 7
- 239000012043 crude product Substances 0.000 claims description 6
- 239000008367 deionised water Substances 0.000 claims description 6
- 229910021641 deionized water Inorganic materials 0.000 claims description 6
- 239000005457 ice water Substances 0.000 claims description 6
- 239000003999 initiator Substances 0.000 claims description 6
- 239000002808 molecular sieve Substances 0.000 claims description 6
- 239000012044 organic layer Substances 0.000 claims description 6
- 238000010992 reflux Methods 0.000 claims description 6
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 239000000725 suspension Substances 0.000 claims description 6
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 4
- 238000004821 distillation Methods 0.000 claims description 4
- 238000006116 polymerization reaction Methods 0.000 claims description 4
- 238000003786 synthesis reaction Methods 0.000 claims description 4
- 239000011964 heteropoly acid Substances 0.000 claims description 3
- 239000012267 brine Substances 0.000 claims description 2
- 150000003384 small molecules Chemical class 0.000 claims 1
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 abstract description 2
- 229910000030 sodium bicarbonate Inorganic materials 0.000 abstract description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract 2
- LRWZZZWJMFNZIK-UHFFFAOYSA-N 2-chloro-3-methyloxirane Chemical compound CC1OC1Cl LRWZZZWJMFNZIK-UHFFFAOYSA-N 0.000 abstract 1
- 239000000654 additive Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 239000000047 product Substances 0.000 description 3
- DTQVDTLACAAQTR-UHFFFAOYSA-N Trifluoroacetic acid Chemical compound OC(=O)C(F)(F)F DTQVDTLACAAQTR-UHFFFAOYSA-N 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 2
- WBYWAXJHAXSJNI-VOTSOKGWSA-M .beta-Phenylacrylic acid Natural products [O-]C(=O)\C=C\C1=CC=CC=C1 WBYWAXJHAXSJNI-VOTSOKGWSA-M 0.000 description 1
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- WBYWAXJHAXSJNI-SREVYHEPSA-N Cinnamic acid Chemical compound OC(=O)\C=C/C1=CC=CC=C1 WBYWAXJHAXSJNI-SREVYHEPSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 239000004831 Hot glue Substances 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229930016911 cinnamic acid Natural products 0.000 description 1
- 235000013985 cinnamic acid Nutrition 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 229910000388 diammonium phosphate Inorganic materials 0.000 description 1
- 235000019838 diammonium phosphate Nutrition 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- WBYWAXJHAXSJNI-UHFFFAOYSA-N methyl p-hydroxycinnamate Natural products OC(=O)C=CC1=CC=CC=C1 WBYWAXJHAXSJNI-UHFFFAOYSA-N 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 229920002120 photoresistant polymer Polymers 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000010189 synthetic method Methods 0.000 description 1
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Abstract
Description
技术领域technical field
本发明属于有聚合反应领域,涉及一种聚环氧氯丙烷的合成方法。The invention belongs to the field of polymerization reaction and relates to a synthesis method of polyepichlorohydrin.
背景技术Background technique
聚环氧氯丙烷是淡黄色至琥珀色粘稠液体或固体。它是经环氧氯丙烯开环聚合二形成的。聚环氧氯丙烷具有耐油性,耐酸性等优点,耐气体穿透性突出。其减震行和耐高温行也很好,并具有良好的粘合性。将聚环氧氯丙烷进行肉桂酸纸花,可制成性能优异的光刻胶。聚环氧氯丙烷可用于制造密封胶垫和耐油热熔胶,耐海水,耐油的胶黏剂等以及阻燃、耐水、耐油的聚氨酯胶黏剂、涂料。环氧化合物的开环聚合产物作为新型聚合物材料中间体系日益重要。Polyepichlorohydrin is light yellow to amber viscous liquid or solid. It is formed by the ring-opening polymerization of epichlorohydrin. Polyepichlorohydrin has the advantages of oil resistance, acid resistance, etc., and has outstanding resistance to gas penetration. Its shock absorption and high temperature resistance are also good, and it has good adhesion. The photoresist with excellent performance can be made by treating polyepichlorohydrin with cinnamic acid. Polyepichlorohydrin can be used to make sealing gaskets and oil-resistant hot melt adhesives, seawater-resistant, oil-resistant adhesives, etc., as well as flame-retardant, water-resistant, and oil-resistant polyurethane adhesives and coatings. The ring-opening polymerization products of epoxy compounds are increasingly important as intermediate systems for new polymer materials.
传统合成聚环氧氯丙烯的引发剂多为1,4-丁醇双三氟甲基磺酸脂、三氟乙酸等;这写合成方法各有优点,但在聚合反应过程中产生大量的齐聚物。因此,必须对聚合产物进行必要的后处理,这就意味着工艺更加繁琐,制的产品质量达不到希望的性能。The traditional initiators for synthesizing polyepichloropropylene are mostly 1,4-butanol bistrifluoromethanesulfonate, trifluoroacetic acid, etc.; these synthetic methods have their own advantages, but a large amount of homogeneous compounds are produced during the polymerization reaction. Polymer. Therefore, necessary aftertreatment must be carried out to the polymerized product, which means that the process is more complicated, and the quality of the manufactured product cannot reach the desired performance.
发明内容Contents of the invention
为了解决现有技术中合成聚环氧氯丙烷产出的大量的杂质,减小工艺繁琐,提高聚环物的质量。In order to solve the large amount of impurities produced by synthesizing polyepichlorohydrin in the prior art, reduce the complicated process and improve the quality of the polycyclic compound.
本发明的合成路线为:The synthetic route of the present invention is:
本发明涉及聚丙烯酸的合成过程包括以下步骤:The synthetic process that the present invention relates to polyacrylic acid comprises the following steps:
1.环氧氯丙烷的合成:1. Synthesis of epichlorohydrin:
(1)向100mL四口烧瓶中投入30g的氯丙烷和6.5g的催化剂(磷钨杂多酸盐/Ti02),再搅拌状态下加入10mL双氧水和5g磷酸氢二胺,于氯丙烷回流下反应6小时;(1) Put 30g of chloropropane and 6.5g of catalyst (phosphotungstic heteropolyacid/Ti0 2 ) into a 100mL four-necked flask, then add 10mL of hydrogen peroxide and 5g of diamine hydrogen phosphate under stirring state, and reflux under chloropropane 6 hours of reaction;
(2)反应结束,静置1-2小时后体系分成油、水相悬浮液;(2) After the reaction is completed, the system is divided into oil and water phase suspensions after standing for 1-2 hours;
(3)油层通过精留分离得到23.36mL的环氧氯丙烷备用。(3) The oil layer was separated to obtain 23.36 mL of epichlorohydrin for future use.
2.引发剂AlEt2Cl的合成:2. Synthesis of initiator AlEt 2 Cl:
(1)先在装有搅拌子的三口烧瓶中依次加入5g二乙基氯化铝,经分子筛干燥的50ml无水乙醚,在常温下搅拌10分钟;(1) earlier in the there-necked flask that stirring bar is housed, add 5g diethyl aluminum chloride successively, the 50ml anhydrous diethyl ether that is dried through molecular sieve, stir 10 minutes at normal temperature;
(2)将搅拌好的溶液用冰盐水降温至0℃,在滴加10mL环氧丙烷。通过控制滴加速率1-2滴/秒和保持在0-20℃的温度。反应30分钟,及时抽出挥发物得到粘稠状引发剂AlEt2Cl。(2) Cool the stirred solution to 0° C. with ice-brine, and add 10 mL of propylene oxide dropwise. By controlling the dropping rate to 1-2 drops/sec and maintaining the temperature at 0-20°C. After reacting for 30 minutes, the volatile matter was extracted in time to obtain viscous initiator AlEt 2 Cl.
3.聚环氧氯丙烷的合成:3. Synthesis of polyepichlorohydrin:
(1)在引发剂溶液中加入20mL事先制备好的环氧氯丙烷在冰水浴保持0℃温度反应8小时;(1) Add 20mL of pre-prepared epichlorohydrin to the initiator solution and keep the temperature at 0°C in an ice-water bath for 8 hours;
(2)再加入10ml含有氢氧化钠的甲醇溶液,在氮气的保护下于25℃聚合5小时后,终止反应;(2) Add 10ml of methanol solution containing sodium hydroxide again, and stop the reaction after polymerization at 25° C. for 5 hours under the protection of nitrogen;
(3)将反应混合物移至1000mL的分液漏斗中,用去离子水洗涤,静置分层。把有机层转移到1000ml蒸馏瓶中;(3) The reaction mixture was transferred to a 1000 mL separatory funnel, washed with deionized water, and allowed to stand to separate layers. Transfer the organic layer to a 1000ml distillation flask;
(4)然后将粗产物依次加入40-50mL,5%的盐酸,55-65mL5%碳酸氢钠,100mL蒸馏水洗至中性。再用旋转蒸发仪减压,加温至70-80℃下除去溶剂等小分子物质,得到聚环氧氯丙烷8.23g,产率为84.9%。(4) Then add 40-50 mL of 5% hydrochloric acid, 55-65 mL of 5% sodium bicarbonate and 100 mL of distilled water to wash the crude product until neutral. Then use a rotary evaporator to depressurize, heat to 70-80° C. to remove solvent and other small molecular substances, and obtain 8.23 g of polyepichlorohydrin with a yield of 84.9%.
具体实施方案:Specific implementation plan:
向100mL四口烧瓶中投入30g的氯丙烷和6.5g的催化剂(磷钨杂多酸盐/Ti02),再搅拌状态下加入10mL双氧水和5g磷酸氢二胺,于氯丙烷回流下反应6小时。反应结束,静置1-2小时后体系分成油、水相悬浮液;油层通过精留分离得到23.36mL的环氧氯丙烷备用。再在装有搅拌子的三口烧瓶中依次加入5g二乙基氯化铝,经分子筛干燥的50ml无水乙醚,在常温下搅拌10分钟,将搅拌好的溶液用冰盐水降温至0℃,在滴加10mL环氧丙烷。通过控制滴加速率1-2滴/秒和保持在0-20℃的温度下。反应30-50分钟,及时抽出挥发物,再溶液中加入20mL事先制备好的环氧氯丙烷在冰水浴保持0℃温度反应8小时。再加入10ml含有氢氧化钠的甲醇溶液,在氮气的保护下于25℃聚合5小时后终止反应。将反应混合物移至1000mL的分液漏斗中,用去离子水洗涤,静置分层。把有机层转移到1000ml蒸馏瓶中。然后将粗产物依次加入40-50mL,5%的盐酸,55-65mL5%碳酸氢钠,100mL蒸馏水洗至中性。再用旋转蒸发仪减压,加温至70-80℃下除去溶剂等小分子物质,得到聚环氧氯丙烷8.23g,产率为84.9%。Put 30g of chloropropane and 6.5g of catalyst (phosphotungstopolyacid/Ti0 2 ) into a 100mL four-neck flask, then add 10mL of hydrogen peroxide and 5g of diamine hydrogen phosphate under stirring, and react for 6 hours under reflux of chloropropane . After the reaction was completed, the system was separated into oil and water phase suspensions after standing for 1-2 hours; the oil layer was separated by essence to obtain 23.36 mL of epichlorohydrin for later use. Then add 5g of diethylaluminum chloride and 50ml of anhydrous diethyl ether dried over molecular sieves to the three-necked flask equipped with a stirring bar, and stir at room temperature for 10 minutes. Cool the stirred solution to 0°C with ice-salt water, Add 10 mL of propylene oxide dropwise. By controlling the dropping rate to 1-2 drops/second and maintaining the temperature at 0-20°C. React for 30-50 minutes, extract volatile matter in time, add 20 mL of pre-prepared epichlorohydrin to the solution, and keep the temperature at 0° C. in an ice-water bath for 8 hours. Add 10 ml of methanol solution containing sodium hydroxide, and polymerize at 25° C. for 5 hours under the protection of nitrogen to terminate the reaction. The reaction mixture was transferred to a 1000 mL separatory funnel, washed with deionized water, and allowed to stand to separate layers. Transfer the organic layer to a 1000ml retort. Then add 40-50 mL of the crude product, 5% hydrochloric acid, 55-65 mL of 5% sodium bicarbonate, and 100 mL of distilled water to wash until neutral. Then use a rotary evaporator to depressurize, heat to 70-80° C. to remove solvent and other small molecular substances, and obtain 8.23 g of polyepichlorohydrin with a yield of 84.9%.
实例1Example 1
向100mL四口烧瓶中投入30g的氯丙烷和6.5g的催化剂(磷钨杂多酸盐/Ti02),再搅拌状态下加入10mL双氧水和5g磷酸氢二胺,于氯丙烷回流下反应6小时。反应结束,静置1小时后体系分成油、水相悬浮液;油层通过精留分离得到23.36mL的环氧氯丙烷备用。再在装有搅拌子的三口烧瓶中依次加入5g二乙基氯化铝,经分子筛干燥的50ml无水乙醚,在常温下搅拌10分钟,将搅拌好的溶液用冰盐水降温至0℃,在滴加10mL环氧丙烷。通过控制滴加速率1滴/秒和保持在5℃的温度下。反应30分钟,及时抽出挥发物,再溶液中加入20mL事先制备好的环氧氯丙烷在冰水浴保持0℃温度反应8小时。再加入10ml含有氢氧化钠的甲醇溶液,在氮气的保护下于25℃聚合5小时后终止反应。将反应混合物移至1000mL的分液漏斗中,用去离子水洗涤,静置分层。把有机层转移到1000ml蒸馏瓶中。然后将粗产物依次加入40mL,5%的盐酸,55mL5%碳酸氢钠,100mL蒸馏水洗至中性。再用旋转蒸发仪减压,加温至70-80℃下除去溶剂等小分子物质,得到聚环氧氯丙烷8.15g,产率为82.9%。Put 30g of chloropropane and 6.5g of catalyst (phosphotungstopolyacid/Ti0 2 ) into a 100mL four-neck flask, then add 10mL of hydrogen peroxide and 5g of diamine hydrogen phosphate under stirring, and react for 6 hours under reflux of chloropropane . After the reaction was completed, the system was separated into oil and water phase suspensions after standing for 1 hour; the oil layer was separated by distillation to obtain 23.36 mL of epichlorohydrin for future use. Then add 5g of diethylaluminum chloride and 50ml of anhydrous diethyl ether dried over molecular sieves to the three-necked flask equipped with a stirring bar, and stir at room temperature for 10 minutes. Cool the stirred solution to 0°C with ice-salt water, Add 10 mL of propylene oxide dropwise. By controlling the dropping rate to 1 drop/sec and maintaining the temperature at 5 °C. After reacting for 30 minutes, the volatile matter was extracted in time, and then 20 mL of pre-prepared epichlorohydrin was added to the solution, and the temperature was kept at 0° C. in an ice-water bath for 8 hours to react. Add 10 ml of methanol solution containing sodium hydroxide, and polymerize at 25° C. for 5 hours under the protection of nitrogen to terminate the reaction. The reaction mixture was transferred to a 1000 mL separatory funnel, washed with deionized water, and allowed to stand to separate layers. Transfer the organic layer to a 1000ml retort. Then the crude product was sequentially added to 40mL, 5% hydrochloric acid, 55mL 5% sodium bicarbonate, and 100mL distilled water to wash until neutral. Then use a rotary evaporator to depressurize, heat to 70-80° C. to remove small molecular substances such as solvents, and obtain 8.15 g of polyepichlorohydrin with a yield of 82.9%.
实例2Example 2
向100mL四口烧瓶中投入30g的氯丙烷和6.5g的催化剂(磷钨杂多酸盐/Ti02),再搅拌状态下加入10mL双氧水和5g磷酸氢二胺,于氯丙烷回流下反应6小时。反应结束,静置1.5小时后体系分成油、水相悬浮液;油层通过精留分离得到23.36mL的环氧氯丙烷备用。再在装有搅拌子的三口烧瓶中依次加入5g二乙基氯化铝,经分子筛干燥的50ml无水乙醚,在常温下搅拌10分钟,将搅拌好的溶液用冰盐水降温至10℃,在滴加10mL环氧丙烷。通过控制滴加速率1滴/秒和保持在0℃的温度下。反应30分钟,及时抽出挥发物,再溶液中加入20mL事先制备好的环氧氯丙烷在冰水浴保持0℃温度反应8小时。再加入10ml含有氢氧化钠的甲醇溶液,在氮气的保护下于25℃聚合5小时后终止反应。将反应混合物移至1000mL的分液漏斗中,用去离子水洗涤,静置分层。把有机层转移到1000ml蒸馏瓶中。然后将粗产物依次加入45mL,5%的盐酸,60mL5%碳酸氢钠,100mL蒸馏水洗至中性。再用旋转蒸发仪减压,加温至70-80℃下除去溶剂等小分子物质,得到聚环氧氯丙烷8.00g,产率为80.5%。Put 30g of chloropropane and 6.5g of catalyst (phosphotungstic heteropoly acid salt/Ti02) into a 100mL four-neck flask, then add 10mL of hydrogen peroxide and 5g of diammonium hydrogen phosphate under stirring, and react under reflux of chloropropane for 6 hours. After the reaction was completed, the system was separated into oil and water phase suspensions after standing for 1.5 hours; the oil layer was separated by distillation to obtain 23.36 mL of epichlorohydrin for future use. Then add 5g of diethylaluminum chloride and 50ml of anhydrous diethyl ether dried by molecular sieves to the three-necked flask equipped with a stirring bar, and stir at room temperature for 10 minutes, then cool the stirred solution to 10°C with ice-salt water, Add 10 mL of propylene oxide dropwise. By controlling the dropping rate to 1 drop/sec and maintaining the temperature at 0 °C. After reacting for 30 minutes, the volatile matter was extracted in time, and 20 mL of pre-prepared epichlorohydrin was added to the solution, and the reaction was carried out at 0°C in an ice-water bath for 8 hours. Add 10 ml of methanol solution containing sodium hydroxide, and polymerize at 25° C. for 5 hours under the protection of nitrogen to terminate the reaction. The reaction mixture was transferred to a 1000 mL separatory funnel, washed with deionized water, and allowed to stand to separate layers. Transfer the organic layer to a 1000ml retort. Then the crude product was sequentially added to 45mL, 5% hydrochloric acid, 60mL 5% sodium bicarbonate, and 100mL distilled water to wash until neutral. Then use a rotary evaporator to depressurize, heat to 70-80° C. to remove solvent and other small molecular substances, and obtain 8.00 g of polyepichlorohydrin with a yield of 80.5%.
实例3Example 3
向100mL四口烧瓶中投入30g的氯丙烷和6.5g的催化剂(磷钨杂多酸盐/Ti02),再搅拌状态下加入10mL双氧水和5g磷酸氢二胺,于氯丙烷回流下反应6小时;反应结束,静置1-2小时后体系分成油、水相悬浮液;油层通过精留分离得到23.36mL的环氧氯丙烷备用。再在装有搅拌子的三口烧瓶中依次加入5g二乙基氯化铝,经分子筛干燥的50ml无水乙醚,在常温下搅拌10分钟,将搅拌好的溶液用冰盐水降温至0℃,在滴加10mL环氧丙烷。通过控制滴加速率1滴/秒和保持在20℃的温度下。反应30分钟,及时抽出挥发物,再溶液中加入20mL事先制备好的环氧氯丙烷在冰水浴保持0℃温度反应8小时。再加入10ml含有氢氧化钠的甲醇溶液,在常温下搅拌50分钟后终止反应。将反应混合物移至1000mL的分液漏斗中,用去离子水洗涤,静置分层。把有机层转移到1000ml蒸馏瓶中。然后将粗产物依次加入50mL,5%的盐酸,65mL5%碳酸氢钠,100mL蒸馏水洗至中性。再用旋转蒸发仪减压,加温至70-80℃下除去溶剂等小分子物质,得到聚环氧氯丙烷8.13g,产率为81.6%。Put 30g of chloropropane and 6.5g of catalyst (phosphotungstopolyacid/Ti0 2 ) into a 100mL four-neck flask, then add 10mL of hydrogen peroxide and 5g of diamine hydrogen phosphate under stirring, and react for 6 hours under reflux of chloropropane After the reaction is over, the system is divided into oil and water phase suspensions after standing for 1-2 hours; the oil layer is separated by essence to obtain 23.36mL of epichlorohydrin for subsequent use. Then add 5g of diethylaluminum chloride and 50ml of anhydrous diethyl ether dried over molecular sieves to the three-necked flask equipped with a stirring bar, and stir at room temperature for 10 minutes. Cool the stirred solution to 0°C with ice-salt water, Add 10 mL of propylene oxide dropwise. By controlling the dropping rate to 1 drop/sec and maintaining the temperature at 20 °C. After reacting for 30 minutes, the volatile matter was extracted in time, and then 20 mL of pre-prepared epichlorohydrin was added to the solution, and the temperature was kept at 0° C. in an ice-water bath for 8 hours to react. Add 10 ml of methanol solution containing sodium hydroxide, and stir at room temperature for 50 minutes to terminate the reaction. The reaction mixture was transferred to a 1000 mL separatory funnel, washed with deionized water, and allowed to stand to separate layers. Transfer the organic layer to a 1000ml retort. Then the crude product was sequentially added to 50 mL, 5% hydrochloric acid, 65 mL 5% sodium bicarbonate, and 100 mL distilled water to wash until neutral. Then use a rotary evaporator to depressurize, heat to 70-80° C. to remove small molecular substances such as solvents, and obtain 8.13 g of polyepichlorohydrin with a yield of 81.6%.
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