CN103420836A - 含氟低碳脂肪酸的提纯方法 - Google Patents
含氟低碳脂肪酸的提纯方法 Download PDFInfo
- Publication number
- CN103420836A CN103420836A CN2012101584928A CN201210158492A CN103420836A CN 103420836 A CN103420836 A CN 103420836A CN 2012101584928 A CN2012101584928 A CN 2012101584928A CN 201210158492 A CN201210158492 A CN 201210158492A CN 103420836 A CN103420836 A CN 103420836A
- Authority
- CN
- China
- Prior art keywords
- acetic acid
- dichloro acetic
- ester
- dichloro
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 24
- 229910052799 carbon Inorganic materials 0.000 title claims description 12
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 title description 10
- 239000011737 fluorine Substances 0.000 title description 10
- 229910052731 fluorine Inorganic materials 0.000 title description 10
- 239000002253 acid Substances 0.000 title description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000006243 chemical reaction Methods 0.000 claims abstract description 11
- JXTHNDFMNIQAHM-UHFFFAOYSA-N dichloroacetic acid Chemical compound OC(=O)C(Cl)Cl JXTHNDFMNIQAHM-UHFFFAOYSA-N 0.000 claims abstract 15
- PBWZKZYHONABLN-UHFFFAOYSA-M difluoroacetate Chemical compound [O-]C(=O)C(F)F PBWZKZYHONABLN-UHFFFAOYSA-M 0.000 claims abstract 3
- HXELGNKCCDGMMN-UHFFFAOYSA-N [F].[Cl] Chemical group [F].[Cl] HXELGNKCCDGMMN-UHFFFAOYSA-N 0.000 claims abstract 2
- -1 dichloro acetic acid dimethyl benzyl ethanol ester Chemical class 0.000 claims description 11
- 238000000746 purification Methods 0.000 claims description 9
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical group F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims description 2
- 229910000040 hydrogen fluoride Inorganic materials 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 229960005215 dichloroacetic acid Drugs 0.000 claims 8
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims 6
- 239000003153 chemical reaction reagent Substances 0.000 claims 4
- 125000001153 fluoro group Chemical group F* 0.000 claims 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims 2
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 claims 2
- XJHCXCQVJFPJIK-UHFFFAOYSA-M caesium fluoride Chemical compound [F-].[Cs+] XJHCXCQVJFPJIK-UHFFFAOYSA-M 0.000 claims 2
- 125000004432 carbon atom Chemical group C* 0.000 claims 2
- 150000002148 esters Chemical class 0.000 claims 2
- GNOIPBMMFNIUFM-UHFFFAOYSA-N hexamethylphosphoric triamide Chemical compound CN(C)P(=O)(N(C)C)N(C)C GNOIPBMMFNIUFM-UHFFFAOYSA-N 0.000 claims 2
- 229910052757 nitrogen Inorganic materials 0.000 claims 2
- 239000002798 polar solvent Substances 0.000 claims 2
- DCKVNWZUADLDEH-UHFFFAOYSA-N sec-butyl acetate Chemical compound CCC(C)OC(C)=O DCKVNWZUADLDEH-UHFFFAOYSA-N 0.000 claims 2
- PUZPDOWCWNUUKD-UHFFFAOYSA-M sodium fluoride Chemical compound [F-].[Na+] PUZPDOWCWNUUKD-UHFFFAOYSA-M 0.000 claims 2
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical compound O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 claims 2
- UXFQFBNBSPQBJW-UHFFFAOYSA-N 2-amino-2-methylpropane-1,3-diol Chemical compound OCC(N)(C)CO UXFQFBNBSPQBJW-UHFFFAOYSA-N 0.000 claims 1
- XLKJPQKUATYFQJ-UHFFFAOYSA-N 2-methylpropyl 2,2-dichloroacetate Chemical compound CC(C)COC(=O)C(Cl)Cl XLKJPQKUATYFQJ-UHFFFAOYSA-N 0.000 claims 1
- UQQSGXRKRFDREY-UHFFFAOYSA-N 3-methylbutyl 2,2-dichloroacetate Chemical compound CC(C)CCOC(=O)C(Cl)Cl UQQSGXRKRFDREY-UHFFFAOYSA-N 0.000 claims 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims 1
- MHABMANUFPZXEB-UHFFFAOYSA-N O-demethyl-aloesaponarin I Natural products O=C1C2=CC=CC(O)=C2C(=O)C2=C1C=C(O)C(C(O)=O)=C2C MHABMANUFPZXEB-UHFFFAOYSA-N 0.000 claims 1
- 125000005257 alkyl acyl group Chemical group 0.000 claims 1
- SMWDFEZZVXVKRB-UHFFFAOYSA-N anhydrous quinoline Natural products N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 claims 1
- JFDZBHWFFUWGJE-UHFFFAOYSA-N benzenecarbonitrile Natural products N#CC1=CC=CC=C1 JFDZBHWFFUWGJE-UHFFFAOYSA-N 0.000 claims 1
- VAJCQZBNDWEQRU-UHFFFAOYSA-N benzyl 2,2-dichloroacetate Chemical compound ClC(Cl)C(=O)OCC1=CC=CC=C1 VAJCQZBNDWEQRU-UHFFFAOYSA-N 0.000 claims 1
- MASXONVJEAXEIV-UHFFFAOYSA-N butyl 2,2-dichloroacetate Chemical compound CCCCOC(=O)C(Cl)Cl MASXONVJEAXEIV-UHFFFAOYSA-N 0.000 claims 1
- IWYBVQLPTCMVFO-UHFFFAOYSA-N ethyl 2,2-dichloroacetate Chemical compound CCOC(=O)C(Cl)Cl IWYBVQLPTCMVFO-UHFFFAOYSA-N 0.000 claims 1
- 125000003709 fluoroalkyl group Chemical group 0.000 claims 1
- 235000011187 glycerol Nutrition 0.000 claims 1
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Substances C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 claims 1
- 239000011261 inert gas Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- HKMLRUAPIDAGIE-UHFFFAOYSA-N methyl 2,2-dichloroacetate Chemical group COC(=O)C(Cl)Cl HKMLRUAPIDAGIE-UHFFFAOYSA-N 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims 1
- UIFCHGLUUASAAI-UHFFFAOYSA-N pentyl 2,2-dichloroacetate Chemical compound CCCCCOC(=O)C(Cl)Cl UIFCHGLUUASAAI-UHFFFAOYSA-N 0.000 claims 1
- FALZSEYHTLDSIT-UHFFFAOYSA-N phenyl 2,2-dichloroacetate Chemical compound ClC(Cl)C(=O)OC1=CC=CC=C1 FALZSEYHTLDSIT-UHFFFAOYSA-N 0.000 claims 1
- SUSQOBVLVYHIEX-UHFFFAOYSA-N phenylacetonitrile Chemical compound N#CCC1=CC=CC=C1 SUSQOBVLVYHIEX-UHFFFAOYSA-N 0.000 claims 1
- NROKBHXJSPEDAR-UHFFFAOYSA-M potassium fluoride Chemical compound [F-].[K+] NROKBHXJSPEDAR-UHFFFAOYSA-M 0.000 claims 1
- 238000002360 preparation method Methods 0.000 claims 1
- JBTISLVNJCYZCH-UHFFFAOYSA-N propan-2-yl 2,2-dichloroacetate Chemical compound CC(C)OC(=O)C(Cl)Cl JBTISLVNJCYZCH-UHFFFAOYSA-N 0.000 claims 1
- GRJJQCWNZGRKAU-UHFFFAOYSA-N pyridin-1-ium;fluoride Chemical compound F.C1=CC=NC=C1 GRJJQCWNZGRKAU-UHFFFAOYSA-N 0.000 claims 1
- 235000013024 sodium fluoride Nutrition 0.000 claims 1
- 239000011775 sodium fluoride Substances 0.000 claims 1
- FOLRKRMAFDGZRR-UHFFFAOYSA-N tert-butyl 2,2-dichloroacetate Chemical compound CC(C)(C)OC(=O)C(Cl)Cl FOLRKRMAFDGZRR-UHFFFAOYSA-N 0.000 claims 1
- 229940120124 dichloroacetate Drugs 0.000 abstract 1
- 239000012025 fluorinating agent Substances 0.000 abstract 1
- 238000001308 synthesis method Methods 0.000 abstract 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 12
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 12
- DTQVDTLACAAQTR-UHFFFAOYSA-N Trifluoroacetic acid Chemical compound OC(=O)C(F)(F)F DTQVDTLACAAQTR-UHFFFAOYSA-N 0.000 description 12
- 238000003756 stirring Methods 0.000 description 12
- 238000009835 boiling Methods 0.000 description 9
- 235000014113 dietary fatty acids Nutrition 0.000 description 9
- 229930195729 fatty acid Natural products 0.000 description 9
- 239000000194 fatty acid Substances 0.000 description 9
- PBWZKZYHONABLN-UHFFFAOYSA-N difluoroacetic acid Chemical compound OC(=O)C(F)F PBWZKZYHONABLN-UHFFFAOYSA-N 0.000 description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 238000004821 distillation Methods 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 239000012043 crude product Substances 0.000 description 5
- 238000010992 reflux Methods 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 230000006837 decompression Effects 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 4
- 238000001291 vacuum drying Methods 0.000 description 4
- 238000010792 warming Methods 0.000 description 4
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- SBSKRVZFWQPJID-UHFFFAOYSA-N 2,2-difluorobutanoic acid Chemical compound CCC(F)(F)C(O)=O SBSKRVZFWQPJID-UHFFFAOYSA-N 0.000 description 1
- PMWGIVRHUIAIII-UHFFFAOYSA-N 2,2-difluoropropanoic acid Chemical compound CC(F)(F)C(O)=O PMWGIVRHUIAIII-UHFFFAOYSA-N 0.000 description 1
- RTAOVOAKTDWSFE-UHFFFAOYSA-N C(CCC)(=O)O.[F] Chemical compound C(CCC)(=O)O.[F] RTAOVOAKTDWSFE-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- PZSXCNWLLFEOPM-UHFFFAOYSA-N [F].C(CC)(=O)O Chemical compound [F].C(CC)(=O)O PZSXCNWLLFEOPM-UHFFFAOYSA-N 0.000 description 1
- CPZZKNJKGDORHK-UHFFFAOYSA-N [K].OC(=O)C(F)F Chemical compound [K].OC(=O)C(F)F CPZZKNJKGDORHK-UHFFFAOYSA-N 0.000 description 1
- CXFQOWRZKBPHHQ-UHFFFAOYSA-N [Na].FC(C(=O)O)F Chemical compound [Na].FC(C(=O)O)F CXFQOWRZKBPHHQ-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- FBCCMZVIWNDFMO-UHFFFAOYSA-N dichloroacetyl chloride Chemical compound ClC(Cl)C(Cl)=O FBCCMZVIWNDFMO-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 150000002222 fluorine compounds Chemical class 0.000 description 1
- QEWYKACRFQMRMB-UHFFFAOYSA-N fluoroacetic acid Chemical compound OC(=O)CF QEWYKACRFQMRMB-UHFFFAOYSA-N 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- UYCAUPASBSROMS-UHFFFAOYSA-M sodium;2,2,2-trifluoroacetate Chemical compound [Na+].[O-]C(=O)C(F)(F)F UYCAUPASBSROMS-UHFFFAOYSA-M 0.000 description 1
- UYCAUPASBSROMS-AWQJXPNKSA-M sodium;2,2,2-trifluoroacetate Chemical compound [Na+].[O-][13C](=O)[13C](F)(F)F UYCAUPASBSROMS-AWQJXPNKSA-M 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
本发明公开了一种合成二氟乙酸酯的方法。该方法在压力容器下,采用二氯乙酸酯在无水、较高温度条件下,与氟代试剂进行氟氯交换反应,产物选择性达到95%以上。
Description
技术领域
本发明涉及含氟低碳脂肪酸的一种提纯方法。
背景技术
CN97109774提供了一种有机磺酸的提纯方法,采用pH为-0.57~7酸水处理后,将水相分离。
US2011065995公开了一种合成和分离二氟乙酸的方法,该方法以二氯乙酰氯和氟化氢为原料,在铬基催化剂存在下的气相合成二氟乙酰氟和二氟乙酸,并利用分馏塔将二氟乙酸分离出来。
CN101967091公开了一种提纯有机酸的方法,母液先经过超滤或微滤形成渗透液,再经活性炭脱色,最后用阴、阳离子交换树脂除杂,提高了有机酸的纯度。
CN1131139公开了一种利用精馏的方式提纯乙酸的方法,精馏柱塔板数不低于30,回流比不低于4,真空度在40~760mmHg,得到高纯度的乙酸。
CN1944374公开了一种醋酸的提纯方法,粗品经过吸收和气提两步骤后,经过脱轻相、脱水、脱重相、脱废酸处理后得到高产率的醋酸。
上述的提纯方法都存在各种问题,其中最主要的就是都不能严格地控制产品的含水量。采用分液、离子交换的方式,得到产品的含水量都较大。采用塔分离的方式由于含氟酸和水共沸的原因对设备要求较高,工艺上也较难控制。
发明内容
本发明的目的是提供一种含氟低碳脂肪酸的提纯方法。
含氟低碳脂肪酸的提纯方法是将含氟低碳脂肪酸粗产品经过加热蒸出低沸点杂质,加热温度为30~100℃,然后趁热过滤,用0.5~3当量的无机强碱处理,生成的含氟低碳脂肪酸盐经干燥处理,使之含水量不超过1‰,再用0.5~5当量的高浓度强酸酸化。
所述的含氟低碳脂肪酸是氟乙酸、二氟乙酸、三氟乙酸、氟丙酸、二氟丙酸、三氟丙酸、氟丁酸、二氟丁酸,以及三氟丁酸。加热温度为30~100℃,优选为50~80℃。无机强碱是氢氧化锂、氢氧化钠、氢氧化钾。高浓度强酸为98%的浓硫酸。含氟低碳脂肪酸和无机强碱的摩尔比是1∶0.5~3,优选为1∶1~2。含氟低碳脂肪酸盐与高浓度强酸的摩尔比为1∶0.5~5,优选为1∶1~4。
具体实施方式
实施例1
向500ml四口烧瓶中加入100g粗品二氟乙酸,升温至80℃,常压精馏掉低沸杂质。降温至0~10℃,滴加100g40%质量分数NaOH水溶液,滴毕搅拌反应1小时。减压蒸掉大部分水,加入200ml甲苯,升温回流至分水器基本无水分出。物料降温至5℃搅拌1小时,过滤。收集白色或淡黄色晶体,真空干燥箱中70℃烘4~6小时,水份检测<0.1%。(滤液回收套用收率可达100%)
500ml四口烧瓶中加入98%浓硫酸300g,搅拌,冰浴控温10~20℃。缓慢、分批加入无水二氟乙酸钠118g(1mol),加毕,撤冰浴。缓慢升温,75mmHg减压精馏得无水二氟乙酸(88.3g,收率92%)。
实施例2
向500ml四口烧瓶中加入100g粗品二氟乙酸,升温至80℃,常压精馏掉低沸杂质。降温至0~10℃,滴加140g40%质量分数KOH水溶液,滴毕搅拌反应1小时。减压蒸掉大部分水,加入200ml甲苯,升温回流至分水器基本无水分出。物料降温至5℃搅拌1小时,过滤。收集白色或淡黄色晶体,真空干燥箱中70℃烘4~6小时,水份检测<0.1%。(滤液回收套用收率可达100%)
500ml四口烧瓶中加入98%浓硫酸300g,搅拌,冰浴控温10~20℃。缓慢、分批加入无水二氟乙酸钾134g(1mol),加毕,撤冰浴。缓慢升温,常压精馏收集132~134℃馏分(79.7g,收率83%)。
实施例3
向500ml四口烧瓶中加入58g粗品三氟乙酸,升温至40℃,常压精馏掉低沸杂质。降温至0~10℃,滴加50g40%质量分数NaOH水溶液,滴毕搅拌反应1小时。减压蒸掉大部分水,加入200ml甲苯,升温回流至分水器基本无水分出。物料降温至5℃搅拌1小时,过滤。收集白色或淡黄色晶体,真空干燥箱中70℃烘4~6小时,水份检测<0.1%。(滤液回收套用收率可达100%)
250ml四口烧瓶中加入98%浓硫酸150g,搅拌,冰浴控温5~10℃。缓慢、分批加入无水三氟乙酸钠68g(0.5mol),加毕,撤冰浴。缓慢升温,常压精馏,收集72~73℃馏分(53g,收率93%)。
实施例4
向500ml四口烧瓶中加入65g粗品三氟丙酸,升温至80℃,常压精馏掉低沸杂质。降温至10~20℃,滴加50g40%质量分数NaOH水溶液,滴毕搅拌反应1小时。减压蒸掉大部分水,加入200ml甲苯,升温回流至分水器基本无水分出。物料降温至5℃搅拌1小时,过滤。收集白色或淡黄色晶体,真空干燥箱中70℃烘4~6小时,水份检测<0.1%。(滤液回收套用收率可达100%)
向250ml四口烧瓶中加入98%浓硫酸150g,搅拌,冰浴控温5~10℃。缓慢、分批加入无水三氟丙酸钠75g(0.5mol),加毕,撤冰浴。缓慢升温,75mmHg减压精馏收集三氟丙酸(54.4g,收率85%)。
Claims (8)
2.根据权利要求1的方法,其特征在于所述的二氯乙酸酯为二氯乙酸甲酯、二氯乙酸乙酯、二氯乙酸正丙酯、二氯乙酸异丙酯、二氯乙酸正丁酯、二氯乙酸仲丁酯、二氯乙酸异丁酯、二氯乙酸叔丁酯、二氯乙酸正戊酯、二氯乙酸异戊酯、二氯乙酸丁酯、二氯乙酸苯酯、二氯乙酸苄酯、二氯乙酸二甲基苄基原酯、二氯乙酸二甲基苯乙基原酯、二氯乙酸二甲基苄基乙醇酯。
3.根据权利要求1的方法,其特征在于所述的氟代试剂为氟化氢、氟化钠、氟化钾、氟化铯、氟代烷基磺酰氟、烷基酰氟、吡啶-氟化氢络合液。
4.根据权利要求1的方法,其特征在于二氯乙酸酯与氟代试剂的摩尔配比为1∶0.5~5.0,优选为1∶1.0~4.0。
5.根据权利要求1的方法,其特征在于所述的极性溶剂为N,N-二甲基甲酰胺(DMF)、二甲基亚砜(DMSO)、N,N-二甲基乙酰胺(DMAC)、乙二醇、1,2-丙二醇、1,3-丙二醇、甘油、二乙二醇、N-甲基吡咯烷酮(NMP)、环丁砜(TMS)、苄基腈、吡啶基腈、六甲基磷酸三酰胺(HMPA)、1,3-二甲基-2-咪唑喹啉酮(DMI)。
6.根据权利要求1的方法,其特征在于反应体系含水量不超过200ppm,优选为不超过100ppm。
7.根据权利要求1的方法,其特征在于反应温度从0℃到350℃,优选为80℃到300℃。
8.根据权利要求1的方法,其特征在于所述的惰性气体为氮气。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101584928A CN103420836A (zh) | 2012-05-21 | 2012-05-21 | 含氟低碳脂肪酸的提纯方法 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101584928A CN103420836A (zh) | 2012-05-21 | 2012-05-21 | 含氟低碳脂肪酸的提纯方法 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103420836A true CN103420836A (zh) | 2013-12-04 |
Family
ID=49646268
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012101584928A Pending CN103420836A (zh) | 2012-05-21 | 2012-05-21 | 含氟低碳脂肪酸的提纯方法 |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103420836A (zh) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1447787A (zh) * | 2000-08-23 | 2003-10-08 | 纳幕尔杜邦公司 | 氟代烷酸的纯化方法 |
| CN1944376A (zh) * | 2006-10-10 | 2007-04-11 | 中昊晨光化工研究院 | 一种全氟辛酸的提纯方法 |
| CN101878189A (zh) * | 2007-09-28 | 2010-11-03 | 罗地亚管理公司 | 回收氟代羧酸的方法 |
| US20110065955A1 (en) * | 2008-03-19 | 2011-03-17 | Rhodia Operations | Method For Preparing Difluoroacetic Acid and Salts Thereof |
-
2012
- 2012-05-21 CN CN2012101584928A patent/CN103420836A/zh active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1447787A (zh) * | 2000-08-23 | 2003-10-08 | 纳幕尔杜邦公司 | 氟代烷酸的纯化方法 |
| CN1944376A (zh) * | 2006-10-10 | 2007-04-11 | 中昊晨光化工研究院 | 一种全氟辛酸的提纯方法 |
| CN101878189A (zh) * | 2007-09-28 | 2010-11-03 | 罗地亚管理公司 | 回收氟代羧酸的方法 |
| US20110065955A1 (en) * | 2008-03-19 | 2011-03-17 | Rhodia Operations | Method For Preparing Difluoroacetic Acid and Salts Thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| ES2615053T3 (es) | Proceso para la preparación de ácido 2,5-furano-dicarboxílico | |
| CN104402780A (zh) | 4,4’-二氯二苯砜的合成工艺 | |
| CN111099566A (zh) | 一种联产双氯磺酰亚胺酸和双氟磺酰亚胺锂的制备方法 | |
| US8633334B2 (en) | Method for preparing trifluoromethanesulphinic acid | |
| CN103012183A (zh) | N,n-二乙基甲酰胺的制备方法 | |
| CN103694118A (zh) | 一种三氟乙酸乙酯及其中间体的制备方法 | |
| CN101475482B (zh) | 一种丙酮二羧酸二甲酯的制备方法 | |
| US20150203449A1 (en) | Method for preparing a sulfonimide compound and salts thereof | |
| KR101421332B1 (ko) | 디플루오로아세트산의 제조 방법 | |
| CN103420836A (zh) | 含氟低碳脂肪酸的提纯方法 | |
| CN104829465A (zh) | 一种4-异丙氨基-1-丁醇的制备方法 | |
| CN115894229A (zh) | 一种己二酸单乙酯选择性合成工艺 | |
| CN103254074B (zh) | 一种二氟乙酸乙酯及其中间体的制备方法 | |
| US4215056A (en) | Formation, purification and recovery of phthalic anhydride | |
| US4215055A (en) | Production of liquid ortho-phthalic acid and its conversion to high _purity phthalic anhdyride | |
| US9394225B2 (en) | Method for processing fluoric acid | |
| ES2963357T3 (es) | Proceso para la producción de peróxidos de diacilo | |
| EP2522652B1 (en) | Method for producing difluoroacetic acid ester | |
| CN106966850A (zh) | 一种高纯度1‑甲基萘的制备方法 | |
| CN114477239A (zh) | 一种制备六氟磷酸锂的方法 | |
| CN103420825A (zh) | 二氟乙酸酯的合成方法 | |
| JP5811671B2 (ja) | フルオロアルカンスルホン酸の製造方法 | |
| KR102206139B1 (ko) | 탄산디페닐의 제조 방법, 그 제조 방법에 의해 얻어지는 탄산디페닐, 그 탄산디페닐로부터 제조되는 폴리카보네이트, 탄산디페닐 제조용 촉매, 그 촉매의 제조 방법, 촉매의 회수·재이용 방법 | |
| KR20150119372A (ko) | 이온성 액체의 제조 공정 | |
| EP3983369B1 (en) | Process for the production of diacyl peroxides |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20131204 |