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    • 31. 发明授权
    • Sulphonic fluorinated ionomers
    • 磺化氟化离聚物
    • US06706834B2
    • 2004-03-16
    • US09922741
    • 2001-08-07
    • Ivan WlassicsVito Tortelli
    • Ivan WlassicsVito Tortelli
    • C08F11418
    • H01M8/1053C08F8/18C08F214/26C08F214/265C08J5/2237C08J2327/18H01M8/1023H01M8/1025H01M8/1039H01M8/106H01M8/1072H01M8/1088H01M2300/0082Y02P70/56
    • Sulphonic fluorinated ionomers crosslinked by radical crosslinking of: A) crosslinkable sulphonic fluorinated ionomers, having equivalent weight 380-1300 g/eq and comprising: from 48% to 85% by moles of monomeric units deriving from tetrafluoroethylene (TFE); from 15% to 47% by moles of fluorinated monomeric units containing sulphonyl groups —SO2F; from 0.01% to 5% by moles of monomeric units deriving from a bis-olefin of formula: wherein: m=2-10, preferably 4-8; R1, R2, R5, R6, equal to or different from each other, are H or C1-C5 alkyl groups; B) a fluorinated compound as crosslinking radical initiator; C) a fluorinated bis-olefin of structure (I) as crosslinking agent; the radical crosslinking being carried out at a temperature in the range 250° C.-310° C., preferably 260° C.-300° C.
    • 通过自由基交联交联的磺化氟化离聚物:A)具有当量重量380-1300g / eq的可交联磺化氟化离聚物,并且包含:衍生自四氟乙烯(TFE)的48%至85%摩尔的单体单元; 15%至 含有磺酰基-SO2F的氟化单体单元47% 衍生自下式的双烯烃的单体单元的0.01%至5%摩尔:其中:m = 2-10,优选4-8; R 1,R 2,R 5,R 6等于或不同的是H或C 1 -C 5烷基; B)作为交联自由基引发剂的氟化化合物; C)结构(I)的氟化双烯烃作为交联剂 自由基交联在250℃-310℃,优选260℃-300℃的温度下进行。
    • 38. 发明授权
    • Addition reaction to fluoroallylfluorosulfate
    • 氟代氟代硫酸盐的加成反应
    • US08268947B2
    • 2012-09-18
    • US12745869
    • 2008-12-17
    • Giuseppe MarchionniVito Tortelli
    • Giuseppe MarchionniVito Tortelli
    • C08F16/24
    • C07D317/42C07C41/24C07C51/58C07C303/24C08F214/18C08F259/08C07C59/135C07C305/26C07C43/126
    • The invention pertains to a process for preparing compounds of formula (I-A) or (I-B) here below: by reaction of perfluoroallylfluorosulfate (FAFS) of formula (II): with at least one hypofluorite of formula (II-A) or (II-B): wherein: RF in formulae (I-A) and (II-A) is a monovalent fluorocarbon C1-C20 group, optionally comprising oxygen catenary atoms, optionally comprising functional groups comprising heteroatoms (e.g. —SO2F groups); R′F in formulae (I-B) and (II-B) is a divalent fluorocarbon C1-C6 group, preferably a group of formula wherein X1 and X2, equal to or different from each other, are independently a fluorine atom or a C1-C3 fluorocarbon group. The FAFS-hypofluorite adducts of formulae (I-A) and (I-B) can be produced with high selectivity so as to access useful intermediates which can further be reacted taking advantage of the un-modified fluorosulfate group chemistry.
    • 本发明涉及如下制备式(IA)或(IB)化合物的方法:通过式(II)的全氟代氟代硫酸盐(FAFS)与至少一种式(II-A)的次氟酸盐或(II- B):其中:式(IA)和(II-A)中的RF是任选包含氧连接原子的任选包含杂原子的官能团(例如-SO 2 F基团)的单价碳氟化合物C1-C20基团; 式(IB)和(II-B)中的R'F是二价碳氟化合物C1-C6基团,优选下式的基团:其中X1和X2彼此相同或不同,分别为氟原子或C1- C3碳氟化合物。 可以高选择性地制备式(I-A)和(I-B)的FAFS-次氟化物加合物,以便获得可利用未改性的氟硫酸盐基团化学进一步反应的有用的中间体。
    • 39. 发明授权
    • Process for preparing fluorohalogenethers
    • 制备氟卤醚的方法
    • US07208638B2
    • 2007-04-24
    • US11044022
    • 2005-01-28
    • Vito TortelliStefano MillefantiPierangelo Calini
    • Vito TortelliStefano MillefantiPierangelo Calini
    • C07C41/18
    • C07C41/48C07C43/313C07C43/315
    • A process for preparing (per)fluorohalogenethers having general formula: wherein: A and A′, equal to or different from each other, are selected among Cl, Br and H; m=1, 2; n=0, 1; R′ is a C1 to C3 (per)fluoroalkyl substituent; R is a (per)fluoropolyether substituent; z and z′ are 1 or zero, X1=F, CF3; by reaction of carbonyl compounds having formula: (R′)n—C(O)(F)q(CFX1(CF2)z(CH2)z′OR1)  (II) wherein: R′ and n are as above; q=0, 1; X1=F or CF3; z=0 or 1; R1 is a (per)fluoropolyether substituent; in liquid phase, with elemental fluorine and with olefinic compounds of formula: CAF=CA′F2   (III) wherein A and A′ are as above, at temperatures from −120° C. to −20° C., preferably from −100° C. to −40° C.
    • 制备具有以下通式的(全)氟卤醚的方法:其中:A和A'彼此相同或不同,选自Cl,Br和H; m = 1,2; n = 0,1; R'是C 3〜C 3(全)氟烷基取代基的C 1〜C 3。 R是一个(全)氟聚醚取代基; z和z'为1或0,X 1 = F,CF 3 3; 通过具有下式的羰基化合物的反应:<?in-line-formula description =“In-line formula”end =“lead”→(R')n -C(O)(F) (CF 2)(CF 2)2(CF 2)2(CF 2)(CH 2)其中:R'和n分别为 以上; q = 0,1; X 1 = F或CF 3 N; z = 0或1; R 1是一个(全)氟聚醚取代基; 在液相中使用元素氟和具有下式的烯属化合物:<?in-line-formula description =“In-line Formulas”end =“lead”?> CAF = CA'F 2 III)<?in-line-formula description =“In-line Formulas”end =“tail”?>其中A和A'如上所述,在-120℃至-20℃的温度下,优选地 -100°C至-40°C
    • 40. 发明申请
    • Process for preparing fluorohalogenethers
    • 制备氟卤醚的方法
    • US20070004940A1
    • 2007-01-04
    • US11044021
    • 2005-01-28
    • Vito TortelliStefano MillefantiPierangelo Calini
    • Vito TortelliStefano MillefantiPierangelo Calini
    • C07C43/02C07C43/20
    • C07C43/123C07C41/01C07C43/126
    • A process for preparing (per)fluorohalogenethers having general formula: wherein: A and A′, equal to our different from each other, are selected among Cl, Br, H; m=1, 2; n=0, 1; R1 is a fluorinated substituent, preferably perfluorinated, selected from the following groups: C1-C20 linear or branched alkylic; C3-C7 cycloalkylic; aromatic, C6-C10 arylalkyl; heterocyclic or C5-C10-alkylheterocyclic; preferably perfluoroalkyl; R′ is as defined in the application; by reaction of carbonyl compounds having formula: wherein: R1 and n are as above; u=0, 1; R′ is as defined in the application; in liquid phase, with elemental fluorine and with olefinic compounds of formula: CAF═CA′F2  (III) wherein A and A′ are as above, at temperatures from −120° C. to −20° C., preferably from −100° C. to −40° C., optionally in the presence of an inert solvent under the reaction conditions.
    • 制备具有以下通式的(全)氟卤醚的方法:其中:A和A'等于我们彼此不同,选自Cl,Br,H; m = 1,2; n = 0,1; R 1是优选全氟化的氟化取代基,其选自以下基团:C 1 -C 20直链或支链烷基; C 3 -C 7环烷基; 芳族C 6 -C 10芳基烷基; 杂环或C 5 -C 10 - 烷基杂环; 优选全氟烷基; R'如申请中所定义; 通过具有下式的羰基化合物的反应:其中:R 1和n如上所述; u = 0,1; R'如申请中所定义; 在液相中使用元素氟和具有下式的烯属化合物:<?in-line-formula description =“In-line Formulas”end =“lead”?> CAF-CA'F 2 III)<?in-line-formula description =“In-line Formulas”end =“tail”?>其中A和A'如上所述,在-120℃至-20℃的温度下,优选地 -100℃至-40℃,任选在惰性溶剂存在下,在反应条件下进行。