Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G73/00—Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
  • C08G73/06—Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
  • C08G73/08—Polyhydrazides; Polytriazoles; Polyaminotriazoles; Polyoxadiazoles
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
  • C08F214/18—Monomers containing fluorine
  • C08F214/22—Vinylidene fluoride
  • C08F214/222—Vinylidene fluoride with fluorinated vinyl ethers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F8/00—Chemical modification by after-treatment
  • C08F8/30—Introducing nitrogen atoms or nitrogen-containing groups
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F2800/00—Copolymer characterised by the proportions of the comonomers expressed
  • C08F2800/10—Copolymer characterised by the proportions of the comonomers expressed as molar percentages
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F2810/00—Chemical modification of a polymer
  • C08F2810/40—Chemical modification of a polymer taking place solely at one end or both ends of the polymer backbone, i.e. not in the side or lateral chains

Definitions

• Fluoropolymers are typically manufactured in a free radical emulsion, solution or suspension polymerization process from fluorooiefins and fiuorovinyl ethers.
• the types of fluoropolymers that have been made are thus limited to those that can be manufactured by such processes.
• the 1 ,3-dtpolar cycloaddJtion between an azide and an alkyne to result in a 1 ,2,3-triazole is referred to as the Huisgen reaction, The reaction is among those also referred to as "Click Chemistry" H. C. KoIb. M. G. Finn and K. B. Sharpless Angewandte Chemie International Edition 40( 11 ), 2004-2021 (2001 ).
• the present invention is a new copolycondensation polymerization process for the manufacture of fluorinated copolymers. Accordingly an aspect of the present invention is a process for the manufacture of fluorinated copolymers comprising:
• R is selected from the group consisting of i) a C 3 ⁇ C10 fiuoroalkylene group, ii) a C 3 - C 10 fluoroalkoxylene group, iii) a substituted aryl group, iv) an oligomer comprising copoiymerized units of vinyiidene fluoride and perfluoro(methyl vinyl ether), v) an oligomer comprising copoiymerized units of vinyiidene fluoride and hexafluoropropylene, vi) an oligomer comprising copoiymerized units of tetrafluoroethyiene and perf!uoro ⁇ methyl vinyl ether), and vii) an oligomer comprising copotymerized units of tetrafluoroethyiene and a hydrocarbon olefin; C) adding to the reactor a tele
• the present invention ⁇ s directed to a copolycondensation polymerization process for the manufacture of fluorinated copolymers.
• copolycondensation condensation between reactants leading to new products.
• a telecheiic fluorinated bisazido compound is reacted with a telecheiic diyne or dinitrile (dicyano) compound in the presence of a copper(l) halide catalyst.
• the copper(l) halide may be generated in-situ by reaction of a copper(il) halide with a reducing agent such as ascorbic acid.
• the polymerization medium is a nitrogen-based ligand such as a bidentate nitrogen complexing agent (e.g. 2,2'-bipyrjdine), hexamethylene tetramine, 2-pyrtdinecarbaldehyde alkylimine, muttidendate linear poiyamines, 1 ,10-phenanthroiine, and 1 , 1 ,4,7, 1O 1 10-hexamethyltriethylenetetramine.
• a bidentate nitrogen complexing agent e.g. 2,2'-bipyrjdine
• oligomers i.e. low molecular weight copolymers
• VF 2 or TFE is iodine transfer copolymerized in the presence of 1-(CF 2 ) 4 -I.
• the resulting copolymers are then ethylenated and eventually reacted with Nalsb to yield the diazide telechelic oligomers.
• Such oligomers preferably contain 10 to 60 mole percent perfluoro(methyl vinyl ether).
• the oligomers have a number average molecular weight of 1000 to 25,000, preferably 1200 to 12,000, most preferably 1500 to 5000,
• Telecheltc diyne or di ⁇ it ⁇ le (di ⁇ ya ⁇ o) compounds that may be employed in the process of this invention include, but are not limited to NC-(CF 2 )n ⁇ CN (n - 2-20), see US 2,515,246 and Journal of Industrial and Engineering Chemistry (Washington, D.
• the polymerization reaction may be run at a temperature between 15°C and 100°C (preferably between 20°C and 80°C) and at a pressure between 0.1 and 7 MPa (preferably between 0.1 and 0.7 MPa).
• R is the same as that defined in the telechelic fiuorinated bisazido compound formula.
• CuBr is shown as the catalyst in the above reaction, any co ⁇ per(l) halide may be employed.
• Copolymers made by the copolycondensation process of this invention have a number average molecular weight between 5000 and 200,000, preferably 10,000 to 100,000, These copolymers are useful in many industrial applications including sealants, O-rings, shaft seals for use in the automotive, aerospace and the electronics industries.
• the experimental conditions for 1 H (or 19 F) NMR spectra were the following: flip angle 90 ° (or 30 °), acquisition time 4,5 s (or 0.7 s) . pulse delay 2 s (or 5 s) , number of scans 16 (or 128), and a pulse width of 5 ⁇ s for 19 F NMR.
• SEC Size Exclusion Chromatography
• T g glass transition temperatures
• TGA analyses were performed using a Texas Instrument ATG 51- 133 apparatus under air at the heating rate of 20°C/min from room temperature (approximately 20°C) up to 550°C.
• HC-276 Hastelloy (HC-276) autoclave, equipped with inlet and outlet valves, a manometer and a rupture disc, was degassed and pressurized with 3.0 MPa of nitrogen for
• the monomers were introduced by a gas transfer of perfluoro(methyl vinyl ether) (PMVE) (332 g, 2.0 mole) and vinylidene fluoride (VF 2 ) (192 g, 3.0 mole).
• PMVE perfluoro(methyl vinyl ether)
• VF 2 vinylidene fluoride
• the molar ratio VF 2 /PMVE of the feed was 60/40.
• the autoclave was cooled to about -40 °C in a dry ice/acetone bath, A small increase in the reactor pressure was observed (from 0 to 0.2 MPa) during the introduction of PMVE.
• the autoclave was then warmed to room temperature. Pressure in the autoclave increased from 0.2 to 0.5 MPa.
• VF ⁇ was introduced at room temperature.
• the oligomer was characterized by 19 F and 1 H NMR spectroscopy and SEC analysis as described in the Test Methods.
• the number average molecular weight was 2410 g/m ⁇ l (by 19 F NMR); 2765 g/mo! (by SEC) and had a polydispersity index (PDI) of 1.147,
• the composition of the oligomer was 73.4 mol% VF 2 and 26.6 mol% PMVE.
• the glass transition temperature (Tg) was -55°C
• the decomposition temperature (Td) was 220 °C.
• the above oligomer was ethylenated by the following procedure.
• the autoclave was placed in an tee bath for about 60 minutes and 0.5 g of unreacted ethylene was slowly released.
• the reaction mixture was dissolved in 100 ml of 2-butanone (MEK) and washed with distilled water (2 x 100 ml), Na 2 S 2 O 5 solution (100 mt) and brine (100 ml) respectively in a separating funnel.
• MEK 2-butanone
• the organic phase was dried over MgSO 4 and filtered through sintered glass (G4).
• the organic solvent was removed by a rotating vacuum evaporator at 40°C under a vacuum of about 10 mm Hg.
• the resulting slightly yellow viscous liquid was dried at 40°C under 0.01 mbar pressure to constant weight.
• This ethylenated oligomer was then reacted with sodium azide to form the telechelic bis(azido) PoIy(VF 2 -CO-PMVE) copolymer.
• the nucleophilic substitution of 2.03 g (1.3 mmol) of ethylenated diiodo poly(VDF-co-PMVE) oligomer with 2.70 g (4.0 mmol) of sodium azide was carried out in a round bottom flask containing 20 mL of DMSO at 50°C for 12 hours. Then, the diazido dissolved with diethyl ether was precipitated from water, washed 5 times with distilled water and dried over magnesium sulfate.
• the batch bismonoaddition of ⁇ . ⁇ -diiodoperfluorohexane onto ethylene was performed in a 160 mL Hastelloy (HC276) autoclave Parr System, equipped with a manometer, a rupture disk, inlet and outlet valves, and a mechanical anchor. An electronic device regulated and controlled both the stirring and the heating of the autoclave.
• the autoclave was left dosed for 20 min. and purged with 30 bars of nitrogen pressure to prevent any leakage, and degassed afterwards. Then, a 2 mm Hg vacuum was operated for 15 min.
• the initiator di-4-tert- butylcyclohexyl peroxydicarbonate (4.22 g, 10 mmol) and 30,13 g (54.2 mmol) of 1-CeF 52 -I in dry tert-butanol (40 mL) were introduced via a funnel tightly connected to the introduction valve.
• ethylene 4.0 g, 0, 14 mol
• the autoclave was then heated up to 50 c C for 7 hours. After reaction, the autoclave was cooled to room temperature and then put into an ice bath. After degassing the unreacted monomer, the autoclave was opened.
• a mixture comprised of 3.70 g (6.0 mmol) of the UO-ditodo-3- trifluoromethyl-3A4, 5,57,7, 8,8-nonafluorodecane (prepared above) and 1.21 g (18.0 mmol) sodium azide dissolved in DMSO (25 mL) and water (0.5 mL) was stirred at 50°C for 48 hours, Then, the reaction mixture was poured into water and was extracted with diethyl oxide. This procedure was repeated twice.
• Example 1 the process of the invention was employed to manufacture a copolymer of telechelic bis(azido) poly(VF 2 -co-PMVE) copolymer with telechelic ⁇ , ⁇ dtpropargyl ether bisphenol AF.
• a copolymer of telechelic bis(azido) poly(VF 2 -co-PMVE) copolymer with telechelic ⁇ , ⁇ dtpropargyl ether bisphenol AF In a three- necked round bottom flask equipped with a condenser, 47 mg (0.3 mmol) of CuBr, 272 mg of bipyridine and 20 mi of THF were mixed. The mixture was purged with argon for 10 minutes in order to avoid excess oxidation of the Cu(I).
• the process of the invention was employed to manufacture poly( ⁇ , ⁇ ditfiazolo-1 ,10-diazido-3-trifluoromethyl- 3,4,4,5,5,7,7,8,8-nonafluorodecane -co- methyleneetherhexafluorobisphenoi AF) copolymer.
• 1 ,10-diazido-3- trifluoromethyl-3,4,4,5, 5,7,7, 8,8-Nonafluorodecane is sometimes referred to as TFE/VF 2 /HFP.
• Copper bromide 100 mg, 0.66 mmol
• 2,2'-bipyridine dNbipy

Landscapes

• Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• General Chemical & Material Sciences (AREA)
• Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
• Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)

Priority Applications (3)

Applications Claiming Priority (2)

Publications (1)

Family

ID=43354895

Family Applications (1)

Country Status (5)

Families Citing this family (9)

Citations (1)

Family Cites Families (20)

• 2009
  • 2009-06-17 US US12/486,378 patent/US8247614B2/en not_active Expired - Fee Related
• 2010
  • 2010-04-12 JP JP2012516081A patent/JP5635084B2/ja not_active Expired - Fee Related
  • 2010-04-12 EP EP10789892.6A patent/EP2443162A4/en not_active Withdrawn
  • 2010-04-12 WO PCT/US2010/030676 patent/WO2010147696A1/en not_active Ceased
  • 2010-04-12 CN CN201080027106.0A patent/CN102612526B/zh not_active Expired - Fee Related

Patent Citations (1)

Non-Patent Citations (5)

Also Published As

Similar Documents

Legal Events