This application claims priority filed on 1 Jul. 2021 in EUROPE with Nr. 21183256.3, the whole content of this application being incorporated herein by reference for all purposes.
The present patent application relates to copolymers comprising (per)fluoropolyether chains, characterized by increased viscosity.
Lubrication is an important aspect of maintaining machinery in proper operating condition. Machine elements such as bearings, pins, shafts, gears and joints require proper lubrication between their moving surfaces to decrease friction, prevent contamination, reduce wear and dissipate heat. Improper lubrication is likely to lead to premature component wear and component or system failure.
(Per)fluoropolyether polymers (in the following referred to as “PFPE polymers”) have been long known as base oils or as additives in several lubricant applications.
Several syntheses of PFPE polymers have been disclosed in the art. The first synthesis of unspecified perfluorinated polyether mixtures was reported in 1953, when an oily product was obtained in the course of photoligomerization of hexafluoropropene. Since then, a number of different perfluorinated polyethers have been synthesized and described in literature.
U.S. Pat. No. 4,500,739 (in the name of Montedison) discloses the reaction of a peroxidic PFPE with—among the others—perfluoro butadiene (Group II of fluoroolefins). Example 4 discloses the reaction with perfluoro butadiene, with a large excess of perfluorinated bis-olefin, resulting in pendant unsaturated groups along the macromolecular chain such that the reaction can further proceed in the presence of hexamethylenediamine.
U.S. Pat. No. 8,258,090 B2 (in the name of Solvay Solexis S.p.A.) discloses fluorinated lubricants of formula:
T-O—[A-B]z-[A′-B′]2′-A-T (I)
—[(CR1R2—CR3R4)j—(CR5R6—CR7R8)j′]— (Ia)
This patent discloses block copolymers characterized by a linear backbone, without any branching. Indeed, no branching is obtained within B, notably comprising (per)fluoropolyether chains.
Polymers obtained using PFPE polymeric units have been disclosed in the art. Crossed-linked fluoroelastomers are among those. On this regard, S. P. Krukovsky et al.—J of Fluorine Chemistry 96 (1999) 31-33—disclosed copolymerization of perfluoroalkyleneoxides containing peroxide groups in the chain with perfluorodivinyl ethers under UV radiation and heating to provide cross-linked polymers, referred to as elastomers. This document does not disclose any amount for the reactants, and does not address a method for manufacturing polymers suitable for use for lubricants.
While research and development in the recent years focused on mono- and/or bi-functional (per)fluoropolyether (PFPE) polymers, the Applicant perceived that there is still the need for providing neutral PFPE polymers that can be used as lubricants.
The Applicant faced the problem of providing new neutral PFPE polymers characterized by an increased viscosity (as measured by complex viscosity at 0.1 rad/s at 25° C.), while maintaining low glass transition temperature (Tg) and still being in the liquid state at room temperature.
The Applicant surprisingly found that neutral branched (per)fluoropolyether polymers characterized by increased viscosity, due to an increase of the number average molecular weight, can be provided via a process easy to implement on industrial scale.
Advantageously, the process allows to manufacture neutral (per)fluoropolyether polymers having high thermal stability while maintaining a low glass transition temperature and a good viscosity index (ASTM D2270), such that such polymers are particularly useful as lubricants in harsh environments, including for example applications requiring wide range of working temperatures or high heat generation.
In a first aspect, the present invention relates to a block copolymer [copolymer (P)] comprising a first and a second (per)fluoropolyether chain [PFPE chain] each having two chain ends, wherein the first chain end of said first and second PFPE chain comprises a perfluorinated alkyl group and the second chain end of said first and second PFPE chain are bonded to each other via:
—(R10)t[C(R1)(R2)—C(R13)(R14)(R15)]z (II)
-[(A{circumflex over ( )})a{circumflex over ( )}-(B{circumflex over ( )})v{circumflex over ( )}-(E{circumflex over ( )})L{circumflex over ( )}]u{circumflex over ( )}-(C{circumflex over ( )})-T (III)
—[C(R1{circumflex over ( )})(R2{circumflex over ( )})—C(R3{circumflex over ( )})(R4{circumflex over ( )})]—
—[(CR1*R2*CR3*R4*)n*-(E)L]— (IV)
In a second aspect, the present invention relates to a process [process (P)] for the manufacture of copolymer (P) as defined above.
Advantageously, copolymer (P) according to the present invention is prepared via a process [process (P)], which comprises contacting:
In the process according to the present invention, it is important that the amount of the compound of formula (X-p) is properly selected to be lower than the amount of the PFPE peroxy.
Advantageously, by selecting such amount, more than 85%, more preferably more than 90% and even more preferably more than 95% of the unsaturated moieties of compound of formula (III) react with at least one peroxy group of the starting PFPE peroxy, and branched block copolymers (P) free from unsaturated moieties as pendant groups (also referred to as “functional groups”) are obtained.
Copolymer (P) is advantageously free from pendant groups comprising any moiety capable of undergoing a further chemical reaction. In particular, copolymer (P) is free from unsaturated moieties as pendant groups.
In a third aspect, the present invention relates to copolymer (P) obtained via process (P) as described above.
While purification steps can be performed at the end of said process (P), it will be clear to those skilled in the art that the copolymers (P) according to the present invention are obtained at the end of process (P) as a mixture.
Thus, in a further aspect, the present invention relates to a mixture [mixture (P)] comprising two or more copolymers (P) as defined above.
It will be clear to those skilled in the art that mixture (P) is obtained via process (P) as described above.
Advantageously, said mixture (P) can be subjected to one or more purification steps (also referred to as “fractionation” steps), thus obtaining separate copolymers (P) characterized by different viscosities.
For the purpose of the present description and of the following claims:
Advantageously, said copolymer (P) is characterized by a complex viscosity, measured at 0.1 rad/s and at 25° C., from 10 Pa*s to 2000 Pa*s.
It will be understood by those skilled in the art that said first chain end of said first and second PFPE chain correspond to the two chain ends of copolymer (P).
Preferably, said first chain end of said first and second PFPE chain comprise a perfluorinated linear alkyl group having from 1 to 3 carbon atoms.
Preferably, said perfluorinated alkyl groups are the same from each other.
Preferably, said first chain end of said first and second PFPE chain and said T in formula (III), equal or different from each other, are a perfluorinated alkyl group having from 1 to 3 carbon atoms.
Preferably, said first and second PFPE chain, said A{circumflex over ( )} and said C{circumflex over ( )} are equal or different from each other.
Preferably, in copolymer (P), said first PFPE chain is bonded to said block (1) via a sigma bond or a group —(C)— selected from —CF2—, —CF2CF2— or —O—.
Preferably, in copolymer (P), said block (2) is bonded to said second PFPE chain via a sigma bond or a group —(C)— selected from —CF2—, —CF2CF2— or —O—.
Preferably, when both said block (1) and said block (2) are present, they are linked via a sigma bond.
Preferably, in said copolymer (P), each of said PFPE chain is a partially or fully fluorinated chain [chain (Rf)] comprising, preferably consists of, repeating units Ro, said repeating units being independently selected from the group consisting of:
Preferably, chain (Rf) complies with the following formula:
—[(CFX1O)g1(CFX2CFX3O)g2(CF2CF2CF2O)93(CF2CF2CF2CF2O)g4]— (Rf—I)
More preferably, chain (Rf) is selected from chains of formula:
—[(CF2CF2O)a1(CF2O)a2]— (Rf—IIA)
—[(CF2CF2O)b1(CF2O)b2(CF(CF3)O)b3(CF2CF(CF3)O)b4]— (Rf—IIB)
—[(CF2CF2O)c1(CF2O)c2(CF2(CF2)cwCF2O)c3]— (Rf—IIC)
Still more preferably, chain (Rf) complies with formula (Rf—μl) here below:
—[(CF2CF2O)a1(CF2O)a2]— (Rf—III)
Preferably, in formula (I), at least one of substituents R1 to R4 is a group of formula (II) and the other substituents are each independently selected from a fluorine atom or a perfluorinated alkyl chain having from 1 to 3 carbon atoms, more preferably a fluorine atom or a perfluorinated alkyl chain having 1 carbon atoms.
According to one embodiment, in formula (II), t is 0.
According to another embodiment, in formula (II) t is 1 and R10 complies with one of the following formulae:
—(CF2)d(O)e(CF2O)fRCF(O)e*(CF2)d*(CF2O)f* (R10-i)
—O—(C3F6O)h—(CF2)i—(C3F6O)j—O— (R10-ii)
According to this embodiment, preferably R10 complies with formula:
—(CF2)d(O)e(CF2O)fRCF(O)e*(CF2)d*(CF2O)f* (R10-i)
Preferably, in formula (II), z is equal to 1 and R10 is an oxygen atom or a bivalent perfluorinated alkyl chain comprising from 1 to 24 carbon atoms and being optionally interrupted by and/or comprising at least one oxygen atom.
Preferably, in formula (II), one of substituents R11 and R12 is a group of formula (III) and the other substituent is selected from a fluorine atom or a perfluorinated alkyl chain having from 1 to 3 carbon atoms, more preferably a fluorine atom or a perfluorinated alkyl chain having 1 to 3 carbon atoms. According to a preferred embodiment, one of substituents R11 and R12 is a group of formula (III) and the other substituent is a fluorine atoms.
Preferably, in formula (II), one of substituents R13 to R15 is a group of formula (III) and the other two substituents are independently selected from a fluorine atom or a perfluorinated alkyl chain having from 1 to 3 carbon atoms, more preferably a fluorine atom or a perfluorinated alkyl chain having 1 carbon atoms. More preferably said two substituents are the same and are a fluorine atom.
Preferably, in formula (III), v{circumflex over ( )} is an integer from 1 to 3, more preferably 1.
Preferably, in formula (III), L{circumflex over ( )} is an integer from 1 to 250, more preferably from 2 to 250.
Preferably, in formula (III), -(E{circumflex over ( )})L{circumflex over ( )}- complies with the following formula:
—(CR100{circumflex over ( )}R101{circumflex over ( )}CR102{circumflex over ( )}R103{circumflex over ( )})l{circumflex over ( )}—(CR110{circumflex over ( )}R111{circumflex over ( )}CR112{circumflex over ( )}R113{circumflex over ( )})m{circumflex over ( )}—
Preferably, in formula (IV), n* is an integer from 1 to 10, more preferably from 1 to 5, even more preferably from 1 to 3, and still more preferably 1.
Preferably, in formula (IV), L is an integer from 2 to 250.
Preferably, in formula (IV), -(E)L- complies with the following formula:
—(CR100R101CR102R103)l—(CR110R111CR112R113)m—
Preferably, in formula (IV), I is an integer from 1 to 250.
According to a first preferred embodiment, the copolymer (P) according to the present invention (hereinafter referred to as “copolymer (P-1)”) is a block copolymer comprising a first and a second PFPE chain, each having two chain ends, wherein the first chain end of said first and second PFPE chain comprises a perfluorinated alkyl group and the second chain end of said first and second PFPE chain are bonded to each other via:
—[(CR1*R2*CR3*R4*)n*-(E)L]- (IV)
—(R10)t[C(R11)(R12)—C(R13)(R14)(R15)]z (II)
—[(A{circumflex over ( )})a{circumflex over ( )}-(B{circumflex over ( )})v{circumflex over ( )}-(E{circumflex over ( )})L{circumflex over ( )}]u{circumflex over ( )}-(C{circumflex over ( )})-T (III)
According to a second preferred embodiment, the copolymer (P) according to the present invention (hereinafter referred to as “copolymer (P-2)”) is a block copolymer comprising a first and a second PFPE chain, each having two chain ends, wherein the first chain end of said first and second PFPE chain comprises a perfluorinated alkyl group and the second chain end of said first and second PFPE chain are bonded to each other via:
—(R10)t[C(R1)(R12)—C(R13)(R14)(R15)]z (II)
—[(A{circumflex over ( )})a{circumflex over ( )}-(B{circumflex over ( )})v{circumflex over ( )}-(E{circumflex over ( )})L{circumflex over ( )}]u{circumflex over ( )}-(C{circumflex over ( )})-T (III)
—[C(R1{circumflex over ( )})(R2{circumflex over ( )})—C(R3{circumflex over ( )})(R4{circumflex over ( )})]—
—(CR100{circumflex over ( )}R101{circumflex over ( )}CR102{circumflex over ( )}R103{circumflex over ( )})—
—[(CR1*R2*CR3*R4*)n*-(E)L*]- (IV)
Preferably, in said copolymer (P-1) and in said copolymer (P-2), each of said (E) and (E{circumflex over ( )}) is a group of formula:
—(CR100R101CR102R103)L—(CR110R111CR112R113)m—
Copolymers (P) according to the present invention can be advantageously prepared via a process that can be easily scaled up.
Preferably, in the process (P) of the present invention, the amount of the compound of formula (X-p) is less than 3 wt. %, even more preferably less than 1 wt. %, of the amount of the PFPE peroxy.
Preferably, said PFPE peroxy is a peroxidic (per)fluoropolyether polymer comprising a (per)fluoropolyether chain having two chain ends, each of said chain ends comprising a (per)fluorinated alkyl chain having from 1 to 3 carbon atoms, optionally containing one or more chlorine atoms or functional end groups selected from acyl fluoride, fluoroformate and ketones, said chain ends being bonded to opposite sides of said (per)fluoropolyether chain, said (per)fluoropolyether chain comprising, preferably consisting of, repeating units being independently selected from the group consisting of formulae (Rf-i) to (Rf-v) as above defined and having a peroxidic content (PO), defined as grams of active oxygen (Mw=16) in 100 g of PFPE peroxy between 0.1 and 4, preferably between 0.1 and 3.5.
The PFPE peroxy can be used as such or it can be subjected to partial reduction of the peroxid bonds, for example by chemical reduction or UV treatment or thermal treatment.
Preferably, in said compound of formula (X-p), when t is 1, the one, two, three or four unsaturated moieties are bonded to the same or different atoms, preferably carbon atoms, belonging to R10.
Preferably, said at least one compound of formula (X-p) complies with the following formula:
CF2═CF(R10)tCF═CF2
—(CF2)d(O)e(CF2O)fRCF(O)e*(CF2)d*(CF2O)f* (R10-i)
—O—(C3F6O)h—(CF2)i—(C3F6O)j—O— (R10-ii)
Preferably, said compound of formula (X-p) is selected from the group comprising, more preferably consisting of:
According to a particularly preferred embodiment, said at least one compound of formula (X-p) complies with the following formula:
CF2═CF(R10)tCF═CF2
—(CF2)d(O)e(CF2O)fRCF(O)e*(CF2)d*(CF2O)f* (R10-i)
According to a preferred embodiment, process (P) of the invention is performed contacting said PFPE peroxy and said compound of formula (X-p) with at least two of said compounds (0).
Preferably, a first compound (O) is selected in the group comprising, preferably consisting of fully halogenated olefin comprising from 2 to 8 carbon atoms, such as tetrafluoroethylene (TFE), hexafluoropropylene (HFP), chlorotrifluoroethylene (CTFE). TFE and HFP being particularly preferred.
Preferably, a second compound (O) is selected in the group comprising, preferably consisting of:
According to a first embodiment, said process [process (P1)] for the manufacture of copolymer (P1) as defined above, said process (P1) comprising the steps of: a*) contacting at least one peroxidic (per)fluoropolyether polymer [PFPE peroxy] with
Preferably, said step (a*) comprises contacting said at least one PFPE peroxy with at least one compound of formula (X-p) and two of said compounds (0).
Preferably, a first compound (O) is selected in the group comprising, preferably consisting of fully halogenated olefin comprising from 2 to 8 carbon atoms, such as tetrafluoroethylene (TFE), hexafluoropropylene (HFP), chlorotrifluoroethylene (CTFE). TFE and HFP being particularly preferred.
Preferably, a second compound (O) is selected in the group comprising, preferably consisting of:
Step (a*) and step (b*) can be performed in the presence of a fluorinated solvent. Preferably said fluorinated solvent is selected in the group comprising: perfluorocarbons, hydrofluorocarbons, perfluoropolyethers, hydrofluoropolyethers.
Preferably, step (b*) is performed in the presence of UV radiation for a time from 2 to 60 hours.
Preferably, step (b*) is performed in the presence of UV radiation at a temperature from −60° C. to +60° C., more preferably from −20° C. to +40° C. and even more preferably from 0° C. to 30° C.
As an alternative, step (b*) can be performed under thermal treatment, preferably by heating at a temperature from 100° C. to 250° C.
It will be clear to those skilled in the art that the polymer obtained at the end of step (b*) has a peroxide content (PO) lower than 0.05, preferably lower than 0.001.
Preferably, said step (c*) is performed by treating with fluorine in the presence of anhydrous nitrogen flow.
Preferably, said step (c*) is performed in the presence of UV radiation or under heating. Alternatively, said step (c*) can be performed as chemically assisted fluorination.
Preferably, said process (P1) comprises after step (c*), step (d*) of removal of the solvent and/or step (e*) of fractionation.
Said step (d*) of removal of the solvent can be carried out by evaporation, for example by distillation under vacuum.
Said step (e*) of fractionation can be performed via solvent extraction, using supercritical CO2, hexafluoroxylene or hydrofluorocarbons as solvents, and mixtures thereof when the fractionation step is performed via precipitation fractionation. Supercritical CO2 is preferred.
As explained above, although purification steps can be performed, it will be clear to those skilled in the art that at the end of process (P1), copolymers (P) according to the present invention are obtained in the form of mixtures comprising more then one copolymer (P) each characterized by different viscosities and/or molecular weight and/or substituents.
According to a second embodiment, the process [process (P2-a)] for the manufacture of copolymer (P2) comprises the steps of:
Preferably, said step (a′) comprises contacting said at least one PFPE peroxy with at least two compounds (O).
Advantageously, a first compound (O) and a second compound (O) comply with the definition provided above.
Alternatively, the process [process (P2-b)] for the manufacture of copolymer (P2) comprises the steps of:
Preferably, said step (d″) comprises contacting the reaction mixture obtained in step (c″) with at least two compounds (O).
Advantageously, a first compound (O) and a second compound (O) comply with the definition provided above.
Steps (a′) to (c′) as well as steps (a″) to (c″) can be performed in the presence of a fluorinated solvent.
Preferably said fluorinated solvent is selected in the group comprising: perfluorocarbons, hydrofluorocarbons, perfluoropolyethers, hydrofluoropolyethers.
Preferably, step (b′) and step (b″) are each independently performed in the presence of UV radiation for a time from 2 to 60 hours.
Preferably, step (b′) and step (b″) are each independently performed in the presence of UV radiation at a temperature from −60° C. to +60° C., more preferably from −20° C. to +40° C. and even more preferably from 0° C. to 30° C.
As an alternative, step (b′) and step (b″) are each independently performed under thermal treatment, preferably by heating at a temperature from 100° C. to 250° C.
It will be clear to those skilled in the art that the polymer obtained at the end of step (c′) or step (c″) has a peroxide content (PO) lower than 0.05, preferably lower than 0.001.
Preferably, said step (f′) and step (f″) are each performed by treating with fluorine in the presence of anhydrous nitrogen flow.
Preferably, said step (f′) and step (f″) are each performed in the presence of UV radiation or under heating. Alternatively, step (f′) and step (f″) are each performed as chemically assisted fluorination.
Preferably, said process (P2-a) and said process (P2-b) comprises after step (f′) and (f′), respectively, step (g′) and step (g″) of removal of the solvent and/or step (h′) and step (h″) of fractionation.
Said step (g′) or (g″) of removal of the solvent can be carried out by evaporation, for example by distillation under vacuum.
Said step (h′) or (h″) of fractionation can be performed via solvent extraction, using supercritical CO2, hexafluoroxylene or hydrofluorocarbons as solvents, and mixtures thereof when the fractionation step is performed via precipitation fractionation. Supercritical CO2 is preferred.
As explained above, although purification steps can be performed, it will be clear to those skilled in the art that at the end of process (P), process (P1), process (P2-a) and process (P2-b) step (c) or of step (d) of process (P) as mixture (P), copolymers (P) according to the present invention are obtained in the form of mixtures comprising more then one copolymer (P) each characterized by different viscosities and/or molecular weight and/or substituents.
Copolymer (P) is advantageously used as a lubricant, notably for application in harsh environments, for example subjected to a wide range of working temperatures.
Copolymer (P) or mixture (P) can be used as such, or in admixture with additive(s) known to the person skilled in the art of lubrication, so that a composition [composition (CL)] is obtained.
For example, composition (CL) can comprise other suitable lubricants as base oil, such base oil being selected in the group comprising partially fluorinated, fully fluorinated and hydrogenated base oils, provided that said base oil is capable of forming a solution with copolymer (P).
Non-limiting examples of fully fluorinated lubricant base oils are those identified as compounds (1)-(8) EP 2100909 A (SOLVAY SOLEXIS S.p.A.).
For example, suitable additives are selected from thickening agents, anti rust agents, antioxidants, thermal stabilizers, pour-point depressants, anti-wear agents, including those for high pressures, dispersants, tracers, dyestuffs, talc and inorganic fillers.
Examples of thickening agents are talc, silica, boron nitride, polyureas, alkali or alkali-earth metals terephthalates, calcium and lithium soaps and complexes thereof and PTFE (polytetrafluoroethylene); among them, PTFE is preferred.
Examples of dispersants are, for example, surfactants, preferably non-ionic surfactants, more preferably (per)fluoropolyether surfactants and (per)fluoroalkyl surfactants.
If required by the application, solvents can also be used.
Examples of solvents are fluorinated or partially fluorinated solvents, such as Galden® PFPEs, Novec® HFEs and other organic solvents like fluoro-alkane, fluoro-aromatic compound, fluoroalkyl ether, fluoroalkyl amine, fluoro-alcohol, ketone such as methyl-ethyl-ketone, alcohol such as isopropyl alcohol, ester such as butyl acetate, hydrofluorocarbons, and the like.
Thus, in a further aspect, the present invention relates to a method for lubricating at least one surface of at least one article, said method comprising contacting said copolymer (P) or said mixture (P) with said at least one surface.
The article that can benefit from the lubricant properties of copolymer (P), mixture (P) or composition (CL) according to the present invention is not particularly limited.
Said article preferably comprises at least one metal surface.
Examples of said article are pumps for use in oil and gas applications, such as electrical submersible pump and the like, rotary machines, such as steam turbines and gas turbines; electrical connectors; bearings of fan clutches or cooling fans; or heavy duty truck automatic clutches, more particularly bearings of said clutches.
Copolymer (P), mixture (P) or composition (CL) according to the present invention can be advantageously used as damper fluids in a damping device.
Thus, in a further aspect, the present invention relates to a method for counteract vibrations and/or shocks in a device, said method comprising providing an apparatus comprising a damper device, said damper device comprising at least one copolymer (P), mixture (P) or composition (CL) as defined above.
Should the disclosure of any patents, patent applications, and publications which are incorporated herein by reference conflict with the description of the present application to the extent that it may render a term unclear, the present description shall take precedence.
The invention will be now described in connection with the following examples, whose purpose is merely illustrative and not intended to limit the scope of the invention.
Peroxidic perfluoropolyether oil having formula
T-O—(CF2CF2O)m(CF2O)n—(O)h-T′
Tetrafluoroethylene (TFE), perfluoro(methyl vinyl ether) (PMVE) and Galden® HT200 were obtained by Solvay Specialty Polymers Italy S.p.A.
Perfluoro(bis vinyl ether) (PBVE) was obtained by Anles Ltd..
Hexafluorobenzene was obtained by Sigma Aldrich.
Varian Mercury 200 MHz spectrometer working for the fluorine nucleus was used to obtain the structure, the number average molecular weight and the composition of the PFPE oils reported in the following examples. The 19F-NMR spectrum was obtained on pure samples using CFCl3 as internal reference. Hexafluorobenzene was also used as a solvent.
The peroxidic content (PO) is expressed as grams of peroxidic oxygen per 100 g of polymer. The analysis of the peroxide content was carried out by iodometric titration using a Mettler DL40 device equipped with platinum electrode. The sensitivity limit for the PO determination was 0.0002%.
The complex viscosity was measured with frequency sweep tests using an MCR502 Anton-Paar rheometer with parallel plate geometry (25 mm diameter) according to ISO 6271 part 10.
The analysis was performed with a Mixed CCD column with a Waters 410 refractometer detector using HFE7100 as eluent.
The reaction was performed using a 1000 mL cylindrical photochemical glass reactor equipped with a high-pressure mercury lamp (HANAU TQ150) enclosed in a quartz cylinder, a magnetic stirrer, a thermocouple and a condenser.
200.0 g of the starting peroxidic perfluoropolyether oil were charged in the photochemical reactor together with 1499 g of Galden® HT200 and stirred thoroughly to obtain a homogenous mixture. The reaction mixture was then cooled down to about 10° C. with an ice/water bath.
Two fluorinated olefins, PMVE and TFE, were introduced into the reactor, at a rate of 2.20 and 1.60 NI/h, respectively. After the flow started, the UV lamp was switched on. After 4 h, the UV lamp was switched off and 1.31 g of PBVE were added to the reactor. Under vigorous stirring and nitrogen, the UV lamp was switched on again.
After 51 hours of irradiation, the lamp was switched off and the reaction mixture was transferred into a second glass reactor and fluorinated at 40° C. with 1.0 NI/h of fluorine gas for a total of 24 hours in the presence of UV radiation. 19F-NMR analysis confirmed the complete fluorination of the product and the absence of —CF2COF and —COF terminals at the chain ends.
The obtained solution was distilled at 240° C. for 4 h in a round bottom flask equipped with a magnetic stirrer in order to remove the solvent.
The distillation was conducted first at atmospheric pressure, then under reduced pressure (0.1 mbar) until complete removal of the solvent.
203.4 g of copolymer (1) in the form of a clear viscous oil were obtained as residue, which was analyzed by iodometric titration to confirm the complete removal of the peroxide units.
19F-NMR analysis confirmed the absence of residual peroxide and the incorporation of TFE and PMVE at a concentration respectively of 10.2 and 10.1 weight %.
Copolymer (1) had m/n=0.96, and the chain ends T, T′=—CF3.
The same photochemical apparatus and peroxidic perfluoropolyether precursor as Example 1 were adopted for this example.
200.8 g of the starting peroxidic perfluoropolyether oil were charged in the photochemical reactor together with 1494 g of Galden HT200 and 1.35 g of PBVE and stirred thoroughly to obtain a homogenous mixture.
The reaction mixture was then cooled down to about 10° C. by means of an ice/water bath. Two fluorinated olefins, PMVE and TFE, were introduced into the reactor, at a rate of 2.20 and 1.60 NI/h respectively. Immediately after the olefin flow started, the UV lamp was switched on. After 4 h, the olefins flow was interrupted and the reaction continued for 51 h under UV radiation.
The lamp was switched off and the reaction mixture was transferred into a second glass reactor to be fluorinated at 40° C. with 1.0 NI/h of fluorine gas for a total of 24 hours in the presence of UV radiation.
19F-NMR analysis confirmed the complete fluorination of the product and absence of —COF, —CF2COF terminals at the chain ends.
The obtained solution was distilled at 240° C. for 4 h in a round bottom flask equipped with a magnetic stirrer in order to remove the solvent. The distillation was conducted first at atmospheric pressure, then under reduced pressure (0.1 mbar) until complete removal of the solvent.
205.8 g of copolymer (2) in the form of a clear viscous oil were obtained as residue, which was analyzed by iodometric titration to confirm the complete removal of the peroxide units.
19F-NMR analysis confirmed the absence of residual peroxide and the incorporation of TFE and PMVE at a concentration respectively of 8.8 and 11.8 weight %.
Copolymer (2) had m/n=0.99, T, T′=—CF3.
The same photochemical apparatus and peroxidic perfluoropolyether precursor as Example 1 were adopted for this comparative example.
200.4 g of the starting peroxidic perfluoropolyether oil were charged in the photochemical reactor together with 1502 g of Galden® HT200 and stirred thoroughly to obtain a homogenous mixture.
The reaction proceeded as described in Example 2. The reaction mixture was then cooled down to about 10° C. by means of an ice/water bath. Two fluorinated olefins, PMVE and TFE, were introduced into the reactor, at a rate of 2.20 and 1.60 NI/h respectively. Immediately after the olefin flow started, the UV lamp was switched on. After 4 h, the olefins flow was interrupted and the reaction continued for 51 h under UV radiation.
19F-NMR analysis confirmed the complete fluorination of the product and the absence of —CF2COF and —COF terminals at the chain ends.
Distillation was also performed as described in Example 2.
206.3 g of comparative polymer (C-1{circumflex over ( )}) in the form of a clear viscous oil were obtained as residue, which was analyzed by iodometric titration to confirm the complete removal of the peroxide units.
19F-NMR analysis confirmed the absence of residual peroxide. Comparative copolymer (C-1{circumflex over ( )}) had m/n=1.0 and T, T′=—CF3.
The increased molecular weight distribution and complex viscosity of copolymer (1) and (2) according to the present invention confirmed the chain extension with respect to the comparative polymer (C-1{circumflex over ( )}).
Number | Date | Country | Kind |
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21183256.3 | Jul 2021 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2022/067112 | 6/23/2022 | WO |