Process for preparing perfluoropolyoxyalkylene endowed with a high viscosity and a low peroxide oxygen content

Abstract: Peroxy perfluoropolyoxyalkylenes are prepared with high yields by carrying out the photo-oxidation of tetrafluoroethylene with molecular oxygen, by means of ultraviolet radiations, operating in the presence of pentafluorochloroethane as a solvent for tetrafluoroethylene. Thus, it is possible to obtain peroxy perfluoropolyoxyalkylenes having a viscosity at 20°C ranging from 300,000 to 8,000,000 cSt and endowed with a peroxide content not higher than 4. Such perfluoropolyoxyalkylenes provide, through chemical reduction, perfluoropolyoxyalkylenes endowed with a functionality higher than 1.9 and at the same time with a high molecular weight.

Description: The present invention relates to a process for preparing peroxy perfluoropolyoxyalkylenes having a high viscosity and a high molecular weight. In particular it relates to the preparation with high yield and conversion of peroxy perfluoropolyoxyalkylenes endowed with a high viscosity and a high molecular weight which are suited to prepare, by reduction, perfluoropolyoxyalkylenes endowed with a high functionality and a high molecular weight. From U.S. patent No. 4,859,299 it is known to prepare perfluoropolyoxyalkylenes containing halogen atoms in the macromolecule by effecting the photo-oxidation of tetrafluoroethylene under ultraviolet radiations in a fluorinated or chlorofluorinated solvent, in the presence of a chain transfer agent consisting of halogenated hydrocarbons. As solvents there are mentioned dichlorotetrafluoroethane, trichlorotrifluoroethane, dichlorodifluoromethane. The perfluoropolyoxyalkylenes so obtained have the structure -(C 2 F 4 O) a -(CF 2 O) b -(O) c -, a molecular weight ranging from 200 to 25,000, c / a+b ratios ranging from 0.01 to 1, and b/a ratios ranging from 0.1 to 10. Furthermore, from U.S. patent No. 4,451,646 it is known to prepare perfluoropolyoxyalkylenes having a high molecular weight by subjecting tetrafluoroethylene to photo-oxidation in a fluorinated or chlorofluorinated solvent such as dichlorodifluoromethane, perfluorodimethylcyclobutane, 1,2-dichlorotetrafluoroethane, 1,2-dichlorohexafluoropropane, operating at temperatures ranging from -80 to -35°C, with C 2 F 4 /O 2 molar ratios ranging from 0.1 to 2 and F/VxE ratios higher than 3x10 -4 (where F is the number of mols of C 2 F 4 fed per hour, V is the reactor volume in ml and E represents the watts of ultraviolet radiation with wavelength lower than 330 nm). Operating according to said process there are obtained perfluoropolyoxyalkylenes with a theoretical number average weight not higher than 116,000, the conversions being not higher than 35%. Such perfluoropolyoxyalkylenes exhibit a peroxide content, for molecular weights higher than 75,000, which is higher than 5% by weight. By reduction, such products provide perfluoropolyoxyalkylenes having a very low molecular weight and a high functionality. Lastly, from U.S. patent No. 4,500,739 it is known to prepare high-viscosity perfluoropolyoxyalkylenes by subjecting tetrafluoroethylene to photo-oxidation in a solution consiting of difluorodichloromethane, filtering the ultraviolet radiations by means of an aqueous solution of CuSO 4 at a concentration up to 2% so as to eliminate the radiations with λ <280 nm. According to such process it is possible to obtain perfluoropolyoxyalkylenes having a viscosity not exceeding 300,000 cSt at 25°C. In such perfluoropolyoxyalkylenes, the peroxide oxygen content is equal to at least 4.1 % by weight for a viscosity equal to or higher than 0.3 m 2 /s (300,000 cSt). Such products, subjected to reduction of the peroxide oxygen, can provide perfluoropolyoxyalkylenes having a high content of difunctional products, but a very low molecular weight. An object of the present invention consists in providing peroxy perfluoropolyoxyalkylenes of general formula: T-O(CF 2 O) q (CF 2 CF 2 O) p -(-O) s -T' where T, T', like or different from each other, are -CF 3 , -C 2 F 5 , -CF 2 Cl, -CF 2 CF 2 Cl, -COF, -CF 2 COF having a viscosity (at 20°C) and determined by means of a flat-cone rotational viscosimeter) ranging from 0.3 to 8 m 2 /s (300,000 to 8,000,000 cSt), but preferably from 0.5 to 6 m 2 /s (500,000 to 6,000,000 cSt), and a peroxide oxygen content ranging from 0.1 to 4, and preferably ranging from 0.1 to 3.5, but more preferably from 0.3 to 3.5 % by weight. In the above-mentioned perfluoropolyoxyalkylenes, the value of the P / q ratio ranges from 0.4 to 5, preferably from 0.6 to 3. The abovesaid viscosity values correspond, respectively, to weight average molecular weights (Mw) ranging from 140,000 to 420,000, with preferred values being those from 160,000 to 390,000, or to number average molecular weight (Mn) ranging from 100,000 to 300,000, with preferred values being those from 120,000 to 280,000. The Mw values are generally measured by means of Light Scattering (L.S.) methods according to known techniques. The Mn values can be measured by means of N.M.R. for Mn values up to about 200,000. For values higher than 200,000, reliable Mn values can be obtained through the empiric relation: Viscosity (c.St.) = K Mn a where K, a are constants. This relation is well known to those skilled in the art. It is reported for example in published European patent application No. 259,980, wherein the value of K and a, restectively equal to 6.05x10 -11 and 3.07, were determined in relation to Mn values (measured by means of NMR techniques) ranging from 15,000 to 50,000. In order to apply such relation to the measures of the Mn values of the high molecular weight products of the present invention, the values of constants K and a were determined in relation to Mn values (determined by NMR) ranging from 9,000 to 200,000, thereby obtaining a value of 4.34x10 -10 for K and a value of 2.97 for a. So it is possible, through absolute viscosity measures, to calculate the Mn values also if they exceed the limit value of 200,000, which can be calculated by means of NMR-based techniques. The process for preparing the perfluoropolyoxyalkylen defined above consists in subjecting tetrafluoroethylene to photo-oxidation by means of molecular oxygen, under the action of radiation having a wavelength ranging from 200 to 600 nm, operating in the presence of pentafluorochloroethane (CF 3 CF 2 Cl) as a solvent for tetrafluoroethylene, the concentration of tetrafluoroethylene in the solvent during the reaction being at least 6·10 -2 moles/liter. The invention is further directed to a process for preparing peroxy perfluoropolyoxyalkylenes, which consists in subjecting tetrafluoroethylene to photo-oxidation by means of oxygen, under radiation having a wavelength from 200 to 600 nm, in the presence of a chlorofluorinated solvent characterized by the use of pentafluorochloroethane as solvent to obtain peroxy perfluoropolyoxyalkylenes having a viscosity of from 0.3 to 8 m 2 /s (300,000 to 8,000,000 cSt) at 20°C, determined by means of a flat-cone rotational viscosimeter and a peroxidic oxygen content from 0.1 to 4% by weight. Preferred conditions for practising such process consist in operating with values of the F/VxE ratio (where F, V, E have the meaning defined hereinbefore) ranging from 0.1 to 50x10 -4 , and more preferably from 0.1 to 3x10 -4 . The photo-oxidation reaction is preferably conducted at temperatures ranging from -40 to -100°C, and more preferably from -45 to -80°C. The flow conditions of tetrafluoroethylene are such as to achieve the above tetrafluoroethylene concentration in the solvent in the reactor and to obtain, in the presence of pentafluorochloroethane as the solvent, perfluoropolyoxyalkylenes having the above viscosity. In practice the reaction is e.g. operated by bubbling a gaseous mixture of tetrafluoroethylene and oxygen, in O 2 /C 2 F 4 molar ratios ranging from 10 to 0.5, but preferably from 6 to 1, into the solvent maintained at the abovesaid temperature, in the presence of ultraviolet radiation. The total pressure of the gaseous reagents in the reaction area ranges in general from 1013 to 1,013,250 Pa (0.01 to 10 atm.), and preferably from 5066 to 101,325 Pa (0.05 to 1 atm.). The process of the invention not only permits to obtain products having a higher molecular weight and a lower peroxide content, but also to obtain such products with higher yields and conversions than in the processes of the prior art, in particular the ones described in U.S. patents Nos. 4,451,646 and 4,500,739, the operative conditions being equal. The products obtained according to the present invention can provide, by chemical reduction of the peroxide oxygen contained in them, perfluroopolyoxyalkylenes having a number average molecular weight ranging from 400 to 20,000 and a functionality respectively ranging from 1.99 to 1.88. In particular, the products obtained from the chemical reduction of the present peroxy perfluoropolyoxyalkylenes exhibit, with a molecular weight being equal to the molecular weight of those of the prior art, a considerably higher functionality or, vice-versa, with the functionality being equal, they exhibit a much higher molecular weight. This is possible because the peroxy perfluoropolyoxyalkylenes obtained according to the invention exhibit - the peroxide oxygen content being equal - a much higher molecular weight (and therefore higher viscosity) than the products of the prior art, thereby permitting to obtain, in particular, reduction derivatives having an equal molecular weight but a much higher functionality. With reference to example 1 given hereinafter, the following table shows the characteristics of the reduction products obtained from the peroxy perfluoropolyoxyalkylene obtained according to the invention. Example Peroxide precursor Reduction derivative PO Mn Viscosity m 2 /s (cSt) Mn Functionality 1 2.6 200,000 3.2 (3,2o0,000) 1,000 1.99 The chemical reduction of the peroxy groups is effected according to conventional techniques such as, for example, the ones described in U.S. patents Nos. 4,451,646 and 3,847,978. The reduction of the peroxy groups can be directly carried out on the fluoroolefin photo-oxidation product, or it can be carried out after a thermal and/or photochemical treatment of such product, according to conventional techniques, such as e.g. the ones described in U.S. patent No.4,668,357, in order to reduce the peroxy group content present therein and therefore to obtain, by subsequent chemical reduction, higher molecular weight functionalized derivatives. The perfluoropolyoxyalkylenes obtained after chemical reduction exhibit end groups of the type -CF 2 COOR (R = H, CH 3 ), or -CF 2 COF. Such functionalized perfluoropolyoxyalkylenes can be subjected to reactions for the conversion of the end groups, such as reduction to alcohols, transesterification, salification and amidization, as are described for example in U.S. patent No. 3,810,874. The high molecular weight functionalized perfluoropolyoxyalkylenes so obtained are particularly suitable for being used in polycondensation reactions, for example in the preparation of polyesters and polyurethanes, or for being utilized as such for coating stony and metallic materials, and as lubricants for magnetic discs and tapes. The following examples are given to illustrate the present invention; however they are not to be considered as a limitation of the scope thereof. EXAMPLE 1 500 ml of CF 3 -CF 2 Cl were introduced into a cylindrical glass reactor (500-ml volume and optical path of 1 cm), equipped with a sintered glass bottom and with a coaxial quartz inner sheath, with a thermoregulation system utilizing a perfluorinated liquid and also equipped with a plunging pipe for letting in the gases, with a sheath with a thermocouple for taking the inner temperature, and with a reflux cooler maintained at a temperature of -80°C. Through the plunging pipe, a gaseous mixture composed of 35.4 N l/h of O 2 and 12.6 N l/h of CF 2 =CF 2 (O 2 /CF 2 =CF 2 molar ratio = 2.8) was bubbled into the reactor. By means of a cooling bath arranged outside the reactor, the temperature of the reacting liquid phase was maintained at -50°C for all the duration of the test. After having introduced into the quartz sheath a Hanau type TQ 150 ultraviolet lamp (which emitted 13.2 W of ultraviolet radiation having a wavelength from 2,000·10 -10 m to 3,300·10 -10 m (2,000 to 3,300 A°)), the lamp was switched on, and the irradiation and the feeding of the two reacting gases were tarried on for five hours. The concentration of CF 2 =CF 2 and of the by-products (such as for example COF 2 , ) both in the liquid phase and in the gases leaving the reactor was determined by gas-chromatographic analysis as the average of five samples drawn at regular intervals during the test. After a five-hour irradiation, the lamp was switched off and the solvent was removed from the reactor by evaporation at room temperature. 124 g of a polymeric oily residue exhibiting a very high viscosity were obtained. Such product, subjected to iodometric analysis, exhibited an active oxygen content equal to 2.6%. On NMR 19 F (300 MH Z ) analysis it resulted to be composed of polyethereal-polyperoxy chains: T-O-(CF 2 CF 2 O)p (CF 2 O) q (O) s - T' with a P/q ratio equal to 1.56, where T and T' are end groups such as -CF 3 , -CF 2 CF 3 and -CF 2 COF; the number average molecular weight (Mn) resulted to be equal to 200,000. The product viscosity was determined by means of a flat-cone rotational viscosimeter, at 20°C, and resulted to be equal to 3.2 m 2 /s (3,200,000 cSt). The weight average molecular weight (Mw) was determined by means of fixed-angle light scattering measurement, thereby obtaining a value of 240,000. The yield, expressed as grams of CF 2 CF 2 converted into oil/grams of reacted CF 2 CF 2 , was of 51%, with a conversion, expressed as grams of CF 2 CF 2 into oil/grams of fed CF 2 CF 2 , equal to 42%. The data relating to the example are reported in Table I.In said Table, the solvents utilized in the examples are indicated with the following reference numbers: Pentafluorochloroethane : 115 Dichlorodifluoromethane : 12 EXAMPLE 2 a) An amount of 22.6 g of the product obtained in example 1 was introduced into a 250-cc flask equipped with mechanical stirrer, thermometer, reflux cooler and dropping funnel, and 80 ml of CF 2 Cl-CFCl 2 and 40 ml of CH 3 OH were added thereto. 20 ml of HI at 57% by weight in aqueous solution were then gradually fed under stirring by means of the dropping funnel. On conclusion of the addition, the mixture was maintained at reflux for about 2 hours in order to complete the reaction. After having checked by means of NMR 19 F analysis the complete disappearance of the peroxide, the mixture was transferred to the dropping funnel. The lower phase was separated, washed one time with a 0,01 N solution of Na 2 S 2 O 3 in order to remove the I 2 residues, then it was washed with H 2 O and anhydrified with Na 2 SO 4 . After evaporation of the solvent under vacuum (2666 Pa (20 torr.)) there were obtained 16.0 g of a product, which on NMR 19 F analysis resulted to be composed of polyethereal chains: Y - O(CF 2 CF 2 O) p (CF 2 O) q - Y' with a p/q ratio = 1.14, were Y and Y' are end groups of the type: -CF 3 , -CF 2 CF 3 , -CF 2 COOCH 3 , -CF 2 COOH, wherefrom it results a functionality (F) expressed by the relation F = 2x(Ester+acid end groups) Total end groups equal to 1.99. -------- The number average molecular weight was equal to 1,000. b) An amount of 22.3 g of the product obtained in example 1 dissolved in 200 ml of n-perfluoroheptane was introduced into a cylindrical glass reactor (volume = 250 ml and optical path = 0.5 cm) equipped with a quartz inner sheath coaxial to a thermoregulating system utilizing perfluorinated liquids, and furthermore equipped with a plunging pipe for introducing an inert gas (N 2 at 0.5 l/h), a sheath with a thermocouple for detecting the inner temperature and a magnetic stirrer arranged on the flat bottom of the reactor. By means of a refrigerating bath arranged outside the reactor, the temperature of the reacting liquid phase was maintained at 0°C for all the duration of the test. After having introduced an ultraviolet lamp, type Hanau T.Q. 150, into the quartz sheath, the lamp was switched on and the irradiation was continued for 2 hours. Then the solvent was evaporated at a temperature of 20°C and under a vacuum of (66.6 Pa (0.5 torr). Subsequently the temperature was brought to 70°C in order to completely remove the solvent traces. There were obtained 16.7 g of a product which, on iodometric analysis, exhibited a peroxide content equal to 0.9%. On NMR 19 F analysis, the product resulted to be composed of polyethereal chains: Y - O(CF 2 CF 2 O) p (CF 2 O) q (O) s Y' with a p/q ratio = 1.23, where Y and Y' are end groups of the type: -CF 3 , -CF 2 CF 3 , -CF 2 COF, -COF, and having a number average molecular weight equal to 56,000. The product so obtained was reduced according to the modalities indicated at point (a) of the present example. There were obtained 14.7 g of a product, which on NMR 19 F analysis resulted to be composed of chains: Y - O(CF 2 CF 2 O) p (CF 2 O) q Y' with a p/q ratio = 1.14, where Y and Y' are end groups of formula - CF 3 , -CF 2 CF 3 , -CF 2 COOCH 3 , -CF 2 COOH, wherefrom it resulted a functionality equal to 1.97. The number average molecular weight of the product was equal to 2,100. c) An amount of 22.3 g of the product of example 1 was treated according to the same modalities as per point (b) of this example, but with a reaction time of 3 hours. After irradiation, the product (15.0 g) exhibited an active oxygen content equal to 0.5% and on NMR 19 F analysis it resulted to be composed of chains: Y-O(CF 2 CF 2 O) p (CF 2 O) q - (O) s -Y' with a p/q ratio = 1.12, where Y and Y' are end groups -CF 3 , -CF 2 CF 3 , -CF 2 COF, -COF, and with a number average molecular weight equal to 28,000. After reduction according to procedure (a) of the present example, the product (12.9 g), subjected to NMR 19 F analysis, resulted to be composed of chains: Y'-O-(CF 2 CF 2 O) p (CF 2 O) q Y' with a p/q ratio = 1.12, and in which Y, Y' are end groups of the type: -CF 3 , -CF 2 CF 3 , -CF 2 COOCH 3 , -CF 2 COOH. The product exhibited a functionality of 1.94 and a number average molecular weight equal to 3,200. d) A portion of 39.6 g of the product of example 1 was introduced into a 250 cc flask equipped with a thermometer, and by means of a thermostatic bath it was gradually heated up to a temperature of 185°C and was maintained at this temperature for 3 hours under a slight nitrogen flow (0.5 l/h). After reaction, the product (29.8 g) had an -------------active oxygen content equal to 0.7%. On NMR 19 F analysis, it resulted to be composed of chains: Y O(CF 2 CF 2 O) p (O) s (CF 2 O) q Y' with a p/q ratio = 1.22, where Y and Y' are end groups of formula -CF 3 , -CF 2 CF 3 , -CF 2 COF and -COF, and it had a number average molecular weight equal to 103,000. The product so obtained was reduced according to the procedure illustrated under point (a) of this example. 26.6 g of product were obtained, which, subjected to NMR 19 F analysis, resulted to be composed of chains: Y O(CF 2 CF 2 O) p (CF 2 O) q Y' with a p/q ratio = 1.07, where Y and Y' are end groups of formula -CF 3 , -CF 2 CF 3 , -CF 2 COOCH 3 , -CF 2 COOH. Such product exhibited a functionality equal to 1.97 and a molecular weight equal to 2,400. EXAMPLE 3 Using the same apparatus as in example 1, a photosynthesis was effected under the same conditions as in said example, with the exception that it was operated at -45°C with a CF 2 CF 2 flowrate equal to 11 N l/h and an oxygen flow-rate equal to 33 N l/h. After a 5-hour reaction, 139 g of polymer were discharged from the reactor; on iodometric analysis, the polymer exhibited a PO content equal to 2.0%. On NMR 19 F analysis, the polymer resulted to be composed of perfluoroethereal-polyperoxy chains having structure: T O(CF 2 CF 2 O) p (CF 2 O) q (O) s T' with a p/q ratio = 1.23, where T and T' are end groups -CF 3 , -CF 2 CF 3 , -CF 2 CF 2 Cl, -CF 2 COF and with a number average molecular weight equal to 100,000. The determination of the weight average molecular weight (Mw) effected by means of light scattering gave a value equal to 141,000. In this case, the product viscosity was determined at 20°C by means of a flat-cone rotational viscosimeter and --------- it resulted to be equal to 0.378 m 2 /s (378,000 cSt). EXAMPLE 4 (comparative) A photosynthesis was carried out under the same conditions of example 3, but using difluorodichloromethane as a solvent. After a 5-hour reaction, 124 g of polymer were discharged from the reactor; on iodometric analysis, the polymer exhibited a PO content equal to 2.1%. On NMR 19 F analysis, the polymer resulted to be composed of polyethereal-polyperoxy chains of structure: T O(CF 2 CF 2 O) p (CF 2 O) q (O) s T' with a p/q ratio = 0.98, where T and T' are end groups -CF 3 , -CF 2 Cl, -CF 2 CF 2 Cl, -CF 2 COF, and with a number average molecular weight equal to 11,600. The viscosity, determined at 20°C by means of an Ostwald-Fenske viscosimeter, was equal to 0.000660 m 2 /s (660 cSt). EXAMPLE 5 Using the same apparatus of example 1, a photosynthesis was carried out under the same conditions as in said example except that it was operated at a temperature of -55°C, with a CF 2 CF 2 flowrate equal to 11 N l/h and a oxygen flowrate equal to 33 N l/h. After a 4-hour reaction, 120 g of polymer were discharged from the reactor; on iodometric analysis, the polymer exhibited a PO content equal to 2.7%. On NMR 19 F analysis the polymer resulted to be composed of polyethereal-polyperoxy chains having structure: T O(CF 2 CF 2 O) p (CF 2 O) q (O) S T' with a p/q ratio = 2.13, where T and T' are end groups -CF 3 , -CF 2 CF 3 , -CF 2 CF 2 Cl, -CF 2 COF, and with a number average molecular weight equal to 155,000. The weight average molecular weight (Mw) determined by means of light scattering was equal to 170,000. The product viscosity, determined at 20°C by means of a flat-cone rotational viscosimeter, was equal to 1.19 m 2 /s (1,190,000 cSt). EXAMPLE 6 (comparative) A photosynthesis was carried out under the same conditions as in example 5, but using difluorodichloromethane as a solvent. After a 5-hour reaction, 151 g of polymer were discharged from the reactor; on iodometric analysis, the polymer exhibited a PO content equal to 2.3%. On NMR 19 F analysis, the polymer resulted to be composed of polyethereal-polyperoxy chains of structure: T O(CF 2 CF 2 O) p (CF 2 O) q (O) s T' with a p/q ratio = 1.47, where T and T' are end groups -CF 3 , -CF 2 Cl, -CF 2 CF 2 Cl, -CF 2 COF, and with a number average molecular weight equal to 17,200. The product viscosity, determined at 20°C by means of an Ostwald-Fenske viscosimeter, was equal to 0.0026 m 2 /s (2,600 cSt). EXAMPLE 7 Following the same modalities of example 1, a photosynthesis was carried out in a 250 ml reactor by using 250 ml of solvent. In this case, the test was conducted at a temperature of -45°C with a C 2 F 4 flowrate equal to 22.4 N1/h and an oxigen flowrate equal to 37.5 N1/h. After 1-hour reaction, 57 g of polymer were discharged from the reactor; on iodometric analysis, the polymer exhibited a PO content equal to 3.1% On NMR 19 F analysis, the polymer resulted to be composed of polyethereal-polyperoxy chains of structure: T O(CF 2 CF 2 O) p (CF 2 O) q (O) s T' with a p/q ratio = 2.63, where T and T' are end groups -CF 3 , -CF 2 CF 3 , -CF 2 CF 2 Cl, -CF 2 COF. The product viscosity, determined at 20°C by means of a flat-cone rotational viscosimeter, was equal to 0.65 m 2 /s (650,000 cSt). The weight average molecular weight (Mw) determined by means of light scattering was equal to 150,000. EXAMPLE 8 (comparative) A photosynthesis was carried out under the same conditions as in example 7, but using difluorodichloromethane as a solvent. After a 1-hour reaction, 58 g of polymer were discharged from the reactor; on iodometric analysis, the polymer exhibited a PO content equal to 2.5%. On NMR 19 F analysis, the polymer resulted to be composed of polyethereal-polyperoxy chains of structure: T O(CF 2 CF 2 O) p (CF 2 O) q (O) s T' with a p/q ratio = 1.61, Where T and T' are end groups -CF 3 , -CF 2 Cl, -CF 2 CF 2 Cl, -CF 2 COF. The viscosity, determined at 20°C by means of an Ostwald-Fenske viscosimeter, was equal to 0.0038 m 2 /s (3,850 cSt). EXAMPLE 9 Following the same procedure of example 1, a photosynthesis was effected in a 900 ml reactor. In this case the test was carried out at a temperature of -45°C with a C 2 F 4 flowrate equal to 28 Nl/h and an oxygen flowrate equal to 40 Nl/h. After a 2.5-hour reaction, 185 g of polymer were discharged from the reactor; on iodometric analysis, the polymer exhibited a PO content equal to 3.5%. On NMR 19 F analysis the polymer resulted to be composed of polyethereal-polyperoxy chains having structure: T O(CF 2 CF 2 O) p (CF 2 O) q (O) s T' with a p/q ratio = 2.38, where T and T' are end groups -CF 3 , -CF 2 CF 3 , - CF 2 CF 2 Cl, -COF. The product viscosity, determined at 20°C by means of a flat-cone rotational viscosimeter, was equal to 3.784 m 2 /s (3,784,000 cSt). The weight average molecular weight (Mw) determined by means of light scattering was equal to 280,000. The operative modalities utilized in the examples and the characteristics of the obtained products are reported in Table I.

Claims: A process for preparing peroxy perfluoropolyoxyalkylenes consisting of -CF 2 O- and -CF 2 CF 2 O- units, peroxidic oxygen atoms, and two end groups, wherein the end groups, like or different from each other, are selected from the group consisting of -CF 3 , -C 2 F 5 , -CF 2 Cl, -CF 2 CF 2 Cl, -COF and -CF 2 COF, and wherein said peroxy perfluoro polyoxyalkylenes have a ratio of -CF 2 CF 2 O- units to -CF 2 O- units of from 0.4 to 5, a peroxidic oxygen content from 0.1 to 4% by weight, and a viscosity of from 0.3 to 8 m 2 /s (300,000 to 8,000,000 cSt) at 20°C, determined by means of a flat-cone rotational viscosimeter which process consists in subjecting tetrafluoroethylene to photo-oxidation by means of oxygen, under radiation having a wavelength from 200 to 600 nm, in the presence of pentafluorochloroethane as a solvent, wherein the concentration of tetrafluoroethylene in the solvent during the reaction is at least 6·10 -2 moles/liter. The process of claim 1, wherein it is operated with F/VxE ratio values ranging from 0.1 to 50x10 -4 , where F is the number of mols/h of tetrafluoroethylene fed to the reactor, V is the reactor volume in ml, E represents the watts of radiation having a wavelength below 330 nm. The process of claim 1, wherein it is operated with F/VxE ratio values ranging from 0.1 to 3x10 -4 , where F, V and E are defined as in claim 2. The process of claims 1 to 3, wherein the reaction is conducted at temperatures ranging from -45°C to -80°C. A process for preparing peroxy perfluoropolyoxyalkylenes, which consists in subjecting tetrafluoroethylene to photo-oxidation by means of oxygen, under radiation having a wavelength from 200 to 600 nm, in the presence of a chlorofluorinated solvent characterized by the use of pentafluorochloroethane as solvent to obtain peroxy perfluoropolyoxyalkylenes having a viscosity of from 0.3 to 8 m 2 /s (300,000 to 8,000,000 cSt) at 20°C, determined by means of a flat-cone rotational viscosimeter and a peroxidic oxygen content from 0.1 to 4% by weight.

Inventors: GUARDA PIER ANTONIO, MARCHIONNI GIUSEPPE, STACCIONE ANNA MARIA, GUARDA, PIER ANTONIO, MARCHIONNI, GIUSEPPE, STACCIONE, ANNA MARIA
Applicants: AUSIMONT SPA, AUSIMONT S.P.A.
Application year: 1992
Main classification: C08G65
IPC codes: C07C409, C07C41, C08G18, C08G65, C08G63, C07C43, C07C407