PROCESS FOR THE PREPARATION OF PERFLUOROACYL FLUORIDES

Abstract: The present invention relates to a process for the preparation of a perfluoroacyl fluorides wherein the acyl radical is a propionyl or butyryl group. The process is characterized in that a perfluoroalkylvinylether wherein the alkyl radical is a methyl or ethyl group is thermally treated in the presence of a catalyst selected from: A) a fluoride of Li, Na, K, Cs or Rb, or a compound of Li, Na, K, Cs or Rb, which is easily fluorinated under the reaction conditions; B) a fluoride of Be, Mg, Ca, Sr, or Ba, or a compound of Be, Mg, Ca, Sr, or Ba, which is easily fluorinated under the reaction conditions; C) a fluoroaluminate, fluorosilicate, fluorotitanate or fluorometallate of an alkali metal, or of a metal belonging to group IIA of the Periodic Table or a compound, which is easily fluorinated to yield one of the above-said fluoroaluminates, fluorosilicates, fluorotitanates or fluorometallates under the reaction conditions; D) a fluoride of a metal of the first transition series, or the corresponding metal, or a compound of such a metal, which is easily fluorinated under the reaction conditions; E) a fluoride of a lanthanide or the corresponding metal or a compound of such a metal, which is easily fluorinated under the reaction conditions;& <LIT>F) an oxyfluoride of Si, Al, Ti, Ge, Sn or Pb, or a compound of Si, Al, Ti, Ge, Sn or Pb, which is easily fluorinated to yield one of the above-said oxyfluorides under the reaction conditions.

Description: The present invention relates to a process for the preparation of perfluoroacyl fluorides wherein the perfluoroacyl radical is a perfluoropropionyl or perfluorobutyryl group. The perfluoroacyl fluorides are intermediate products which are considerably interesting from the commercial viewpoint. They can be used, e.g., for the purpose of obtaining water-repellent and oil-repellent products on paper and fabrics, for the preparation of surface active agents, e.g., flame-proofing agents, and for the production of emulsifier agents for the polymerization of the fluorinated olefins. The perfluoroacyl fluorides can be obtained by means of various methods, among which the electrochemical fluorination of the carboxylic acids or of their derivatives (chlorides, esters), and by starting from iodoperfluoroalkanes. As reported in the treatise by R.E. Banks, "Preparation, Properties and Industrial Applications of Organofluorine Compounds", Chapter 1, Ellis Horwood Ltd., Chichester, 1982, these processes result in general expensive, they do not allow high yields and high purities to be achieved, as in the case of electrochemical fluorination, or they require many steps and starting from expensive starting materials, as in case of starting from iodoperfluoroalkanes. The purity is an essential requirement in perfluoroacyl fluorides, in that its lack can prevent the use of these intermediate products in subsequent conversion reactions, wherein a high purity is required, such as, e.g., in the conversion into perfluoroalkyl-fluorooxy-compounds which are known to give rise to explosive decompositions, initiated by traces of impurities. R.N. Hazeldine and A.E. Tipping (J. Chem. Soc. (C), 398-405, 1968), report a reaction of pyrolytic rearrangement of trifluoromethyltrifluorovinylether at 595°C, inside a platinum reactor. This reaction causes the formation of several products, among which perfluoropropionyl fluoride, this latter product being obtained with a yield of 53%. A purpose of the present invention is that of supplying a process for the preparation of perfluoroacyl fluorides, wherein the perfluoroacyl radical is a perfluoropropionyl or perfluorobutyryl group, which gives high yields and a high selectivity. Another purpose is that of supplying very pure products, rendering useless, or reducing to the very minimum the operations of purification, thus avoiding the risks connected with the instability e.g., to hydrolysis, of such products. These and still further purposes are achieved by the process of the present invention for the preparation of perfluoroacyl fluorides, wherein the perfluoroacyl radical is a perfluoropropionyl or perfluorobutyryl group. This process is characterized in that a perfluoroalkylvinylether wherein the perfluoroalkyl radical is a trifluoromethyl or a perfluoroethyl group, is thermally treated in the presence of a catalyst selected from: A) a fluoride of Li, Na, K, Cs or Rb, or a compound of Li, Na, K, Cs or Rb, which is easily fluorinated under the reaction conditions; B) a fluoride of Be, Mg, Ca, Sr, or Ba, or a compound of Be, Mg, Ca, Sr, or Ba, which is easily fluorinated under the reaction conditions; C) a fluoroaluminate, fluorosilicate, fluorotitanate or fluorometallate of an alkali metal, or of a metal belonging to group IIA of the Periodic Table or a compound, which is easily fluorinated to yield one of the above said fluoroaluminates, fluorosilicates, fluorotitanates or fluorometallates under the reaction conditions; D) a fluoride of a metal of the first transition series (i.e., of the metals having an atomic number of from 21 to 30), or the corresponding metal, or a compound of such a metal, which is easily fluorinated under the reaction conditions; E) a fluoride of a lanthanide, or the corresponding metal or a com pound of such a metal, which is easily fluorinated under the reaction conditions; F) an oxyfluoride of Si, Al, Ti, Ge, Sn or Pb, or a compound of Si, Al, Ti, Ge, Sn or Pb, which is easily fluorinated to yield one of the above-said oxyfluorides under the reaction conditions. The reaction is the following: wherein R F is either CF₃ or C₂F₅. The metals and the other easily fluorinatable compounds, used as catalysts, form in situ , under the reaction conditions, fluorinated species, under the action of the perfluoroalkylvinylether. They can also be fluorinated, before carrying out the reaction, by means of another reactant capable of fluorinating them, e.g., fluorine or hydrofluoric acid. Among the compounds of Li, Na, K, Cs and Rb, which are easily fluorinatable under the reaction conditions, the oxides, the hydroxides and the oxyhalides, e.g., Li₂O, Na₂O, K₂O, Cs₂O, LiOH, NaOH, KOH, CsOH, LiOCl, NaOCl, KOCl and CsOCl can be mentioned. Among the compounds of Be, Mg, Ca, Sr and Ba, which are easily fluorinatable under the reaction conditions, the oxides, the hydroxides and the oxyhalides, e.g. BaO, MgO, CaO, SrO, Ba(OH)₂, Mg(OH)₂, Ca(OH)₂, Sr(OH)₂, Ba(OCl)₂, Mg(OCl)₂, Ca(OCl)₂ and Sr(OCl)₂ can be mentioned. Among the fluoroaluminates, fluorosilicates, fluorotitanates and fluorometallates of alkali metals, or of the metals belonging to group IIA of the Periodic Table, for example K₃AlF₆, Cs₃AlF₆, K₂SiF₆, Cs₂SiF₆, CsCuF₃, KCuF₃, CsNiF₃ can be mentioned. The preferred compounds of this category are K₃AlF₆, Cs₃AlF₆, K₂SiF₆ and Cs₂SiF₆. Among the compounds which are easily fluorinatable to yield one of the above said fluoroaluminates, fluorosilicates, fluorotitanates or fluorometallates under the reaction conditions, e.g., the aluminates, the silicates and the titanates of the alkali metals, and of the metals belonging to Group IIA, e.g., Na₂Al₂O₄, Na₂SiO₃, K₂Al₂O₄, MgAl₂O₄ and Na₂TiO₃ can be mentioned. Also the mixed oxides of the alkali metals or of the metals of Group IIA with other metals, such as Cu, Zn and Mg, e.g., MgO.CuO, MgO.ZnO, K₂O.CuO nd Cs₂O.MgO can be mentioned. Among the fluorides of the metals of the first transition series, e.g., the following can be mentioned: CuF₂, NiF₂, ZnF₂, CoF₂, CoF₃, CrF₃, MnF₂, FeF₂ and FeF₃. Among the corresponding metals, for example, Cu, Ni, Zn, Cr, Mn, Fe and Co can be mentioned; from these latter, Cu, Ni, Zn and Fe are preferred. Most preferred is Cu. Among the compounds of such metals, which are easily fluorinatable under the reaction conditions, e.g., the oxides, such as Fe₂O₃, CuO, NiO, Cr₂O₃, Co₂O₃, Cu₂Cr₂O₄; the hydroxides, such as FeO(OH), Cu(OH)₂, Ni(OH)₂, CrO(OH), CoO(OH), and the oxyhalides, such as FeOCl, Ni(OH)Cl, CrOCl, Cu(OH)Cl, Co(OH)Cl, can be mentioned. Among the lanthanide fluorides, for example, LaF₃ and CeF₄ can be mentioned. Among the corresponding metals, lanthanum can be mentioned. Among the lanthanide compounds which are easily fluorinatable under the reaction conditions, e.g., the oxides such as La₂O₃ and CeO₂; the oxide-hydroxides, such as LaO(OH) and CeO(OH)₂; the hydroxides, such as La(OH)₃ and Ce(OH)₄ and the oxyhalides, such as LaOCl and CeOCl₂, can be mentioned. Among the oxyfluorides of Si, Al, Ti, Ge, Sn and Pb, SiO x F y , wherein 2x+y = 4, is preferred. Among the compounds which are easily fluorinatable to yield the above-said oxyfluorides, the oxides, such as SiO₂, Al₂O₃ and TiO₂; and the oxide-hydroxides, such as SiO x (OH) y , wit h 2x+y = 4 and AlO x (OH) y , with 2x+y = 3, can be mentioned. Instead of the metals of the first transition series, or of the lanthanides, their alloys, e.g., steel, brass and bronze, can be used. Among the pre-formed fluorinated catalysts, the most preferred is MgF₂. When a pre-formed fluoride is used as the starting material, and also when the catalyst is obtained by means of in situ fluorination of the metal or of the easily fluorina table compound by means of is often convenient to activate it in situ , under the action of the reactant itself, i.e. the perfluoro alkylvinylether. When as the starting material a metal, or a not fluorinated compound, is used, the treatment with the reactant itself is necessary and can lead both to the formation of fluorinated species, and to the at least partial activation of the starting material. Instead of the reactant itself another fluorinating agent, such as, e.g., F₂ or HF, can be used, leading to the formation of fluorides and to the at least partial activation of the raw material used. Before submitting the metal, or the not fluorinated compound, to the treatment of fluorination and activation, it is preferably submitted to a thermal treatment. This thermal treatment is generally carried out at temperatures comprised within the range of from 300 to 650°C in case of metals, and of from 250 to 500°C, in case of the other fluorinatable compounds, compatibly with their chemical and physical stability; usually, the duration of such thermal treatment is comprised within the range of from 1 to 3 hours. Also an already fluorinated catalyst can be thermally activated: this activation is generally carried out at the same temperatures at which the reaction takes place, or at higher temperatures. The temperature range within which the reaction can be carried out varies according to the catalyst, and can depend on its chemical nature, its physical shape, and its degree of activation. In general, the conversion tends to increase with increasing temperatures, whilst the selectivity increases up to certain values of temperature, and then decreases at higher temperatures. For each catalyst, a range of temperatures hence exists, within which good results are obtained, and a narrower range exists, within which the best combination of conversion and selectivity is achieved, for the obtainment of high yields of perfluoroacyl fluoride. With the metals of the first transition series, good results are generally obtained within the range of from 300 to 500°C, whilst the best results are commonly obtained at temperatures of from 350 to 450°C in case of Cu, Ni, Zn and Fe. With the oxyfluorides of Si, Al, Ti, Ge, Sn and Pb, and the compounds of Si, Al, Ti, Ge, Sn and Pb which are easily fluorinatable to yield the above-said oxyfluorides under the reaction conditions, good results are generally obtained at temperatures of from 250 to 400°C, whilst the best results are obtained at temperatures of from 300 to 400°C in case of fluorinated silica. With the fluorides of Be, Mg, Ca, Sr and Ba, and the compounds of Be, Mg, Ca, Sr and Ba which are easily fluorinatable under the reaction conditions, good results are generally obained at temperatures of from 300 to 450°C, with the best results being obtained from 350 to 450°C in case of MgF₂. With the fluorides of Li, Na, K, Cs and Rb and the compounds of Li, Na, K, Cs and Rb which are easily fluorinatable under the reaction conditions, good results are generally obtained at temperatures comprised within the range of from 300 to 450°C; in case of KF, the preferred operating range is of from 320 to 360°C. The activation temperature and time vary from catalyst to catalyst. In general, the activation is faster with increasing temperatures. In case of a pre-formed catalyst, the activation is commonly carried out at the same temperatures at which the reaction is carried out. Also the fluorination and activation of a metal, or of anoth er fluorinatable compound takes usually place at the same temperatures at which the reaction is carried out. The granulometry and the physical shape of the catalyst are not critical. The catalyst is commonly used with a granulometry comprised within the range of from 250 microns to 2 mm. When the catalyst is a metal, it can be in the form of filaments, chips, needles, and so forth, of dimensions of a few mm. The metal surface can be smooth, or it can show a certain porosity, with a specific surface area comprised e.g., within the range of from 0.05 to 0.1 m²/g. Fluorinated catalysts in mixture with metals can be used as well; such metals can be both metals which, by fluorination, yield catalysts in accordance with the present invention, e.g., Cu and Ni, and other metals, e.g., Al. The presence of the metal helps to remove heat from the reaction medium. As an alternative, the fluorinated catalyst can be supported on the metal material. A method of preparation of a fluorinated catalyst supported on copper consists in submitting a copper oxide (CuO or Cu₂O or a mixture thereof), in the shape of filaments or needles or granules having a diameter comprised within the range of from 250 microns to 2 mm, to reduction with hydrogen diluted with nitrogen, at a temperature of from 250 to 350°C, thus a support being obtained, which is constituted by metal copper in porous form, having a specific surface area, e.g., of from 0.05 to 0.1 m²/g. This support is then impregnated with a solution (e.g., an aqueous or alcoholic solution) of a fluoride, e.g., NaF. Finally, the solvent used is evaporated off under vacuum. In the process of the present invention, either a single catalyst, or a mixture of catalysts can be used. The process can be carried out batchwise or, preferably, continuously. When the process is carried out batchwise, the reaction can be carried out in an autoclave, operating under the endogenous pressure developed by the system. Preferably, the process is carried out continuously, by flowing a stream of perfluoalkylvinylether in gas phase through over a catalyst bed. The perfluoroalkylvinylether can be used alone, or as a mixture with a gaseous diluent inert under the reaction conditions, e.g., N₂, He or CF₄. When a diluent is used, the perfluoroalkylvinylether/diluent volume ratio is e.g., comprised within the range of from 100:1 to 1:1. When a gaseous stream of perfluoroalkylvinylether is made is made to flow over a catalytic bed, its flow rate is comprised, e.g. within the range of from 0.025 to 0.1 Nl/h per (normal litres/hour) per gram catalyst The contact time of the reactant with the catalyst can vary within a wide range, according to the used method (whether batchwise or continuous), the catalyst nature, its physical shape, the possible dilution degree of the reactant, and the reaction temperature. When the process is carried out continuously over already activated catalysts, and under steady-state conditions, with reactant flow rates comprised within the range of from 0.025 to 0.1 Nl/h per catalyst gram, the contact time can range, e.g., from 10 to 90 seconds. The catalysts of the present invention are endowed with a long activity life. With the process of the present invention, conversions of up to approximately 99%, and selectivities of up to approximately 90% can be obtained. The impurities present in the end product are mostly constituted by unreacted perfluoroalkylvinylether, and fluorinated olefins. These impurities can be possibly removed by using conventional techniques. The fluorinated olefins can be separated by, e.g., bubbling the gaseous reaction mixture through liquid bromine: the unsaturated products turn into liquid brominated compounds, which can be separated, e.g., by distillation. The main advantages of the present invention can be summarized as follows: the reaction can be carrie d out at lower temperatures than in the absence of a catalyst; the reaction is very selective, and the yield in perfluoroacyl fluoride is high; by operating at lower temperatures, the formation can be controlled and limited to the very minimum of the many byproducts - in particular, perfluoroisobutene, which is very toxic - which otherways are unavoidably formed in the pyrolytic process in the absence of a catalyst; the end product can be purified of its more abundant impurities, i.e., from the unsaturated impurities, in a simple and efficacious way; the catalysts are endowed with a long activity life. Example 1 In all examples, tubular reactors 250 mm long, and having an inner diameter of 10.9 mm are used. In each test, new reactors were used. In Example 1, an unpacked reactor of steel AISI 316 is used. The reactor is pre-heated at 600°C under an atmosphere of N₂ for two hours, and is then adjusted at the controlled temperature of 380°C. Perfluoromethylvinylether is fed to the reactor at a flow rate of 0.6 Nl/h. The leaving gases are detected by I.R. spectrophotometry and gas-mass spectrometry. They are analyzed on-line in the gas phase by gas-chromatography. After 5 minutes from the feeding beginning, a conversion of 49.9% and a zero selectivity to perfluoropropionyl fluoride is observed. After a further 30 minutes, the conversion is of 69.5%, and the selectivity is of 49.4%. The test demonstrates the non-selectivity of the thermal process, and the formation in situ , with time, of the active catalytic species, in the presence of the reactant. Example 2 The process is carried out as in Example 1, inside a reactor of AISI 316 steel. The conditions shown in the Table are used. The Table reports also the results obtained. The test demonstrates the formation of the catalytic species, and their progressive activation, with the consequent increase in selectivity and yield. Example 3 The reaction is carried out inside a reactor of copper packed with copper needles having a length ranging from 1 to 10 mm. The packed reactor is thermally pre-treated at 600°C for 3 hours, under a nitrogen atmosphere. The reactor is then adjusted at the controlled temperature of 390°C, and perfluoromethylvinylether is fed to it at a flow rate of 0.6 Nl/h. The results obtained as a function of time are reported in the following Table. Example 4 The reaction is carried out as in Example 3, carrying out a thermal pre-treatment at 600°C, and adjusting the reactor at the controlled temperature of 395°C before starting feeding the perfluoromethylvinylether stream. After about 120 minutes, a conversion of 98.6%, and a selectivity of 83.9% is obtained. After 8 running hours, the catalyst does not show any losses of efficiency. Example 5 The reaction is carried out as in Example 4, with the only difference that the thermal pre-treatment of the reactor takes place at 300°C. The same results are obtained. The impurities are constituted by CF₃-CF=CF₂ and negligible amounts of other fluorocarbons. Example 6 An unpacked quartz reactor is used. The reactor is pre-heated at 400°C under a N₂ atmosphere for half an hour, and at 350°C for 1 hour, and is initially adjusted at the controlled temperature of 330°C. A stream of perfluoromethylvinyl ether is fed at the flow rate of 0.6 Nl/h. The results obtained as a function of time and temperature are reported in the following Table. After 8 running hours, the catalyst does not show any efficiency losses. The impurities are constituted by CF₃-CF=CF 2 and negligible amounts of other fluorocarbons. Example 7 A reactor of copper, packed with copper needles, as in Example 3, is used. The packed reactor is thermally pre-treated at 600°C for 3 hours, under a nitrogen atmosphere, and is then adjusted at the controlled temperature of 120°C. Through it, a mixed stream of 2 Nl/h of nitrogen, and 1 Nl/h of fluorine is fed for 2 hours; then, a stream of 2 Nl/h of fluorine for 2 hours is fed. The reactor temperature is then adjusted at 390°C, and a stream of 0.6 Nl/h of perfluoromethylvinylether is then made flow through the reactor, with the results being obtained, which are reported in the following Table. This Example demonstrates that active and selective species are formed, not only in the presence of the reactant, as demonstrated by Example 3, but also, alternatively, in the presence of a different fluorinating agent, such as elemental fluorine. Example 8 The reaction is carried out inside a glass reactor, packed with sodium aluminate powder, through which a stream of perfluoromethylvinylether is fed at the flow rate of 0.6 Nl/h. The conditions are used, which are indicated in the Table, in which also the results are reported. Example 9 A tubular reactor of AISI 316 steel, 250 mm long, and having an inner diameter of 10.9 mm is filled with 30 g of anhydrous MgF₂, the particles of which have a diameter comprised within the range of from 0.7 to 1.5 mm. The reactor is heated to, and kept at the temperature of 400°C, and, under atmospheric pressure, through it a continuous stream of 0.6 Nl/h of perfluoromethylvinylether is flown. After one hour, the leaving gases, analysed by gas-chromatography, I.R. spectrophotometry and mass spectrometry, result to be constituted by perfluoropropionyl fluoride (82 mol %), perfluoromethylvinylether (3%), hexafluoropropene (5%) and small amounts of other fluorocarbons, each present in an amount lower than, or equal to, 1%. The conversion is of 97%, the selectivity of 85%. After more than 40 running hours, the catalyst resulted to be still totally efficient. Examples 10-12 By operating inside the reactor of Example 9, and following the same modalities as of such Example, except for those as specifically described, the isomerization of perfluoromethylvinylether to perfluoropropionyl fluoride is carried out by using the catalysts and the operating parameters as reported in the following Table. Example 13 As the catalyst, MgF₂ is used. Through the reactor of Example 9, maintained at a temperature of 380°C, a stream of CF₃CF₂-O-CF=CF₂ is fed at a flow rate of 0.25 Nl/hour, under atmospheric pressure. After 1 running hour, the gases leaving the reactor, analysed as in Example 1, result to contain 90% of CF₃CF₂CF₂COF, and traces of CF₃CF₂-O-CF=CF₂, the balance being essentially constituted by CF₃CF=CF₂. The conversion results to be of 99%, the selectivity is of about 90%.

Claims: Process for the preparation of a perfluoroacyl fluoride, wherein the perfluoroacyl radical is a perfluoropropionyl or perfluorobutyryl group, characterized in that a perfluoroalkylvinylether wherein the perfluoroalkyl radical is a trifluoromethyl or an perfluoroethyl group, is thermally treated in the presence of a catalyst selected from: A) a fluoride of Li, Na, K, Cs or Rb, or a compound of Li, Na, K, Cs or Rb, which is easily fluorinated under the reaction conditions; B) a fluoride of Be, Mg, Ca, Sr, or Ba, or a compound of Be, Mg, Ca, Sr, or Ba, which is easily fluorinated under the reactio n conditions; C) a fluoroaluminate, fluorosilicate, fluorotitanate or fluorometallate of an alkali metal, or of a metal belonging to group II A of the Periodic Table of a compound, which is easily fluorinated to yield one of the above said fluoroaluminates, fluorosilicates, fluorotitanates or fluorometallates under the reaction conditions; D) a fluoride of a metal of the first transition series, or the corresponding metal, or a compound of such a metal, which is easily fluorinated under the reaction conditions; E) a fluoride of a lanthanide, or the corresponding metal or a compound of such a metal, which is easily fluorinated under the reaction conditions; F) an oxyfluoride of Si, Al, Ti, Ge, Sn or Pb, or a compound of Si, Al, Ti, Ge, Sn or Pb, which is easily fluorinated to yield one of the above-said fluorides under the reaction conditions. Process according to claim 1, characterized in that the compound of Li, Na, K, Cs or Rb, which is easily fluorinated under the reaction conditions, is an oxide, a hydroxide or a oxyhalide. Process according to claim 1, characterized in that the compound of Be, Mg, Ca, Sr, or Ba, which is easily fluorinated under the reaction conditions, is an oxide, a hydroxide or a oxyhalide. Process according to claim 1, characterized in that the fluoroaluminate, the fluorosilicate, the fluorotitanate or the fluorometallate of an alkali metal, or of a metal belonging to group IIA of the Periodic Table, is selected from K₃AlF₆, Cs₃AlF₆, K₂SiF₆, Cs₂SiF₆, CsCuF₃, KCuF₃ and CsNiF₃. Process according to claim 1, characterized in that the fluoride of a metal of the first transition series is selected from: CuF₂, NiF₂, ZnF₂, CoF₂, CoF₃, CrF₃, MnF₂, FeF₂ and FeF₃. Process according to claim 1, characterized in that the metal of the first transition series is selected from Cu, Ni, Zn, Cr, Mn, Fe and Co. Process according to claim 6, characterized in that the metal of the first transition series is copper. Process according to claim 1, characterized in that the fluoride of a lanthanide is selected from LaF₃ and CeF₄. Process according to claim 1, characterized in that the compound of Si, Al, Ti, Ge, Sn or Pb which is easily fluorinated to yield the oxyfluoride under the reaction conditions is an oxide or an oxide-hydroxide. Process according to claims 1, 2, 3, 6, 7 or 9, characterized in that the metal or the compound which is easily fluorinated under the reaction conditions is fluorinated in situ under the action of the perfluoroalkylvinylether or of another fluorinating agent. Process according to claim 10, characterized in that the other fluorinating agent is fluorine or hydrofluoric acid. Process according to claim 10 or 11, characterized in that the catalyst obtained by means of the in situ fluorination of the metal, or of the easily fluorinatable compound is activated in situ under the action of the perfluoroalkylvinylether at a temperature equal or higher than the reaction temperature. Process according to one of claims 1, 4, 5 or 8, characterized in that the pre-formed catalyst is activated in situ under the action of the perfluoroalkylvinylether at a temperature equal or higher than the reaction temperature. Process according to one or more of claims 1, 6, 7, 10, 11 or 12, characterized in that the metal is submitted to a thermal treatment at temperatures comprised within the range of from 300 to 650°C before being fluorinated. Process according to one or more of claims 1, 2, 3, 9, 10, 11 or 12, characterized in that the compound easily fluorinatable under the reaction conditions is submitted to a thermal treatment at temperatures comprised within the range of from 250 to 500°C before being fluorinated. Process accord ing to one or more of claims 1, 6, 7, 10, 11, 12 or 14, characterized in that when as the catalyst a metal of the first transition series is used, the reaction is carried out at temperatures comprised within the range of from 300 to 500°C. Process according to claim 16, characterized in that when as the catalyst Cu, Ni, Zn or Fe is used, the reaction is carried out at temperatures comprised within the range of from 350 to 450°C. Process according to one or more claims 1, 9, 10, 11, 12, 13 or 15, characterized in that when as the catalyst an oxyfluoride of Si, Al, Ti, Ge, Sn or Pb is used, or a compound of Si, Al, Ti, Ge, Sn or Pb is used, which is easily fluorinated to one of the above-said oxyfluorides under the reaction conditions, this latter is carried out at temperatures comprised within the range of from 250 to 400°C. Process according to claim 18, characterized in that when as the catalyst fluorinated silica is used, the reaction is carried out at temperatures comprised within the range of from 300 to 400°C. Process according to one or more of claims 1, 3, 10, 11, 12, 13 or 15, characterized in that when as the catalyst a fluoride of Be, Mg, Ca, Sr or Ba is used, or a compound of Be, Mg, Ca, Sr or Ba is used, which is easily fluorinated under the reaction conditions, this latter is carried out at temperatures comprised within the range of from 300 to 450°C. Process according to claim 20, characterized in that when as the catalyst magnesium fluoride is used, the reaction is carried out at temperatures comprised within the range of from 350 to 450°C. Process according to one or more of claims 1, 2, 10, 11, 12, 13 or 15, characterized in that when as the catalyst a fluoride of Li, Na, K, Cs or Rb is used, or a compound of Li, Na, K, Cs or Rb is used, which is easily fluorinated under the reaction conditions, this latter is carried out at temperatures comprised within the range of from 300 to 450°C. Process according to one or more of the preceding claims, characterized in that the process is carried out continuously, with a stream of perfluoroalkylvinylether being flown over a catalyst layer. Process according to one or more of the preceding claims, characterized in that the perfluoroacyl fluoride is purified of its unsaturated impurities by bubbling it, in the gas state, through liquid bromine.

Inventors: CASTELLAN, ARSENIO, CUZZATO, PAOLO, PASQUALE, ANTONIO
Applicants: AUSIMONT S.P.A.
Application year: 1987
Main classification: C07C53
IPC codes: C07C53, C07C67, B01J27, C07B61, C07C51