专利摘要:
1528342 Cross-linkable bromine-containing fluoropolymer compositions E I DU PONT DE NEMOURS & CO 23 March 1976 [27 March 1975] 15252/78 Divided out of 1528341 Heading C3P A composition comprises (A) a copolymer consisting of (1) up to 3 mole per cent of a brominecontaining olefin, sufficient being present to provide # 0À05 weight per cent of Br in the copolymer, with the remainder of the copolymer being provided by either (2a) at least one fluorine-containing, bromine-free C 2 -C 7 monomer wherein the F : C atomic ratio # 1, or (2b) a mixture comprising 50-99 mole per cent of tetra fluoroethylene, 1-50 mole per cent of a C 2 -C 4 olefin, and 0-30 mole per cent of vinylidene fluoride, and (B) 0À5-10% of an organic peroxide. In the examples the brominecontaining olefin is bromotrifluoroethylene, bromodifluoroethylene, perfluoroallyl bromide, 3,3- difluoroallyl bromide, 4-bromo-3,3,4,4-tetrafluorobutene-1, 4-bromoperfluorobutene-1, or vinyl bromide, while the other monomers are tetrafluoroethylene, perfluoromethyl perfluorovinyl ether, vinylidene fluoride, hexafluoropropylene and propylene.
公开号:SU747434A3
申请号:SU762325451
申请日:1976-02-27
公开日:1980-07-23
发明作者:Апотекер Дэвид;Джозеф Крусик Пол
申请人:Е.И.Дюпон Де Немур Энд Компани (Фирма);
IPC主号:
专利说明:

one
The invention relates to fluoropolymer-based compositions used in the manufacture of orifice fluoropolymer products.
In the industry engaged in the production and use of fluoroelastomers and fluoropolymer-plastic materials, there is a need for polymeric materials, whose curing can be carried out easily and economically. This applies, in particular, to those areas of application in which it is desirable to obtain a product with good resistance to aging when heated, to the action of solvents and / or chemicals that cause corrosion, and resistance to creep is of great importance.
Known compositions based on fluoropolymers, for example, a copolymer of trifluoroethylene, fluoride vinylidene and perfluoroolefine Sh.
However, these compositions have low technical characteristics.
Closest to the technical essence of the invention is a polymeric composition containing a fluoropolymer copolymer of hexafen-propylene with vinylidene fluoride - and organic peroxide 2.
However, this curable composition also has low performance.
The purpose of the invention is to increase the resistance of the composition to heat, creep and the action of aggressive media.
The goal is achieved by
10 that composition I containing organic peroxide and a fluoropolymer contains as the last a copolymer, the polymerized units of which are
a) from links whose source
15 is a brominated olefin selected from the group including bromotrifluoroethylene, bromofluoroethylene, perfluoroallyl bromide, 4-bromo-3,3,4,4-tetrafluoro-Uten-1, 4-bromoperfluorobutene-1 and
20 vinyl bromide, in the amount of 0.372, 4 mol.%,
b) from the units whose source is monomers — 65-69.6 mol.% tetrafluoroethylene and 30-33.5 mol.% per25 fluoromethylperfluorovinyl ether; or 52–55 mol% tetrafluoroethylene, 31–45 mApp.% propylene and vinylidene fluoride residue, or 51–78 mol% vinylidene fluoride, 20–49 mol% hexafluoro 30
.propylene and / or tetrafluoroethylene and
the residue perfluoromethyl perfluorovinyl ether, in the following ratio of components, parts:
Fluoropolymer100
Organic
peroxide 0.5-10
The composition according to the invention may also contain 1-15 wt. Of magnesium oxide or calcium.
According to another embodiment of the invention, besides all the above components, it may contain trialisyl isocyanurate in the amount of 0.510 parts by weight.
The copolymer must have a sufficient number of units so that it contains approximately 0.3-1.5% by weight of bromine. Bromotrifluoroethylene is particularly recommended.
In one of the most preferred embodiments of the invention, the new copolymer is a fluoroelastomer, in which the component b consists of units, the source of which is approximately tetrafluoroethylene and perfluoromethylperfluorovinyl ether.
In other embodiments, the copolymer is a fluoropolymer, in which component b consists of units, the source of which are monomers in any of the above combinations,
In preparing the composition, it is recommended to use a free radical initiating agent, and to carry out a reaction to obtain a copolymer in the presence of free radical polymerization in an emulsion. Free radical initiating agents most suitable for such a reaction include ammonium persulphate, sodium persulphate, potassium persulphate, or mixtures of two or more of these compounds. Other water-soluble inorganic peroxide compounds are also suitable, for example, perphosphates, perborate and sodium, potassium and ammonium percarbonates. The initiator can be used in combination with a reducing agent such as sulfite, bisulfite, metabisulfite, hyposulfite, thiosulfate, phosphite or hypophosphite of sodium, potassium or ammonium, or in combination with a salt of ferrous iron, monovalent copper or silver or other easily oxidizable metal compound . It is also possible to use well-known organic: free radical free radical initiators,. preferably in combination with a surfactant such as sodium lauryl sulfate or ammonium perfluorooctonoate.
Surfactant can be selected from among those related. which it is known that they are successfully used in the preparation of fluoropolymers,
A surfactant can also be used with inorganic initiators.
During the emulsion polymerization reaction, known chain transfer agents may also be present, but in many cases this is not recommended.
After completion of the emulsion polymerization reaction carried out under the recommended conditions, the copolymer can be isolated from the polymer latex formed by known methods, for example, by coagulation, carried out with the introduction of electrolytes or by WEDGMoin followed by centrifuging or filtering and drying the copolymer
The reaction, in which the formation of a copolymer occurs, can also be carried out in a block method or in an organic liquid medium containing an organic free radical initiator. It is generally recommended that none of the organic liquids present should be a chain transfer agent.
During the preparation of the copolymer, the reaction mixture is preferably heated in a reactor in the presence of an inert gas at a temperature of 50ISOc and pressure above atmospheric, for example under a pressure of 7-140 kg / cm, preferably 35-105 kg / cm. In one of the most preferred options, the polymerization is carried out continuously and the average duration the reaction mixture stays in the reactor for about 5-30 minutes, and sometimes reaches 2-3 hours. The duration of the reaction can be calculated by dividing the reactor volume by the volume of latex formed per hour.
New fluoropolymer in most cases has a true viscosity of about 0.01 or higher, preferably about 0.2 to 1.2.
Dialkyl peroxide is preferably used as the organic peroxide. An organic peroxide is selected to serve as a curing agent for the composition in the presence of other components that will be present in the final composition, at curing temperatures not causing excessive curing during mixing or other operations prior to the curing process. Dialkyl peroxide is particularly desirable, decomposing at temperature, if the composition is to undergo processing, at elevated temperatures prior to its unscrewing. In many cases, di-tert-butyl peroxide can be used, in which a tertiary carbon atom is bound to the oxygen atom of a parecis group. To the most
Valuable peroxides of this type include 2,5-dimethyl-2,5-di- {tritbutillo) -hexene-3 and 2,5-dimethyl-2, 5-di- (t-butylperoxy) -hexane. As the peroxide, dicumyl peroxide, dibenzoyl peroxide, t-butyl perbenzoate and di-tl, 3-dimethyl-3- (tert-butyl-peroxide) -butil-carbonate, etc. can be used.
You can get the composition at room temperature in the form of a liquid film-forming composition containing an organic solvent to / or a diluent, applying a layer of liquid composition on a substrate, drying this layer and curing it at a temperature below.
The composition, which is a mixture of fluoropolymer and peroxide, is a marketable product that can be supplied to the manufacturers of finished products if they wish to modify the material with some other additives in accordance with the necessary requirements. Magnesium oxide or calcium and trilyl isocyanurate may be added to the composition.
The composition may also contain one or more targeted additives. By adding a suitable solvent, a liquid composition can be prepared, which can be used to produce adhesives, coatings, films, and the like.
When preparing the fluoropolymer composition, the copolymer can be mixed with other components using any known mixer, for example, a roller type rubber mixer or a closed type rubber mixer (Banbury) can be used to make the process at a temperature below the decomposition point of organic peroxide.
Curing of compositions containing the proposed components is, in most cases, recommended to be carried out by heating it for 160 minutes at a temperature of about 149,204 ° C. You can use conventional presses to cure rubber and harden plastic material. If it is desirable to obtain a product with maximum heat resistance and stability, it is recommended to carry out additional curing, in which the product is heated for about 1-48 hours at a temperature of about 180-300 ° C.
The following examples illustrate the invention. All quantities, except when it is particularly oroBofieHO, are expressed in weight percent and parts by weight.
Example 1 A suitable for curing fluoropolymer encompassed by the invention, in the form of an elastomeric copolymer of tetrafluoroethylene, perfluoromethylperfluorovinyl ether and bromotrifluoroethylene, is prepared in a continuous manner, from the following operations:
1. A continuous feed of 5 three monomers described in Table 1 is produced,
into a stainless steel reactor, with a capacity of 3.8 liters, purged with nitrogen with a stirrer, rotating at 500 rpm, heating the contents of the reactor at a temperature of 700 ° C under a pressure of 42 kg / cm - The resulting reaction mixture is subjected to emulsion polymerization while passing through reactor. The residence time of the mixture in the reactor was 2.7 hours (calculated on the basis of dividing the reactor volume of 3.8 liters by the emulsion removal rate of about 1.4 liters / h). The monomers and their feed rate are shown in Table 1.
2. During operation 1, a solution consisting of 6.38 g of persulphate is continuously fed into the reactor at the netJBoro metering pump.
5 ammonium, 4.5 g of sodium hydrogen phosphate secondary phosphate heptahydrate and 126.0 g of ammonium perfluorooctanoate dissolved in 600 ml of water (distilled), with simultaneous introduction into the reactor using a second dosing pump for 1 h of a solution consisting of 5, 25 g of sodium sulfite, dissolved in 600 MP of water. The pH of the reaction mixture is maintained at 6.1,
5 3. The latex of the copolymer formed during operations 1 and 2 is continuously removed from the reactor. The latex passes first through a check valve, adjusted in such a way that the reactor maintains a pressure of 42 kg / cm and then enters a sealed container, from which the exhaust gases (unreacted monomers)
5, a gas chromatograph chromatograph is supplied, in which their composition is given, as shown in the table.
4. After the latex formed during the initial four residence periods of the reaction mixture in the reactor is removed, collect the desired amount of latex, mix it up to ensure greater homogeneity. Get latex with a pH of 6.1, with a solid content of the copolymer of 26.0%.
5 5. The resulting latex copolymer is then isolated by gradually adding a 4% aqueous solution of potassium sulphate-aluminum to coagulate the copolymer, the copolymer particles are washed with distilled water / the water is removed using a filtering apparatus and the copolymer is dried in an air circulating oven temperature 100 ° C to moisture content5. or less than 1%.
260 14 246 56.0 68.5
300 117 183 41.6 30.0
10 1 9 2.4 1.5
The resulting copolymer is an elastomer, which can be cured according to the method described in Example 2. As indicated in the table, in each 100 g, about 56 g of polymerized tetrafluoroethylene, 41.6 g of polymerized perfluoromethyluerfluorovinyl ether and 2 , 4 g of bromotrifluoroethylene. The true viscosity of the copolymer is 0.38. This characteristic was determined at a temperature and polymer concentration of 0.2% by weight in a solvent consisting of 58% by volume of 2,3,3-trichloroperfluorobutane, 39% by volume of FC-75 and 3% by volume of diethylene glycol dimethyl ether. The solvent FC-75 is a fluorinated cyclic ether, the empirical formula of which is Cd F, c O, manufactured by the Minnesota Mining and Menfefechuri Company (MM). Instead of this solvent, it is possible to use the product of fluorination of tetrahydrofuran, carried out to obtain a solvent, consisting essentially of 2-perfluorobutyl perfluorotetrahydrofuran. The content of the carb in the copolymer is 1.2% by weight. The copolymer is insoluble in aliphatic and aromatic carbons and hydrogens. It can be mixed with additives, as described in example 2 and overiden. Example 2. A curable fluorine elastomer is obtained by repeating the experiment described in example 1 / with the exception that the feed rate is set so that a copolymer containing 65.0 mol% of tetrafluoroethane units, 33.5 mol% can be obtained. % of links perfluoromethylperfluorovinyl ether and 1.5 mol.% links bromotrifluoroethylene. The copolymer obtained in example 2 contains the same amount of bromine and has the same true bone as the copolymer obtained in example 1. A curable composition is prepared by mixing on a two-roll rubber mixer with a roll temperature of about - 100 hours copolymer, 10 hours SAF carbon black , 4 parts of magnesium oxide, 2 parts of calcium oxide, 4 parts of triallylisodianurate and 4 parts of a peroxide curing agent, 45% of 2,5-dimethyl-2,5-di- (tert-butylperoxy) hexane-3 and 55% of an inert filler , manufactured by Wallace and Tiernen under the brand name Luperko 130 XL, The curing ticks are carried out using an SDT (oscillator disk rheometer) according to the method described in patent CL4A No. 3876654 at the test temperature. With a cure time of 30 minutes, the torque value increases by 138 cm-kg. In this case, a fast and high degree of cure is achieved. Shore hardness (durometer A) of the composition corresponds to 92 when tested according to ASTM D-676 on samples of the composition, cured in a press, for 15 minutes at a temperature of 190 ° C under a pressure of 18150 kg with additional curing in a furnace according to the following mode: curing for 6 hours at a temperature of 204С, holding at this temperature for 18 hours, hardening for 6 hours at a tempo of 288 ° C, holding at this temperature for 18 hours. Residual deformation of the composition under compression 50 when tested at a temperature of 204 ° С for 70 h on meth ASTM D-395-61, method B, using as test samples. tablets with a thickness of 1.27 cm, a diameter of 1.9 cm, opened in stages, as indicated above, Example 3. A curable elastomer is prepared, a composition is prepared from it and cured by the method. described in example 2, with the following exceptions: 1) the monomer feed rate is set to obtain a copolymer containing 65.6 mol.% tetrafluoroethylene units, 83.0 mol.% perfluoromethylperfluoro vinyl ether and 1.4 mol. % of bromotrifluoroethylene. This copolymer contains 0.9% by weight bromine and has a true viscosity of 0.35 (measured as described in Example 1); 2) in the preparation of curable compositions, the amount of carbon black is 5 hours, magnesium oxide is 5 hours and the peroxide curing agent is 5 hours; 3) test specimens are cured in a press for 30 minutes at a temperature. And additional curing is carried out as described in example 2. Tensile strength at break (0) 147 kg / cm value of the relative elongation at discharge (L) 60%, and residual strain at break 3% {ASTM D-412). For comparison, a fluoroelastomer is obtained beyond the scope of the invention, and a composition is prepared from it, which is cured as described in Example 3, except that the monomer is fed in this way (the amount of bromotrifluoroethylene is increased), so that the copolymer obtained contains 7.2 % by weight of bromine (this corresponds to 11.4 mol.% units of bromotrifluoroethylene). The ratio of tetrafluoroethylene and ether is the same as in measure 3, i.e. it corresponds to 2: 1. The samples of the cured product obtained are so fragile that it is not possible to obtain indicators of tensile strength, elongation and residual strain at break. Example 4. A curable composition based on a fluoroelastomer is prepared and cured as described in Example 2, except for the fact that bromotrifluoroethylene is replaced by bromofluoroethylene. The feed rate of the monomers is set to obtain a copolymer containing 69.63 mol.% Of tetrafluoroethylene units, 30.0 mol.% Of perfluoromethylperfluorovinyl ether units and 0.37 mol.% Of bromodifluoroethylene units. This copolymer contains 0.3% by weight bromine and has a true viscosity of 0.27 (measured by the method described in Example 1). In tests on SDR, the torque increase is 46 cm-k with a cure time of 30 minutes. The composition has a Shore hardness (scale A) 90, residual deformation under compression 99, ® 194 kg / s L 140%, modulus at 100% elongation (M, ° A according to ASTM D-412) 147 kg / cm and residual deformation at a break of 19%. Example 5. A fluoroelastomer-based composition was prepared as described in Example 2, with the exception that bromotrifluoroethylene was replaced with perfluoroallyl bromide. The feed rate of the monomers is set to obtain a copolymer containing 69.2 mol% of perfluoromethylperfluorovinyl ether units, 0.8 mol% of perfluorlyl bromide units. This copolymer contains 0.3% bromine by weight and has a true viscosity of 0.21. When testing for SDTs, the torque increase in 30 minutes is 19.6 cm-kg. The composition has (about 151 kg / cm L100%, 151 kg / cm and residual deformation at break 13%. Example 6. A composition based on a fluoroelastomer is prepared as described in Example 2, with the exception that bromotrifluoroethylene is replaced by 3.3 -difluoroallyl bromide. The monomer feed rate is set to obtain a copolymer containing 66 mol.% tetrafluoroethylene units, 33 mol.% simple perfluoromethylperfluorovinyl Zfira units and 1 mol.% bromide units. The copolymer contains 0.7% by weight of bromine. on SDT increase in torque for 30 m n is 23 cm-kg, the composition has & 103 kg / cm - I 90% and residual deformation at break 8%. Example 7. A fluoroelastomer is prepared as in example 1 with the following exceptions: monomers are introduced into the reactor - 56 hours Vinylidene fluoride, 44 parts of hexafluoropropylene and 0.8 parts of brooksp: rifto-zstilene B. A 2-liter reactor was used in experiments. The pressure in the reactor was 63 kg / cm, the stirring temperature, the pH value was 3.3. about 15 min Operation (2) consists of feeding to the reactor (for every 100 hours, monomer) 40 parts of water containing 0.3 parts of ammonium persulfate and 0.05 parts of sodium hydroxide. The resulting copolymer contains 59, .1% vinylidene fluoride units, 40% hexafluoropropylene units and 0.9% bromotrifluoroethylene units (in weight percent). Latex contains 18.7% solids - copolymer. The fluoroelastomer obtained has a Mooney viscosity of 94 at a temperature of 100 ° C. This viscosity index, measured on a Mooney plastometer, is determined using a large rotor and a 10-minute shear duration. Example 8: A mega 8, A curable composition based on a fluoroelastomer is prepared by mixing on a two-roll mixer with a roll temperature around the following components; 100 parts of the copolymer, the preparation of which is described in Example 1, 15 parts MT, 10 hours, fine-grained bituminous coal (Austin Black), 1 H-. calcium oxide hydrate, 2 hours; calcium silicate (microcellular E), 4 parts of triallylisocyanurate and 4 parts of peroxide curing agent (luperko 101 XL). Samples of the test composition are cured in a press for 30 minutes at a temperature of 177-sec and subjected to additional curing in a furnace, the temperature being brought to 26 ° C for 4 hours and kept at this temperature for 18 hours. The resulting hardened fluoroelastomer has a residual deformation under compression 27, © 154 kg / cm, L 17 and 75.5 kg / cm. Example 9. The experiments described in examples 7 and 8 were repeated, but with the following changes. The copolymer is prepared from 82 parts of vinyl denfluoride, 67 parts of hexafluoropropylene, 1.4 parts of 4-bromo-3, 3, 4, 4-tetrafluorobutane -1 and (600 parts of monomer) 600 parts of water containing 0.4 hours ammonium persulfate and. 0.08 parts sodium hydroxide. The pH of the reaction mixture was 4.3, the residence time of the reaction mixture in the reactor was 20 min, the solid co-dimer content in the latex was 18%. The resulting copolymer contains 58 ,. 9% of vinylidene fluoride units, 40% of hexafluoropropylene units and 1.1% of bromo-containing compounds. The fluoroelastomer obtained has a Mooney viscosity of 100 (method described in Example 3, Example 3), its true viscosity is 1.57 at a temperature of 30 ° C and a concentration of 0/1% by weight, in a solvent consisting of 87% by volume: rofuran tetrahydride and 13% by volume of N, M dimeti of formarv1ida. A curable composition based on a fluoroelastomer base is prepared by mixing on a roller mixer 10Q parts from polymer, 15 hours, carbon black MT, 10 hours, a / steel black, 1 part magnesium oxide, 3 .4, dibasic lead phosphite, 3.3 hours trialily isocyanurate and 3.3. The peroxide curing agent described in Example 8. The test specimens after opening them according to the method described in Example 8 have residual deformation after compression 25, Q 144 kg / L 185% and M., 59.6 kg / kg cm. . When making a fluoropolymer that runs outside the scope of the invention, according to the same method, but without using a bromine-containing compound, a copolymer of vinylidene fluoride and hexafluoropropylene is obtained, and is used to prepare the composition and cure in a press. The resulting porous product cannot be used for technical applications. Example 10. A fluoropolymer was prepared according to the method described in Example 7, except that the copolymer was prepared from 77 parts of tetrafluoroethylene, 23 parts of propylene, 1.1 parts of bromotrifluoroethylene and (for every 100 parts of monomer) 359 hours , water containing 2.87 parts of surfactant (33% aqueous solution of sodium lauryl sulfate), 1.65 parts of ammonium persulfate and 1.08 parts of sodium hydroxide. The reaction conditions are as follows: a pressure of 42 kg / cm, a temperature of 80 ° C, a residence time of the reaction mixture in the reactor for 3 hours, a pH value of 9.0. The content of solid copolymer in latex is 20.7%. The copolymer contains about 73.4% tetrafluoroethylene, 25.3% propylene and 1.3% bromotrifluoroethylene (by weight). Mooney viscosity 61. A curable composition based on fluoropolymer is prepared by mixing the following components on a two-roll rubber mixer: 100 parts of copolymer, 30 hours, carbon black MT, - 4 parts of magnesium oxide, 2 hours, calcium oxide, 4 parts of trilylisocyanurate and 5 hours of peroxide curing agent, the composition of which is given in example 2. Samples of the test composition are subjected to curing in a press for 30 minutes npij temperature 177 ° C and additionally cured in a furnace, and for 4 hours the temperature is raised to, and then kept 24 h at a temperature of 130CC, Paul chenny fluoropolymer has a residual strain after compression 50 (0-rings tested for 70 hours at a temperature of ASTM method) 0 63 kg / cm, L and M 200%. 00 28 kg / cm. Example 11. A fluoropolymer is prepared as described in example 10, except that the copolymer is obtained from 68 h. tetrafluoroethylene, 18.3 parts of vinylidene fluoride, 13.1 parts of propylene, 0.67 parts of bromotrifluoroethylene and (per 100 hours, monomer) 343 hours, water containing 3.1 parts of the surfactant described in Example 10 , 1.96 parts of ammonium persulfate and 1.37 parts of sodium hydroxide. The residence time of the reaction mixture in the reactor is 90 minutes. The content of solid copolymer in latex is 17.8%. The copolymer contains approximately
68.6% tetrafluoroethylene, 12.9% vinylidene fluoride, 17.5% propylene and 1.0% bromotrifluoroethylene.
A fluoropolymer-based curable composition was prepared according to the procedure of Example 10. Test specimens were cured as described in Example 10, but at an additional curing temperature.
The resulting cured, valuable fluoropolymer has a residual strain after compression 85, & 80.4 kg / cm
45.6 kg / cm 140% and M
yo
Example 12. A fluoropolymer was prepared according to the method of Example 8, except that the copolymer was prepared from 46 parts of vinylidene fluoride, 51 parts of hexafluoropropylene, 41 parts of tetrafluoroethylene, 1.2 parts of bromotrifluoroethylene and (for every 140 hours monomer) 600 parts of water containing 0.59 parts of ammonium persulfate and 0.15 sodium hydroxide. The pH of the reaction mixture is 2.9, the residence time of the reaction mixture in the reactor is 20 minutes. The content of solid copolymer in latex is 17.7%. The copolymer contains 36% vinylidene fluoride, 31% hexafluoropropylene, 32% tetrafluoroethylene and 1% bromotrifluoroethylene.
Prepare a fluoropolymer-based curable composition according to the method described in Example 9. The amount of triallyl isocyanurate is 1.5 hours and the amount of peroxide curing agent described in Example 8/2 hours. Test specimens are prepared by curing in a press for 15 minutes at a temperature of 177s and subjected to additional curing in a furnace with an increase in temperature for 4 hours before and at 18 hours at this temperature.
The obtained hardened fluoropolymer has a residual deformation under compression 24 (tablets, exposure 70 hours at a temperature of 232 ° C), 0 150 kg / cm L 185% and M,
fOO 57.7 kg / cm
Example 13. A fluoropolymer according to Example 7 is prepared, except that the copolymer is prepared from 55 parts of vinylidene fluoride, 35 parts of perfluoromethylperfluorovinyl ether, 10 parts of tetrafluoroethylene and 0.5 parts of vinyl bromide (added in the form of 16% by weight the volume of solution in trichlorotrifluoroethane), and (for every 100 hours of monomer) 400 parts of water containing 0.6 parts of ammonium persulfate and 0.1 parts of sodium hydroxide. The pH of the reaction mixture is 3.3, the residence time of the reaction mixture in the reactor 30 min, the content of solid copolymer in latex. The copolymer contains 55% vinylidene fluoride, 34.5% perfluoromethylperfluorovinyl ether, 10% tetrafluoroethylene and 0.5% vinylbro. (weight percent content of copolymerized units), Mu viscosity, none 32.
Prepare a curable composition 5 based on a fluoropolymer by mixing on a two-roll mixer 100 parts of copolymer, 30 parts of carbon black, 1 part of magnesium oxide 3 hours, dibasic lead phosphite, 5 parts of peroxide
n curing agent, the composition of which is given in Example 9, and 4 o'clock, triallylisocyanurate. Test specimens are prepared by curing in a press for 15 minutes at a temperature followed by raising the temperature for 4 hours to 260 ° C and holding for 24 hours at a temperature of 260 seconds. The obtained hardened fluoropolymer has a residual deformation under compression 66 (0-shaped rings 7 hours
 kept at a temperature of 0.205 kg / cm, L 165% and M, 00 54.2 kg / cm. In the manufacture of a fluoropolymer that goes beyond the scope of the invention, for comparison, the process is carried out similarly,
5 but without vinyl bromide. The resulting vinylidene fluoride copolymer, perfluoromethylperfluorovinyl ether and tetrafluoroethylene are taken for the preparation of the composition and cured
0 at a temperature of 15 minutes, but at the same time receive a porous product that has no technical value.
权利要求:
Claims (2)
[1]
Invention Formula
5 1- Polymer composition containing fluoropolymer and organic peroxide, characterized in that, in order to increase its resistance to heat, creep and the action of corrosive media, it contains as a fluoropolymer a copolymer, the polymerized units of which consist of:
a) from the units, the source of the cattle is bromine-containing olefin,
selected from the group including bromotrifluoroethylene, broedifluoroethylene, perfluoroallyl bromide, 4-bromo-3,3,4,4-tetrafluorobutene-1, 4-bromoperfluorobutene-1 and vinyl bromide in an amount of 0.37-2.4 mol%.
b) from the links, the source of which is mono-measures - 65-69.6 mol.% tetrafluoroethylene and 30-33.5 mol.% perfluoromethylperfluorovinyl ether, or 52-55 mol.% tetrafluoroethylene, 31-45 mol.% propylene and vinyl residue, centrifluoride, or 51-78 mol.% vinylidene fluoride, 20-49 mol.% hexafluoropropylene and / or ethylene tetrafluoro0 and the perfluoromethylperfluorovinyl ether residue, in the following ratio of components, parts: Part: Fluoropolymer 100 Organic
5 peroxide 0.5-10, 15. ,; r- 2, Composition according to 0.1, about t l with the fact that it additionally contains 1-15 weight parts. magnesium oxide or calcium. 3. The composition according to claim 2, about t is about the fact that it up to-5 contains 0.5 to 10 parts by weight. . triallylisocyanurate. 7474 34 -b Sources of information taken into account during the examination 1. CTJA patent No. 3053818, cl. 260-77, publ. thirty..
[2]
2. US Patent No. 29449E5, cl. 260-41, published. 15.C5.59 (prototype).
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同族专利:
公开号 | 公开日
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DK149170B|1986-02-24|
US4035565A|1977-07-12|
JPS5281360A|1977-07-07|
IT1061505B|1983-04-19|
DK571777A|1977-12-21|
GB1528341A|1978-10-11|
CA1076298A|1980-04-22|
IE42664B1|1980-09-24|
NL162669B|1980-01-15|
LU74645A1|1977-01-28|
SE410001B|1979-09-17|
JPS534115B2|1978-02-14|
AU1239876A|1977-10-13|
US4214060A|1980-07-22|
DE2612360C3|1979-04-19|
DK148061B|1985-02-18|
FR2305462A1|1976-10-22|
DE2612360A1|1976-09-30|
IE42664L|1976-09-27|
DK148061C|1985-08-12|
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法律状态:
优先权:
申请号 | 申请日 | 专利标题
US05/562,648|US4035565A|1975-03-27|1975-03-27|Fluoropolymer containing a small amount of bromine-containing olefin units|
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