Novel block copolymer and preparation thereof

Abstract: A block copolymer comprising at least two kinds of blocks in a molecule wherein at least one kind of the blocks is a homopolymeric or random copolymeric block comprising at least one block selected from the group consisting of: (a) a block consisting of at least two repeating units selected from the formulae: -(CH₂CF₂CF₂O) a - -(CHClCF₂CF₂O) b - -(CCl₂CF₂CF₂O) c - -(CHFCF₂CF₂O) d - -(CFClCF₂CF₂O) e - -(CF₂CF₂CF₂O) f - a, b, c, d, e and f are each 0 or a positive integer and satisfy the following equations: 2 ≦ a+b+c+d+e+f ≦ 200 and 1 ≦ a+c+d+f, (b) a block consisting of the repeating units of the formula: wherein p, q and r are each 0 or a positive integer and satisfy the following equations: 2 ≦ p+q+r ≦ 200 and 1 ≦ p+q, (c) a block consisting of the repeating units of the formula: wherein R f1 and R f2 are the same or different and C₁-C₃ perfluoroalkyl, k and m are each a positive integer and satisfy the equations: 2 ≦ k+m ≦ 50 and 0.2 ≦ m/(k+m), and n is an integer of 0 to 10, and (d) a block consisting of repeating units of the formula: -(CF₂CFCl) x - wherein x is an integer of 2 to 11, and at least one kind of other blocks is a homopolymeric or random copolymeric block consisting of repeating units of the formula: -(CF₂CXY)- wherein X is hydrogen or fluorine, Y is hydrogen, chlorine, fluorine, difluoromethyl or C₁-C₈ perfluoroalkyl or perfluoroalkoxy provided that when the former block consists of the repeating unit (d) alone, the combination of X=fluorine and Y=chlorine is excluded, the content of the latter block being 1 to 95 % by weight based on the whole weight of the block copolymer and a number average molecular weight of the whole block copolymer being from 1 x 10³ to 1 x 10⁶ and a process for preparing same.

Description: The present invention relates to a fluorine-containing block copolymer comprising at least two kinds of blocks in a molecule and more particularly to a fluorine-containing polyether block copolymer. A linear polyether comprising repeating units of the formulae: -(CH 2 CF 2 CF 2 O) a - -(CHClCF 2 CF 2 O) b - -(CCl 2 CF 2 CF 2 O) c - -(CHFCF 2 CF 2 O) d - -(CFClCF 2 CF 2 O) e - -(CF 2 CF 2 CF 2 O) f - wherein a, b, c, d, e and f are each 0 or a positive integer and satisfy the following equations: 2 ≤ a+b+c+d+e+f ≤ 200 and 1 ≤ a+c+d+f is known (cf. Japanese Patent Kokai Publication Nos. 137928/1985, 202122/1985 and 113616/1986 and EP-A-0148482). Japanese Patent Kokai Publication No. 3495/1978 or U.S. Patent No. 4,158,678 discloses a fluorine-containing polysegmented polymer. However, a block copolymer comprising the above described repeating units has not been known. EP-A-0180996 describes a grease composition comprising a halogen-containing polyether having the above described repeating units wherein the indices a to f have the same meanings as defined above, and a fluororesin in an amount of 0,5 to 60% by weight. An object of the present invention is to provide a novel block copolymer which is useful as a grease or an ingredient of a grease composition. Figs. 1 and 2 show shear stress-shear rate curves for the blocked grease and the non-blocked grease in Example 7, respectively. According to the present invention, there is provided a block copolymer comprising at least two kinds of blocks in a molecule wherein at least one kind of the blocks (hereinafter referred to as "block A") is a homopolymeric or random copolymeric block comprising at least one block selected from (a) a block consisting of at least two repeating units selected from the formulae: -(CH 2 CF 2 CF 2 O) a - -(CHClCF 2 CF 2 O) b - -(CCl 2 CF 2 CF 2 O) c - -(CHFCF 2 CF 2 O) d - -(CFClCF 2 CF 2 O) e - -(CF 2 CF 2 CF 2 O) f - wherein a, b, c, d, e and f are each 0 or a positive integer and satisfy the following equations: 2≤ a + b + c + d + e + f ≤200 and 1≤ a + c + d + f , (b) a block consisting of the repeating units of the formula: wherein p, q and r are each 0 or a positive integer and satisfy the following equations: 2 ≤ p+q+r ≤ 200 and 1 ≤ p+q, (c) a block consisting of the repeating units of the formula: wherein R f1 and R f2 are the same or different and C 1 -C 3 perfluoroalkyl, k and m are each a positive integer and satisfy the equations: 2 ≤ k+m ≤ 50 and 0.2 ≤ m/(k+m), and n is an integer of 0 to 10, and at least one kind of other blocks (hereinafter referred to as "block B") is a homopolymeric or random copolymeric block consisting of repeating units of the formula: -(CF 2 CXY)- wherein X is hydrogen or fluorine, Y is hydrogen, chlorine, fluorine, difluoromethyl or C 1 -C 8 perfluoroalkyl or perfluoroalkoxy. The content of the latter block is 1 to 95 % by weight based on the whole weight of the block copolymer and the number average molecular weight of the whole block copolymer is from 1 x 10 3 to 1 x 10 6 . A typical block copolymer of the present invention has a block structure of A-B or A-B-A. The block copolymer of the present invention may be prepared by polymerizing at least one fluorine-containing olefin of the formula: CF 2 =CXY wherein X and Y are the same as defined above in the presence of an iodinated compound comprising the block A and an iodine atom at at least one end, and a radical-generating source. Chain propagation of the fluorine-containing olefin is stopped by the elimination of iodine atom from the iodine-containing compound, namely a chain transfer reaction. However, since a bonding between the polymer end and the iodine atom formed by the chain transfer reaction at the chain end is relatively weak, and olefinic repeating units can be easily added by cleaving said bonding in the presence of a radical-generating source and an olefin, the chain propagation reaction can be reinitiated in the presence of a radically polymerizable compound, when a radical is formed at the chain end by the radical-generating source. Therefore, the polymer chain end acts as if it were a living end in an ionic polymerization. The block copolymer of the present invention has an iodine atom at at least one chain end. If desired, the iodine atom may be substituted with other atom or an atomic group to stabilize or activate the block copolymer. Examples of other atom or atomic group are hydrogen, fluorine, chlorine, bromine, -CF 2 H, -CF 2 Z, -CH 2 OH, -CH 2 CH 2 OH, -COZ, -COR, -COOH, -COOM, -COOR, -CF 2 R, -CH 2 NH 2 , -CH 2 CH 2 NH 2 , -CH 2 NCO, -CH 2 CH 2 -NCO, -CN, -N 3 , -CH 2 OCOR, -SO 3 H, -SO 3 M, -PO(OH) 2 , wherein Z is fluorine, chlorine or bromine, M is ammonium or monovalent metal, and R is alkyl or aryl. The other end of block copolymer (other than the iodine atom) has an end group corresponding to the kind of the initiator which is used in the preparation of a polymer which comprises the above described repeating units. The iodinated compound to be used for the preparation of the block copolymer of the present invention (namely, the block A having an iodine atom at at least one end) may be prepared by iodinating a known compound comprising at least one of the blocks (a) to (c). The compound comprising the block (a) is disclosed in Japanese Patent Kokai Publication Nos. 137928/1985, 202122/1985 and 113616/ 1986 and EP-A-0148482, the compound comprising the block (b) is disclosed in Japanese Patent Publication No. 45719/1974 and U.S. Patent No. 3,250,807, and the compound comprising the block (c) is disclosed in Japanese Patent Kokai Publication No. 189210/1983 and U.S. Patent No. 4,499,249. Examples of the fluorine-containing olefin are vinylidene fluoride, tetrafluoroethylene, trifluoroethylene, trifluorochloroethylene, hexafluoropropylene, pentafluoropropylene, perfluoromethyl vinyl ether, perfluoroethyl vinyl ether and perfluoropropyl vinyl ether. A ratio of the iodinated compound and the fluorine-containing olefin depends on the ratio of the block A and the block B in the block copolymer. Any conventional radical-generating source may be used according to the present invention. The preferred radical-generating sources are light and heat, which can selectively cleave the I-C bonding in the iodinated compound. As light, one having a wavelength of from infrared range to ultraviolet range can be used. Although actinic ultraviolet light may be used, it cleaves not only the I-C bonding but also other bondings to generate radicals. The same phenomenon is observed when ionizing radiation is used as the radical-generating source. When heat is used as the radical-generating source, preferably a temperature not lower than 200°C is applied. It is possible to use, as the radical-generating source, a conventional radical polymerization initiator which induces substantially no chain transfer reaction and is decomposed at a moderate rate under radical polymerization conditions. As the radical polymerization initiator, organic or inorganic peroxides, azo compounds, organometallic compounds, metals, are exemplified. Among them, the organometallic compounds are less preferred, since they generate radicals by eliminating not only the iodine atom but also other atoms or atomic groups. Preferred examples of the radical polymerization initiator are persulfates (e.g. potassium persulfate and amminium persulfate), hydrogen peroxide, (R f CO) 2 O 2 , R f OOR f , R f C(O)OOR f , (R f ) 3 COOC(O)OC(R f ) 3 , N 2 F 2 , R f -N-N-R f , Hg(R f ) 2 , Li, K, Na, Mg, Zn, Hg and Al wherein R f is polyfluoroalkyl. When the radical polymerization initiator is used, it is preferred to keep its concentration as low as possible so as to suppress a termination reaction caused by bonding of the radicals and to predominantly proceed the chain propagation. A polymerization temperature may be any temperature insofar as the reaction is initiated and the produced polymer chain is not thermally decomposed. Preferably, it is from -20°C to +150°C when the radical-generating source other than heat is used. When heat is used, a temperature not lower than 200°C, preferably not lower than 250°C is applied. A polymerization pressure is not critical in the present invention. Preferably, it is from atmospheric pressure to autogenous pressure. The radical polymerization may be carried out in any conventional manner such as bulk, solution, suspension and emulsion polymerization. All the steps of the polymerization can be carried out in the same manner, although the steps may be carried out in different manners from each other. In view of homogeneity of the reaction system, emulsion polymerization is most preferred. Other preferred polymerization methods are solution polymerization and suspension polymerization utilizing a solvent which is essentially inactive against radical. Examples of such solvent are perfluoro(dimethylcyclobutane), perfluorocyclohexane, dichlorotetrafluoroethane, trichlorotrifluoropropane, polyfluoroalkanes, or perfluoro(ethylene glycol methyl ethyl ether). The novel block copolymer of the present invention has good lubrication and protective properties and finds many applications. Particularly, the block polymer can be used as a grease. Although it can be used as a thickening agent to be added to a base oil, it can be used as a grease as such. This is because the block copolymer of the present invention has the block having good lubricity like an oil (block A) and the block which acts as a thickening agent (block B). Therefore, according to further aspect of the present invention, there is provided a grease which comprises a block copolymer comprising at least two kinds of blocks at least one of which consists of a homopolymeric or random copolymeric block which acts as a viscous liquid component and at least one of other of which consists of a homopolymeric or random copolymeric block bonded to the former block to make the block copolymer solid or semi-solid. In this specification, "a block which acts as a viscous liquid" is intended to mean that the a compound comprising said block is a liquid having a viscosity of 10 to 500 cSt at 37.8°C. "To make the block polymer solid or semi-solid" is intended to mean that said block makes the block copolymer to have a consistency of 85 to 475 according to ASTM D 271-60T. According to a conventional definition of "grease" according to JIS, a grease is defined as a solid or semi-solid lubricating composition comprising a liquid lubricant (base oil) and a thickening agent. A grease composition comprising perfluoropolyether as a base oil and polytetrafluoroethylene powder as a thickening agent is known as a heat resistant grease composition. However, such conventional composition type grease inevitably has a drawback that the liquid lubricant (base oil) and the thickening agent separate from each other after long time use, since they are not completely compatible with each other. When the block copolymer as defined above is used as a single component grease, the grease does not suffer from such drawback, so that it can be stably used for a long time. In such case, the content of block B is preferably from 10 to 30 % by weight. When the content of block B is from 1 to 10 % by weight, preferably the polymer terminal has -COOM group in which M is metal. The number average molecular weight is preferably from 1 x 10 3 to 3 x 10 4 . Further, such block copolymer has good compatibility with an organic solvent and forms a useful grease composition. In addition to the novel block polymer comprising one of the blocks (a), (b) and (c), the homopolymer or random copolymer which acts as the viscous liquid component may be selected from a wide range of conventional synthetic lubricants. Examples of such lubricants are (1) synthetic hydrocarbon lubricants (e.g. an α - olefin oligomer of the formula: -(CH 2 CHR 1 ) n - wherein R 1 is hydrogen, C m H 2m+1 (in which m is an integer of 1 to 8) or C m' H 2m'+1 (in which m' is 5, 6 or 7 and n is a positive integer, and alkylbenzene of the formula: wherein R 2 and R 3 are each C 4 -C 20 alkyl); (2) polyethers (e.g. polyalkylene glycol of the formula: R 4 -O-(CH 2 CHR-O) n -R 5 wherein R 4 , R 5 and R 6 are each hydrogen, methyl or ethyl and n is a number of 8 to 100, and polyphenyl ether of the formula: wherein n is a number of 8 to 100); (3) esters (e.g. a diester of the formula: and neopentylpolyol ester of the formula: wherein n is a number of 4 to 20. (4) silicone oils (e.g. alkylmethylsilicone of the formula: wherein R is hydrogen, methyl, ethyl or phenyl, and m and n are each a number of 4 to 100, and fluorosilicone of the formula: wherein x and y are each a number of 4 to 100. As the homopolymeric or random copolymeric block bonded to the former block which acts as a viscous liquid component to make the block copolymer solid or semi-solid, exemplified are polyolefins (e.g. polyethylene and polypropylene), polystyrene, polyacrylate (e.g. polymethyl (meth)acrylate and polyethyl (meth)acrylate), or fluororesin. Preferred combinations of the polymeric block which acts as a viscous liquid component and the polymer block bonded to the former block to make the block copolymer solid or semi-solid are (i) A fluorine-containing polymeric block and a fluororesin block, (ii) A non-fluorine containing polymer block and a fluororesin block, and (iii) A fluorine-containing polymer block and a non-fluorine containing resin block. The combination (i) corresponds to the novel block copolymer according to the present invention. Thus, the combinations (ii) and (iii) are now explained in detail. (ii) A non-fluorine containing polymer block and a fluororesin block A block copolymer having such structure may be prepared by radically adding a halogenated hydrocarbon of the formula: CF 3 (CF 2 ) z I wherein z is an integer of 5 to 100 to a hydrocarbon, an ester, a phosphate and a silicone which have a vinyl, vinylene or allyl group. The obtained block copolymer can be stabilized by removing the iodine atom at the molecular end by a catalytic hydrogenation in the presence of a metal hydride (e.g. LiAlH 4 ), a combination of zinc and hydrogen chloride or a catalyst such as Ni and Pd. For example, in case of the silicone oil, the block copolymer can be prepared according to following reaction: or In case of the α-olefin oligomer, the block can be prepared according to the following reaction: In case of the ester, from an ally ester, the block copolymer can be prepared according to the following reaction: (iii) A fluorine-containing polymeric block and a non-fluorine containing resin block This kind of block copolymer can be prepared according to the following reaction: C 3 F 7 -(C 3 F 6 O) n -C 2 F 4 -COF + H-(OC 2 H 4 ) m -OH → C 3 F 7 -(C 3 F 6 O) n -C 2 F 4 -CO-(OC 2 H 4 ) m -OH or When styrene is used in place of methyl acrylate in the above reaction, can be prepared Such the block copolymer is useful not only as the grease but also as an additive for an automobile engine oil. It is known that combustion efficiency in the engine is increased by improving lubricity between a cylinder and a piston of the engine by the addition of a solid lubricant comprising polytetrafluoroethylene powder. However, isolation of polytetrafluoroethylene powder is problem. The above described block copolymer can provide a lubricant to be used in the engine oil. Therefore, according to a yet further aspect of the present invention, there is provided a lubricant composition comprising 0.5 to 60 % by weight of the above described block copolymer and the rest of an organic liquid. Such composition is also useful as a lubricant for a surface of a magnetic recording medium such as a recording tape, a video tape, a magnetic disc, a magnetic card, etc. The organic liquid can be selected from a wide variety of organic liquids. Specific examples of the organic liquid are trichlorotrifluoroethane, tetrachlorodifluoroethane, dichlorotetrafluoroethane, perfluorohexane, perfluorotributylamine, acetone, tetrahydrofuran, dimethylformamide and diglyme. By selecting the ratio of the block A and the block B, the block copolymer in the form of from grease to wax can be prepared. The above described block copolymer may be used as a thickening agent for a conventional grease or as a mold release agent, or in the preparation of an ink composition. Further, some block copolymers can be used as a water- and oil-repellent, a leveling agent, or a toner aid (an off-set preventing agent). The present invention will be illustrated by following Examples. Example 1 To F(CF 2 CF 2 CF 2 O) n CF 2 CF 2 COOH (n = 26 on the average) (200 g, 4.46 x 10 -2 mole) in trichlorotrifluoroethane (100 ml), 80 ml of an aqueous solution of potassium hydroxide (containing 4.87 g of KOH) was added with stirring to form a potassium salt. It was confirmed that, in the IR spectrum, a peak for -C(=O)-OH at 1,770 cm -1 completely shifted to a peak for -C(=O)-OK at 1,680 cm -1 . The obtained potassium salt was dried at 100°C under reduced pressure to form particles. Then, the particulate potassium salt (200 g, 0.044 mole) was dispersed in trichlorotrifluoroethane (600 ml) in a nitrogen stream followed by the addition of iodine (100 g, 0.39 mole). The mixture was heated at 200°C for 1.5 hours to iodinate the molecular end. While the unreacted potassium salt was in the particle form, the resulting product was a white opaque oil. In the IR spectrum, the peak for -C(=O)-OK at 1,680 cm -1 disappeared and a peak for -CF 2 CF 2 I appeared at 910 cm -1 . 19 F-NMR spectrum of the resulting oil had a chemical shift at -12.5 ppm, which indicated the formation of -OCF 2 CF 2 I. When the white opaque oil was dissolved in trichlorotrifluoroethane and kept standing at -20°C, the white material was precipitated to form a transparent supernatant. The precipitate was filtered off. From the filtrate, trichlorotrifluoroethane was evaporated off to give transparent F(CF 2 CF 2 CF 2 O) n CF 2 CF 2 I (n = 26 on the average) (176 g). Reference Example Preparation of In a one liter autoclave, CF 3 (CF 2 ) 3 I (276.8 g, 0.80 mole), di(3,5,6-trichloroperfluorohexyl peroxide) (45.3 g, 6.52 x 10 -2 mole) and CF 2 =CF(OC 3 F 7 ) (300 g, 1.13 mole) were charged. Then, the autoclave was pressurized by tetrafluoroethylene to proceed polymerization at 20°C under pressure of from 0.5 to 0.3 kg/cm 2 for 41.5 hours to obtain (m/n = 32/68, number average molecular weight = 840) (175 g) as an oily product. Example 2 In a one liter autoclave, F(CF 2 CF 2 CF 2 O) n CF 2 CF 2 I (n = 26 on the average) prepared in Example 1 (140 g, 3.07 x 10 -2 mole), trichlorotrifluoroethane (600 ml) and di-tert.-butyl peroxide (8.25 x 10 -2 g, 5.65 x 10 -4 mole) were charged. After purging the interior space with tetrafluoroethylene, the autoclave content was heated to 120°C. Then, the autoclave was pressurized with tetrafluoroethylene with stirring and polymerization was continued at 120°C under pressure of from 6.1 to 6.4 kg/cm 2 for 27.6 hours. The solution in the autoclave which was transparent before polymerization was converted to a white opaque mixture after polymerization. Complete evaporation of trichlorotrifluoroethane from the reaction mixture gave a greasy polymeric product having a number average molecular weight of 5,240 (161 g). The content of the polytetrafluoroethylene block was 13 % by weight. Example 3 In the same autoclave as used in Example 2, F(CF 2 CF 2 CF 2 O) n CF 2 CF 2 I (n = 26 on the average) prepared in Example 1 (200 g, 4.89 x 10 -2 mole), trichlorotrifluoroethane (500 ml) and di-tert.-butyl peroxide (0.19 g, 1.32 x 10 -3 mole) were charged. After purging the interior space with tetrafluoroethylene, the autoclave content was heated to 120°C. Then, the autoclave was pressurized with tetrafluoroethylene with stirring and polymerization was continued at 120°C under pressure of from 6.6 to 7.1 kg/cm 2 for 54.4 hours. Evaporation of trichlorotrifluoroethane from the reaction mixture gave a greasy (almost waxy) polymeric product having a number average molecular weight of 6,200 (303 g). The content of the polytetrafluoroethylene block was 34 % by weight. Example 4 In a 100 ml autoclave, F(CF 2 CF 2 CF 2 O) n CF 2 CF 2 I (n = 26 on the average) prepared in Example 1 (7.69 g, 1.69 x 10 -3 mole), trichlorotrifluoroethane (30 ml) and tert.-butylperoxy isobutyrate (2.20 x 10 -2 g, 1.51 x 10 -4 mole) were charged. After purging the interior space with a gaseous mixture of vinylidene fluoride and trifluoroethylene (molar ratio of 75/25), the autoclave content was heated to 80°C. Then, the autoclave was pressurized with the same gaseous mixture of vinylidene fluoride and tetrafluoroethylene with stirring and polymerization was continued at 80°C under pressure of from 3 to 5 kg/cm 2 for 12.56 hours to give a waxy polymeric product having a number average molecular weight of 5,520 (9.33 g). The content of the vinylidene fluoride/tetrafluoroethylene copolymer block was 18 % by weight. The produced block copolymer is soluble in tetrahydrofuran as well as trichlorotrifluoroethane. Example 5 In a one liter autoclave, (m/n = 32/68) prepared in Reference Example (97 g, 0.12 mole), trichlorotrifluoroethane (410 ml) and di(3,5,6-trichloroperfluorohexyl peroxide) (0.14 g, 1.94 x 10 -4 mole) were charged. Then, the autoclave was pressurized with tetrafluoroethylene with stirring and polymerization was continued at 20°C under pressure of from 2.0 to 1.5 kg/cm 2 for 4.3 hours. Evaporation of trichlorotrifluoroethane from the reaction mixture gave a greasy polymeric product having a number average molecular weight of 980 (118 g). The content of the polytetrafluoroethylene block was 18 % by weight. Example 6 The greasy block copolymer prepared in Example 2 (50 g) was dispersed in trichlorotrifluoroethane (225 ml) and heated to 50°C. To the heated dispersion, a gaseous mixture of fluorine and nitrogen containing 10 % by weight of fluorine was bubbled at a rate of from 20 to 30 ml/min. for 8.6 hours to fluorinate the block copolymer. In the IR spectrum of the fluorinated copolymer, a peak for -CF 2 CF 2 I at 910 cm -1 completely disappeared. The product was not colored by the addition of ethanol, which indicated no liberation of iodine. Therefore, the complete substitution of the terminal iodine with fluorine was confirmed. Example 7 The block copolymer prepared in Example 6 (hereinafter referred to as "Blocked grease") was examined on the following properties. For comparison, a grease comprising F(CF 2 CF 2 CF 2 O) n CF 2 CF 3 (n = 28 on the average) as a base oil and polytetrafluoroethylene powder as a thickening agent in a weight ratio of 67:33 (hereinafter referred to as "Non-blocked grease") was used. Appearance By visual inspection, the blocked grease was transparent, while the non-blocked grease was white. This may be because the blocked grease had such structure that the base oil element and the thickening agent element were chemically bonded in the molecule and their compatibility was increased, whereby the grease was transparent. The particle size in the grease was inspected by a polarization microscope (x 200). In the non-blocked grease, polytetrafluoroethylene particles having a diameter of from 1 x 10 -5 to 5 x 10 -5 m were observed, while in the blocked grease, no particle was observed. From the above results, it can be concluded that the particles of the blocked grease according to the present invention is smaller and more homogeneous than those of the non-blocked crease. Settling of particles The blocked or non-blocked grease was added to trichlorotrifluoroethane to prepare a dispersion with a concentration of 10 % by weight and kept standing to observe the settling state. While in case of the non-blocked grease, the particles settled immediately, while in case of the blocked grease, the dispersion was stable at least two days. From these results, it can be said that the blocked grease is less separated from an organic solvent than the non-blocked grease. Lubricity By using a cone-plate type viscometer, viscosity was measured and expressed in the form of a shear stress-shear rate curve. The results for the blocked grease and the non-blocked grease are shown in Figs. 1 and 2, respectively. The viscosity measurement was carried out as follows: At a temperature of 30°C or 80°C, the shear rate was increased to 307.2 sec -1 for the blocked grease or 3072 sec -1 for the non-blocked grease over 3 minutes and kept at said rate for 0.2 minute. Then, the shear rate was decreased to 0 (zero) over 3 minutes. In Figs. 1 and 2, in both cases of the blocked and non-blocked grease, the shear stress during increasing the shear rate is smaller than that during decreasing the shear rate at 30°C and 80°C. This showed that both greases had thixotropy. In case of the non-blocked grease, the shear stress increased substantially linearly as the shear rate was increased, while in case of the blocked grease, as the shear rate was increased, the shear stress reached the maximum value and thereafter gradually decreased with the increase of the shear rate. In addition, a rather clear yield value was observed in the blocked grease, but no clear yield value was observed in the non-blocked grease. In view of the properties of a grease, it is preferred that the grease does not flow under a small shear stress, namely it has a yield value, but once it begins to flow, it easily flows. Thus, the blocked grease of the present invention has better properties than the non-blocked grease. Example 8 In the same manner as in Example 6, the blocked polymer prepared in Example 3 was fluorinated. To the fluorinated block polymer (70.0 g), F(CF 2 CF 2 CF 2 O) n CF 2 CF 3 (n = 28 on the average) (49.8 g) was added as a lubricant oil to prepare a grease composition. The obtained grease composition was a semi-solid material with good transparency. It had no dropping point not higher than 200°C. A degree of oil separation measured at 200°C for 200 hours was 0 (zero). Example 9 To Cl(CF 2 CF 2 ) 2 Cl (20 ml), C 3 F 7 O-(CF 2 CF 2 CF 2 O) 24 -CF 2 CF 2 -I (10 g) and azobisisobutyronitrile (0.05 g) were dissolved and charged in a 50 ml airtight reactor. Then, methyl acrylate (10 g) was added and reacted at 70°C with stirring in the absence of air. In less than 10 minutes, the reactor content became white opaque, which indicated initiation of polymerization. After 3 hours, the temperature was raised to 80°C and the reaction mixture was stirred for another 3 hours to complete the polymerization. While the starting material C 3 F 7 O-(CF 2 CF 2 CF 2 O) 24 -CF 2 CF 2 -I was soluble in Cl(CF 2 CF 2 ) 2 Cl, the opaque viscous greasy product contained a large amount of materials insoluble in Cl(CF 2 CF 2 ) 2 Cl. Further, the product is soluble in acetone, in which C 3 F 7 -(CF 2 CF 2 CF 2 O) 24 -CF 2 CF 2 -I is insoluble. According to GPC analysis of the product, the formation of a block polymer was confirmed. A filter paper dipped in the product and dried had water- and oil-repellency.

Claims: A block copolymer comprising at least two kinds of blocks in a molecule wherein at least one kind of the blocks is a homopolymeric or random copolymeric block comprising at least one block selected from the group consisting of: (a) a block consisting of at least two repeating units selected from the formulae: -(CH 2 CF 2 CF 2 O) a - -(CHClCF 2 CF 2 O) b - -(CCl 2 CF 2 CF 2 O) c - -(CHFCF 2 CF 2 O) d - -(CFClCF 2 CF 2 O) e - -(CF 2 CF 2 CF 2 O) f - a, b, c, d, e and f are each 0 or a positive integer and satisfy the following equations: 2 ≤ a+b+c+d+e+f ≤ 200 and 1 ≤ a+c+d+f, (b) a block consisting of the repeating units of the formula: wherein p, q and r are each 0 or a positive integer and satisfy the following equations: 2 ≤ p+q+r ≤ 200 and 1 ≤ p+q, and (c) a block consisting of the repeating units of the formula: wherein R f1 and R f2 are the same or different and C 1 -C 3 perfluoroalkyl, k and m are each a positive integer and satisfy the equations: 2 ≤ k+m ≤ 50 and 0.2 ≤ m/(k+m), and n is an integer of 0 to 10, and at least one kind of other blocks is a homopolymeric or random copolymeric block consisting of repeating units of the formula: -(CF 2 CXY)- wherein X is hydrogen or fluorine, Y is hydrogen, chlorine, fluorine, difluoromethyl or C 1 -C 8 perfluoroalkyl or perfluoroalkoxy, the content of the latter block being 1 to 95 % by weight based on the whole weight of the block copolymer and a number average molecular weight of the whole block copolymer being from 1 x 10 3 to 1 x 10 6 . A process for preparing the block copolymer of claim 1, which process comprises polymerizing at least one fluorine-containing olefin of the formula: CF 2 =CXY wherein X and Y are the same as defined in claim 1 in the presence of a polymer comprising at least one block selected from the group consisting of the blocks (a), (b) and (c) and an iodine atom at at least one end, and a radical-generating source. Use of the block copolymer as defined in claim 1 for preparing a grease.

Inventors: FUJIWARA KOJI, TATEMOTO MASAYOSHI, YUTANI YUJI, FUJIWARA, KOJI, TATEMOTO, MASAYOSHI, YUTANI, YUJI
Applicants: DAIKIN IND LTD, DAIKIN INDUSTRIES, LIMITED
Application year: 1987
Main classification: C08G65
IPC codes: C10M147, C08F293, C08G65, C10M107, G11B5