Patent Application
20110112265
The present invention relates to a curable composition comprising a specific vinylidene fluoride type elastomer. The present invention further relates to a molded article obtained by curing this curable composition.
Fluorine-containing elastomers are molded into O-ring, hose, stem seal, shaft seal, diaphragm, etc., and are widely used in the fields of automobile industry, semiconductor industry and chemical industry because of their superior heat resistance, chemical resistance, solvent resistance and fuel oil resistance.
However, with advances in technologies, more rigorous demand for characteristics have been imposed, and in the fields of aviation and space industries, semiconductor manufacturing equipment, chemical plant and automobile industry, sealing property under higher temperature environment of more than 200° C. is demanded.
Perfluoroelastomers are known as a fluorine-containing elastomer having such performance as mentioned above (JP2004-500459A, JP2003-531222A, WO 00/09603, JP11-111081A and WO 98/23675), and investigation has been made using vinylidene fluoride type elastomer comprising more than 20% by mole of vinylidene fluoride (WO 05/105917 and WO 2007/049469).
It has been considered that in the case of a vinylidene fluoride type elastomer, in order to achieve sealing property under high temperature environment exceeding 200° C., it is essential to carry out crosslinking with a specific curing agent as proposed in WO 05/105917 and WO 2007/049469. However, as a result of further investigation by the inventors of the present invention, it was found that in the techniques proposed in WO 05/105917 and WO 2007/049469, there remains room for improvement in a crosslinking speed from practical point of view. The inventors of the present invention, to their surprise, have found that with respect to a vinylidene fluoride type elastomer, not only characteristics mentioned above are achieved but also a crosslinking speed can be improved at low cost without using such a specific curing agent at all.
In the present invention, it was found that in a vinylidene fluoride type elastomer, curing can be done with only ammonia, and it is an object of the present invention to provide a curable composition of a vinylidene fluoride type elastomer having an improved crosslinking speed, and a molded article obtained from the curable composition.
Namely, the present invention relates to a curable composition comprising:
The compound (B) generating ammonia is preferably urea or an ammonium salt from the viewpoint of satisfactory crosslinking speed.
The present invention also relates to a molded article obtained by curing the curable composition of the present invention. The molded article is suitable for a sealing material for an oxygen sensor, a sealing material for a fuel-air ratio sensor, a turbo-charger hose or a hose for control of exhaust gas recirculation combustion equipment (EGR), for which higher crosslinking speed and heat resistance are required.
Further, the present invention relates to a process for preparing the above-mentioned curable composition comprising the specific vinylidene fluoride type elastomer (A) and the compound (B) generating ammonia alone as a curing agent, and the process is characterized in that the compound (B) generating ammonia is mixed with the other components in the presence of a solvent (D) having affinity for the compound (B) generating ammonia, for example, water or an organic solvent having affinity for the compound (B) generating ammonia.
In the curable composition of the present invention, only the compound (B) generating ammonia is blended as a curing agent to the specific vinylidene fluoride type elastomer (A).
Each component is then explained below.
The specific VdF type elastomer (A) is a VdF type elastomer which is a copolymer of the vinylidene fluoride (VdF) (a1), at least one perfluoroolefin (a2) selected from the group consisting of tetrafluoroethylene (TFE), hexafluoropropylene (HFP) and perfluoro(alkyl vinyl ether) (PAVE) and the cyano group-containing monomer (a3).
It is important that the proportion of VdF exceeds 20% by mole in order to make improvement in brittleness at low temperature.
It is possible to use, as perfluoro(alkyl vinyl ether) (PAVE), one of or a combination of two or more of compounds represented by the general formula (24):
CF2═CFO(CF2CFY2O)p—(CF2CF2CF2O)q—Rf3 (24)
wherein Y2 represents a fluorine atom or —CF3; Rf3 represents a perfluoroalkyl group having 1 to 5 carbon atoms; p is 0 or an integer of 1 to 5; q is 0 or an integer of 1 to 5, or the general formula (25):
CFX═CXOCF2OR (25)
wherein X is F or H; R is a linear or branched C1 to C6 fluoroalkyl group, or a cyclic C5 to C6 fluoroalkyl group or fluorooxyalkyl group and may have 1 to 2 atoms selected from H, Cl, Br and I.
Among those represented by the general formula (24) and the general formula (25), perfluoro(methyl vinyl ether) and perfluoro(propyl vinyl ether) are preferred, and especially perfluoro(methyl vinyl ether) is preferred.
These can be used alone or can be used in optional combination thereof.
With respect to the proportions of the VdF (a1) and the specific perfluoroolefin (a2), the proportion of VdF should exceed 20% by mole. Particularly, the fluorine-containing elastomer comprising 45 to 85% by mole of the VdF and 55 to 15% by mole of the specific perfluoroolefin is preferred, and the fluorine-containing elastomer comprising 50 to 80% by mole of the VdF and 50 to 20% by mole of the specific perfluoroolefin is further preferred.
Preferred examples of a combination of the VdF (a1) and the specific perfluoroolefin (a2) are VdF/HFP copolymer, VdF/HFP/TFE copolymer, VdF/PAVE copolymer, VdF/TFE/PAVE copolymer, VdF/HFP/PAVE copolymer and VdF/HFP/TFE/PAVE copolymer.
In the VdF/HFP copolymer, a ratio of VdF/HFP is preferably 45 to 85/55 to 15 in molar percent, more preferably 50 to 80/50 to 20 in molar percent, further preferably 60 to 80/40 to 20 in molar percent.
Preferred VdF/HFP/TFE copolymer is one comprising VdF/HFP/TFE in a ratio of 40 to 80/10 to 35/10 to 35 in molar percent.
Preferred VdF/PAVE copolymer is one comprising VdF/PAVE in a ratio of 65 to 90/35 to 10 in molar percent.
Preferred VdF/TFE/PAVE copolymer is one comprising VdF/TFE/PAVE in a ratio of 40 to 80/3 to 40/15 to 35 in molar percent.
Preferred VdF/HFP/PAVE copolymer is one comprising VdF/HFP/PAVE in a ratio of 65 to 90/3 to 25/3 to 25 in molar percent.
Preferred VdF/HFP/TFE/PAVE copolymer is one comprising VdF/HFP/TFE/PAVE in a ratio of 40 to 90/0 to 25/0 to 40/3 to 35 in molar percent, more preferably one comprising VdF/HFP/TFE/PAVE in a ratio of 40 to 80/3 to 25/3 to 40/3 to 25 in molar percent.
From the viewpoint of satisfactory crosslinking characteristics and heat resistance, the amount of cyano group-containing monomer (a3) is preferably 0.1 to 5% by mole, more preferably 0.3 to 3% by mole based on the total amount of VdF (a1) and specific perfluoroolefin (a2).
Examples of the cyano group-containing monomer (a3) are, for instance, monomers represented by the formulas (5) to (21):
CY12═CY1(CF2)n—CN (5)
where Y1 is hydrogen atom or fluorine atom, n is an integer of 1 to 8,
CF2═CFCF2R12—CN (6)
where R12 is —(OCF2)m or —(OCF(CF3)—)n, n is 0 or an integer of 1 to 5,
CF2═CFCF2(OCF(CF3)CF2)m(OCH2CF2CF2)nOCH2CF2—CN (7)
where m is 0 or an integer of 1 to 5, n is 0 or an integer of 1 to 5,
CF2═CFCF2(OCH2CF2CF2)m(OCF(CF3)CF2)nOCF(CF3)—CN (8)
where m is 0 or an integer of 1 to 5, n is 0 or an integer of 1 to 5,
CF2═CF(OCF2CF(CF3))mO(CF2)n—CN (9)
where m is 0 or an integer of 1 to 5, n is an integer of 1 to 8,
CF2═CF(OCF2CF(CF3))m—CN (10)
where m is an integer of 1 to 5,
CF2═CFOCF2(CF(CF3)OCF2)nCF(—CN)CF3 (11)
where n is an integer of 1 to 4,
CF2═CFO(CF2)nOCF(CF3)—CN (12)
where n is an integer of 2 to 5,
CF2═CFO(CF2)n—(C6H4)—CN (13)
where n is an integer of 1 to 6,
CF2═CF(OCF2CF(CF3))nOCF2CF(CF3)—CN (14)
where n is an integer of 1 to 2,
CH2═CFCF2O(CF(CF3)CF2O)nCF(CF3)—CN (15)
where n is 0 or an integer of 1 to 5,
CF2═CFO(CF2CF(CF3)O)m(CF2)n—CN (16)
where m is 0 or an integer of 1 to 5, n is an integer of 1 to 3,
CH2═CFCF2OCF(CF3)OCF(CF3)—CN (17)
CH2═CFCF2OCH2CF2—CN (18)
CF2═CFO(CF2CF(CF3)O)mCF2CF(CF3)—CN (19)
where m is an integer of not less than 0,
CF2═CFOCF(CF3)CF2O(CF2)n—CN (20)
where n is an integer of not less than 1, and
CF2═CFOCF2OCF2CF(CF3)OCF2—CN (21),
and these can be used alone or can be used in an optional combination thereof.
Among these, the formula (9) or (16) is preferred from the viewpoint of satisfactory copolymerizability and vulcanizability, and CF2═CFOCF2CF(CF3)OCF2CF2CN and CF2═CFO(CF2)5CN are more preferred.
In the cyano group-containing monomers represented by the formulas (5) to (21), triazine crosslinking proceeds by a cyclic trimerization reaction of the cyano group thereof.
These VdF type elastomers can be prepared by known methods.
For introducing a cyano group, the method described in WO 00/05959 can also be used.
The VdF type elastomer used in the present invention is preferably one having a Mooney viscosity (ML1
Ammonia-generating compounds have not been positively investigated due to a problem with amine resistance in the case of VdF type elastomers. However, it was found that even without using the curing agent proposed in WO 05/105917 and WO 2007/049469, sealing property under high temperature environment exceeding 200° C. can be achieved and crosslinking speed can be improved.
Ammonia generated by this ammonia-generating compound (B) at a crosslinking reaction temperature (40° to 330° C.) causes crosslinking of the VdF type elastomer, resulting in occurrence of curing. Therefore, the ammonia-generating compound functions independently as a curing agent. In the present invention, other curing agent is not used, and curing is caused by the ammonia-generating compound alone. There is a compound undergoing reaction with a trace amount of water to generate ammonia.
Preferred examples of the ammonia-generating compound (B) are urea and ammonium salts, and either an organic ammonium salt and an inorganic ammonium salt may be used as an ammonium salt.
Examples of urea are urea and in addition, urea derivatives such as biurea, thiourea, hydrochloric acid salt urea and biuret.
Examples of an organic ammonium salt are compounds described in JP9-111081A, WO 00/09603 and WO 98/23675, for example, ammonium salts of polyfluorocarboxylic acid such as ammonium perfluorohexanoate, ammonium perfluorooctanoate, ammonium perfluorobutyrate, ammonium perfluoroacetylate, ammonium perfluorododecanoate and ammonium perfluorohexadecanoate; ammonium salts of polyfluorosulfonic acid such as ammonium perfluorohexane sulfonate, ammonium perfluorooctane sulfonate, ammonium perfluorododecane sulfonate and ammonium perfluorohexadecane sulfonate; ammonium salts of phosphoric acids or phosphonic acids having polyfluoroalkyl group such as ammonium perfluorohexane phosphate, ammonium perfluorooctane phosphate, ammonium perfluorohexane phosphonate and ammonium perfluorooctane phosphonate; and ammonium salts of non-fluorine-containing carboxylic acids or sulfonic acids such as ammonium benzoate, ammonium adipate and ammonium phthalate. Among these, ammonium salts of fluorine-containing carboxylic acids, sulfonic acids or phosphoric acids are preferred in consideration of dispersibility in the VdF type elastomer, and ammonium salts of non-fluorine-containing carboxylic acids, sulfonic acids or phosphoric acids are preferred from the viewpoint of low price.
Examples of an inorganic ammonium salt are compounds described in JP9-111081A, for example, ammonium sulfate, ammonium carbonate, ammonium nitrate and ammonium phosphate, and in consideration of vulcanization characteristics, ammonium phosphate is preferred.
In addition, there can be used acetaldehyde ammonia, hexamethylenetetramine, formamidine, formamidine hydrochloric acid salt, formamidine acetic acid salt, t-butyl carbamate, benzyl carbamate, HCF2CF2CH(CH3)OCONH2 and phthalamide.
These ammonia-generating compounds (B) may be used alone or may be used in combination of two or more thereof.
The blending amount of ammonia-generating compound (B) may be optionally selected depending on an amount of ammonia to be generated, and is usually 0.05 to 10 parts by mass, preferably 0.1 to 5 parts by mass, more preferably 0.2 to 3 parts by mass based on 100 parts by mass of the VdF type elastomer. When the amount of ammonia-generating compound is too small, since crosslinking density becomes low, there is a tendency that heat resistance and chemical resistance sufficient for practical use are not exhibited. When the amount of ammonia-generating compound is too large, there is a problem that scorching may occur and storage stability is lowered and there is a tendency that a tone of color of a molded article lacks in transparency.
In the present invention, curing reaction proceeds with only the ammonia-generating compound, and other curing agent is not used. Examples of curing agents which are not used are the following curing agents known as curing agents for fluorine-containing elastomers.
A compound having at least two crosslinkable reaction groups represented by the formula (1):
wherein R1s are the same or different and each is —NH2, —NHR2, —OH or —SH; R2 is a fluorine atom or a monovalent organic group, a compound represented by the formula (2):
wherein R3 is —SO2—, —O—, —CO—, an alkylene group having 1 to 6 carbon atoms, a perfluoroalkylene group having 1 to 10 carbon atoms or a single bond; R4 is
a compound represented by the formula (3):
in which Rf1 is a perfluoroalkylene group having 1 to 10 carbon atoms, and a compound represented by the formula (4):
in which n is an integer of 1 to 10.
Concrete examples of other curing agents which are not used are compounds which have two crosslinkable reaction groups represented by the formula (1) and are represented by the general formula (22):
wherein R1 is as defined above, R5 is —SO2—, —O—, —CO—, an alkylene group having 1 to 6 carbon atoms, a perfluoroalkylene group having 1 to 10 carbon atoms, a single bond or a group represented by:
2,2-bis(3-amino-4-hydroxyphenyl)hexafluoropropane, 2,2-bis(3-amino-4-mercaptophenyl)hexafluoropropane, 2,2-bis(3,4-diaminophenyl)hexafluoropropane, and compounds represented by the formula (23):
wherein R6s are the same or different and each is an alkyl group having 1 to 10 carbon atoms; a fluorine atom-containing alkyl group having 1 to 10 carbon atoms; a phenyl group; a benzyl group; or a phenyl group or benzyl group, in which 1 to 5 hydrogen atoms are replaced by fluorine atoms and/or —CF3.
Non-limiting examples of the curing agent represented by the formula (23) are, for instance, 2,2-bis[3-amino-4-(N-methylamino)phenyl]hexafluoropropane, 2,2-bis[3-amino-4-(N-ethylamino)phenyl]hexafluoropropane, 2,2-bis[3-amino-4-(N-propylamino)phenyl]hexafluoropropane, 2,2-bis[3-amino-4-(N-phenylamino)phenyl]hexafluoropropane, 2,2-bis[3-amino-4-(N-perfluorophenylamino)phenyl]hexafluoropropane, 2,2-bis[3amino-4-(N-benzylamino)phenyl]hexafluoropropane, and the like.
In the curable composition of the present invention, usual additives to be added to curable compositions, as case demands, for example, a filler, a processing aid, a plasticizer, a colorant, a stabilizer and an adhesive aid can be blended for applications particularly in the fields where high purity and non-contaminating property are not demanded.
A mixing method and a mixing order of each component of the above-mentioned curable composition are not limited particularly.
Nonlimiting examples of a mixing method are as follows.
When the other additive (C) is blended, it may be blended in any stage of the above-mentioned methods.
When the other additive (C), especially the filler (C1) is used, (1-3) a method of previously mixing the component (B), the filler (C1) and, if necessary, a part of the component (A) to make a master batch, and then mixing the remaining components to the master batch (in this case, the remaining components may have been previously mixed) can be employed.
The amount of VdF type elastomer (A) to be used for preparing a master batch is preferably 1 to 50% by mass based on the whole VdF type elastomer (A) from the viewpoint of achieving satisfactory dispersibility of the ammonia-generating compound (B). When the amount of elastomer to be used for preparing a master batch is smaller, the elastomer to be used for preparing a master batch is not always limited to the VdF type elastomer (A), and other elastomers, for example, elastomers undergoing no scorching during the mixing such as elastomers having no cyano group may be used alone or may be used together. From the viewpoint of satisfactory compatibility with the VdF type elastomer (A), preferred example of other elastomer is a VdF type elastomer, more preferably the VdF type elastomer (A) comprising no cyano group-containing monomer (a3).
Also with respect to the composition of the master batch, it is preferable that the ammonia-generating compound (B) is blended in an amount of 5 to 120 parts by mass based on 100 parts by mass of the elastomer for the master batch.
The curable composition can be prepared by mixing the above-mentioned components by using usual elastomer processing machine, for example, an open roll, a Banbury mixer or a kneader. In addition, the composition can be prepared also by a method of using a closed mixer.
In the case of directly kneading the powder of the solid ammonia-generating compound (B) with the VdF type elastomer (A) by using a kneader or an open roll to disperse the ammonia-generating compound (B) in the VdF type elastomer (A), since the VdF type elastomer (A) has high surface sliding property, though it is possible to incorporate the ammonia-generating compound (B) in the elastomer, it is not easy to homogeneously knead and disperse the compound.
The inventors of the present invention have found that the ammonia-generating compound (B) can be homogeneously dispersed in the VdF type elastomer (A) by letting a solvent having affinity for the ammonia-generating compound (B) to be present in the mixing system.
Namely, the present invention also relates to the process for preparing the curable composition of the present invention, in which the ammonia-generating compound (B) is homogeneously dispersed.
The preparation process of the present invention is characterized in that for preparing the above-mentioned curable composition comprising the specific vinylidene fluoride type elastomer (A) and the ammonia-generating compound (B) alone as a curing agent, the mixing of the ammonia-generating compound (B) with the other components is carried out in the presence of the solvent (D) having affinity for the ammonia-generating compound (B).
The meaning of the solvent (D) having affinity for the ammonia-generating compound (B) is that the solvent (D) has, for example, property of undergoing dissolution, dispersion or swelling of the ammonia-generating compound (B), and, for example, water (D1) or an organic solvent (D2) having affinity for the ammonia-generating compound (B) is preferred.
Examples of the organic solvent (D2) are alcohol solvents such as methanol, ethanol and glycerin.
Especially, water (D1) is preferred since it is cheap, is easily handled and removed and does not have much effect on environment.
The amount of solvent (D) greatly changes depending on kind and an amount of ammonia-generating compound (B) and an amount of VdF type elastomer (A), and from the viewpoint of further improving dispersibility of the ammonia-generating compound (B), the amount of solvent (D) is preferably not less than 0.1 part by mass, further preferably not less than 1.0 part by mass based on 100 parts by mass of the VdF type elastomer (A). An upper limit of the amount is not limited particularly, and can be 500 parts by mass, further 100 parts by mass, especially 50 parts by mass based on 100 parts by mass of the VdF type elastomer (A).
Nonlimiting examples of a method of mixing each component of the composition of the present invention by using the solvent (D) are the following methods.
When the other additive (C) is blended, it may be blended in any stage of the above-mentioned methods.
When the other additive, especially the filler (C1) is used,
The amount of VdF type elastomer (A) to be used for preparing a master batch is preferably 1 to 50% by mass based on the whole VdF type elastomer (A) from the viewpoint of achieving satisfactory dispersibility of the ammonia-generating compound (B). When the amount of elastomer to be used for preparing a master batch is smaller, the elastomer to be used for preparing a master batch is not always limited to the VdF type elastomer (A), and other elastomers, for example, elastomers undergoing no scorching during the mixing such as elastomers having no cyano group may be used alone or may be used together. From the viewpoint of satisfactory compatibility with the VdF type elastomer (A), preferred example of other elastomer is a VdF type elastomer, more preferably the VdF type elastomer (A) comprising no cyano group-containing monomer (a3).
Also with respect to the composition of the master batch, it is preferable that the ammonia-generating compound (B) is blended in an amount of 5 to 120 parts by mass based on 100 parts by mass of the elastomer for the master batch.
Except the mixing with the VdF type elastomer (A), usual stirring and mixing methods are enough for mixing each component.
Preparation of the master batch and further the mixing with the VdF type elastomer (A) can be carried out by mixing with usual elastomer processing equipment, for example, an open roll, a Banbury mixer, a kneader, or the like. In addition, a method of using a closed mixer can be employed.
The solvent (D) used for the mixing is removed by the time when the curing (crosslinking and molding) is completed. For removing the solvent (D), a drying step may be employed as an individual step, may be conducted in the last stage of the mixing or in the extension stage of the mixing, or may be conducted in the first half of a curing (crosslinking and molding) step or during the curing step.
When the drying step is carried out independently, the mixture obtained by the mixing is dried.
The drying temperature is preferably not more than 40° C. since the organic solvent can be removed and crosslinking reaction hardly proceeds. In addition, the drying time is preferably 6 to 72 hours from the viewpoint of accelerating removal of the solvent. The drying step may be conducted once or may be conducted plural times.
The curable composition of the present invention can be subjected to crosslinking by a usual method, for example, a method of heating and compressing in a metal die, a method of charging the composition into a heated metal die under pressure or a method of crosslinking after extruding the composition with an extruder. The crosslinking is carried out in order of primary crosslinking and lastly secondary crosslinking, and thus a molded article can be obtained.
Primary crosslinking is carried out preferably at 150° C. to 230° C. for 5 to 120 minutes, more preferably at 160° C. to 200° C. for 5 to 60 minutes, especially preferably at 170° C. to 190° C. for 5 to 60 minutes. For crosslinking, known crosslinking means may be employed, for example, press-crosslinking.
Secondary crosslinking is carried out preferably at 160° C. to 320° C. for 2 to 24 hours, more preferably at 180° C. to 310° C. for 4 to 20 hours. For crosslinking, known crosslinking means may be employed, for example, oven-crosslinking.
The molded article of the present invention can be obtained by crosslinking and molding the curable composition of the present invention. The molded article of the present invention is excellent in heat resistance and has satisfactory compression set.
The molded article of the present invention can be widely used in the fields of automobile, aircraft, rocket, marine vessel, excavation of oil field, chemical plants, chemicals such as pharmaceuticals, photograph such as developing machine, printing such as printing machine, painting such as painting equipment, analytical, physical and chemical appliances, equipment in food plants, equipment in atomic power plants, iron and steel industry such as steel sheet processing equipment, general industry, electricity, fuel cells, electronic parts and molding at site.
Examples of application of the molded article of the present invention are sealing materials such as gaskets and non-contact type and contact type packings (self-seal packing, piston ring, split ring packing, mechanical seal, oil seal, etc.) which are required to have heat resistance, oil resistance, fuel oil resistance, resistance to an anti-freezing fluid for cooling an engine and steam resistance and are used for engine body, main engine-driving system, valve gear system, lubricating and cooling system, fuel system, and suction/exhaust system; transmission of driving gear system; steering system of chassis; brake system; standard electrical parts, electrical parts for control and accessory electrical parts for automobiles.
Sealing materials used on an engine body of automobiles are not limited particularly, and examples thereof are, for instance, gaskets such as a cylinder head gasket, cylinder head cover gasket, oil pan packing and general gaskets, and sealing materials such as an O-ring, packing and timing belt cover gasket.
Sealing materials used for a main engine-drive system of automobile are not limited particularly, and examples thereof are, for instance, shaft seals such as crank shaft seal and cam shaft seal.
Sealing materials used for valve gear system of an automobile engine are not limited particularly, and examples thereof are, for instance, a valve stem oil seal of an engine valve.
Sealing materials used for a lubricating and cooling system of an automobile engine are not limited particularly, and examples thereof are, for instance, a seal gasket for engine oil cooler and the like. Sealing materials used for a fuel system of an automobile engine are not limited particularly, and examples thereof are, for instance, an oil seal of a fuel pump, a filler seal and tank packing of a fuel tank, a connector O-ring of a fuel tube, an injector cushion ring, an injector seal ring and an injector O-ring of a fuel injector, a flange gasket of a carburetor and the like.
Sealing materials used for a suction/exhaust system of an automobile engine are not limited particularly, and examples thereof are, for instance, a suction manifold packing and exhaust manifold packing of a manifold, a throttle body packing, a turbine shaft seal of a turbo charger and the like.
Sealing materials used for a transmission system of automobile are not limited particularly, and examples thereof are, for instance, a bearing seal, oil seal, O-ring and packing for transmission and an O-ring and packing for automatic transmission.
Sealing materials used for a brake system of automobile are not limited particularly, and examples thereof are, for instance, an oil seal, O-ring, packing, piston cup (rubber cup) of a master cylinder, caliper seal, boots and the like.
Sealing materials used for accessory electrical parts of automobile are not limited particularly, and examples thereof are, for instance, an O-ring and packing of an air conditioner.
The molded article of the present invention is a sealing material suitable especially for an oxygen sensor, further for an oxygen sensor of automobile, and is particularly suitable as sealing materials for an oxygen sensor and a fuel-air ratio sensor for which higher crosslinking speed and heat resistance are demanded, and is also suitable as a turbo-charger hose and EGR hose.
Applications other than automobile application are not limited particularly, and examples thereof are, for instance, packings, O-rings and other sealing materials requiring oil resistance, chemical resistance, heat resistance, steam resistance and weather resistance in transport means such as ships and air planes; packings, O-rings and other sealing materials requiring oil resistance, heat resistance, steam resistance and weather resistance in excavation of oil field; similar packings, O-rings and sealing materials for chemical plants; similar packings, O-rings and sealing materials for food plant equipment and food processing equipment (including those for domestic use); similar packings, O-rings and sealing materials for equipment of atomic power plant; and similar packings, O-rings and sealing materials for general industrial parts.
The present invention is then explained by means of examples, but is not limited to them.
Crosslinking conditions used in the present invention are the following conditions.
In the present invention, various characteristics are measured by the following methods.
By using DSC (differential scanning calorimeter), in the 1st run, temperature is raised up to 200° C. at a temperature elevating rate of 10° C./min, followed by maintaining at 200° C. for one minute and cooling down to 25° C. at a temperature decreasing rate of 10° C./min, and then a center point of heat absorption curve obtained in the 2nd run of heating at a temperature elevating rate of 10° C./min is assumed to be Tg. The used differential scanning calorimeter is one available from Seiko Instruments Kabushiki Kaisha.
Mooney viscosity is measured in accordance with ASTM-D 1646 and JIS K6300.
Measuring is carried out in accordance with JIS K6300 with JSR Curastometer Model II (available from Nichigo Shoji Kabushiki Kaisha) at primary press-crosslinking. A crosslinking curve at 180° C. is made, and a minimum viscosity (ML), degree of crosslinking (MH), induction time (T10) and optimum crosslinking time (T90) are determined.
A curable composition shown in Table 1 is subjected to primary press-crosslinking and secondary oven-crosslinking under the standard crosslinking conditions to prepare a 2 mm thick sheet, and measuring is carried out in accordance with JIS K6251.
A curable composition shown in Table 1 is subjected to primary press-crosslinking and secondary oven-crosslinking under the standard crosslinking conditions to prepare a 2 mm thick sheet, and measuring is carried out in accordance with JIS K6251.
Measuring is carried out in accordance with ASTM D2240 using an analog hardness meter Model A available from Kobunshi Keiki Kabushiki Kaisha.
Compression set (CS) of O-ring (AS-568A-214) after compression at 260° C. for 70 hours, 168 hours and 336 hours is measured in accordance with JIS K6301.
Into a 6-liter stainless steel autoclave having no ignition source were poured 3.0 liter of pure water, 6.0 g of C5F11COONH4 and 0.15 g of CH2═CFCF2OCF(CF3)CF2OCF(CF3)COONH4 as emulsifying agents, 3.5 g of disodium hydrogen phosphate and 0.6 g of sodium hydroxide, and the inside of a system was sufficiently replaced with nitrogen gas and subjected to deaeration. Then the autoclave was heated up to 80° C. with stirring at 600 rpm, and a gas mixture of VdF, TFE and HFP (VdF/TFE/HFP=19/11/70 in molar percent) was introduced so that the inside pressure became 1.52 MPa·G. Then, an aqueous solution of ammonium persulfate (APS) of 1.8 g/2 ml and 1.8 g of CF2═CFOCF2CF(CF3)OCF2CF2CN (CNVE) were introduced with pressurized nitrogen gas to initiate a reaction.
As the polymerization proceeded, when the inside pressure decreased to 1.48 MPa·G, 0.2 g of diethyl malonate was introduced with pressurized nitrogen gas. Then, a pressurized gas mixture of VdF, TFE and HFP (VdF/TFE/HFP=50/20/30 in molar percent) was introduced so that the inside pressure became 1.52 MPa·G. Thereafter, as the reaction proceeded, a pressurized gas mixture of VdF, TFE and HFP was introduced, and increasing and decreasing of the inside pressure were repeated between 1.48 MPa·G and 1.52 MPa·G, and 30 g of CNVE and 1.2 g of sodium hydroxide were introduced with pressurized nitrogen gas.
When the total amount of introduced VdF, TFE and HFP reached 1,000 g ten hours after starting of the polymerization reaction, the autoclave was cooled, and unreacted monomers were discharged to obtain 3,984 g of an aqueous dispersion having a solid content of 25.5% by mass.
2,000 g of this aqueous dispersion was slowly added to 2,000 g of an aqueous solution of magnesium sulfate with stirring. The solution was stirred for one minute after the addition, and then a coagulated product was filtered off, followed by repeating the washing with water and the filtering off three times and drying at 70° C. for 24 hours to obtain 499 g of a polymer.
As a result of analysis, this polymer was one comprising monomer units of VdF/TFE/HFP/CNVE=49.6/18.3/31.2/0.9 in molar percent. In addition, according to measurement by infrared spectroscopic analysis, characteristic absorption of nitrile group was recognized around 2,169 cm−1. Mooney viscosity (ML1
Into a 6-liter stainless steel autoclave having no ignition source were poured 3.0 liter of pure water, 6.0 g of C5F11COONH4 and 0.15 g of CH2═CFCF2OCF(CF3)CF2OCF(CF3)COONH4 as emulsifying agents, 3.5 g of disodium hydrogen phosphate and 0.6 g of sodium hydroxide, and the inside of a system was sufficiently replaced with nitrogen gas and subjected to deaeration. Then, the autoclave was heated up to 80° C. with stirring at 600 rpm, and a gas mixture of VdF, TFE and PMVE (VdF/TFE/PMVE=64/8/28 in molar percent) was introduced so that the inside pressure became 1.53 MPa·G. Then, an aqueous solution of ammonium persulfate (APS) of 1.8 g/2 ml and 1.8 g of CF2═CFOCF2CF(CF3)OCF2CF2CN (CNVE) were introduced with pressurized nitrogen gas to initiate a reaction.
As the polymerization proceeded, when the inside pressure decreased to 1.48 MPa·G, 0.2 g of diethyl malonate was introduced with pressurized nitrogen gas. Then, a pressurized gas mixture of VdF, TFE and PMVE (VdF/TFE/PMVE=70/12/18 in molar percent) was introduced so that the inside pressure became 1.53 MPa·G. Thereafter, as the reaction proceeded, a pressurized gas mixture of VdF, TFE and PMVE was introduced, and increasing and decreasing of the inside pressure were repeated between 1.48 MPa·G and 1.53 MPa·G, and 30 g of CNVE and 1.2 g of sodium hydroxide were introduced with pressurized nitrogen gas.
When the total amount of introduced VdF, TFE and PMVE reached 1,000 g ten hours after starting of the polymerization reaction, the autoclave was cooled, and unreacted monomers were discharged to obtain 4,061 g of an aqueous dispersion having a solid content of 25.1% by mass.
2,000 g of this aqueous dispersion was slowly added to 2,000 g of an aqueous solution of magnesium sulfate with stirring. The solution was stirred for one minute after the addition, and then a coagulated product was filtered off, followed by repeating the washing with water and the filtering off three times, washing with methanol and drying at 70° C. for 48 hours to obtain 498 g of a polymer.
As a result of analysis, this polymer was one comprising monomer units of VdF/TFE/PMVE/CNVE=66.2/13.5/19.3/1.0 in molar percent. In addition, according to measurement by infrared spectroscopic analysis, characteristic absorption of nitrile group was recognized around 2,169 cm−1. Mooney viscosity (ML1
A curable composition was prepared by mixing 0.1 part by mass of urea (available from Kishida Chemical Co., Ltd.) and 20 parts by mass of carbon black (CB) (Thermax N990 available from Cancarb Co., Ltd.) to 100 parts by mass of CN group-containing copolymer (A1) prepared in Preparation Example 1 and then kneading with an open roll. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and 100% modulus, tensile strength at break, tensile elongation at break, Shore A hardness and compression set were measured. The results are shown in Table 1.
A curable composition was prepared in the same manner as in Example 1 except that the amount of urea was changed to 0.5 part by mass. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and 100% modulus, tensile strength at break, tensile elongation at break, Shore A hardness and compression set were measured. The results are shown in Table 1.
A curable composition was prepared in the same manner as in Example 1 except that the amount of urea was changed to 2.0 parts by mass. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and 100% modulus, tensile strength at break, tensile elongation at break, Shore A hardness and compression set were measured. The results are shown in Table 1.
A curable composition was prepared in the same manner as in Example 1 except that 0.5 part by mass of ammonium perfluorohexanoate was added instead of urea. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking at 180° C. for 20 minutes to prepare a sample sheet, and 100% modulus, tensile strength at break, tensile elongation at break, Shore A hardness and compression set were measured. The results are shown in Table 1.
A curable composition was prepared in the same manner as in Example 4 except that the amount of ammonium perfluorohexanoate was changed to 1.0 part by mass. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and compression set was measured. The results are shown in Table 1.
A curable composition was prepared in the same manner as in Example 4 except that the amount of ammonium perfluorohexanoate was changed to 2.8 parts by mass. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and 100% modulus, tensile strength at break, tensile elongation at break, Shore A hardness and compression set were measured. The results are shown in Table 1.
A curable composition was prepared in the same manner as in Example 1 except that 0.5 part by mass of tribasic ammonium phosphate was added instead of urea. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and compression set was measured. The results are shown in Table 1.
A curable composition was prepared in the same manner as in Example 1 except that the CN group-containing copolymer (A2) prepared in Preparation Example 2 was used instead of the CN group-containing copolymer (A1) and the amount of urea was changed to 0.5 part by mass. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer.
The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and compression set was measured. The results are shown in Table 1.
A solution of urea was prepared by dissolving 0.5 part by mass of urea (powder available from Kishida Chemical Co., Ltd.) in the same amount of water. Then, a curable composition was prepared by mixing the prepared solution of urea containing 0.5 part by mass of urea and 20 parts by mass of carbon black (CB) (Thermax N990 available from Cancarb Co., Ltd.) to 100 parts by mass of CN group-containing copolymer (A1) prepared in Preparation Example 1 and then kneading with an open roll. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and 100% modulus, tensile strength at break, tensile elongation at break, Shore A hardness and compression set were measured. The results are shown in Table 1.
Into a 6-liter stainless steel autoclave having no ignition source were poured 3.0 liter of pure water, 6.0 g of C5F11COONH4 and 0.15 g of CH2═CFCF2OCF(CF3)CF2OCF(CF3)COONH4 as emulsifying agents, 3.5 g of disodium hydrogen phosphate and 0.6 g of sodium hydroxide, and the inside of a system was sufficiently replaced with nitrogen gas and subjected to deaeration. Then, the autoclave was heated up to 80° C. with stirring at 600 rpm, and a gas mixture of VdF and HFP (VdF/HFP=50/50 in molar percent) was introduced so that the inside pressure became 1.52 MPa·G. Then, an aqueous solution of ammonium persulfate (APS) of 1.8 g/2 ml and 1.8 g of CF2═CFOCF2CF(CF3)OCF2CF2CN (CNVE) were introduced with pressurized nitrogen gas to initiate a reaction.
As the polymerization proceeded, when the inside pressure decreased to 1.48 MPa·G, 0.2 g of diethyl malonate was introduced with pressurized nitrogen gas. Then, a pressurized gas mixture of VdF and HFP (VdF/HFP=78/22 in molar percent) was introduced so that the inside pressure became 1.52 MPa·G. Thereafter, as the reaction proceeded, a pressurized gas mixture of VdF and HFP was introduced, and increasing and decreasing of the inside pressure were repeated between 1.48 MPa·G and 1.52 MPa·G, and 50 g of CNVE and 1.2 g of sodium hydroxide were introduced with pressurized nitrogen gas.
When the total amount of introduced VdF and HFP reached 1,000 g ten hours after starting of the polymerization reaction, the autoclave was cooled, and unreacted monomers were discharged to obtain 4,052 g of an aqueous dispersion having a solid content of 24.6% by mass.
2,000 g of this aqueous dispersion was slowly added to 2,000 g of an aqueous solution of magnesium sulfate with stirring. The solution was stirred for one minute after the addition, and then a coagulated product was filtered off, followed by repeating the washing with water and the filtering off three times and drying at 70° C. for 24 hours to obtain 490 g of a polymer.
As a result of analysis, this polymer was one comprising monomer units of VdF/HFP/CNVE=77.4/21.6/1.0 in molar percent. In addition, according to measurement by infrared spectroscopic analysis, characteristic absorption of nitrile group was recognized around 2,169 cm−1. Mooney viscosity (ML1
Into a 6-liter stainless steel autoclave having no ignition source were poured 3.0 liter of pure water, 6.0 g of C5F11COONH4 and 0.15 g of CH2═CFCF2OCF(CF3)CF2OCF(CF3)COONH4 as emulsifying agents, 3.5 g of disodium hydrogen phosphate and 0.6 g of sodium hydroxide, and the inside of a system was sufficiently replaced with nitrogen gas and subjected to deaeration. Then, the autoclave was heated up to 80° C. with stirring at 600 rpm, and a gas mixture of VdF, TFE and HFP (VdF/TFE/HFP=70/11/19 in molar percent) was introduced so that the inside pressure became 1.52 MPa·G. Then, an aqueous solution of ammonium persulfate (APS) of 1.8 g/2 ml and 1.8 g of CF2═CFO(CF2)5CN (CNVE-2) were introduced with pressurized nitrogen gas to initiate a reaction.
As the polymerization proceeded, when the inside pressure decreased to 1.48 MPa·G, 0.2 g of diethyl malonate was introduced with pressurized nitrogen gas. Then, a pressurized gas mixture of VdF, TFE and HFP (VdF/TFE/HFP=50/20/30 in molar percent) was introduced so that the inside pressure became 1.52 MPa·G. Thereafter, as the reaction proceeded, a pressurized gas mixture of VdF, TFE and HFP was introduced, and increasing and decreasing of the inside pressure were repeated between 1.48 MPa·G and 1.52 MPa·G, and 48 g of CLAVE-2 and 1.2 g of sodium hydroxide were introduced with pressurized nitrogen gas.
When the total amount of introduced VdF, TFE and HFP reached 1,000 g ten hours after starting of the polymerization reaction, the autoclave was cooled, and unreacted monomers were discharged to obtain 4,160 g of an aqueous dispersion having a solid content of 24.5% by mass.
2,000 g of this aqueous dispersion was slowly added to 2,000 g of an aqueous solution of magnesium sulfate with stirring. The solution was stirred for one minute after the addition, and then a coagulated product was filtered off, followed by repeating the washing with water and the filtering off three times and drying at 70° C. for 24 hours to obtain 490 g of a polymer.
As a result of analysis, this polymer was one comprising monomer units of VdF/TFE/HFP/CNVE=50.1/18.6/30.3/1.0 in molar percent. In addition, according to measurement by infrared spectroscopic analysis, characteristic absorption of nitrile group was recognized around 2,169 cm−1. Mooney viscosity (ML1
A curable composition was prepared by mixing 0.5 part by mass of urea (available from Kishida Chemical Co., Ltd.) and 20 parts by mass of carbon black (CB) (Thermax N990 available from Cancarb Co., Ltd.) to 100 parts by mass of CN group-containing copolymer (A3) prepared in Preparation Example 3 and then kneading with an open roll. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and compression set was measured. The results are shown in Table 1.
A curable composition was prepared by mixing 0.5 part by mass of urea (available from Kishida Chemical Co., Ltd.) and 20 parts by mass of carbon black (CB) (Thermax N990 available from Cancarb Co., Ltd.) to 100 parts by mass of CN group-containing copolymer (A4) prepared in Preparation Example 4 and then kneading with an open roll. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and compression set was measured. The results are shown in Table 1.
A curable composition was prepared by mixing 0.4 part by mass of ammonium adipate and 20 parts by mass of carbon black (CB) (Thermax N990 available from Cancarb Co., Ltd.) to 100 parts by mass of CN group-containing copolymer (A1) prepared in Preparation Example 1 and then kneading with an open roll. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and compression set was measured. The results are shown in Table 1.
A curable composition was prepared by mixing 1.0 part by mass of ammonium phthalate and 20 parts by mass of carbon black (CB) (Thermax N990 available from Cancarb Co., Ltd.) to 100 parts by mass of CN group-containing copolymer (A1) prepared in Preparation Example 1 and then kneading with an open roll. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and compression set was measured. The results are shown in Table 1.
10 parts by mass of methanol, 0.5 part by mass of urea (available from Kishida Chemical Co., Ltd.) and 20 parts by mass of carbon black (CB) (Thermax N990 available from Cancarb Co., Ltd.) were previously mixed and then the mixture was blended to 100 parts by mass of CN group-containing copolymer (A1) prepared in Preparation Example 1, followed by kneading with an open roll to prepare a curable composition. A part of this curable composition was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer. The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and compression set was measured. The results are shown in Table 1.
A curable composition for comparison was prepared by mixing 20 parts by mass of carbon black (N990) to 100 parts by mass of CN group-containing copolymer (A1) and then kneading with an open roll. Crosslinking characteristics of the composition were examined. The results are shown in Table 1.
A curable composition for comparison was prepared by mixing 1.8 parts by mass of 2,2-bis(3-amino-4-hydroxyphenyl)hexafluoropropane (OH-AF) as a curing agent and 20 parts by mass of carbon black (N990) to 100 parts by mass of CN group-containing copolymer (A1) and then kneading with an open roll. A part of this curable composition for comparison was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer.
This curable composition was subjected to crosslinking at 180° C. for 30 minutes to prepare a sample sheet, and 100% modulus, tensile strength at break, tensile elongation at break, Shore A hardness and compression set were measured. The results are shown in Table 1.
A curable composition was prepared in the same manner as in Comparative Example 2 except that 2,2-bis[3-amino-4-(N-phenylamino)phenyl)hexafluoropropane (Nph-AF) was used as a curing agent instead of OH-AF. A part of this curable composition for comparison was collected, and crosslinking characteristics thereof at 180° C. were examined with a Curastometer.
The composition was subjected to crosslinking under the above-mentioned standard crosslinking conditions to prepare a sample sheet, and 100% modulus, tensile strength at break, tensile elongation at break, Shore A hardness and compression set were measured. The results are shown in Table 1.
A curable composition for comparison was prepared by mixing 1.8parts by mass of 2, 2-bis(3-amino-4-hydroxyphenyl)hexafluoropropane (OH-AF) as a curing agent and 20 parts by mass of carbon black (N990) to 100 parts by mass of CN group-containing copolymer (A2) and then kneading with an open roll.
This curable composition for comparison was subjected to crosslinking at 180° C. for 50 minutes to prepare a sample sheet. Crosslinking characteristics of the composition were examined. The results are shown in Table 1.
From the results shown in Table 1, it is seen that crosslinking speed is greatly improved. Further, it is seen that physical properties under normal conditions are improved by the presence of the solvent (water) having affinity for urea.
The present invention can provide a curable composition of a vinylidene fluoride type elastomer assuring improved crosslinking speed and making it possible to use a cheap curing agent, and a molded article obtained from the curable composition.
This application claims benefit under 35 U.S.C. §119(e) of U.S. Provisional Application No. 61/077,058 filed on Jun. 30, 2008 and U.S. Provisional Application No. 61/100,199 filed on Sep. 25, 2008, incorporated herein by reference in its entirety.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP2009/062241 | 6/29/2009 | WO | 00 | 12/29/2010 |
| Number | Date | Country | |
|---|---|---|---|
| 61077058 | Jun 2008 | US | |
| 61100199 | Sep 2008 | US |
