JP2013083340A - Seal member - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a seal member excellent in fluorocarbon fluid resistance and a valve using the seal member.SOLUTION: The seal member contains 5 pts.mass to 25 pts.mass of carbon nanofiber, 10 pts.mass to 40 pts.mass of carbon black based on 100 pts.mass of a ternary fluorine elastomer containing 65 mass% or more of fluorine. In the seal member, the stress when extended 50% after a liquid resistant test where the seal member is submerged in perfluoropolyether (>99.9%[w/w]) at 130°C for 103 hr is 8 MPa or more. The volume change ratio of the seal member before and after the liquid resistant test is 4.0% or less. The valve V is constituted by using the seal member 9.

Description

  The present invention relates to a seal member excellent in fluorine-based fluid resistance and a valve using the seal member.

  As a fluorinated fluid that can be used in a wide temperature range from low temperature to high temperature and has excellent thermal conductivity, for example, perfluoropolyether is used as a heat medium for adjusting the temperature of the chamber. In chamber temperature control of a semiconductor manufacturing apparatus, inertness, high electrical insulation, low toxicity, nonflammability, solvent resistance, and the like may be required for a heat medium. Perfluoropolyether is a heat medium that meets these requirements, and is used as a heat medium for semiconductor manufacturing equipment (see, for example, Patent Document 1).

  For example, when using perfluoropolyether to control the chamber temperature of semiconductor manufacturing equipment, piping and valves are required to transfer the perfluoropolyether to each part of the equipment, and the piping and valves are made of elastic material. A large number of sealed members are mounted. In particular, when perfluoropolyether is used at a high temperature, the sealing member is also required to have heat resistance, and a fluororubber-based sealing member is desired.

  However, when a fluororubber-based seal member is employed, perfluoropolyether may act as a solvent on the fluororubber and the seal member may be deteriorated.

JP 2008-31346 A

  An object of the present invention is to provide a seal member excellent in fluorine-based fluid resistance and a valve using the seal member. Another object of the present invention is to provide a valve evaluation method for numerically evaluating the controllability of a minute flow rate.

The sealing member according to the present invention is
For 100 parts by mass of a ternary fluorine-containing elastomer having a fluorine content of 65% by mass or less, 5 to 25 parts by mass of carbon nanofibers, and 10 to 40 parts by mass of carbon black,
The stress at 50% elongation after a liquid resistance test immersed in perfluoropolyether at 130 ° C. (> 99.9% [W / W]) for 103 hours is 8.0 MPa or more,
The volume change rate before and after the liquid resistance test is 4.0% or less.

  According to the seal member of the present invention, deterioration due to contact with perfluoropolyether can be suppressed.

In the sealing member according to the present invention,
The mass change rate before and after the liquid resistance test may be 4.0% or less.

In the sealing member according to the present invention,
The rate of change of stress at 50% elongation before and after the liquid resistance test can be within ± 7.0%.

In the sealing member according to the present invention,
Before and after the liquid resistance test, the rate of change of stress at 50% elongation cannot be negative.

  The valve according to the present invention uses the seal member.

  According to the valve of the present invention, since the deterioration due to the seal member coming into contact with the perfluoropolyether is suppressed, a stable flow rate control characteristic can be provided.

The method for evaluating a valve according to the present invention is as follows.
A valve evaluation method for controlling the flow rate of fluid by moving a valve body forward and backward relative to a valve seat,
A first flow characteristic curve composed of Cv values with respect to the valve opening degree (%) in the valve opening operation and a second flow characteristic curve composed of Cv values with respect to the valve opening degree (%) in the valve closing operation are measured. And
Calculating the area of the closed region formed between the first flow characteristic curve and the second flow characteristic curve at the minute opening of the valve as a flow control index;
The controllability of the flow rate is evaluated by the flow rate control index.

In the valve evaluation method according to the present invention,
The flow rate control index of the valve equipped with the seal material before the liquid resistance test immersed in perfluoropolyether (> 99.9% [W / W]) at 130 ° C. for 103 hours is calculated as the first flow rate control index. And
Calculating the flow rate control index of the valve equipped with the sealing material after the liquid resistance test as a second flow rate control index;
The controllability of the flow rate can be evaluated by the difference between the first flow rate control index and the second flow rate control index.

It is a longitudinal cross-sectional view of the needle valve concerning one embodiment of the present invention. It is the elements on larger scale which showed the valve opening state of the needle valve in FIG. It is the elements on larger scale which showed the valve closing state of the needle valve in FIG. It is a schematic diagram explaining the crushing rate of an O-ring. 6 is a graph showing flow characteristics in the needle valve of Comparative Example 1. 6 is a graph showing flow characteristics in the needle valve of Example 3. 6 is a graph showing flow characteristics in the needle valve of Comparative Example 1. 10 is a graph showing a flow characteristic in the needle valve of Comparative Example 4. 6 is a graph showing flow characteristics in the needle valve of Example 3. 14 is a graph showing flow characteristics in the needle valve of Example 11. It is a graph which shows the flow volume characteristic in the needle valve of Example 12. It is a graph which shows the flow volume characteristic in the needle valve of Example 13. It is a graph which shows the flow volume characteristic in the needle valve of Example 14. It is a figure explaining the measuring method of the flow control index using the graph which shows the flow characteristic in the needle valve of comparative example 1.

  Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

  The sealing member according to one embodiment of the present invention is composed of 5 to 25 parts by mass of carbon nanofibers and 10 parts by mass of carbon black with respect to 100 parts by mass of a ternary fluorine-containing elastomer having a fluorine content of 65% by mass or less. To 40 parts by mass, and the stress at 50% elongation after a liquid resistance test immersed in perfluoropolyether (> 99.9% [W / W]) at 130 ° C. for 103 hours is 8.0 MPa. The volume change rate before and after the liquid resistance test is 4.0% or less.

  A valve according to an embodiment of the present invention is characterized by using the seal member.

  A valve evaluation method according to an embodiment of the present invention is a valve evaluation method for controlling the flow rate of a fluid by moving a valve body forward and backward with respect to a valve seat, and includes a valve opening degree ( %) And a second flow characteristic curve consisting of Cv value with respect to the opening degree (%) of the valve in the valve closing operation, and measuring at a minute opening degree of the valve Calculating an area of a closed region formed between the first flow characteristic curve and the second flow characteristic curve as a flow control index, and evaluating the controllability of the flow by the flow control index. Features.

  A seal member according to an embodiment of the present invention will be described. The sealing member includes carbon nanofibers and carbon black in a ternary fluorine-containing elastomer.

The ternary fluorine-containing elastomer is a vinylidene fluoride-based synthetic rubber containing a fluorine atom in the molecule, and is also called a ternary fluorine-containing rubber. For example, vinylidene fluoride (VDF) -hexafluoropropylene (HFP) -Tetrafluoroethylene (TFE) terpolymer (VDF-HFP-TFE), vinylidene fluoride (VDF) -perfluoro (methyl vinyl ether) (FMVE) -tetrafluoroethylene (TFE) terpolymer (VDF) -HFP-TFE) and the like. Examples of ternary fluorine-containing elastomers include DuPont's trade name Viton, Daikin Industries 'trade name Daiel, and Solvay Solexis' trade name Technoflon. In the following description, the ternary fluorine-containing elastomer may be abbreviated as FKM. The ternary fluorine-containing elastomer preferably has a weight average molecular weight of 50,000 to 300,000. If the molecular weight of the ternary fluorine-containing elastomer is within this range, the ternary fluorine-containing elastomer molecules are entangled with each other and connected to each other, so the ternary fluorine-containing elastomer disperses the carbon nanofibers. Can have good elasticity. The ternary fluorine-containing elastomer has viscosity, so that the aggregated carbon nanofibers can easily enter each other, and the carbon nanofibers can be separated by having elasticity. If the weight average molecular weight of the ternary fluorine-containing elastomer is smaller than 50,000, the ternary fluorine-containing elastomer molecules cannot be sufficiently entangled with each other, and elasticity is exerted even if a shearing force is applied in a later step. Since it is small, the effect of dispersing the carbon nanofibers tends to be small. If the weight average molecular weight of the ternary fluorine-containing elastomer is larger than 300,000, the ternary fluorine-containing elastomer tends to be too hard and difficult to process. The ternary fluorine-containing elastomer has a fluorine content of 65% by mass or less, can be 60% by mass to 65% by mass, and particularly 63% by mass to 65% by mass. The ternary fluorine-containing elastomer can be excellent in perfluoropolyether resistance when the fluorine content is 65% by mass or less. The ternary fluorine-containing elastomer has a central value of Mooney viscosity (ML _{1 + 4} 121 ° C.) of 25 to 65 or a central value of Mooney viscosity (ML _{1 + 4} 100 ° C.) of 25 to 70, and a specific gravity of 1.75 g / cm ³ to It can be 2.0 g / cm ³ . Further, when the median value of Mooney viscosity (ML _{1 + 4} 121 ° C.) is 25 or more or the median value of Mooney viscosity (ML _{1 + 4} 100 ° C.) is 25 or more, the basics such as tensile strength (TS) and compression set (CS) are obtained. If the median value of Mooney viscosity (ML _{1 + 4} 121 ° C.) is 65 or less or the median value of Mooney viscosity (ML _{1 + 4} 100 ° C.) is 70 or less, it has an appropriate viscosity and can be processed. it can.

  The carbon nanofibers used in one embodiment of the present invention can have an average diameter (fiber diameter) of 9 nm to 110 nm, and more preferably 9 nm to 20 nm. Since such carbon nanofibers have a relatively small average diameter, the specific surface area is large, the surface reactivity with the matrix elastomer is improved, and the carbon nanofibers in the elastomer tend to be poorly dispersed. is there. Carbon nanofibers are expected to have moderate flexibility when the diameter is 9 nm or more so that the microcell structure formed by the carbon nanofibers surrounding the matrix material is not too small. Conversely, when the diameter is 110 nm or less, the microcell structure is large. However, it is expected to have an effect of wear resistance. The micro cell structure formed by the carbon nanofibers can be formed so as to surround the matrix material by a network structure in which the carbon nanofibers are stretched in three dimensions. The carbon nanofibers can be subjected to a known activation treatment in order to improve the reactivity with the elastomer on the surface. The average diameter of the carbon nanofiber can be measured by observation with an electron microscope. In the detailed description of the present invention, the average diameter and the average length of the carbon nanofibers are, for example, 5,000 times or more from an electron microscope (the magnification can be appropriately changed depending on the size of the carbon nanofibers), and the diameters of 200 or more locations. And the length can be measured and calculated as the arithmetic average value.

  The carbon nanofiber is a so-called multi-walled carbon nanotube (MWNT: multi-wall carbon nanotube) having a shape formed by winding one surface (graphene sheet) of graphite having a carbon hexagonal mesh surface into a cylindrical shape. A carbon material having a structure can also be used. In addition to the name “carbon nanotube”, it may be called “graphite fibril nanotube” or “vapor-grown carbon fiber”.

Carbon nanofibers can be obtained by a vapor deposition method. Vapor phase growth is also called catalytic chemical vapor deposition (CCVD), which produces untreated carbon nanofibers by gas phase pyrolysis of hydrocarbons and other gases in the presence of metal catalysts. It is a method to do. The vapor phase growth method will be described in more detail. For example, an organic compound such as benzene or toluene is used as a raw material, an organic transition metal compound such as ferrocene or nickelcene is used as a metal catalyst, and these are used together with a carrier gas at a high temperature such as 400 ° C. Introduced into a reaction furnace set at a reaction temperature of ~ 1000 ° C and floated on a floating reaction method (floating reaction method) that generates carbon nanofibers on the reaction furnace wall or ceramics such as alumina and magnesium oxide in advance A catalyst-supporting reaction method (Substrate Reaction Method) in which the supported metal-containing particles are brought into contact with a carbon-containing compound at a high temperature to generate carbon nanofibers on the substrate can be used. For example, carbon nanofibers having an average diameter of 9 nm to 20 nm can be obtained by a catalyst-supporting reaction method, and carbon nanofibers thicker than this can be obtained by a floating flow reaction method. The diameter of the carbon nanofiber can be adjusted by, for example, the size of the metal-containing particles and the reaction time.

  The compounding quantity of carbon nanofiber can be adjusted with the compounding quantity of carbon black, and 5 mass parts-25 mass parts are mix | blended with respect to 100 mass parts of ternary type fluorine-containing elastomers. In particular, the carbon nanofiber can be blended in an amount of 10 to 20 parts by mass with respect to 100 parts by mass of the ternary fluorine-containing elastomer. Carbon nanofibers can form a nano-sized cell structure by blending 5 parts by mass or more into a ternary fluorine-containing elastomer, particularly when carbon nanofibers having an average diameter of 9 nm to 20 nm are used. It is considered possible. Moreover, if carbon nanofiber is a compounding quantity of 25 mass parts or less, there exists a tendency for perfluoropolyether resistance to improve. Here, “parts by mass” indicates “phr” unless otherwise specified, and “phr” is an abbreviation for “parts per undred of resin or rubber”, and represents the percentage of external additives such as additives to rubber and the like. It is.

  The carbon black may have an average particle size of 10 nm to 300 nm. By blending carbon black into a ternary fluorine-containing elastomer, the matrix region of the fluorine-containing elastomer can be divided into fine sizes by carbon black, and the matrix region divided into fine sizes is reinforced by carbon nanofibers. Therefore, the blending amount of carbon nanofibers can be reduced by blending carbon black. The compounding amount of the carbon black can be adjusted in accordance with the compounding amount of the carbon nanofiber, and is 10 to 40 parts by mass, particularly 15 parts by mass with respect to 100 parts by mass of the ternary fluorine-containing elastomer. It can be -25 mass parts.

  As the filler, at least one selected from silica, clay, talc and the like, which can be used as an elastomer filler, can be selected. Silica, talc and clay may have an average particle size of 5 nm to 50 nm.

  The seal member has a stress at the time of 50% elongation after a liquid resistance test immersed in perfluoropolyether (> 99.9% [W / W]) at 130 ° C. for 103 hours of 8.0 MPa or more. The rate of volume change is 4.0% or less before and after the liquid test. When a sealing member made of a fluorine-containing elastomer is immersed in perfluoropolyether at 130 ° C. for a long time, the sealing member tends to deteriorate and a volume change tends to occur. On the other hand, in the sealing member according to the present embodiment, the volume change rate before and after the liquid resistance test is as small as 4.0% or less, and the stress at 50% elongation after the liquid resistance test is also 8.0 MPa. Since it is high as mentioned above, it can be said that it is excellent in perfluoropolyether resistance. In the present specification, the liquid resistance test refers to immersion in a perfluoropolyether at 130 ° C. for 103 hours. Further, the seal member may have a stress at 50% elongation after the liquid resistance test of 8.0 MPa or more and 30.0 MPa or less, and in particular, a stress at 50% elongation after the liquid resistance test of 8%. It can be 0.0 MPa or more and 20.0 MPa or less. If the stress at 50% elongation after the liquid resistance test of the seal member is 8.0 MPa or more, high strength can be maintained even in an environment where the seal member is in contact with the perfluoropolyether. For example, the seal member can be used as a valve. When used, the fine flow rate controllability can be excellent. Furthermore, the sealing member may have a volume change rate of 0.0% to 4.0% before and after the liquid resistance test, and in particular, 1.0% to 3.0%. When the seal member has a volume change rate of 4.0% or less before and after the liquid resistance test, it can be said that there is little deterioration of the seal member even in an environment in contact with the perfluoropolyether. When used in the above, stable flow rate control characteristics can be obtained. In this specification, “change rate” is the percentage of the difference between the measured value before and after the liquid resistance test with respect to the measured value before the liquid resistance test, and the difference between the measured values before and after the liquid resistance test is the liquid resistance. The measured value before the liquid resistance test is subtracted from the measured value after the test. For example, the volume change rate is (Vc1−Vc0) / Vc0 × 100. Vc0 is the volume before the liquid resistance test, and Vc1 is the volume after the liquid resistance test.

  The sealing member can have a mass change rate of 4.0% or less before and after the liquid resistance test, and the mass change rate before and after the liquid resistance test is 4.0% or less, 0.0% or more. In particular, the mass change rate before and after the liquid resistance test can be 3.0% or less and 1.0% or more. When the sealing member has a mass change rate of 4.0% or less before and after the liquid resistance test, it can be said that the deterioration of the sealing member is small even in an environment where it comes into contact with the perfluoropolyether.

  The sealing member can have a stress change rate of ± 7.0% within 50% before and after the liquid resistance test, and the stress change rate during 50% elongation before and after the liquid resistance test. It can be within ± 6.5%. If the rate of change of stress when the seal member is 50% elongated before and after the liquid resistance test is 7.0% or less, high strength can be maintained before and after the liquid resistance test. When it is used, it can be excellent in minute flow rate controllability. The seal member can have a negative rate of change in stress when stretched by 50% before and after the liquid resistance test. When such a seal member is used for a valve, a minute flow rate at the time of opening and closing the valve Excellent control reproducibility. The reproducibility of the minute flow rate control means that a flow rate increase curve with respect to the valve opening degree when the valve is opened approximates a flow rate decrease curve with respect to the valve opening degree when the valve is closed.

  In the sealing member according to one embodiment of the present invention, carbon nanofibers and carbon black are mixed with a ternary fluorine-containing elastomer and uniformly dispersed in the ternary fluorine-containing elastomer by a shearing force. Thus, it can be obtained by a production method including a step of obtaining a carbon fiber composite material. The seal member can be obtained by molding a carbon fiber composite material into a desired shape. Generally, it is not easy to disperse and disperse carbon nanofibers that easily aggregate in a ternary fluorine-containing elastomer. As described below, it can be produced by utilizing the characteristics of a ternary fluorine-containing elastomer and carbon nanofibers. A method for producing a carbon fiber composite material by the open roll method will be described. In the description of the production method, the ternary fluorine-containing elastomer is simply abbreviated as elastomer.

  The first roll and the second roll in the two-roll open roll are arranged at a predetermined interval, for example, an interval of 0.5 mm to 1.5 mm, and rotate at rotation speeds V1 and V2. First, the elastomer wound around the first roll is masticated, and the elastomer molecular chain is appropriately cut to generate free radicals. Free radicals of the elastomer generated by mastication are likely to be combined with carbon nanofibers.

  Next, carbon nanofibers and carbon black are put into an elastomer bank wound around the first roll and kneaded. The temperature of the elastomer in this kneading can be, for example, 100 ° C. to 200 ° C., and further can be 150 ° C. to 200 ° C. As described above, it is considered that the elastomer and the carbon nanofibers are kneaded at a relatively high temperature as compared with the thin thread to be described later, so that the elastomer easily enters the gap between the carbon nanofibers. The step of mixing the elastomer and the carbon nanofiber is not limited to the open roll method, and for example, a closed kneading method or a multiaxial extrusion kneading method can be used.

  Furthermore, the roll interval between the first roll and the second roll is set to, for example, 0.5 mm or less, more preferably 0 to 0.5 mm, and the mixture is put into an open roll to pass through once. ~ Repeat multiple times. For example, the thinning can be performed about 1 to 10 times. When the surface speed of the first roll is V1, and the surface speed of the second roll is V2, the surface speed ratio (V1 / V2) of both in thinness can be 1.05 to 3.00, Furthermore, it can be 1.05-1.2. By using such a surface velocity ratio, a desired shear force can be obtained. The carbon fiber composite material extruded from between the narrow rolls as described above is greatly deformed by the restoring force due to the elasticity of the elastomer, and at that time, the carbon nanofibers move greatly together with the elastomer. In this thinning process, in order to obtain as high a shearing force as possible, the roll temperature is set to a relatively low temperature of, for example, 0 to 50 ° C., more preferably 5 to 30 ° C., and the measured temperature of the elastomer is also 0. It can be adjusted to -50 ° C. The shearing force thus obtained causes a high shearing force to act on the elastomer, so that the aggregated carbon nanofibers are separated from each other so as to be pulled out one by one to the elastomer molecules and dispersed in the elastomer. In particular, since an elastomer has elasticity, viscosity, and chemical interaction with carbon nanofibers, the carbon nanofibers can be easily dispersed. And the carbon fiber composite material excellent in the dispersibility and dispersion stability of carbon nanofiber (it is hard to re-aggregate carbon nanofiber) can be obtained. The carbon fiber composite material obtained through thinning can be further rolled with a roll and dispensed into a sheet having a predetermined thickness.

  More specifically, when an elastomer and carbon nanofibers are mixed with an open roll, the viscous elastomer penetrates into the carbon nanofibers, and a specific part of the elastomer is chemically interacted with the carbon nanofibers. Binds to highly active moieties. Next, when a strong shearing force acts on the elastomer, the carbon nanofibers move with the movement of the elastomer molecules, and the aggregated carbon nanofibers are separated by the restoring force of the elastomer due to the elasticity after shearing, It will be dispersed in the elastomer. According to the present embodiment, when the carbon fiber composite material is extruded through a narrow and narrow roll, the carbon fiber composite material is deformed to be thicker than the roll interval due to the restoring force due to the elasticity of the elastomer. The deformation can be presumed to cause the carbon fiber composite material subjected to a strong shear force to flow more complicatedly and disperse the carbon nanofibers in the elastomer. The carbon nanofibers once dispersed are prevented from reaggregating due to chemical interaction with the elastomer, and can have good dispersion stability.

  The step of dispersing the carbon nanofibers in the elastomer by a shearing force is not limited to the open roll method, and a closed kneading method or a multiaxial extrusion kneading method can also be used. In short, in this step, it is sufficient that a shearing force capable of separating the aggregated carbon nanofibers can be given to the elastomer. In particular, the open roll method is preferable because it can measure and manage not only the roll temperature but also the actual temperature of the mixture. For crosslinking of the elastomer, for example, peroxide vulcanization excellent in chemical resistance can be used. The cross-linking agent can be added, for example, before mixing the carbon nanofibers and carbon black into the elastomer, together with the carbon nanofibers and carbon black, or after mixing the carbon nanofibers, carbon black, and elastomer. Therefore, a crosslinking agent can be mix | blended with the uncrosslinked carbon fiber composite material after passing through.

  The seal member can be obtained by molding a carbon fiber composite material into a desired shape, for example, endless shape by a rubber molding process generally employed, for example, a press molding method, an injection molding method, an extrusion molding method, or the like. The sealing member can be formed of a vulcanized carbon fiber composite material. For example, after the primary vulcanization in press molding, the sealing member can be secondary vulcanized in a heat oven or the like.

  In the manufacturing method of the seal member according to the present embodiment, a compounding agent usually used for processing an elastomer can be added. A well-known thing can be used as a compounding agent. Examples of the compounding agent include a crosslinking agent, a vulcanizing agent, a vulcanization accelerator, a vulcanization retarder, a softening agent, a plasticizer, a curing agent, a reinforcing agent, a filler, an anti-aging agent, a colorant, and an acid acceptor. Can be mentioned. These compounding agents can be added to the elastomer at an appropriate time during the mixing process.

  The seal member can be used as, for example, a gasket used for a fixed part or a packing used for a movable part. For example, there is an endless seal member having an endless continuous outer shape. The endless seal member is not limited to a circular outer shape, and may be, for example, a polygon in accordance with the shape of the groove or member in which the seal member is disposed. The endless seal member may be an O-ring having a circular cross section. The seal member can be used by being mounted in a pipe or valve that contacts the perfluoropolyether. In the piping, for example, a seal member is used at a joint portion that connects the piping to each other or between the piping and another device, and can be sealed liquid-tightly. In the valve, for example, a seal member is attached to a valve body which is a movable part in the valve, the seal member and the valve seat are closely sealed, and a predetermined interval is provided between the seal member and the valve seat. Thus, the flow rate of the fluid flowing in the valve can be controlled.

The carbon fiber composite material is an uncrosslinked body, measured at 150 ° C. by the Hahn-echo method using pulsed NMR, with the observation nucleus measured at ¹ H, and the characteristic relaxation time (T2′HE / 150 ° C.) is 500 to 1200 μsec. Can be further 500 to 1300 microseconds, in particular 500 to 1100 microseconds. Note that “HE” in the characteristic relaxation time (T2′HE) is a notation used to distinguish from “SE” in the solid echo method described later. The characteristic relaxation time (T2′HE) by the Hahn-echo method is a measure showing the molecular mobility of the ternary fluorine-containing elastomer and represents the average relaxation time of a multicomponent system. Therefore, the characteristic relaxation time (T2′HE) is an average value of a plurality of relaxation times detected by the Hahn echo method, and is expressed as “1 / T2′HE = fa / T2a + fb / T2b + fc / T2c. Can do. It can be said that the carbon fiber composite material in which the carbon nanofibers are dispersed represents the force by which the carbon nanofibers restrain the elastomer molecules as a matrix, and (T2′HE / 150 ° C.) is a ternary fluorine-containing elastomer alone. It becomes small according to the compounding quantity of carbon nanofiber. Therefore, even if it is a carbon fiber composite material mixed with carbon nanofibers, if the carbon nanofibers are not uniformly dispersed, it is difficult to restrain the elastomer molecules as a whole. It is considered that (T2′HE / 150 ° C.) is not significantly different from that of a ternary fluorine-containing elastomer alone.

The carbon fiber composite material is an uncrosslinked body, measured at 150 ° C. by a solid echo method using pulsed NMR, and the observation nucleus is ¹ H, and the characteristic relaxation time (T2′SE / 150 ° C.) is 10 to 700 μsec. Further, the characteristic relaxation time (T2′SE / 150 ° C.) can be 10 to 500 μsec, and the characteristic relaxation time (T2′SE / 150 ° C.) can be 10 to 200 μsec. The characteristic relaxation time (T2′SE) by the solid echo method is a measure showing the non-uniformity of the magnetic field due to the carbon nanofibers, and represents the average relaxation time of a multicomponent system. Therefore, the characteristic relaxation time (T2′SE) is an average value of a plurality of relaxation times detected by the Hahn echo method, and is expressed as “1 / T2′SE = fa / T2a + fb / T2b + fc / T2c. Can do. In the carbon fiber composite material in which carbon nanofibers are dispersed, nonuniformity of the magnetic field occurs due to the uniform dispersion of carbon nanofibers, and the characteristic relaxation time (T2′SE / 150 ° C.) by the solid echo method at 150 ° C. is 3. Compared to the original fluorine-containing elastomer alone, it becomes smaller according to the blending amount of carbon nanofibers. In addition, even when carbon nanofibers are mixed with carbon nanofibers, non-uniformity of the magnetic field is not introduced when carbon nanofibers are not uniformly dispersed. The relaxation time (T2′SE / 150 ° C.) is considered to be almost the same as that of the ternary fluorine-containing elastomer alone.

  In addition, around the carbon nanofibers, a part of the elastomer is molecular chain cleaved during kneading, and the free radicals generated thereby attack the surface of the carbon nanofibers and are considered to be aggregates of elastomer molecules. An interfacial phase is formed. The interfacial phase is considered to be similar to a bound rubber formed around carbon black when, for example, an elastomer and carbon black are kneaded. Such an interfacial phase is coated and protected with carbon nanofibers, and by blending more than a predetermined amount of carbon nanofibers, the interfacial phase is surrounded by an interfacial phase and is divided into nanometer-sized elastomers. Are estimated to form small cells. By forming such small cells almost uniformly throughout the carbon fiber composite material, it is possible to expect an effect that exceeds the effect of simply combining the two materials.

  Next, a needle valve will be described as an example of a valve using a seal member according to an embodiment of the present invention as an O-ring. FIG. 1 is a longitudinal sectional view of a needle valve V according to an embodiment of the present invention. The valve body 1 of the needle valve V has an inlet 2, an outlet 3, a valve chamber 4 provided in a flow path from the inlet 2 to the outlet 3, and a shaft mounting hole 5 communicating with the valve chamber 4. , Is provided. The valve chamber 4 includes an annular valve seat 6 that is attached to the inlet 2, a cylinder 13 that fixes the valve seat 6 in the valve chamber 4, and a needle 7 that is separated from the valve seat 6. Has been placed. The needle 7 includes a conical tapered portion 7a seated on the valve seat 6, a flange portion 7b having an outer diameter larger than the tapered portion 7a, and an annular groove formed between the tapered portion 7a and the flange portion 7b. The outer peripheral groove 10, the O-ring 9 which is a seal member mounted on the outer peripheral groove 10, the shaft portion 8 extending from the flange portion 7 b in the opposite direction to the taper portion 7 a, and the end portion of the shaft portion 8. And an engagement piece 16 having an outer diameter larger than that of the shaft portion 8. In the shaft mounting hole 5 of the valve body 1, a holding body 14, a cylindrical bush 17, and a guide body disposed between the cylindrical body 13 and the holding body 14 on the side facing the valve seat 6 of the cylindrical body 13. 31, a spring 15 disposed between the engagement piece 16 and the holding body 14, and a bearing 30 that contacts the end of the shaft portion 8 and can move within the inner wall of the bush 17. . The bush 17 is mounted in an annular heat insulating plate 32, and the bush 17 and the heat insulating plate 32 are provided with communication holes 32 a and 17 a that communicate from the inside of the bush 17 to the outside.

  An actuator 20 is attached to the valve body 1 via a heat insulating plate 32 and a bush 17. The actuator 20 includes a direct-acting electric motor 18 that is screwed into the housing 20a. The DC electric motor 18 includes a rotor (not shown), an output shaft (screw shaft) 19 having a threaded portion, a rotation transmission mechanism (not shown) that transmits the rotational force of the rotor to the output shaft 19, and the like. The rotational force is converted into a linear motion by the output shaft 19, and the output shaft 19 is configured to slide in the axial direction.

  The needle valve V is excellent in controlling the flow rate of a fluid, particularly an aqueous fluid and an oil fluid, and can be used as a flow control valve for perfluoropolyether.

  FIG. 2 is a partially enlarged cross-sectional view showing the opened state of the needle valve in FIG. FIG. 3 is a partially enlarged cross-sectional view showing a closed state of the needle valve in FIG. FIG. 4 is a schematic diagram for explaining the crushing rate of the O-ring. The valve seat 6 is attached to a step portion 1b provided on the inlet 2 side of the valve chamber 4 via a seal ring 21, and a valve port 6b which is an opening on the inlet 2 side of the valve seat 6; An inclined surface 6a that expands upward (in the direction from the inflow port 2 toward the valve chamber 4) and a reduced diameter portion 6c that is a corner portion connecting the valve port 6b and the inclined surface 6a are formed. In this example, the valve seat 6 made of metal is adopted, but it may be made of resin or other materials, and can be arbitrarily adopted depending on the implementation. Of course, other components can be arbitrarily adopted according to the implementation.

  A conical tapered portion 7a whose diameter decreases toward the distal end is formed on the outer peripheral portion of the needle 7 and an outer peripheral groove 10 is provided at a position above the tapered portion 7a, that is, between the tapered portion 7a and the flange 7b. An O-ring 9 is attached to seal between the needle 7 and the valve seat 6 when seated. The outer circumferential groove 10 is formed with a gap portion 10a that is inclined so that the tapered portion 7a side of the outer circumferential groove 10 is inclined downward, and the surface of the outer circumferential groove 10 that contacts the O-ring 9 is an arcuate surface. 10 b is formed, and the radius of the circular arc surface 10 b is made substantially coincident with the radius of the O-ring 9. With the structure of the outer peripheral groove 10, the function of reducing the influence of the fluid pressure in the valve slightly opened state and preventing the so-called blowout phenomenon is exhibited.

  The shaft portion 8 of the needle 7 is guided by a through hole 31 a formed by combining the guide body 31 and the disc-shaped holding body 14. The cylindrical body 13 and the holding body 14 form a mounting groove 12 for mounting the dust seal 33, the guide body 31 and the O-ring 11 around the shaft portion 8. The cylinder 13, the guide body 31, and the holding body 14 can be made of resin. Before the needle 7 is assembled to the valve body 1, the holding body 14 is assembled to the shaft portion 8 via the cylindrical body 13, the dust seal member 33, the guide body 31, and the O-ring 11. One end of the spring 15 is attached to the upper portion, and the other end of the spring 15 is locked while being compressed by the engagement piece 16 provided on the shaft portion 8, so that the needle unit 23 can be assembled.

  In the valve body 1, the valve seat 6 is placed on the step portion 1 b in the valve chamber 4, and the needle unit 23 is inserted into the valve body 1 from the shaft mounting hole 5 formed to communicate with the valve chamber 4. Then, the bush 17 is inserted from the shaft mounting hole 5 to be positioned on the upper surface of the holding body 14, and the bearing 30 is inserted into the bush 17 to push down the shaft portion 8. The valve seat 6 can be aligned via In the present embodiment, the enlarged diameter portion 7c having the maximum diameter in the tapered portion 7a of the needle 7 can be aligned while pressing a part of the reduced diameter portion 6c below the inclined surface 6a of the valve seat 6. After the alignment of the valve seat 6 is completed, when the housing 20a of the actuator 20 is fixed to the valve body 1 via the heat insulating plate 32 using mounting parts such as bolts, the shaft assembly is connected via the bush 17 A certain cylinder 13 and holding body 14 are pressed, and the valve seat 6 is also fixed to the valve body 1. Therefore, in the present embodiment, when the installation of the actuator 20 is completed, the axial center o of the needle 7 and the axial center o of the valve seat 6 are in agreement.

  In the needle 7, the tip 19 a of the output shaft 19 of the direct acting electric motor 18 presses the end of the shaft portion 8 of the needle 7 via the bearing 30. Further, the needle 7 always presses the bearing 30 by the urging force of the spring 15. That is, the up-and-down movement of the needle 7 can immediately follow the driving of the direct acting electric motor 18, and the opening degree of the valve can be accurately controlled.

  As shown in FIG. 3, the O-ring 9 attached to the outer peripheral groove 10 of the needle 7 has an annular inclined surface 6a of the valve seat 6 when the valve 7 closes when the lower surface of the flange 7b contacts the upper surface of the valve seat 6. The channel can be liquid-tightly closed by being crushed against the liquid. The O-ring 9 is in surface contact with the flat inclined surface 6a, and can close the flow path without contacting the reduced diameter portion 6c that is a corner. The O-ring 9 is formed of a carbon fiber composite material including carbon nanofibers in an elastomer. By using a carbon fiber composite material including carbon nanofibers, the rigidity of the O-ring 9 can be improved, and even if the crushing rate of the O-ring 9 is small, excellent sealing properties can be obtained. The crushing rate of the O-ring using the carbon fiber composite material can be set to 11% or less, for example. Thus, since the crushing rate of the O-ring 9 can be reduced, an excellent minute flow rate control characteristic at the moment when the O-ring 9 is separated from and contacting the inclined surface 6a of the valve seat 6 can be obtained. More specifically, by using the highly rigid O-ring 9, a minute flow rate immediately after the O-ring 9 is separated from the valve seat 6 during the valve opening operation, and the O-ring 9 to the valve seat 6 during the valve closing operation. The difference from the minute flow rate immediately before contact can be reduced.

In the present embodiment, the inclination angle of the inclined surface 6a is set to about 45 degrees. Thereby, the crushing rate of the O-ring 9 of the needle valve V is set to 11% or less when the valve is closed. Specifically, the crushing rate of the O-ring 9 can be greater than 3% and 11% or less. Also, if the crushing rate of the O-ring 9 is greater than 3%, minute fluid leakage can be reliably prevented when the valve is closed, and if it is 11% or less, minute flow control can be performed with almost no decrease in the life of the O-ring. is there. In particular, the crushing rate of the O-ring can be 8% or more and 10% or less. In the present invention, the inclination angle of the inclined surface 6a is the angle of the inclined surface 6a with respect to the virtual plane c orthogonal to the axis o of the shaft portion 8 of the needle 7, and the crushing rate (k) is shown in FIG. As shown in the formula (1), the wire diameter before compression, that is, when the valve is opened, is a, and the wire diameter after compression, that is, when the valve is closed, is b.
k = 100 × (ab) / a (1)

  By using a seal member having excellent perfluoropolyether resistance for such a needle valve, it is possible to obtain a valve having a stable flow rate controllability over a long period of time due to perfluoropolyether. it can.

  Further, when the stress at 50% elongation and the storage elastic modulus at 25 ° C. of the carbon fiber composite material used for the O-ring 9 as the sealing member are increased, the micro flow rate control characteristics in the needle valve V tend to be improved.

  The O-ring 9 can have a stress at 50% elongation of 7.0 MPa or more. The stress at the time of 50% elongation of the O-ring 9 is obtained by performing a tensile test on the crosslinked carbon fiber composite material. Specifically, the stress can be 7.0 MPa or more and 30.0 MPa or less. By using an O-ring 9 with a stress at 50% elongation of 7.0 MPa or more, the micro flow characteristics of the needle valve V are improved, and if the stress at 50% elongation is 30.0 MPa or less, the moldability is impaired. The O-ring 9 having high rigidity can be obtained without bringing In particular, the O-ring 9 can have a stress at 50% elongation of 8.0 MPa or more and 22.0 MPa or less.

  The O-ring 9 can have a storage elastic modulus at 25 ° C. of 60 MPa or more. The storage elastic modulus at 25 ° C. of the O-ring 9 is obtained by performing a storage viscoelasticity test on a crosslinked carbon fiber composite material, and can be specifically set to 60 MPa or more and 250 MPa or less. By using an O-ring 9 having a storage elastic modulus of 60 MPa or more at 25 ° C., the minute flow characteristics of the needle valve V are improved, and if it is 250 MPa or less, the O-ring has a high rigidity without affecting the moldability. 9 can be obtained. In particular, the O-ring 9 can be 70 MPa or more and 200 MPa or less.

  Further, the O-ring 9 can have a compression set of 10.0% or less measured under conditions of a compression rate of 25%, 175 ° C., and 22 hours based on JIS K6262. Although the compression set of the O-ring 9 tends to increase by adding carbon nanofibers, the compression set of the O-ring 9 can be reduced by using carbon nanofibers having a low bulk density. The O-ring 9 using the O-ring 9 having a small compression set can obtain a long-term stable flow rate controllability in the needle valve V. The compression set of the O-ring 9 is obtained by subjecting a crosslinked carbon fiber composite material to a compression set test. Specifically, the compression set can be 1.0% or more and 10.0% or less. By using an O-ring 9 having a compression set of 1.0% or more and 10.0% or less, a long-term stable flow rate characteristic in the needle valve V can be obtained. Further, the O-ring 9 can be 1.0% or more and 9.0% or less, and in particular, the O-ring 9 can be 1.0% or more and 7.0% or less.

  Next, a method for evaluating a valve according to an embodiment of the present invention will be described.

  First, the valve evaluation method includes a first flow characteristic curve composed of a Cv value with respect to a valve opening degree (%) in the valve opening operation, and a second flow characteristic Cv value with respect to the valve opening degree (%) in the valve closing operation. And a flow rate characteristic curve. Next, the closure formed between the measured first flow characteristic curve and the second flow characteristic curve, particularly between the first flow characteristic curve and the second flow characteristic curve at a minute opening of the valve. The area of the obtained area is calculated as a flow rate control index, and the controllability of the flow rate is evaluated by the flow rate control index.

  The opening degree of the valve represents, for example, the interval between the needle 7 and the valve seat 6 in FIGS. 2 and 3, and the opening degree of the valve is 0% when the bottom surface of the flange 7 b is in contact with the upper surface of the valve seat 6. Yes, the position where the needle 7 is farthest from the valve seat 6 after the valve is opened is the valve opening degree 100%. Therefore, since there is an O-ring 9 between the needle 7 and the valve seat 6, the amount of crushing of the O-ring 9 is slightly larger than 0% even when the needle 7 is raised, that is, the valve opening degree is slightly larger than 0%. However, no flow path is formed and no fluid flows. The Cv value is a so-called valve capacity coefficient and is an index representing the capacity of the valve. The Cv value at the opening of a certain valve can be expressed as a value expressed in US gallons of the amount of water flowing at 60 ° F. per minute while maintaining the differential pressure before and after (1 psi).

  The minute opening of the valve is a certain range of the opening of the valve set for evaluating the controllability of the valve at a minute flow rate. The minute opening of the valve can be set as appropriate depending on the size and type of the valve, but the opening of the valve can be in the range of 0% to 10%, and the opening of the valve is 0% to 5. It can be in the range of 0%, in particular the valve opening can be in the range of 0% to 3.5%. The minute opening of the valve is a valve opening range in which different characteristics of the plurality of flow characteristic curves appear prominently when a plurality of flow characteristic curves are measured using a plurality of types of seal members in a predetermined valve. can do.

  Further, the minute opening degree of the valve can also be expressed by a crushing rate of the O-ring 9. For example, when the opening degree of the valve is converted into a crushing rate, in a valve opening range corresponding to a crushing rate of 0% to 50%. It can be estimated that the characteristics of the flow rate characteristic curve at a minute flow rate appear prominently. The general O-ring squashing rate for industrial applications is 8% to 30%. For example, when the squashing rate of the O-ring (maximum squashing rate when the valve is closed) is 30%, the X-axis is The crushing rate can be represented by a crushing rate corresponding to 0% to 20% (a total crushing rate corresponding to 0% to 50%) in addition to a crushing rate of 30% to 0%. The crushing rate corresponding to 0% to 20% is the distance corresponding to the crushing rate of 0% to 20% (that is, until the O-ring is reduced from 0% to 20%). This means that the distance is crushed. Actually, when the crushing rate exceeds 0%, the O-ring is separated from the valve seat and is not crushed. Therefore, it can be explained as a distance corresponding to the crushing rate of the O-ring. Therefore, in this case, assuming that the o-ring crushing rate is 1% and the valve opening is 0.1%, the crushing rate is 30%, the valve opening is 0%, and the crushing rate is 0%. The degree of opening is 3.0% and the degree of crushing is equivalent to 20%. Since the characteristics of the flow characteristic curve appear before and after the crushing rate is 0%, by setting the X axis to a crushing rate of 0% to 50% or equivalent, the crushing rate of a general O-ring for industrial use can be reduced to 8% to 30%. Even when designed, the flow control index can be measured.

  The flow control index is, for example, measuring the area of the closed region formed between the first flow characteristic curve and the second flow characteristic curve printed on the same size. Can be obtained at Specific measurement methods will be described in Examples 3, 11 to 14 and Comparative Examples 1 and 4 described later. The controllability of the flow rate in the valve is evaluated by comparing the flow rate control indexes thus measured. If the flow rate control index is small, the first flow rate characteristic curve and the second flow rate characteristic curve are close to each other, and the flow rate can be controlled in the same way during the valve opening operation and during the valve closing operation. Since it shows, it can be evaluated that it is the valve | bulb which is excellent in controllability of a micro flow rate.

  In addition, the valve evaluation method is the calculation of the flow rate control index of a valve equipped with an O-ring 9 as a sealing material before immersion in a perfluoropolyether at 130 ° C. for 103 hours as the first flow rate control index. The flow rate control index of the valve equipped with the O-ring 9 as the sealing material after the liquid resistance test is calculated as the second flow rate control index, and the difference between the first flow rate control index and the second flow rate control index By evaluating the controllability of the flow rate, it is possible to evaluate that the valve has excellent liquid resistance.

  Although one embodiment of the present invention has been described in detail as described above, those skilled in the art will readily understand that many modifications are possible without departing from the novel matters and effects of the present invention. . Accordingly, all such modifications are intended to be included in the scope of the present invention. In the present embodiment and the following examples, the O-ring is used as a seal member and the use for attaching to the needle of the needle valve has been described. However, the present invention is not limited to this, and other seal members for semiconductor manufacturing apparatuses may be used. It can also be applied to a shape, for example, an annular gasket.

  Examples of the present invention will be described below, but the present invention is not limited thereto.

(1) Preparation of sample Ternary fluorine-containing elastomers (shown as “FKM-1,” “FKM-2,” “FKM-3” in Tables 1 to 3) are put into a closed kneader Brabender. After mastication, a predetermined amount of carbon nanofibers (shown as “CNT-1”, “CNT-2”, “CNT-3”, “CNT-4” in Tables 1 to 3) shown in Tables 1 to 3) and Carbon black (shown as “MT” in Tables 1 to 3) was put into a ternary fluorine-containing elastomer and kneaded at a chamber temperature of 150 ° C. to 200 ° C., and then removed from the roll by performing a first kneading step. Further, the mixture was wound around an open roll (roll temperature: 10 ° C. to 20 ° C., roll interval: 0.3 mm), and thinning was repeated 5 times. At this time, the surface speed ratio of the two rolls was set to 1.1. Further, the rubber composition obtained through thinning was set by setting the roll gap to 1.1 mm and dispensed. The dispensed sheet was compression molded at 120 ° C. for 2 minutes to obtain an uncrosslinked carbon fiber composite material having a thickness of 1 mm. Furthermore, the amount of peroxide (shown as “PO” in Tables 1 to 3) and triallyl isocyanurate (Table 1) shown in Tables 1 to 3 were applied to an uncrosslinked carbon fiber composite material obtained through thinning. -3, indicated by "TAIC"), zinc oxide (shown by "ZnO" in Tables 1-3), and a plasticizer added to the sheet, and press vulcanized (170 ° C / 10 minutes), secondary Molded by vulcanization (200 ° C./24 hours) to obtain sheet-like crosslinked carbon fiber composite materials (Examples 1 to 10 and Comparative Examples 2 to 3) having a thickness of 1 mm. Comparative Example 1 is a rubber composition equivalent to a conventional O-ring whose specific formulation is unknown.

In Tables 1 to 3, “FKM-1” is a ternary FKM having a fluorine content of 66 mass%, a Mooney viscosity (ML _{1 + 10} 121 ° C.) of 53, and a specific gravity of 1.83 g / cm ³ . “FKM-2” is a ternary FKM having a fluorine content of 64 mass%, a Mooney viscosity (ML _{1 + 10} 121 ° C.) of 54, a specific gravity of 1.78 g / cm ³ , and “FKM-3”. Was a ternary FKM with a fluorine content of 64% by weight, a Mooney viscosity (ML _{1 + 10} 100 ° C.) of 65 and a specific gravity of 1.79 g / cm ³ . In Tables 1 to 3, “MT” was MT grade carbon black having an arithmetic average diameter of about 200 nm. In Tables 1 to 3, “CNT-1” is an average diameter of 15 nm, a frequency maximum diameter of 18 nm, a stiffness index of 4.8, a Raman peak ratio (D / G) of 1 produced by a catalyst reaction method (Substrate Reaction Method). 0.7, a multi-layer carbon nanofiber having a nitrogen adsorption specific surface area of 260 m ² / g, “CNT-2” is a multi-layer carbon nanofiber having an average diameter of 15.3 nm and a stiffness index of 4.4, “CNT-3” Is a multilayer carbon nanofiber having an average diameter of 18.6 nm, a stiffness index of 3.1, and a bulk density of 130 to 150 kg / m ³ , and “CNT-4” has an average diameter of 18.6 nm, a stiffness index of 3.1, a bulk It was a multi-layer carbon nanofiber having a density of 45 to 95 kg / m ³ .

(2) Measurement of normal physical properties, storage elastic modulus, etc. As normal physical properties, about the crosslinked carbon fiber composite materials of Examples 1 to 10 and Comparative Examples 1 to 3, hardness at room temperature, tensile strength, elongation at break, 50% And 100% modulus and fracture energy were measured.

Rubber hardness (shown as “Hs (JIS-A)” in Tables 1 to 3) was measured based on JIS K 6253.

  Tensile strength (shown as “TS (MPa)” in Tables 1 to 3), elongation at break (shown as “Eb (%)” in Tables 1 to 3), stress at 50% elongation (Table 1) -3, indicated by "σ50 (MPa)"), stress at 100% elongation (shown as "σ100 (MPa)" in Tables 1-3) and fracture energy (in Tables 1-3, "Fracture E"). (J) ”is a test piece cut into a JIS No. 3 or No. 6 dumbbell shape, using a tensile tester manufactured by Shimadzu Corporation, 23 ± 2 ° C., and a tensile speed of 500 mm / min. Then, a tensile test was performed based on JIS K6251. “Σ50” and “σ100” may be referred to as “50% modulus (M50)” and “100% modulus (M100)”.

  About Examples 1-10 and Comparative Examples 1-3, the storage elastic modulus in 25 degreeC of measurement temperature was measured. The storage elastic modulus (shown as “E ′ (25 ° C.) (MPa)” in Tables 1 to 3)) is a test piece cut into a strip (40 × 1 × 2 (width) mm) manufactured by SII. Using a dynamic viscoelasticity tester DMS6100, the distance between chucks was 20 mm, the measurement temperature was −100 to 300 ° C., the dynamic strain was ± 0.05%, the frequency was 1 Hz, and the dynamic viscoelasticity test was performed based on JIS K6394. .

  About Examples 1-10 and Comparative Examples 1-3, based on JISK6262, a compression set test was performed on the conditions of compression rate 25%, 175 degreeC, and 22 hours, compression set (in Table 1-3, "CS (%) ”).

  According to Examples 1-10 from Tables 1-3, compared with the comparative example 1 of a conventional product, the stress at the time of 50% elongation improved and it was 8.1MPa-10.4MPa. Moreover, according to Examples 1-10, compared with Comparative Examples 2 and 3, the compression set was small and was 4.8% to 10.6%. According to Examples 1 to 10, the storage elastic modulus was 42 MPa to 112 MPa.

(3) Measurement of flow characteristics of needle valve O-rings were prepared using the carbon fiber composite materials of Examples 1 to 10 and Comparative Examples 1 to 3 prepared in (1) above. The nominal dimensions of the O-ring were an inner diameter of 4.5 mm and a wire diameter of 1 mm. 1 to 4 and the electric proportional control needle valve (size 1 / 2B) manufactured by KITZ Corporation in which the O-rings of Examples 1 to 10 and Comparative Examples 1 to 3 are assembled, the valve opening degree is 0% to 100%. Cv value in% was measured. The angle of the inclined surface 6a of the valve seat 6 of the needle valve V of the embodiment shown in FIGS. The crushing rate of the O-ring was 9.0%. Tap water was used as the fluid.

  In Comparative Example 1, a Cv value was measured by assembling a conventional O-ring to the needle valve shown in FIGS. As a result, FIG. 5 shows a flow rate characteristic graph of the Cv value with respect to the valve opening 0 to 7% showing the minute flow rate characteristic. In FIG. 5, the curve indicated by reference numeral 50 is a flow rate characteristic when the needle 7 from the valve closed state (opening degree 0%) to the valve opening state (opening degree 7%) is raised from the valve seat 6. A curve indicated by 51 is a flow rate characteristic when the needle 7 from the valve open state (opening degree 7%) to the valve closing state (opening degree 0%) is lowered to the valve seat 6. In FIG. 5, the flow characteristic graph of Comparative Example 1 shows that the valve opening is 1.0% to 3.5%, the interval between the curve 50 and the curve 51 is wide, and the area closed by the hysteresis loop is large. Therefore, it was found that there was a large difference between the minute flow rate during valve opening operation and the minute flow rate during valve closing operation, and it was not possible to control accurately.

  The C-value was measured by assembling the O-ring of Example 3 to the needle valve shown in FIGS. As a result, FIG. 6 shows a flow characteristic graph of the Cv value with respect to the valve opening degree of 0 to 7% showing a minute flow characteristic. In FIG. 6, the curve indicated by reference numeral 57 is a flow rate characteristic when the needle 7 from the valve closed state (opening degree 0%) to the valve opening state (opening degree 7%) is raised from the valve seat 6. A curve indicated by 58 is a flow rate characteristic when the needle 7 from the valve opening state (opening degree 7%) to the valve closing state (opening degree 0%) is lowered to the valve seat 6.

  Although not shown here, similarly to Example 3 and Comparative Example 1, flow characteristic graphs were obtained for the O-rings of Examples 1-2, 4-10, and Comparative Examples 2-3. As in Example 3, the O-rings of Examples 1-2, 4 and 10 have a narrow interval between the valve opening curve and the valve closing curve, and the area closed by the hysteresis loop is small. It was found that the difference between the minute flow rate during valve operation and the minute flow rate during valve closing operation was small, and the control was accurate. Furthermore, when the valve opening is between 2.0% and 5.0%, the slopes of the curves 57 to 68 are substantially constant, and the flow rate is controlled approximately in proportion to the valve opening. It was shown that the proportional controllability at a minute flow rate is excellent. Further, it was found that Comparative Examples 2 to 3 were also excellent in controllability at a minute flow rate as compared with Comparative Example 1.

(4) Liquid resistance test As a liquid resistance test (shown as "PFPE test" in Tables 4 to 6), the carbon fiber composite materials of Examples 1 to 10 and Comparative Examples 1 to 3 were perfluorocarbon at 130 ° C. With respect to the carbon fiber composite material after being immersed in polyether (> 99.9% [W / W]) for 103 hours, hardness, tensile strength, elongation at break, 50% and 100 under the same conditions as in (2) above. The% modulus was measured. The measurement results are shown in Tables 4-6.

  Moreover, the difference of each measurement result in Tables 4-6 with respect to each measurement result in Tables 1-3 was calculated, and shown in Tables 4-6 as ΔHs, ΔTS, ΔEb, Δσ50, Δσ100. Further, volume changes of the carbon fiber composite materials of Examples 1 to 10 and Comparative Examples 1 to 3 after the liquid resistance test on the carbon fiber composite materials of Examples 1 to 10 and Comparative Examples 1 to 3 before the liquid resistance test. (Shown as “ΔV” in Tables 4-6) and mass change (shown as “ΔW” in Tables 4-6) were measured and shown in Tables 4-6.

  From Tables 4-6, the stress at the time of 50% elongation of the carbon fiber composite materials of Examples 1-10 after the liquid resistance test was 8.0 MPa or more. In addition, the carbon fiber composite materials of Examples 1 to 10 had a volume change rate of 2.5% or less before and after the liquid resistance test. The carbon fiber composite materials of Examples 1 to 10 had a mass change rate of 3.2% or less before and after the liquid resistance test. On the other hand, the carbon fiber composite material of Comparative Example 2-3 using FKM-1 having a fluorine content of 66% by mass had a volume change rate of 7.0% or more before and after the liquid resistance test, and the mass change The rate was 8.0% or more. In the carbon fiber composite materials of Examples 1 to 10, the rate of change in stress at 50% elongation before and after the liquid resistance test was within ± 6.5%. In the carbon fiber composite materials of Examples 1, 3, 4, 6, and 8, the rate of change in stress at 50% elongation was not negative before and after the liquid resistance test. The carbon fiber composite materials of Examples 1 to 10 were not easily deteriorated by the liquid resistance test, and were excellent in minute flow rate controllability when mounted on the valve as an O-ring.

(5) Change in flow rate characteristics of needle valve by liquid resistance test First, carbon fiber composite materials of Examples 11 to 14 and Comparative Example 4 were prepared in the same manner as in (1) above with the formulation shown in Table 7. The carbon fiber composite materials of Examples 11 to 14 and Comparative Example 4 were measured for room temperature hardness, tensile strength, elongation at break, 50% and 100% modulus and fracture energy in the same manner as in (2) above. The measurement results are shown in Table 7. In Table 7, “CNT-5” was a multilayer carbon nanofiber having an average diameter of 12.8 nm, a bulk density of 70 to 110 kg / m ³ , and a stiffness index of 4.7.

  The carbon fiber composite materials of Examples 11 to 14 and Comparative Example 4 were subjected to a liquid resistance test (shown as “PFPE test” in Table 8) in the same manner as in the above (4), and the hardness, tensile strength, elongation at break , 50% and 100% modulus were measured. Table 8 shows ΔHs, ΔTS, ΔEb, Δσ50, and Δσ100 calculated in the same manner as in (4). Further, as in (4) above, the volume change (shown as “ΔV” in Table 8) and mass change (shown as “ΔW” in Table 8) of the carbon fiber composite material before and after the liquid resistance test were measured. Table 8 shows the results.

  O-rings were produced using the carbon fiber composite materials of Examples 3, 11 to 14 and Comparative Examples 1 and 4.

  Using the O-rings of Examples 3 and 11 to 14 and Comparative Examples 1 and 4, the flow characteristics of the needle valve were measured. More specifically, first, an O-ring which has not been subjected to a liquid resistance test was assembled with an electric proportional control needle valve (size 1 / 2B) manufactured by KITZ Corporation shown in FIGS. 1 to 4, and the Cv value was measured. . In addition, a liquid resistance test was performed on the O-rings of the same composition and the same lot as those of the O-rings, and then assembled to the needle valve to measure the Cv value. For the needle valve assembled with each O-ring, the Cv value when the valve opening degree is 0% to 100% is measured, and the Cv value when the opening degree is 0% to 5.0% is enlarged to FIG. Indicated. 7 to 13, the curve indicated by a broken line is a flow characteristic curve of a needle valve assembled with an O-ring not subjected to a liquid resistance test, and the curve indicated by a solid line is after the liquid resistance test is performed. 5 is a flow characteristic curve of a needle valve using an O-ring.

  In the liquid resistance test (shown as “PFPE test” in Table 9), the O-ring was subjected to a perfluoropolyether (> 99.9% [W / W]) at 130 ° C. for 103 hours as in the above (4). Soaked. The angle of the inclined surface 6a of the valve seat 6 of the needle valve V was 45 degrees. The crushing rate of the O-ring was 9.0%. Tap water was used as the fluid. “Opening%” is the interval between the needle 7 and the valve seat 6, that is, the stroke of the needle 7. Therefore, the opening degree of the needle 7 seated on the valve seat 6 is 0%, and the position (upper limit position) where the needle 7 is farthest from the valve seat 6 is 100% opening degree. In an ideal situation where the volume change rate or mass change rate of the seal member is 4.0% or less, water begins to flow when the valve is opened in the range of 0.5% to 2.0%. It can be assumed that the water stops when the valve is closed. Therefore, it can be predicted that the minute flow rate is affected by the material of the O-ring, etc., that the opening degree of the valve is approximately 0% to 3.0%, and considering the mechanical influence described later, the valve It can be estimated that the flow rate controllability of the valve can be evaluated by graphing the flow rate characteristic curve in the range of 0% to 5.0%.

  FIG. 7 is a flow characteristic graph using the O-ring of Comparative Example 1. A broken line curve indicated by reference numeral 60o is a first flow characteristic curve from the valve closed state (opening degree 0%) to the valve opening state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 60s indicates a second curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. Although the flow characteristic graph of Comparative Example 1 is also shown in FIG. 5, another O-ring having the same composition was prepared and attached to a new needle valve. The result of the experiment is shown again in FIG. A solid curve indicated by reference numeral 62o indicates the first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and the broken line curve indicated by reference numeral 62s is the first curve from the open state (opening degree of 5.0%) to the closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG. In FIGS. 5 and 7, there is an error of about 1.3% in terms of opening.

  FIG. 8 is a flow characteristic graph using the O-ring of Comparative Example 4. A broken line curve indicated by reference numeral 64o is a first flow characteristic curve from the valve closed state (opening degree 0%) to the valve opening state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 64s indicates a second curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. A solid curve indicated by reference numeral 66o indicates a first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and a broken line curve indicated by reference numeral 66s indicates the first curve from the valve open state (opening degree of 5.0%) to the valve closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

  FIG. 9 is a flow characteristic graph using the O-ring of Example 3. A broken line curve indicated by reference numeral 68o indicates a first flow characteristic curve from a closed state (opening degree 0%) to a opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 68s indicates a second curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. The flow rate characteristic graph of Example 3 is also shown in FIG. 6, and the results of experimenting with another O-ring having the same composition are shown in FIG. A solid curve indicated by reference numeral 70o indicates the first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and a broken line curve indicated by reference numeral 70s indicates a first curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

  FIG. 10 is a flow characteristic graph using the O-ring of Example 11. A broken line curve indicated by reference numeral 72o indicates a first flow characteristic curve from a closed state (opening degree 0%) to a opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 72s indicates a second curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. The solid curve indicated by reference numeral 74o indicates the first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and a broken line curve indicated by reference numeral 74s indicates the first curve from the valve open state (opening degree of 5.0%) to the valve closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

  FIG. 11 is a flow characteristic graph using the O-ring of Example 12. A broken line curve indicated by reference numeral 76o indicates a first flow characteristic curve from a closed state (opening degree 0%) to a opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 76s indicates a second curve from the valve open state (opening degree of 5.0%) to the valve closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. A solid curve indicated by reference numeral 78o indicates a first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and a broken line curve indicated by reference numeral 78s indicates the first curve from the valve opening state (opening degree 5.0%) to the valve closing state (opening degree 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

  FIG. 12 is a flow characteristic graph using the O-ring of Example 13. A broken line curve indicated by reference numeral 80o indicates a first flow characteristic curve from a closed state (opening degree 0%) to a opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 80s indicates a second curve from the open state (opening degree of 5.0%) to the closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. A solid curve indicated by reference numeral 82o indicates the first flow rate from the valve closing state (opening degree 0%) to the valve opening state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and a broken line curve indicated by reference numeral 82s indicates the first curve from the valve open state (opening degree of 5.0%) to the valve closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

  FIG. 13 is a flow characteristic graph using the O-ring of Example 14. A broken line curve indicated by reference numeral 84o indicates a first flow rate characteristic curve from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 84s indicates a second curve from the open state (opening degree of 5.0%) to the closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. The solid curve indicated by reference numeral 86o indicates the first flow rate from the closed state (opening degree 0%) to the open state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. It is a characteristic curve, and a broken line curve indicated by reference numeral 86s indicates the first curve from the valve opening state (opening degree 5.0%) to the valve closing state (opening degree 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

  7 to 13, the fine flow rate controllability in the needle valves in Examples 3 and 11 to 14 and Comparative Examples 1 and 4 is 0% to 5.0%. %), The characteristics of each flow characteristic curve appeared. Specifically, referring to each graph, there was a tendency that the increase in the Cv value became remarkable from the vicinity of the opening degree of 4.5%. The needle valve of the specimen has a slight variation in its flow characteristics due to the influence of processing tolerances of components. Therefore, depending on the sample, the opening at which the increase in Cv value is noticeable may be around 5.0%. Therefore, in Examples 3, 11 to 14 and Comparative Examples 1 and 4, the first flow rate characteristic at the time of valve opening operation at a valve opening degree (%) of 0% to 5.0% as a minute opening degree of the valve. Judgment was made based on the size of the area of the closed region formed between the curve and the second flow characteristic curve during the valve closing operation. The area of the closed region is a region inside a so-called hysteresis loop formed so as to surround the first flow rate characteristic curve and the second flow rate characteristic curve by drawing different trajectories. When there were a plurality of such hysteresis loops, the total area of the plurality of regions was measured.

  7 (Comparative Example 1) and FIG. 8 (Comparative Example 4) are formed by the first and second flow characteristic curves 60o, 60s, 64o and 64s shown by broken lines in the opening degree of the valve from 0% to 5.0%. The area of the closed region is the first and second flow characteristic curves shown by broken lines at the valve opening of 0% to 5.0% in FIGS. 9 (Example 3) to FIG. 13 (Example 14). It is clearly larger than the area of the region closed by the hysteresis formed by 68o, 68s to 84o, 84s, and the difference between the micro flow rate during the valve opening operation and the micro flow rate during the valve closing operation is large, and accurate control is possible. I knew it was n’t done.

  Next, the area formed by the broken first and second flow characteristic curves 60o, 60s to 84o, 84s shown in FIGS. 7 to 13 and the first and second flow characteristic curves 62o shown by solid lines. , 62s to 86o, and the area formed by 86s, a decrease in controllability of the minute flow rate by the liquid resistance test was judged. That is, the area formed by the first and second flow rate characteristic curves 60o, 60s to 84o, 84s indicated by broken lines and the area formed by the first and second flow rate characteristic curves 62o, 62s to 86o, 86s indicated by solid lines. If the difference is small, the deterioration of the O-ring due to the liquid resistance test is small and the controllability of the minute flow rate in the needle valve is not lowered.

  7 (Comparative Example 1) and FIG. 8 (Comparative Example 4) are formed by the broken first and second flow characteristic curves 60o, 60s, 64o, and 64s at the opening degree of 0% to 5.0%. The area formed by the first and second flow characteristic curves 62o, 62s, 66o, 66s of the solid line is compared with the area of the solid line using the O-ring after the liquid resistance test is performed. The areas of the first and second flow characteristic curves were larger.

  On the other hand, the area formed by the first and second flow characteristic curves 68o, 68s to 84o, 84s shown by the broken lines in FIG. 9 (Example 3) to FIG. 13 (Example 14), and the first solid line. When compared with the areas formed by the second flow characteristic curves 70o, 70s to 86o, 86s, there was almost no difference in the area by visual observation.

  Therefore, a flow rate control index was calculated based on the area formed by the flow rate characteristic curves shown in FIGS. 7 to 13, and the flow rate controllability at a minute flow rate was quantified. The flow control index is shown in Table 9. The flow rate control index includes the area formed by the first and second flow characteristic curves shown by the broken lines at the opening degrees 0% to 5.0% of the valves of FIGS. It was an area formed by the solid line first and second flow rate characteristic curves at the opening degree of 0% to 5.0%. In addition, the flow rate control index in Table 9 is the first and the second on the graph in which the valve opening 0% to 5.0% is 214 mm on the X axis and the Cv value 0.000 to 0.020 is 124 mm on the Y axis. The area when the flow rate characteristic curve of 2 was created was calculated.

The calculation method of the flow rate control index will be specifically described with reference to FIG. 10 (Example 11). A hysteresis loop is formed between 1.5% and 2.2% by the first flow characteristic curve 74o and the second flow characteristic curve 74s indicated by solid lines. Calculate the area closed by this hysteresis loop (mm ² ), and similarly calculate the area closed by other hysteresis loops between 0% and 5.0%, and add them together The flow control index was used.

  Further, due to the mechanical influence of the needle valve itself, for example, as shown in FIG. 7 (Comparative Example 1), the area closed by the flow characteristic curves 60o and 60s may not be accurately measured. The mechanical influence is, for example, the backlash, the non-linearity of the input current (4-20 mA) and the motor stroke (0 to about 10 mm) due to the limit of resolution, which the direct-current electric motor of the needle valve has. . The amount of increase in area due to the mechanical effect was calculated as the area of the mechanical hysteresis loop, and the area obtained by subtracting the area of the mechanical hysteresis loop from the area of the original hysteresis loop was defined as the flow control index (absolute value).

  A specific measurement method in the case where there is a mechanical influence is shown in FIG. FIG. 14 is a diagram illustrating a method for measuring the flow rate control index indicated by broken lines 60o and 60s in FIG. 7 (without the PFPE test of Comparative Example 1). First, the area surrounded by the first flow rate characteristic curve 60o and the second flow rate characteristic curve 60s was measured and described in the column of “Hysteresis loop area” in Table 9.

  Next, the second flow rate characteristic curve 60s is moved away from the first flow rate characteristic curve 60o and the second flow rate characteristic curve 60s so that the valve opening is 4.0% to 5.0%. A hypothetical second flow rate characteristic curve 60s ′ horizontally drawn to the first flow rate characteristic curve 60o by L is drawn. In the region where the valve opening exceeds 4.0%, particularly in the region where it exceeds 4.5%, the influence of the characteristics of the O-ring is reduced, so the first flow characteristic curve is the second flow characteristic curve. Since the flow rate characteristic curves should be almost the same, it can be estimated that there is a mechanical influence by this distance L. Therefore, the virtual second flow rate characteristic curve 60s' obtained by horizontally moving the second flow rate characteristic curve 60s to the first flow rate characteristic curve 60o by the distance L can eliminate the mechanical influence. The closed region N formed between the virtual second flow rate characteristic curve 60s ′ and the second flow rate characteristic curve 60s is a mechanical hysteresis loop. It was described in the “Area” column.

  Furthermore, the difference between the “area of the hysteresis loop” and the “area of the mechanical hysteresis loop” was calculated as a “flow control index” (absolute value) and listed in Table 9. The flow rate control index is a shaded area indicated by a symbol M in FIG. Thus, by removing the area of the mechanical hysteresis loop, it was possible to evaluate the area of the hysteresis loop in the minute opening region of 0% to 5.0% of the valve opening, that is, the flow rate control index.

  The flow rate control indexes of Comparative Example 4, Examples 3, and 11 to 14 were calculated in the same manner as the sample of Comparative Example 1 without the PFPE test, and are shown in Table 9. Except for Comparative Examples 1 and 3, in the example, as shown in FIGS. 9 to 13, even if the area is measured in the range of 0% to 3.5% of the valve opening, the flow rate control is performed. Although it could be evaluated by an index, the area was measured in the range of 0% to 5.0% for accurate comparison with the comparative example.

  According to Table 9, the flow rate control index of Examples 3, 11 to 14 is smaller than that of Comparative Examples 1 and 4, and the valve opening degree is 0% to 5.0%. It was found that the flow rate was accurately controlled at any time during the valve operation. In addition, the flow rate control indexes in Examples 3 and 11 to 14 do not change greatly even when the liquid resistance test is performed, the O-ring does not deteriorate, and even if the liquid resistance test is performed on the O-ring, it is stable and minute. It was found that the flow rate could be controlled.

  From the above results, according to this example, the flow rate control index of the valve equipped with the O-ring not subjected to the liquid resistance test was 20 or less. From this result, the flow rate control index of the valve equipped with the O-ring not subjected to the liquid resistance test in this embodiment can be 20 or less, and can be 10 or less. When the flow rate control index is within this range, the area of the hysteresis loop at the time of valve opening and closing is suppressed when the valve opening is small, in this embodiment, the valve opening is 0% to 5.0%. And the minute flow rate can be accurately controlled.

  Further, according to the present example, the flow rate control index of the valve equipped with the O-ring subjected to the liquid resistance test was 20 or less. From this result, the flow rate control index of the valve equipped with the O-ring subjected to the liquid resistance test in this embodiment can be 20 or less, and further can be 13 or less. When the flow rate control index is within this range, the area of the hysteresis loop at the time of valve opening and closing is suppressed when the valve opening is small, in this embodiment, the valve opening is 0% to 5.0%. And the minute flow rate can be accurately controlled.

  Furthermore, according to this example, the difference between the flow rate control index before the liquid resistance test and the flow rate control index after the liquid resistance test was 12 or less. From this result, the difference between the flow rate control index before the liquid resistance test and the flow rate control index after the liquid resistance test in this embodiment can be within 12 and further within 9. When the difference in the flow rate control index is within this range, even when the liquid resistance test is performed, there is little deterioration of the O-ring, and the minute flow rate can be accurately controlled before and after the liquid resistance test.

V Needle valve, 1 valve body, 2 inlet, 3 outlet, 4 valve chamber, 5 shaft hole, 6
Valve seat, 7 needle, 8 shaft, 9 O-ring, 10 outer peripheral groove, 11 O-ring, 12
Mounting groove, 13 cylinder, 14 holding body, 15 spring, 16 engagement piece, 17 bush, 18 direct acting electric motor, 19 output shaft, 20 actuator, 21 seal ring, 23 needle unit, 30 bearing, 31 guide body , 32 Insulation plate, 33 Dust seal, 60o, 64o, 68o, 72o, 76o, 80o, 84o First flow characteristic curve using O-ring not subjected to liquid resistance test, 60s, 64s, 68s, 72s, 76s 80s, 84s Second flow characteristic curve using an O-ring not subjected to liquid resistance test, 62o, 66o, 70o, 74o, 78o, 82o, 86o First using an O-ring subjected to liquid resistance test Flow rate characteristic curve, 62s, 66s, 70s, 74s, 78s, 82s, 86s 2nd using O-ring not liquid resistance test Flow rate characteristic curve, 60s' virtual second flow characteristic, o central axis, an imaginary plane perpendicular to the c central axis o, L a distance, M region, N region

The present invention relates to excellent sealing member resistant to fluorine-based fluid properties.

An object of the present invention is to provide a superior seal member resistant to fluorine-based fluid properties.

FIG. 7 is a flow characteristic graph using the O-ring of Comparative Example 1. A broken line curve indicated by reference numeral 60o is a first flow characteristic curve from the valve closed state (opening degree 0%) to the valve opening state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 60s indicates a second curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. Although the flow characteristic graph of Comparative Example 1 is also shown in FIG. 5, another O-ring having the same composition was prepared and attached to a new needle valve. The result of the experiment is shown again in FIG. A solid curve indicated by reference numeral 62o indicates the first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and the solid curve indicated by reference numeral 62s is the first curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG. In FIGS. 5 and 7, there is an error of about 1.3% in terms of opening.

FIG. 8 is a flow characteristic graph using the O-ring of Comparative Example 4. A broken line curve indicated by reference numeral 64o is a first flow characteristic curve from the valve closed state (opening degree 0%) to the valve opening state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 64s indicates a second curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. A solid curve indicated by reference numeral 66o indicates a first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and the solid curve indicated by reference numeral 66s is the first curve from the valve open state (opening degree 5.0%) to the valve closed state (opening degree 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

FIG. 9 is a flow characteristic graph using the O-ring of Example 3. A broken line curve indicated by reference numeral 68o indicates a first flow characteristic curve from a closed state (opening degree 0%) to a opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 68s indicates a second curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. The flow rate characteristic graph of Example 3 is also shown in FIG. 6, and the results of experimenting with another O-ring having the same composition are shown in FIG. A solid curve indicated by reference numeral 70o indicates the first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and a solid curve indicated by reference numeral 70s indicates the first curve from the valve open state (opening degree of 5.0%) to the valve closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

FIG. 10 is a flow characteristic graph using the O-ring of Example 11. A broken line curve indicated by reference numeral 72o indicates a first flow characteristic curve from a closed state (opening degree 0%) to a opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 72s indicates a second curve from the valve opening state (opening degree of 5.0%) to the valve closing state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. The solid curve indicated by reference numeral 74o indicates the first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and the solid curve indicated by reference numeral 74s indicates the first curve from the valve open state (opening degree 5.0%) to the valve closed state (opening degree 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

FIG. 11 is a flow characteristic graph using the O-ring of Example 12. A broken line curve indicated by reference numeral 76o indicates a first flow characteristic curve from a closed state (opening degree 0%) to a opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 76s indicates a second curve from the valve open state (opening degree of 5.0%) to the valve closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. A solid curve indicated by reference numeral 78o indicates a first flow rate from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and the solid curve indicated by reference numeral 78s indicates the first curve from the valve open state (opening 5.0%) to the valve closed state (opening 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

FIG. 12 is a flow characteristic graph using the O-ring of Example 13. A broken line curve indicated by reference numeral 80o indicates a first flow characteristic curve from a closed state (opening degree 0%) to a opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 80s indicates a second curve from the open state (opening degree of 5.0%) to the closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. A solid curve indicated by reference numeral 82o indicates the first flow rate from the valve closing state (opening degree 0%) to the valve opening state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and the solid curve indicated by reference numeral 82 s is the first curve from the valve open state (opening 5.0%) to the valve closed state (opening 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

FIG. 13 is a flow characteristic graph using the O-ring of Example 14. A broken line curve indicated by reference numeral 84o indicates a first flow rate characteristic curve from the closed state (opening degree 0%) to the opened state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. A broken line curve indicated by reference numeral 84s indicates a second curve from the open state (opening degree of 5.0%) to the closed state (opening degree of 0%) when the needle 7 is lowered to the valve seat 6. It is a flow characteristic curve. The solid curve indicated by reference numeral 86o indicates the first flow rate from the closed state (opening degree 0%) to the open state (opening degree 5.0%) when the needle 7 is lifted from the valve seat 6. This is a characteristic curve, and the solid curve indicated by reference numeral 86s indicates the first curve from the valve open state (opening 5.0%) to the valve closed state (opening 0%) when the needle 7 is lowered to the valve seat 6. 2 is a flow rate characteristic curve of FIG.

Claims (7)

For 100 parts by mass of a ternary fluorine-containing elastomer having a fluorine content of 65% by mass or less, 5 to 25 parts by mass of carbon nanofibers, and 10 to 40 parts by mass of carbon black,
The stress at 50% elongation after a liquid resistance test immersed in perfluoropolyether at 130 ° C. (> 99.9% [W / W]) for 103 hours is 8 MPa or more,
A seal member having a volume change rate of 4.0% or less before and after the liquid resistance test. In claim 1,
A sealing member having a mass change rate of 4.0% or less before and after the liquid resistance test. In claim 1 or 2,
A sealing member having a rate of change in stress at 50% elongation within ± 7.0% before and after the liquid resistance test. In any one of Claims 1-3,
A sealing member in which the rate of change in stress at 50% elongation is not negative before and after the liquid resistance test.   The valve | bulb using the sealing member as described in any one of Claims 1-4. A valve evaluation method for controlling the flow rate of fluid by moving a valve attached to a seal member forward and backward relative to a valve seat,
A first flow characteristic curve composed of a Cv value with respect to the opening degree (%) of the valve in the valve opening operation; a second flow characteristic curve composed of a Cv value with respect to the opening degree (%) of the valve in the valve closing operation; Measure and
Calculating the area of the closed region formed between the first flow characteristic curve and the second flow characteristic curve at the minute opening of the valve as a flow control index;
A method for evaluating a valve, wherein flow rate controllability is evaluated by the flow rate control index. In claim 6,
The flow rate control index of the valve equipped with the seal member before the liquid resistance test immersed in perfluoropolyether (> 99.9% [W / W]) at 130 ° C. for 103 hours is calculated as the first flow rate control index. And
Calculating the flow rate control index of the valve equipped with the seal member after the liquid resistance test as a second flow rate control index;
A valve evaluation method for evaluating a controllability of a flow rate based on a difference between the first flow rate control index and the second flow rate control index.