WO2019093142A1 - Lubrication system and liquid agent set for lubrication system - Google Patents
Lubrication system and liquid agent set for lubrication system Download PDFInfo
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- WO2019093142A1 WO2019093142A1 PCT/JP2018/039647 JP2018039647W WO2019093142A1 WO 2019093142 A1 WO2019093142 A1 WO 2019093142A1 JP 2018039647 W JP2018039647 W JP 2018039647W WO 2019093142 A1 WO2019093142 A1 WO 2019093142A1
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M173/00—Lubricating compositions containing more than 10% water
- C10M173/02—Lubricating compositions containing more than 10% water not containing mineral or fatty oils
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M125/00—Lubricating compositions characterised by the additive being an inorganic material
- C10M125/02—Carbon; Graphite
Definitions
- the present invention relates to a lubrication system and a liquid agent set for the lubrication system.
- This application claims the priority based on Japanese Patent Application No. 2017-216443 which is a Japanese application dated November 9, 2017, and uses all the contents described in these applications.
- DLC films Since hard carbon (diamond like carbon; DLC) films have high hardness and chemical stability, their application to the surface (sliding surface) of a sliding member is expected.
- the use of the DLC film as the sliding surface as described above is described, for example, in Patent Document 1 below.
- the DLC film is a material which is chemically stable and high in hardness, but is disadvantageous for forming a surface with low friction and low wear. There is a need for a technique for forming a low friction and low wear surface on a sliding surface using a DLC film, and for reducing friction and wear for a long time.
- the present invention has been conceived under the above circumstances, and provides a lubrication system suitable for achieving low friction and low wear on a DLC sliding surface, and a liquid agent set for the lubrication system. Do.
- a lubrication system is provided.
- This lubrication system is a low friction diamond-like carbon (DLC) slide using an initial conformant containing relatively high concentrations of nanodiamond particles (hereinafter sometimes referred to as "ND particles").
- ND particles initial conformant containing relatively high concentrations of nanodiamond particles
- a lubricant containing relatively low concentration of nanodiamond particles is used.
- the initial sliding-adjusting agent having a relatively high concentration of ND particles is first used to Low surface friction can be achieved (initial contact period). Then, a lubricant having a relatively low concentration of ND particles is used as a lubricant for lubricating the DLC sliding surface, whereby the lubricating system of the DLC sliding surface is established and maintained.
- ND particles and water in which carbon atoms are similarly arranged on the surface and are present at a relatively high concentration with respect to the DLC sliding surface on which carbon atoms are arranged on the surface It is thought that the wettability improvement and smoothing of the DLC sliding surface will advance at an early stage by the tribochemical reaction in the system where T and T act in a superimposed manner, and the DLC sliding surface tends to reduce the friction early.
- the present inventors have obtained the knowledge that During the period of use of the lubricant after the initial fitting period, the physical concentration of the ND particles on the DLC sliding surface is reduced because the concentration of the ND particles in the lubricant is relatively low.
- the lubrication system according to the first aspect of the present invention is suitable for achieving low friction and low wear on the DLC sliding surface.
- the ND particle concentration of the initial conformant is 0.01 to 2% by mass.
- the configuration is suitable for early formation of a surface having both smoothness and wettability by tribochemical reaction in a system in which ND particles are present on a DLC sliding surface.
- the ND particle concentration of the lubricant is preferably 0.001% by mass or less.
- the composition is suitable for maintaining the smoothness and wettability of the DLC sliding surface formed by the initial bonding agent, and reducing friction and wear on the sliding surface.
- the friction coefficient of the sliding surface measured in the following friction test is 0.05 or less, and the ball wear volume determined by the following wear amount calculation method after the friction test is 1.0 ⁇ 10 -4 mm It is preferable that it is 3 or less.
- Friction Test First, a disk with a diameter of 30 mm and a thickness of 4 mm having a DLC sliding surface formed by a 3 ⁇ m thick DLC film on the surface and a 8 mm diameter with a DLC sliding surface formed by a 3 ⁇ m thick DLC film on the surface Using a ball-on-disk type sliding friction tester fitted with a ball, drop 1 mL of the initial bonding agent onto the DLC sliding surface of the disk, and place the ball in a load of 10 N While sliding 10 m relatively at a velocity of 10 mm / s in the circumferential direction of the disk, the coefficient of friction between the DLC sliding surfaces of the disk and the ball is measured during the sliding with a sliding distance of 0 to 10 m.
- the disc and ball are then removed from the sliding friction tester and ultrasonic cleaned. After washing, the ball may be wiped with acetone to remove nanodiamonds attached to the ball.
- 1 mL of a lubricant is dropped onto the DLC sliding surface of the disc, and then the ball is abutted with a load of 10 N while the disc circumference
- the sliding is carried out for a further 90 m at a speed of 10 mm / s relative to the direction, and the friction coefficient between the DLC sliding surface of the disc and the ball is measured during the sliding with a sliding distance of 10 to 100 m.
- Wear amount calculation method A circular wear mark formed on the ball subjected to the friction test is observed using a confocal microscope, and from the observation image, a uniformly smooth plane is obtained for the circular wear mark. Assuming that there is a diameter r (mm) is determined. And ball wear volume V (mm ⁇ 3 >) is computed by following formula (1) and Formula (2). H in Formula (1) is height (mm) of the ball crown of the said circular shaped abrasion mark, and is calculated
- the ND particles may be an oxygen oxidation treatment of detonation nano diamond particles. According to the detonation method, it is possible to appropriately generate an ND having a primary particle size of 10 nm or less.
- the zeta potential of ND may be negative.
- the ND particles may be a hydrogen reduction treatment product of the detonation nano diamond particles. According to the detonation method, it is possible to appropriately generate an ND having a primary particle size of 10 nm or less.
- the zeta potential of ND may be positive.
- the lubricant base in the initial adjustor and lubricant is water.
- a fluid system set for a lubrication system comprises an initial blender containing nanodiamond particles with a concentration of 0.01 to 2% by mass, and a lubricant containing nanodiamond particles with a concentration of 0.001% by mass or less.
- the fluid system set for lubrication system according to the second aspect can be used for the lubrication system according to the first aspect.
- Using the liquid lubricant set for the lubricating system can form a low friction surface early on the DLC sliding surface, maintain the low friction surface, and is suitable for reducing wear on the sliding surface. That is, the lubricant system solution set is suitable for achieving low friction and low wear on the DLC sliding surface.
- the lubrication system of the present invention comprises a relatively low concentration of ND particles in the lubrication of a low friction DLC sliding surface using an initial conformant containing a relatively high concentration of ND particles.
- the liquid agent set for lubricating system of the present invention is used for the lubricating system, and includes the above-mentioned initial conformant and lubricant.
- the sliding surface means, for example, a surface that rubs against and slides due to relative movement, such as a contact surface of a shaft and a bearing in a machine.
- the initial adhesion agent is a solution (dispersion liquid) in which the ND particles are dispersed in a lubricant base.
- the ND particle concentration of the initial conformant is, for example, 0.01 to 2% by mass, preferably 0.03 to 1.0% by mass, more preferably 0.05 to 0.8% by mass, more preferably 0.07 to It is 0.6% by mass, more preferably 0.08 to 0.4% by mass. It is suitable for early formation of a surface having both smoothness and wettability by tribochemical reaction in a system in which ND particles exist on the sliding surface of the DLC, when the ND particle concentration of the initial conformant is in the above range .
- the lubricant is a solution (dispersion liquid) in which ND particles are dispersed in a lubricant base.
- the ND particle concentration of the lubricant is, for example, 0.001 mass% or less (1.0 ⁇ 10 ⁇ 5 to 1.0 ⁇ 10 ⁇ 3 mass%), preferably 3.0 ⁇ 10 ⁇ 5 to 5.0 ⁇ 10 It is -4 % by mass, more preferably 5.0 ⁇ 10 -5 to 3.0 ⁇ 10 -4 % by mass, more preferably 8.0 ⁇ 10 -5 to 2.0 ⁇ 10 -4 % by mass.
- the ND particle concentration of the lubricant is in the above range, it is suitable for maintaining the smoothness and the wettability on the DLC sliding surface formed by the initial bonding agent, and reducing the friction and the wear on the sliding surface.
- the ND particles contained in the initial conformant and lubricant are dispersed as primary particles in the initial conformant and lubricant separately from each other.
- the particle size of the ND primary particles is, for example, 10 nm or less.
- the lower limit of the particle size of primary particles of ND is, for example, 1 nm.
- the particle diameter D50 (median diameter) of the ND primary particles is, for example, 10 nm or less, preferably 9 nm or less, more preferably 8 nm or less, more preferably 7 nm or less, more preferably 6 nm or less.
- the particle size D50 of the ND primary particles can be measured, for example, by dynamic light scattering.
- the ND particles are preferably detonation method ND particles (ND particles produced by detonation method). According to the detonation method, it is possible to appropriately generate an ND having a primary particle size of 10 nm or less.
- the ND particles may be an oxygen oxidation treatment of detonation method ND particles.
- the peak position attributed to CCO stretching vibration in the FT-IR of the ND particles tends to be 1750 cm -1 or more, and the zeta potential of the ND particles tends to be negative at this time.
- the oxygen oxidation treatment of the detonation method ND particles is as described in the oxygen oxidation step in the production process described later.
- the ND particles may be a hydrogen reduction treatment product of the detonation method ND particles.
- the hydrogen reduction treatment of the detonation method ND particles is as described in the hydrogen reduction treatment step in the production process described later.
- the value when the so-called zeta potential of the ND particles is negative is, for example, -60 to -30 mV.
- the temperature condition of the oxygen oxidation treatment to a relatively high temperature (for example, 400 to 450 ° C.)
- the negative zeta potential can be obtained for the ND particles.
- the value when the zeta potential is positive is, for example, 30 to 60 mV.
- the initial conformant and lubricant can be produced by mixing the ND dispersion obtained by the method described later with a desired component such as a lubricant base.
- the ND dispersion can be produced, for example, through a process including the following production process S1, purification process S2, oxygen oxidation process S3, and crushing process S4.
- nanodiamonds are produced, for example, by detonation.
- a shaped explosive provided with an electric detonator is installed inside a pressure-resistant container for detonation, and in a state in which a predetermined gas and the used explosive coexist in the container, the container Seal the
- the container is, for example, made of iron, and the volume of the container is, for example, 0.5 to 40 m 3 .
- a mixture of trinitrotoluene (TNT) and cyclotrimethylene trinitroamine or hexogen (RDX) can be used.
- TNT / RDX The mass ratio of TNT to RDX (TNT / RDX) is, for example, in the range of 40/60 to 60/40.
- the amount of explosive used is, for example, 0.05 to 2.0 kg.
- the above-mentioned gas sealed in the container together with the explosive used may have an atmospheric composition or may be an inert gas.
- the above-mentioned gas sealed in the container together with the used explosive is preferably an inert gas. That is, from the viewpoint of producing nanodiamond having a small amount of functional groups on the primary particle surface, detonation for producing nanodiamond is preferably carried out under an inert gas atmosphere.
- the inert gas for example, at least one selected from nitrogen, argon, carbon dioxide, and helium can be used.
- the electric detonator is detonated and the explosive is detonated in the container.
- a detonation refers to an explosion associated with a chemical reaction in which the flame surface on which the reaction occurs travels at a high speed beyond the speed of sound.
- the used explosive partially burns incompletely and liberated carbon is used as a raw material to generate nano diamond by the action of pressure and energy of shock wave generated by explosion.
- the detonation method as described above, it is possible to appropriately generate nanodiamonds having a primary particle size of 10 nm or less.
- the nano diamond is a product obtained by the detonation method, which is very strongly due to the Coulomb interaction between the adjacent primary particles or crystallites in addition to the action of van der Waals force. Assemble and form a cohesive body.
- the container and the inside thereof are cooled by leaving at room temperature, for example, for 24 hours.
- the nanodiamond crude product is recovered.
- the nanodiamond crude product is recovered by scraping off the nanodiamond crude product adhering to the inner wall of the container (including the agglomerates and wrinkles of the nanodiamond produced as described above) with a spatula be able to.
- a crude product of nanodiamond particles can be obtained.
- it is possible to acquire a desired amount of nano diamond crude products by performing the above production processes S1 as many times as necessary.
- the purification step S2 includes an acid treatment in which a crude acid, which is a raw material of the raw nanodiamond material, is reacted with a strong acid in an aqueous solvent, for example.
- a crude nanodiamond product obtained by the detonation method is likely to contain metal oxides, and this metal oxide is an oxide such as Fe, Co, Ni, etc. derived from the container etc. used for the detonation method. is there.
- the metal oxide can be dissolved and removed from the crude nanodiamond product by reacting with a predetermined strong acid in an aqueous solvent (acid treatment).
- the strong acid used for the acid treatment is preferably a mineral acid, and examples thereof include hydrochloric acid, hydrofluoric acid, sulfuric acid, nitric acid, and aqua regia.
- one strong acid may be used, or two or more strong acids may be used.
- the concentration of the strong acid used in the acid treatment is, for example, 1 to 50% by mass.
- the acid treatment temperature is, for example, 70 to 150.degree.
- the acid treatment time is, for example, 0.1 to 24 hours.
- the acid treatment can be performed under reduced pressure, normal pressure, or increased pressure. After such acid treatment, washing with water (including nano-diamond aggregates) of the solid content is performed by, for example, decantation.
- a solution oxidation treatment for removing non-diamond carbon such as graphite and amorphous carbon from a nanodiamond crude product (nanodiamond adhesion body before completion of purification) using an oxidizing agent is used.
- the crude diamond product obtained by the detonation method contains non-diamond carbon such as graphite (graphite) and amorphous carbon. This non-diamond carbon causes partial burnout of the used explosive partially. It originates in carbon which did not form nano diamond crystals among the liberated carbon.
- non-diamond carbon can be removed from the nanodiamond crude product by acting a predetermined oxidizing agent or the like in an aqueous solvent (solution oxidation treatment).
- oxidizing agents used for this solution oxidation treatment include chromic acid, chromic anhydride, dichromic acid, permanganic acid, perchloric acid, salts thereof, nitric acid, and mixed acids (a mixture of sulfuric acid and nitric acid). It can be mentioned.
- one type of oxidizing agent may be used, or two or more types of oxidizing agents may be used.
- the concentration of the oxidizing agent used in the solution oxidation treatment is, for example, 3 to 50% by mass.
- the amount of the oxidizing agent used in the solution oxidation treatment is, for example, 300 to 2000 parts by mass with respect to 100 parts by mass of the nanodiamond crude product subjected to the solution oxidation treatment.
- the solution oxidation treatment temperature is, for example, 50 to 250.degree.
- the solution oxidation treatment time is, for example, 1 to 72 hours.
- Solution oxidation treatment can be performed under reduced pressure, normal pressure or increased pressure. After such solution oxidation treatment, washing with solids (including nano-diamond aggregates) is performed, for example, by decantation. It is preferable to repeatedly carry out washing of the solid content by decantation until the supernatant liquid is colored at the beginning of washing until the supernatant liquid is visually clear.
- the drying treatment include spray drying using a spray drying apparatus and evaporation to dryness using an evaporator.
- the nanodiamond powder that has undergone the purification step S2 is heated in a gas atmosphere of a predetermined composition containing oxygen, using a gas atmosphere furnace.
- a gas atmosphere furnace oxygen-containing gas is supplied or flowed to the furnace, and the temperature in the furnace is raised to the temperature condition set as the heating temperature.
- Oxygen oxidation treatment is carried out.
- the temperature condition of this oxygen oxidation treatment is, for example, 250 to 500.degree.
- the temperature conditions of this oxygen oxidation treatment are preferably relatively high, for example, 400 to 450 ° C.
- the oxygen-containing gas used in the present embodiment is a mixed gas containing an inert gas in addition to oxygen.
- Inert gases include, for example, nitrogen, argon, carbon dioxide, and helium.
- the oxygen concentration of the mixed gas is, for example, 1 to 35% by volume.
- a hydrogen reduction treatment step S3 ' is performed after the above-described oxygen oxidation step S3.
- the nanodiamond powder that has undergone the oxygen oxidation step S3 is heated in a gas atmosphere of a predetermined composition containing hydrogen using a gas atmosphere furnace.
- a hydrogen-containing gas is supplied or flowed to a gas atmosphere furnace in which nanodiamond powder is disposed inside, and the temperature in the furnace is raised to the temperature condition set as the heating temperature, Hydrogen reduction treatment is performed.
- the temperature conditions of this hydrogen reduction treatment are, for example, 400 to 800.degree.
- the hydrogen-containing gas used in the present embodiment is a mixed gas containing an inert gas in addition to hydrogen.
- Inert gases include, for example, nitrogen, argon, carbon dioxide, and helium.
- the hydrogen concentration of the mixed gas is, for example, 1 to 50% by volume.
- detonation nanodiamonds may take the form of an aggregate (secondary particles), and further primary particles from the aggregate.
- a crushing step S4 is performed to separate. Specifically, first, nanodiamonds that have undergone the oxygen oxidation step S3 or the subsequent hydrogen reduction treatment step S3 'are suspended in pure water to prepare a slurry containing nanodiamonds. In preparing the slurry, centrifugation may be performed to remove relatively large assemblies from the nanodiamond suspension, or the nanodiamond suspension may be subjected to ultrasonication. Then, the slurry is subjected to a wet crushing process.
- the crushing process can be performed using, for example, a high shear mixer, a high shear mixer, a homomixer, a ball mill, a bead mill, a high pressure homogenizer, an ultrasonic homogenizer, or a colloid mill.
- the crushing process may be performed by combining these. From the viewpoint of efficiency, it is preferable to use a bead mill.
- the bead mill which is a pulverizer or disperser, includes, for example, a cylindrical mill container, a rotor pin, a centrifugal separator, a raw material tank, and a pump.
- the rotor pin has a common axis with the mill container and is configured to be rotatable at high speed inside the mill container.
- the centrifuge system is disposed at the top in the mill vessel. In bead milling using a bead mill in the crushing step, as a predetermined amount of beads is filled in the mill container and the rotor pins are stirring the beads, the action of the pump acts as a raw material from the raw material tank to the lower part of the mill container.
- the above-mentioned slurry (including nano-diamond aggregates) is introduced.
- the slurry passes through the rapidly stirred beads in the mill vessel to reach the top in the mill vessel.
- the nano-diamond aggregates contained in the slurry are subjected to the action of crushing or dispersion by contact with the vigorously moving beads.
- the disintegration of the nano-diamond agglomerates (secondary particles) into primary particles proceeds.
- the slurry and the beads that reached the upper centrifuge in the mill vessel are centrifuged using the specific gravity difference by the operating centrifuge, the beads remain in the mill vessel, and the slurry It is discharged out of the mill container via a hollow line slidably connected.
- the discharged slurry is returned to the raw material tank and then introduced again into the mill container by the action of the pump (circulation operation).
- the crushing media used is, for example, zirconia beads, and the diameter of the beads is, for example, 15 to 500 ⁇ m.
- the amount (apparent volume) of beads packed in the mill vessel is, for example, 50 to 80% of the volume of the mill vessel.
- the circumferential speed of the rotor pin is, for example, 8 to 12 m / min.
- the amount of slurry to be circulated is, for example, 200 to 600 mL, and the flow rate of the slurry is, for example, 5 to 15 L / hour.
- the processing time (circulation operation time) is, for example, 30 to 300 minutes.
- a batch-type bead mill may be used instead of the continuous-type bead mill as described above.
- an ND dispersion containing nanodiamond primary particles can be obtained.
- the dispersion obtained through the crushing step S4 may be subjected to classification operation for removing coarse particles.
- coarse particles can be removed from the dispersion by classification using centrifugation.
- a black transparent ND dispersion in which primary particles of nanodiamond are dispersed as colloidal particles is obtained.
- Lubricants in initial conformers and lubricants include polar solvents or nonpolar solvents.
- the polar solvent include water, methanol, ethanol, propanol, butanol, polyfunctional alcohols (ethylene glycol, propylene glycol, neopentyl glycol, trimethylolpropane, pentaerythritol and the like), mixed solvents thereof and the like.
- nonpolar solvents synthetic oils (poly- ⁇ -olefin, alkyl naphthalene, polybuden etc.), mineral oils, synthetic hydrocarbon oils, ester oils (polyol esters, diesters, complex esters etc), silicone oils, fluorine oils And castor oil and mixed solvents thereof.
- water is preferred as a lubricant for the initial adjustor and lubricant.
- the content of the lubricant base in the initial fitting agent is, for example, 98% by mass or more, preferably 99% by mass or more, more preferably 99.5% by mass or more, and more preferably 99.9% by mass or more It is.
- the content of the lubricant base in the lubricant is, for example, 99.9% by mass or more, preferably 99.95% by mass or more, more preferably 99.99% by mass or more, and more preferably 99.999%. It is mass% or more.
- Initial conformers and lubricants may contain other components in addition to the ND particles and lubricant base.
- Other components include, for example, surfactants, thickeners, coupling agents, rust inhibitors for rusting of metal members to be lubricated, and corrosion prevention for suppressing corrosion of non-metal members to be lubricated.
- Agents freezing point depressants, antifoam agents, antiwear additives, preservatives, colorants, and solid lubricants other than ND particles.
- a suitable amount of initial welding agent is added to the DLC sliding surface, and friction (pre-slip) is performed in advance. Thereafter, the DLC sliding surface is further slid (sliding) in the presence of the lubricant.
- the lubrication system of the present invention is suitable, for example, to reduce the coefficient of friction and wear on sliding surfaces such as sliding bearings in machines. In the lubrication system of the present invention, it is considered that the wettability improvement and the smoothing of the DLC sliding surface proceed at an early stage due to the tribochemical reaction in the system where the ND particles act when the initial conformant is used. The sliding surface tends to reduce friction early.
- the use of a lubricant tends to maintain low friction while suppressing wear of the DLC sliding surface.
- the lubrication system of the present invention is suitable for achieving low friction and low wear on the DLC sliding surface.
- the particle concentration in the initial habituation agent containing relatively high concentration of nanodiamond particles is preferably 0.01 to 2% by mass, and the particle concentration in the lubricant containing relatively low concentration of nanodiamond particles is , Preferably 0.001 mass% or less.
- the following friction test is, for example, a test imitating a slide bearing having a DLC sliding surface in a machine.
- the coefficient of friction of the sliding surface measured in the following friction test is 0.05 or less (more preferably 0.03 or less), and the ball wear volume determined by the following method for calculating the amount of wear after the friction test is 1.0 ⁇ It is preferably 10 ⁇ 4 mm 3 or less (more preferably 7.0 ⁇ 10 ⁇ 5 mm 3 or less).
- Friction test First, a disk with a diameter of 30 mm and a thickness of 4 mm having a DLC sliding surface formed by a 3 ⁇ m thick DLC film on the surface and a 8 mm diameter with a DLC sliding surface formed by a 3 ⁇ m thick DLC film on the surface Using a ball-on-disk sliding friction tester fitted with a ball, 1 mL of the initial bonding agent is dropped onto the DLC sliding surface of the disk and then the ball is brought into contact with a load of 10 N The disk is slid 10 m relatively at a velocity of 10 mm / s in the circumferential direction of the disk, and the coefficient of friction between the DLC sliding surface of the disk and the ball is measured during the sliding at a sliding distance of 0-10 m.
- the disc and ball are then removed from the sliding friction tester and ultrasonic cleaned. After washing, the ball may be wiped with acetone to remove nanodiamonds attached to the ball.
- 1 mL of the lubricant is dropped onto the DLC sliding surface of the disk and then the ball is abutted with a load of 10 N
- the sliding is further performed 90 m in the circumferential direction relatively at a speed of 10 mm / s, and the coefficient of friction between the disk and the DLC sliding surface of the ball is measured during the sliding at a sliding distance of 10 to 100 m.
- Wear amount calculation method A circular wear mark formed on the ball subjected to the friction test is observed using a confocal microscope, and from the observation image, it is a plane that is uniformly smooth about the circular wear mark. Assuming that the diameter r (mm) is determined. And ball wear volume V (mm ⁇ 3 >) is computed by following formula (1) and Formula (2). H in Formula (1) is height (mm) of the ball crown of the said circular shaped abrasion mark, and is calculated
- the diamond like carbon (DLC) film on the DLC sliding surface is an amorphous (amorphous) hard film mainly composed of a hydrocarbon or an allotrope of carbon. DLC can distinguish its properties depending on the hydrogen content and whether the crystalline electron orbits contained are close to diamond or close to graphite.
- DLC for example, amorphous hydrogenated carbon aC: H, amorphous carbon aC, tetrahedral amorphous carbon ta-C: H, and hydrogenated tetrahedral amorphous carbon ta -C is mentioned.
- a nanodiamond aqueous dispersion X1 (ND aqueous dispersion) was produced through the following production steps, purification steps, oxygen oxidation steps, and crushing steps.
- a shaped explosive provided with an electric detonator was installed inside a pressure-resistant container for detonation to seal the container.
- the container is made of iron and the volume of the container is 15 m 3 .
- As an explosive 0.50 kg of a mixture of trinitrotoluene (TNT) and cyclotrimethylene trinitroamine or hexogen (RDX) was used. The mass ratio of TNT to RDX (TNT / RDX) in the explosive is 50/50.
- the electric detonator was detonated and the explosive was detonated in the container.
- the container and its inside were cooled by leaving at room temperature for 24 hours.
- nanodiamond crude product (including the agglomerates and wrinkles of nanodiamond particles produced by the above detonation method) attached to the inner wall of the vessel was recovered.
- the nanodiamond crude product was obtained by performing the above-mentioned production process a plurality of times.
- acid treatment of the purification step was performed on the nanodiamond crude product obtained in the above generation step. Specifically, the slurry obtained by adding 6 L of 10% by mass hydrochloric acid to 200 g of the crude nanodiamond product was subjected to heat treatment under reflux under normal pressure conditions for 1 hour. The heating temperature in this acid treatment is 85 to 100.degree. Next, after cooling, decantation was performed to wash the solid content (including nano-diamond aggregates and soot) with water. The solid was repeatedly washed with water by decantation until the pH of the precipitate reached 2 from the low pH side. Next, mixed acid treatment was performed as solution oxidation treatment in the purification step.
- a drying step was performed. Specifically, 1000 mL of the nanodiamond-containing liquid obtained through the above-mentioned water washing treatment was subjected to spray drying using a spray dryer (trade name "SPRAY DRYER B-290, manufactured by Nippon Buchi Co., Ltd.) . This gave 50 g of nanodiamond powder.
- an oxygen oxidation step was performed using a gas atmosphere furnace (trade name “gas atmosphere tube furnace KTF045N1” manufactured by Koyo Thermo System Co., Ltd.). Specifically, 4.5 g of nano diamond powder obtained as described above was allowed to stand still in the core tube of a gas atmosphere furnace, and nitrogen gas was allowed to flow through the core tube at a flow rate of 1 L / min for 30 minutes. Thereafter, the flow gas was switched from nitrogen to a mixed gas of oxygen and nitrogen, and the mixed gas was allowed to flow through the core tube at a flow rate of 1 L / min. The oxygen concentration in the mixed gas is 4% by volume. After switching to the mixed gas, the temperature in the furnace was raised to 400 ° C., which is the heating set temperature.
- the temperature rising rate was 10 ° C./min up to 380 ° C., which is 20 ° C. lower than the heating set temperature, and then 1 ° C./min from 380 ° C. to 400 ° C. Then, while maintaining the temperature condition in the furnace at 400 ° C., the oxygen oxidation treatment was performed on the nano diamond powder in the furnace.
- the processing time was 3 hours.
- the crushing process was performed. Specifically, first, 1.8 g of nanodiamond powder that had undergone an oxygen oxidation step and 28.2 mL of pure water were mixed in a 50 mL sample bottle to obtain about 30 mL of a slurry. Next, the pH of the slurry was adjusted by the addition of a 1 M aqueous solution of sodium hydroxide, and then ultrasonication was applied. In the ultrasonic treatment, the slurry was subjected to ultrasonic irradiation for 2 hours using an ultrasonic irradiator (trade name “ultrasonic cleaner AS-3”, manufactured by AS ONE) .
- an ultrasonic irradiator trade name “ultrasonic cleaner AS-3”, manufactured by AS ONE
- bead milling was performed using a bead milling apparatus (trade name “parallel four-cylinder sand grinder LSG-4U-2L type”, manufactured by Imex Co., Ltd.). Specifically, 30 mL of the slurry after ultrasonic wave irradiation and zirconia beads with a diameter of 30 ⁇ m are charged into 100 mL of a mill container, vessel (manufactured by IMEX Co., Ltd.), and sealed, and the device is driven to execute bead milling. did. In this bead milling, the input amount of zirconia beads is about 33% of the volume of the mill vessel, the rotation speed of the mill vessel is 2570 rpm, and the milling time is 2 hours.
- the slurry or suspension subjected to such a crushing step was subjected to centrifugation using a centrifugal separator (classification operation).
- the centrifugal force in this centrifugation was 20000 ⁇ g, and the centrifugation time was 10 minutes.
- 10 mL of the supernatant of the nanodiamond-containing solution subjected to the centrifugation treatment was collected. In this way, an ND aqueous dispersion in which nanodiamonds are dispersed in pure water, which is a stock solution of the initial adjustability composition and the lubricant, was obtained.
- the solid content concentration to the nanodiamond concentration was 59.1 g / L, and the pH was 9.33.
- the particle diameter D50 (median diameter) was 3.97 nm, the particle diameter D90 was 7.20 nm, and the zeta potential was -42 mV.
- ND concentration nanodiamond content of the obtained ND aqueous dispersion is the weighing value of 3 to 5 g of the weighed dispersion, and the dried product remaining after evaporation of the water from the weighing dispersion by heating (powder Body) was calculated based on the value measured by a precision balance.
- the particle diameter (median diameter, D50 to D90) of the nanodiamond particles contained in the obtained ND aqueous dispersion is determined by dynamic light scattering using an apparatus manufactured by Malvern (trade name "Zetasizer Nano ZS"). It was measured by the method (noncontact backscattering method).
- the ND aqueous dispersion subjected to measurement was subjected to ultrasonic irradiation by an ultrasonic cleaner after being diluted with ultrapure water so that the solid content concentration or nano diamond concentration would be 0.5 to 2.0 mass%. It is a thing.
- the zeta potential of the nano diamond particles contained in the obtained ND aqueous dispersion was measured by a laser Doppler electrophoresis method using a device manufactured by Malvern (trade name "Zeta Sizer Nano ZS").
- the ND aqueous dispersions X1 and Y1 subjected to the measurement were subjected to ultrasonic irradiation by an ultrasonic cleaner after being diluted with ultrapure water so that the solid content concentration to nano diamond concentration would be 0.2 mass%.
- the zeta potential measurement temperature is 25.degree.
- FT-IR Fourier transform infrared spectroscopy
- FT-IR apparatus (trade name "Spectrum 400 type FT-IR", manufactured by PerkinElmer Japan Co., Ltd.) for each of the above-described oxygen-oxidized nano diamond samples using Fourier transform infrared spectroscopy (FT- IR) was done.
- FT-IR Fourier transform infrared spectroscopy
- the infrared absorption spectrum was measured while heating a sample to be measured at 150 ° C. in a vacuum atmosphere. Heating under a vacuum atmosphere was realized by using ST-Japan Japan Model-HC900 Heat Chamber and TC-100WA Thermo Controller in combination.
- Example 1 Friction Test For the friction test, a ball-on-disk sliding friction tester was used. Using a SUJ2 ball of 8 mm in diameter and a SUJ2 disk of 30 mm in diameter and 4 mm in thickness as a base material, a DLC film of about 3 ⁇ m was formed on the surface of the ball and the disk. At the start of the test, 1 mL of the initial adhesion agent was dropped on the disc surface, and the ball was allowed to slide 10 m at a speed of 10 mm / s while applying a load of 10 N on the disc. The ball and disc were then removed from the friction tester and subjected to ultrasonic cleaning in purified water for 15 minutes.
- Friction test of Example 1 the horizontal axis sliding distance [m], a graph in which the ordinate the coefficient of friction in Figure 3, the horizontal axis sliding distance [m], Ball Wear volume (amount of wear) [mm 3]
- shaft is shown in FIG.
- the line with the lower end of the coefficient of friction 0 seen at a sliding distance of 10 m and the upper end near 0.10 is the noise when sliding is resumed using a lubricant and is measured in this test It shall not be included in the coefficient of friction.
- Comparative Example 1 Friction Test The friction test was conducted in the same manner as in Example 1 except that water containing no nanodiamond particles was used instead of the above-mentioned initial conformant and lubricant.
- a graph in which the sliding distance [m] is taken along the horizontal axis and the friction coefficient is taken along the vertical axis is shown in FIG. 2; the sliding distance [m] is taken along the horizontal axis; The graph which made the vertical axis
- [Supplementary Note 1] Use a lubricant containing a relatively low concentration of nanodiamond particles for the lubrication of a low friction DLC sliding surface using an initial fluxing agent containing a relatively high concentration of nanodiamond particles Lubrication system.
- [Supplementary Note 2] The lubrication system according to any of the preceding claims, wherein the concentration of nano diamond particles of said initial conformant is 0.01-2 wt%.
- [Supplementary Note 3] The lubrication system according to claim 1 or 2, wherein the concentration of nano diamond particles in the lubricant is 0.001 mass% or less.
- the friction coefficient of the DLC sliding surface measured by the following friction test is 0.05 or less, and the ball wear volume determined by the wear amount calculation method after the following friction test is 1.0 ⁇ 10 -4 mm 3 or less
- the lubricating system according to any one of appendices 1 to 3 (the method of calculating the amount of wear is as described in the present specification).
- the lubrication system according to any one of Appendices 1 to 4 wherein the primary particle size of the nano diamond particles is 10 nm or less.
- a lubrication system according to any one of appendices 1 to 5 and 10 to 12, wherein the peak position attributed to C O stretching vibration in FT-IR of the nanodiamond particles is less than 1750 cm ⁇ 1 .
- the lubricant in the initial conformant and the lubricant is water.
- a liquid agent set for a lubrication system comprising: an initial blender containing nanodiamond particles in a concentration of 0.01 to 2% by mass; and a lubricant containing nanodiamond particles in a concentration of 0.001% by mass or less.
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Abstract
Description
本発明は、潤滑システムおよび潤滑システム用液剤セットに関する。本願は、2017年11月9日付の日本出願である特願2017-216443号に基づく優先権を主張し、これら出願に記載されている全ての内容を援用するものである。 The present invention relates to a lubrication system and a liquid agent set for the lubrication system. This application claims the priority based on Japanese Patent Application No. 2017-216443 which is a Japanese application dated November 9, 2017, and uses all the contents described in these applications.
硬質炭素(ダイヤモンドライクカーボン;DLC)膜は、高硬度および化学安定性を有することから、摺動部材の表面(摺動面)への応用が期待されている。このようにDLC膜を摺動面に用いることについては、例えば下記の特許文献1に記載されている。
Since hard carbon (diamond like carbon; DLC) films have high hardness and chemical stability, their application to the surface (sliding surface) of a sliding member is expected. The use of the DLC film as the sliding surface as described above is described, for example, in
DLC膜は、化学的に安定、かつ高硬度であるが、低摩擦および低摩耗である面を形成するには不利な材料であった。DLC膜を用いた摺動面において、低摩擦および低摩耗である面を形成し、摩擦および摩耗を長時間低減するための技術が求められている。 The DLC film is a material which is chemically stable and high in hardness, but is disadvantageous for forming a surface with low friction and low wear. There is a need for a technique for forming a low friction and low wear surface on a sliding surface using a DLC film, and for reducing friction and wear for a long time.
本発明は、以上のような事情のもとで考え出されたものであり、DLC摺動面において低摩擦および低摩耗を実現するのに適した潤滑システム、および潤滑システム用液剤セットを、提供する。 The present invention has been conceived under the above circumstances, and provides a lubrication system suitable for achieving low friction and low wear on a DLC sliding surface, and a liquid agent set for the lubrication system. Do.
本発明の第1の側面によると潤滑システムが提供される。この潤滑システムは、相対的に高濃度のナノダイヤモンド粒子(以下、「ND粒子」と称する場合がある)を含有する初期なじみ剤を使用して低摩擦化されたダイヤモンドライクカーボン(DLC)摺動面の潤滑に、相対的に低濃度のナノダイヤモンド粒子を含有する潤滑剤を使用するものである。 According to a first aspect of the present invention, a lubrication system is provided. This lubrication system is a low friction diamond-like carbon (DLC) slide using an initial conformant containing relatively high concentrations of nanodiamond particles (hereinafter sometimes referred to as "ND particles"). For lubrication of the surface, a lubricant containing relatively low concentration of nanodiamond particles is used.
本発明者らの知見によると、DLC摺動面の潤滑用液剤として水(純粋)を用いる場合、DLC摺動面の摩擦係数に有意な低下の見られる、いわゆる初期なじみ期間およびその後の期間を通して当該摺動面の摩耗は抑制される傾向にあるものの、前記のような初期なじみ期間を経た後の摺動面摩擦係数は次第に上昇する傾向にある。一方、DLC摺動面の潤滑用液剤として比較的に高濃度のND粒子水分散液を用いる場合、DLC摺動面の摩擦係数に有意な低下の見られる初期なじみ期間の後において、摺動面摩擦係数の上昇は抑制される傾向にあるものの、当該摺動面の摩耗は進行する傾向にある。バルクダイヤモンドがそうであるように高硬度であるND粒子のDLC摺動面への接触頻度が高いほど、摩耗は進行しやすい。 According to the findings of the present inventors, when water (pure) is used as a lubricant solution for the DLC sliding surface, a significant decrease is seen in the friction coefficient of the DLC sliding surface, so-called initial fit-in period and subsequent period Although wear on the sliding surface tends to be suppressed, the sliding surface friction coefficient tends to gradually increase after passing through the initial fitting period as described above. On the other hand, when a relatively high concentration ND particle water dispersion is used as the lubricating liquid agent for the DLC sliding surface, the sliding surface after the initial fitting period in which a significant drop is seen in the friction coefficient of the DLC sliding surface. Although the increase in the coefficient of friction tends to be suppressed, the wear on the sliding surface tends to progress. The higher the frequency of contact of the high-hardness ND particles with the DLC sliding surface, as with bulk diamond, the easier the wear progresses.
これらとは異なり、本発明の第1の側面に係る上述潤滑システムでは、DLC摺動面の潤滑用液剤として、ND粒子濃度が相対的に高い初期なじみ剤を先ずは使用して、DLC摺動面の低摩擦化が図られる(初期なじみ期間)。そのうえで、DLC摺動面の潤滑用液剤として、ND粒子濃度が相対的に低い潤滑剤を使用し、これによってDLC摺動面の潤滑系が成立・維持される。上記初期なじみ剤の使用期間中には、炭素原子が表面に配列しているDLC摺動面に対し、同じく炭素原子が表面に配列し且つ相対的に高濃度で存在しているND粒子と水とが重畳的に作用する系でのトライボ化学反応により、DLC摺動面の濡れ性向上や平滑化が早期に進行するものと考えられ、DLC摺動面が早期に低摩擦化する傾向にあるという知見を本発明者らは得ている。初期なじみ期間を経た後の上記潤滑剤の使用期間中には、潤滑剤中のND粒子が相対的に低濃度であるために当該ND粒子によるDLC摺動面への物理的アタックが減じられつつ、水と相対的に低濃度のND粒子とがDLC摺動面に対して重畳的に作用する系でのトライボ化学反応によってDLC摺動面の濡れ性や平滑性が維持されるものと考えられ、DLC摺動面の摩耗が抑制されつつ低摩擦性が維持される傾向にあるという知見を本発明者らは得ている。以上の知見については、例えば後記の実施例および比較例をもって示すとおりである。 Unlike the above, in the above-described lubrication system according to the first aspect of the present invention, as the lubricating fluid agent for the DLC sliding surface, the initial sliding-adjusting agent having a relatively high concentration of ND particles is first used to Low surface friction can be achieved (initial contact period). Then, a lubricant having a relatively low concentration of ND particles is used as a lubricant for lubricating the DLC sliding surface, whereby the lubricating system of the DLC sliding surface is established and maintained. During the period of use of the above-mentioned initial conformity agent, ND particles and water in which carbon atoms are similarly arranged on the surface and are present at a relatively high concentration with respect to the DLC sliding surface on which carbon atoms are arranged on the surface It is thought that the wettability improvement and smoothing of the DLC sliding surface will advance at an early stage by the tribochemical reaction in the system where T and T act in a superimposed manner, and the DLC sliding surface tends to reduce the friction early. The present inventors have obtained the knowledge that During the period of use of the lubricant after the initial fitting period, the physical concentration of the ND particles on the DLC sliding surface is reduced because the concentration of the ND particles in the lubricant is relatively low. It is considered that the wettability and smoothness of the DLC sliding surface are maintained by the tribochemical reaction in a system in which water and relatively low concentration ND particles act on the DLC sliding surface in an overlapping manner. The inventors of the present invention have obtained the finding that the low friction property tends to be maintained while the wear of the DLC sliding surface is suppressed. The above findings are, for example, as shown in the following Examples and Comparative Examples.
以上のように、本発明の第1の側面に係る潤滑システムは、DLC摺動面において低摩擦および低摩耗を実現するのに適するのである。 As described above, the lubrication system according to the first aspect of the present invention is suitable for achieving low friction and low wear on the DLC sliding surface.
本発明は、初期なじみ剤のND粒子濃度が、0.01~2質量%であることが好ましい。当該構成は、DLC摺動面におけるND粒子が存在する系でのトライボ化学反応によって、平滑性と濡れ性とを兼ね備えた面を早期に形成するのに適する。 In the present invention, it is preferable that the ND particle concentration of the initial conformant is 0.01 to 2% by mass. The configuration is suitable for early formation of a surface having both smoothness and wettability by tribochemical reaction in a system in which ND particles are present on a DLC sliding surface.
本発明は、潤滑剤のND粒子濃度が、0.001質量%以下であることが好ましい。当該構成は、初期なじみ剤により形成したDLC摺動面における平滑性と濡れ性を維持し、摺動面における摩擦および摩耗を低減するのに適する。 In the present invention, the ND particle concentration of the lubricant is preferably 0.001% by mass or less. The composition is suitable for maintaining the smoothness and wettability of the DLC sliding surface formed by the initial bonding agent, and reducing friction and wear on the sliding surface.
本発明は、下記摩擦試験で測定される摺動面の摩擦係数は0.05以下であり、且つ前記摩擦試験後の下記摩耗量算出方法により求めるボール摩耗体積は1.0×10-4mm3以下であることが好ましい。
摩擦試験:まず、厚さ3μmのDLC膜がなすDLC摺動面を表面に有する直径30mmおよび厚さ4mmのディスクと、厚さ3μmのDLC膜がなすDLC摺動面を表面に有する直径8mmのボールとが取り付けられた、ボールオンディスク型の滑り摩擦試験機を使用して、ディスクのDLC摺動面に対し、1mLの前記初期なじみ剤を滴下したうえでボールを10Nの荷重で当接させつつディスク周方向に相対的に10mm/sの速度で10m滑動させ、滑り距離0~10mの当該滑動中、ディスクおよびボールのDLC摺動面間の摩擦係数を測定する。次に、ディスクおよびボールを、滑り摩擦試験機から取り外し、超音波洗浄する。洗浄後、ボールに付着したナノダイヤモンドを除去するためにアセトンを用いてボールを拭いてもよい。次に、ディスクおよびボールが取り付けられた滑り摩擦試験機を使用して、ディスクのDLC摺動面に対し、1mLの潤滑剤を滴下したうえで前記ボールを10Nの荷重で当接させつつディスク周方向に相対的に10mm/sの速度で更に90m滑動させ、滑り距離10~100mの当該滑動中、ディスクおよびボールのDLC摺動面間の摩擦係数を測定する。
摩耗量算出方法:前記摩擦試験を経た前記ボールに形成されている円形状摩耗痕を共焦点顕微鏡を使用して観察し、当該観察像から、前記円形状摩耗痕について一様に滑らかな平面であると仮定したうえで直径r(mm)を求める。そして、下記の式(1)および式(2)によりボール摩耗体積V(mm3)を算出する。式(1)におけるhは、前記円形状摩耗痕の球冠の高さ(mm)であり、下記式(2)より求められる。式(2)におけるRは、前記ボールの半径であって4(mm)である。
Friction test: First, a disk with a diameter of 30 mm and a thickness of 4 mm having a DLC sliding surface formed by a 3 μm thick DLC film on the surface and a 8 mm diameter with a DLC sliding surface formed by a 3 μm thick DLC film on the surface Using a ball-on-disk type sliding friction tester fitted with a ball, drop 1 mL of the initial bonding agent onto the DLC sliding surface of the disk, and place the ball in a load of 10 N While sliding 10 m relatively at a velocity of 10 mm / s in the circumferential direction of the disk, the coefficient of friction between the DLC sliding surfaces of the disk and the ball is measured during the sliding with a sliding distance of 0 to 10 m. The disc and ball are then removed from the sliding friction tester and ultrasonic cleaned. After washing, the ball may be wiped with acetone to remove nanodiamonds attached to the ball. Next, using a sliding friction tester fitted with a disc and a ball, 1 mL of a lubricant is dropped onto the DLC sliding surface of the disc, and then the ball is abutted with a load of 10 N while the disc circumference The sliding is carried out for a further 90 m at a speed of 10 mm / s relative to the direction, and the friction coefficient between the DLC sliding surface of the disc and the ball is measured during the sliding with a sliding distance of 10 to 100 m.
Wear amount calculation method: A circular wear mark formed on the ball subjected to the friction test is observed using a confocal microscope, and from the observation image, a uniformly smooth plane is obtained for the circular wear mark. Assuming that there is a diameter r (mm) is determined. And ball wear volume V (mm < 3 >) is computed by following formula (1) and Formula (2). H in Formula (1) is height (mm) of the ball crown of the said circular shaped abrasion mark, and is calculated | required from following formula (2). R in Formula (2) is a radius of the said ball, and is 4 (mm).
本発明は、ND粒子が爆轟法ナノダイヤモンド粒子の酸素酸化処理物であってもよい。爆轟法によると、一次粒子の粒径が10nm以下のNDを適切に生じさせることが可能である。 In the present invention, the ND particles may be an oxygen oxidation treatment of detonation nano diamond particles. According to the detonation method, it is possible to appropriately generate an ND having a primary particle size of 10 nm or less.
本発明は、NDのゼータ電位がネガティブであってもよい。 In the present invention, the zeta potential of ND may be negative.
本発明は、ND粒子のFT-IRにおけるC=O伸縮振動に帰属されるピーク位置が1750cm-1以上であってもよい。 In the present invention, the peak position attributed to the C = O stretching vibration in the FT-IR of the ND particles may be 1750 cm −1 or more.
本発明は、ND粒子が爆轟法ナノダイヤモンド粒子の水素還元処理物であってもよい。爆轟法によると、一次粒子の粒径が10nm以下のNDを適切に生じさせることが可能である。 In the present invention, the ND particles may be a hydrogen reduction treatment product of the detonation nano diamond particles. According to the detonation method, it is possible to appropriately generate an ND having a primary particle size of 10 nm or less.
本発明は、NDのゼータ電位がポジティブであってもよい。 In the present invention, the zeta potential of ND may be positive.
本発明は、ND粒子のFT-IRにおけるC=O伸縮振動に帰属されるピーク位置が1750cm-1未満であってもよい。 In the present invention, the peak position attributed to the C = O stretching vibration in the FT-IR of the ND particles may be less than 1750 cm −1 .
本発明は、初期なじみ剤および潤滑剤における潤滑基剤が水であることが好ましい。 In the present invention, it is preferable that the lubricant base in the initial adjustor and lubricant is water.
本発明の第2の側面によると潤滑システム用液剤セットが提供される。この潤滑システム用液剤セットは、濃度0.01~2質量%のナノダイヤモンド粒子を含有する初期なじみ剤と、濃度0.001質量%以下のナノダイヤモンド粒子を含有する潤滑剤とを備える。第2の側面による潤滑システム用液剤セットは、第1の側面による潤滑システムに使用することができる。当該潤滑システム用液剤セットを用いることは、DLC摺動面において、低摩擦面を早期に形成し、当該低摩擦面を維持でき、摺動面における摩耗を低減するのに適する。つまり、潤滑システム用液剤セットは、DLC摺動面において、低摩擦および低摩耗を実現するのに適する。 According to a second aspect of the present invention, there is provided a fluid system set for a lubrication system. The liquid lubricant set for lubricating system comprises an initial blender containing nanodiamond particles with a concentration of 0.01 to 2% by mass, and a lubricant containing nanodiamond particles with a concentration of 0.001% by mass or less. The fluid system set for lubrication system according to the second aspect can be used for the lubrication system according to the first aspect. Using the liquid lubricant set for the lubricating system can form a low friction surface early on the DLC sliding surface, maintain the low friction surface, and is suitable for reducing wear on the sliding surface. That is, the lubricant system solution set is suitable for achieving low friction and low wear on the DLC sliding surface.
本発明の潤滑システムは、相対的に高濃度のND粒子を含有する初期なじみ剤を使用して低摩擦化されたDLC摺動面の潤滑に、相対的に低濃度のND粒子を含有する潤滑剤を使用する。本発明の潤滑システム用液剤セットは、当該潤滑システムに用いるものであり、上記の初期なじみ剤と潤滑剤とを備える。摺動面は、例えば、機械における軸と軸受け部の接触面のように、相対的な動きによりこすれながら滑り合う面を意味する。 The lubrication system of the present invention comprises a relatively low concentration of ND particles in the lubrication of a low friction DLC sliding surface using an initial conformant containing a relatively high concentration of ND particles. Use the agent. The liquid agent set for lubricating system of the present invention is used for the lubricating system, and includes the above-mentioned initial conformant and lubricant. The sliding surface means, for example, a surface that rubs against and slides due to relative movement, such as a contact surface of a shaft and a bearing in a machine.
初期なじみ剤は、ND粒子が潤滑基剤に分散した溶液(分散液)である。初期なじみ剤のND粒子濃度は、例えば0.01~2質量%、好ましくは0.03~1.0質量%、より好ましくは0.05~0.8質量%、より好ましくは0.07~0.6質量%、より好ましくは0.08~0.4質量%である。初期なじみ剤のND粒子濃度が上記範囲であると、DLC摺動面におけるND粒子が存在する系でのトライボ化学反応によって、平滑性と濡れ性とを兼ね備えた面を早期に形成するのに適する。 The initial adhesion agent is a solution (dispersion liquid) in which the ND particles are dispersed in a lubricant base. The ND particle concentration of the initial conformant is, for example, 0.01 to 2% by mass, preferably 0.03 to 1.0% by mass, more preferably 0.05 to 0.8% by mass, more preferably 0.07 to It is 0.6% by mass, more preferably 0.08 to 0.4% by mass. It is suitable for early formation of a surface having both smoothness and wettability by tribochemical reaction in a system in which ND particles exist on the sliding surface of the DLC, when the ND particle concentration of the initial conformant is in the above range .
潤滑剤は、ND粒子が潤滑基剤に分散した溶液(分散液)である。潤滑剤のND粒子濃度は、例えば0.001質量%以下(1.0×10-5~1.0×10-3質量%)、好ましくは3.0×10-5~5.0×10-4質量%、より好ましくは5.0×10-5~3.0×10-4質量%、より好ましくは8.0×10-5~2.0×10-4質量%である。潤滑剤のND粒子濃度が上記範囲であると、初期なじみ剤により形成したDLC摺動面における平滑性と濡れ性を維持し、摺動面における摩擦および摩耗を低減するのに適する。 The lubricant is a solution (dispersion liquid) in which ND particles are dispersed in a lubricant base. The ND particle concentration of the lubricant is, for example, 0.001 mass% or less (1.0 × 10 −5 to 1.0 × 10 −3 mass%), preferably 3.0 × 10 −5 to 5.0 × 10 It is -4 % by mass, more preferably 5.0 × 10 -5 to 3.0 × 10 -4 % by mass, more preferably 8.0 × 10 -5 to 2.0 × 10 -4 % by mass. When the ND particle concentration of the lubricant is in the above range, it is suitable for maintaining the smoothness and the wettability on the DLC sliding surface formed by the initial bonding agent, and reducing the friction and the wear on the sliding surface.
初期なじみ剤および潤滑剤に含有されるND粒子は、一次粒子として、初期なじみ剤および潤滑剤中にて互いに離隔して分散している。ND一次粒子の粒径は、例えば10nm以下である。NDの一次粒子の粒径の下限は、例えば1nmである。ND一次粒子の粒径D50(メディアン径)は、例えば10nm以下、好ましくは9nm以下、より好ましくは8nm以下、より好ましくは7nm以下、より好ましくは6nm以下である。ND一次粒子の粒径D50は、例えば動的光散乱法によって測定することが可能である。 The ND particles contained in the initial conformant and lubricant are dispersed as primary particles in the initial conformant and lubricant separately from each other. The particle size of the ND primary particles is, for example, 10 nm or less. The lower limit of the particle size of primary particles of ND is, for example, 1 nm. The particle diameter D50 (median diameter) of the ND primary particles is, for example, 10 nm or less, preferably 9 nm or less, more preferably 8 nm or less, more preferably 7 nm or less, more preferably 6 nm or less. The particle size D50 of the ND primary particles can be measured, for example, by dynamic light scattering.
ND粒子は、好ましくは、爆轟法ND粒子(爆轟法によって生成したND粒子)である。爆轟法によると、一次粒子の粒径が10nm以下のNDを適切に生じさせることが可能である。 The ND particles are preferably detonation method ND particles (ND particles produced by detonation method). According to the detonation method, it is possible to appropriately generate an ND having a primary particle size of 10 nm or less.
ND粒子は、爆轟法ND粒子の酸素酸化処理物であってもよい。当該酸素酸化処理物の場合、ND粒子のFT-IRにおけるC=O伸縮振動に帰属されるピーク位置が1750cm-1以上となる傾向があり、このときのND粒子のゼータ電位はネガティブとなる傾向がある。爆轟法ND粒子の酸素酸化処理については、後記の製造過程における酸素酸化工程に記載のとおりである。 The ND particles may be an oxygen oxidation treatment of detonation method ND particles. In the case of the oxidized oxidized product, the peak position attributed to CCO stretching vibration in the FT-IR of the ND particles tends to be 1750 cm -1 or more, and the zeta potential of the ND particles tends to be negative at this time. There is. The oxygen oxidation treatment of the detonation method ND particles is as described in the oxygen oxidation step in the production process described later.
また、ND粒子は、爆轟法ND粒子の水素還元処理物であってもよい。当該水素還元処理物である場合、ND粒子のFT-IRにおけるC=O伸縮振動に帰属されるピーク位置が1750cm-1未満となる傾向があり、このときのND粒子のゼータ電位はポジティブとなる傾向がある。爆轟法ND粒子の水素還元処理については、後記の製造過程における水素還元処理工程に記載のとおりである。 Further, the ND particles may be a hydrogen reduction treatment product of the detonation method ND particles. In the case of the hydrogen reduction product, the peak position attributed to the C = O stretching vibration in the FT-IR of the ND particles tends to be less than 1750 cm −1, and the zeta potential of the ND particles at this time becomes positive. Tend. The hydrogen reduction treatment of the detonation method ND particles is as described in the hydrogen reduction treatment step in the production process described later.
ND粒子のいわゆるゼータ電位がネガティブの場合の値は、例えば-60~-30mVである。例えば、製造過程において、後記のように酸素酸化処理の温度条件を比較的に高温(例えば400~450℃)とすることで、ND粒子についてネガティブのゼータ電位とすることができる。また、ゼータ電位がポジティブの場合の値は、例えば30~60mVである。例えば、製造過程において、後記のように酸素酸化工程の後に水素還元処理工程を行うことで、ND粒子についてポジティブのゼータ電位とすることができる。 The value when the so-called zeta potential of the ND particles is negative is, for example, -60 to -30 mV. For example, in the production process, as described later, by setting the temperature condition of the oxygen oxidation treatment to a relatively high temperature (for example, 400 to 450 ° C.), the negative zeta potential can be obtained for the ND particles. The value when the zeta potential is positive is, for example, 30 to 60 mV. For example, by performing a hydrogen reduction treatment step after an oxygen oxidation step as described later in the manufacturing process, it is possible to obtain a positive zeta potential for the ND particles.
初期なじみ剤および潤滑剤は、後記の方法で得られたND分散液と、潤滑基剤などの所望の成分とを混合することで製造することができる。上記ND分散液は、例えば、下記の生成工程S1と、精製工程S2と、酸素酸化工程S3と、解砕工程S4とを含む過程を経て作製することができる。 The initial conformant and lubricant can be produced by mixing the ND dispersion obtained by the method described later with a desired component such as a lubricant base. The ND dispersion can be produced, for example, through a process including the following production process S1, purification process S2, oxygen oxidation process S3, and crushing process S4.
生成工程S1では、例えば爆轟法によって、ナノダイヤモンドを生じさせる。具体的には、まず、成形された爆薬に電気雷管が装着されたものを爆轟用の耐圧性容器の内部に設置し、容器内において所定の気体と使用爆薬とが共存する状態で、容器を密閉する。容器は例えば鉄製で、容器の容積は、例えば0.5~40m3である。爆薬としては、トリニトロトルエン(TNT)とシクロトリメチレントリニトロアミンすなわちヘキソーゲン(RDX)との混合物を使用することができる。TNTとRDXの質量比(TNT/RDX)は、例えば40/60~60/40の範囲とされる。爆薬の使用量は、例えば0.05~2.0kgである。使用爆薬とともに容器内に密閉される上記の気体は、大気組成を有してもよいし、不活性ガスであってもよい。一次粒子表面の官能基量の少ないナノダイヤモンドを生じさせるという観点からは、使用爆薬とともに容器内に密閉される上記気体は、不活性ガスであるのが好ましい。すなわち、一次粒子表面の官能基量の少ないナノダイヤモンドを生じさせるという観点からは、ナノダイヤモンドを生じさせるための爆轟法は不活性ガス雰囲気下で行われるのが好ましい。当該不活性ガスとしては、例えば、窒素、アルゴン、二酸化炭素、およびヘリウムから選択される少なくとも一つを用いることができる。 In the production step S1, nanodiamonds are produced, for example, by detonation. Specifically, first, a shaped explosive provided with an electric detonator is installed inside a pressure-resistant container for detonation, and in a state in which a predetermined gas and the used explosive coexist in the container, the container Seal the The container is, for example, made of iron, and the volume of the container is, for example, 0.5 to 40 m 3 . As an explosive, a mixture of trinitrotoluene (TNT) and cyclotrimethylene trinitroamine or hexogen (RDX) can be used. The mass ratio of TNT to RDX (TNT / RDX) is, for example, in the range of 40/60 to 60/40. The amount of explosive used is, for example, 0.05 to 2.0 kg. The above-mentioned gas sealed in the container together with the explosive used may have an atmospheric composition or may be an inert gas. From the viewpoint of producing nanodiamonds having a small amount of functional groups on the primary particle surface, the above-mentioned gas sealed in the container together with the used explosive is preferably an inert gas. That is, from the viewpoint of producing nanodiamond having a small amount of functional groups on the primary particle surface, detonation for producing nanodiamond is preferably carried out under an inert gas atmosphere. As the inert gas, for example, at least one selected from nitrogen, argon, carbon dioxide, and helium can be used.
生成工程S1では、次に、電気雷管を起爆させ、容器内で爆薬を爆轟させる。爆轟とは、化学反応に伴う爆発のうち反応の生じる火炎面が音速を超えた高速で移動するものをいう。爆轟の際、使用爆薬が部分的に不完全燃焼を起こして遊離した炭素を原料として、爆発で生じた衝撃波の圧力とエネルギーの作用によってナノダイヤモンドが生成する。爆轟法によると、上述のように、一次粒子の粒径が10nm以下のナノダイヤモンドを適切に生じさせることが可能である。ナノダイヤモンドは、爆轟法により得られる生成物にて先ずは、隣接する一次粒子ないし結晶子の間がファンデルワールス力の作用に加えて結晶面間クーロン相互作用が寄与して非常に強固に集成し、凝着体をなす。 Next, in the generation step S1, the electric detonator is detonated and the explosive is detonated in the container. A detonation refers to an explosion associated with a chemical reaction in which the flame surface on which the reaction occurs travels at a high speed beyond the speed of sound. At the time of detonation, the used explosive partially burns incompletely and liberated carbon is used as a raw material to generate nano diamond by the action of pressure and energy of shock wave generated by explosion. According to the detonation method, as described above, it is possible to appropriately generate nanodiamonds having a primary particle size of 10 nm or less. The nano diamond is a product obtained by the detonation method, which is very strongly due to the Coulomb interaction between the adjacent primary particles or crystallites in addition to the action of van der Waals force. Assemble and form a cohesive body.
生成工程S1では、次に、室温での例えば24時間の放置により、容器およびその内部を降温させる。この放冷の後、ナノダイヤモンド粗生成物を回収する。例えば、容器の内壁に付着しているナノダイヤモンド粗生成物(上述のようにして生成したナノダイヤモンドの凝着体と煤を含む)をヘラで掻き取る作業によって、ナノダイヤモンド粗生成物を回収することができる。以上のような爆轟法によって、ナノダイヤモンド粒子の粗生成物を得ることができる。また、以上のような生成工程S1を必要回数行うことによって、所望量のナノダイヤモンド粗生成物を取得することが可能である。 Next, in the production step S1, the container and the inside thereof are cooled by leaving at room temperature, for example, for 24 hours. After this cooling, the nanodiamond crude product is recovered. For example, the nanodiamond crude product is recovered by scraping off the nanodiamond crude product adhering to the inner wall of the container (including the agglomerates and wrinkles of the nanodiamond produced as described above) with a spatula be able to. By the detonation method as described above, a crude product of nanodiamond particles can be obtained. Moreover, it is possible to acquire a desired amount of nano diamond crude products by performing the above production processes S1 as many times as necessary.
精製工程S2は、本実施形態では、原料たるナノダイヤモンド粗生成物に例えば水溶媒中で強酸を作用させる酸処理を含む。爆轟法で得られるナノダイヤモンド粗生成物には金属酸化物が含まれやすいところ、この金属酸化物は、爆轟法に使用される容器等に由来するFe,Co,Ni等の酸化物である。例えば水溶媒中で所定の強酸を作用させることにより、ナノダイヤモンド粗生成物から金属酸化物を溶解・除去することができる(酸処理)。この酸処理に用いられる強酸としては、鉱酸が好ましく、例えば、塩酸、フッ化水素酸、硫酸、硝酸、および王水が挙げられる。酸処理では、一種類の強酸を用いてもよいし、二種類以上の強酸を用いてもよい。酸処理で使用される強酸の濃度は例えば1~50質量%である。酸処理温度は例えば70~150℃である。酸処理時間は例えば0.1~24時間である。また、酸処理は、減圧下、常圧下、または加圧下で行うことが可能である。このような酸処理の後、例えばデカンテーションにより、固形分(ナノダイヤモンド凝着体を含む)の水洗を行う。沈殿液のpHが例えば2~3に至るまで、デカンテーションによる当該固形分の水洗を反復して行うのが好ましい。爆轟法で得られるナノダイヤモンド粗生成物における金属酸化物の含有量が少ない場合には、以上のような酸処理を省略してもよい。 In the present embodiment, the purification step S2 includes an acid treatment in which a crude acid, which is a raw material of the raw nanodiamond material, is reacted with a strong acid in an aqueous solvent, for example. A crude nanodiamond product obtained by the detonation method is likely to contain metal oxides, and this metal oxide is an oxide such as Fe, Co, Ni, etc. derived from the container etc. used for the detonation method. is there. For example, the metal oxide can be dissolved and removed from the crude nanodiamond product by reacting with a predetermined strong acid in an aqueous solvent (acid treatment). The strong acid used for the acid treatment is preferably a mineral acid, and examples thereof include hydrochloric acid, hydrofluoric acid, sulfuric acid, nitric acid, and aqua regia. In the acid treatment, one strong acid may be used, or two or more strong acids may be used. The concentration of the strong acid used in the acid treatment is, for example, 1 to 50% by mass. The acid treatment temperature is, for example, 70 to 150.degree. The acid treatment time is, for example, 0.1 to 24 hours. In addition, the acid treatment can be performed under reduced pressure, normal pressure, or increased pressure. After such acid treatment, washing with water (including nano-diamond aggregates) of the solid content is performed by, for example, decantation. It is preferable to repeat the washing of the solid content by decantation repeatedly until the pH of the precipitate reaches, for example, 2 to 3. When the content of the metal oxide in the nanodiamond crude product obtained by the detonation method is small, the above acid treatment may be omitted.
精製工程S2は、本実施形態では、酸化剤を用いてナノダイヤモンド粗生成物(精製終了前のナノダイヤモンド凝着体)からグラファイトやアモルファス炭素等の非ダイヤモンド炭素を除去するための溶液酸化処理を含む。爆轟法で得られるナノダイヤモンド粗生成物にはグラファイト(黒鉛)やアモルファス炭素等の非ダイヤモンド炭素が含まれているところ、この非ダイヤモンド炭素は、使用爆薬が部分的に不完全燃焼を起こして遊離した炭素のうちナノダイヤモンド結晶を形成しなかった炭素に由来する。例えば上記の酸処理を経た後に、水溶媒中で所定の酸化剤などを作用させることにより、ナノダイヤモンド粗生成物から非ダイヤモンド炭素を除去することができる(溶液酸化処理)。この溶液酸化処理に用いられる酸化剤としては、例えば、クロム酸、無水クロム酸、二クロム酸、過マンガン酸、過塩素酸、及びこれらの塩、硝酸、並びに混酸(硫酸と硝酸の混合物)が挙げられる。溶液酸化処理では、一種類の酸化剤を用いてもよいし、二種類以上の酸化剤を用いてもよい。溶液酸化処理で使用される酸化剤の濃度は、例えば3~50質量%である。溶液酸化処理における酸化剤の使用量は、溶液酸化処理に付されるナノダイヤモンド粗生成物100質量部に対して例えば300~2000質量部である。溶液酸化処理温度は例えば50~250℃である。溶液酸化処理時間は、例えば1~72時間である。溶液酸化処理は、減圧下、常圧下、または加圧下で行うことが可能である。このような溶液酸化処理の後、例えばデカンテーションにより、固形分(ナノダイヤモンド凝着体を含む)の水洗を行う。水洗当初の上澄み液は着色しているところ、上澄み液が目視で透明になるまで、デカンテーションによる当該固形分の水洗を反復して行うのが好ましい。 In the purification step S2, in the present embodiment, a solution oxidation treatment for removing non-diamond carbon such as graphite and amorphous carbon from a nanodiamond crude product (nanodiamond adhesion body before completion of purification) using an oxidizing agent is used. Including. The crude diamond product obtained by the detonation method contains non-diamond carbon such as graphite (graphite) and amorphous carbon. This non-diamond carbon causes partial burnout of the used explosive partially. It originates in carbon which did not form nano diamond crystals among the liberated carbon. For example, after the above-mentioned acid treatment, non-diamond carbon can be removed from the nanodiamond crude product by acting a predetermined oxidizing agent or the like in an aqueous solvent (solution oxidation treatment). Examples of oxidizing agents used for this solution oxidation treatment include chromic acid, chromic anhydride, dichromic acid, permanganic acid, perchloric acid, salts thereof, nitric acid, and mixed acids (a mixture of sulfuric acid and nitric acid). It can be mentioned. In the solution oxidation treatment, one type of oxidizing agent may be used, or two or more types of oxidizing agents may be used. The concentration of the oxidizing agent used in the solution oxidation treatment is, for example, 3 to 50% by mass. The amount of the oxidizing agent used in the solution oxidation treatment is, for example, 300 to 2000 parts by mass with respect to 100 parts by mass of the nanodiamond crude product subjected to the solution oxidation treatment. The solution oxidation treatment temperature is, for example, 50 to 250.degree. The solution oxidation treatment time is, for example, 1 to 72 hours. Solution oxidation treatment can be performed under reduced pressure, normal pressure or increased pressure. After such solution oxidation treatment, washing with solids (including nano-diamond aggregates) is performed, for example, by decantation. It is preferable to repeatedly carry out washing of the solid content by decantation until the supernatant liquid is colored at the beginning of washing until the supernatant liquid is visually clear.
本処理を経たナノダイヤモンド含有溶液から、例えばデカンテーションによって上澄みが除かれた後、残留画分について乾燥処理に付して乾燥粉体を得る。乾燥処理の手法としては、例えば、噴霧乾燥装置を使用して行う噴霧乾燥や、エバポレーターを使用して行う蒸発乾固が挙げられる。 After the supernatant is removed from the nanodiamond-containing solution subjected to this treatment, for example, by decantation, the remaining fraction is subjected to a drying treatment to obtain a dry powder. Examples of the drying treatment include spray drying using a spray drying apparatus and evaporation to dryness using an evaporator.
次の酸素酸化工程S3では、精製工程S2を経たナノダイヤモンドの粉体について、ガス雰囲気炉を使用して、酸素を含有する所定組成のガス雰囲気下にて加熱する。具体的には、ガス雰囲気炉内にナノダイヤモンド粉体が配され、当該炉に対して酸素含有ガスが供給ないし通流され、加熱温度として設定された温度条件まで当該炉内が昇温されて、酸素酸化処理が実施される。この酸素酸化処理の温度条件は、例えば250~500℃である。作製されるND分散液に含まれるND粒子について、ネガティブのゼータ電位を実現するためには、この酸素酸化処理の温度条件は、比較的に高温であるのが好ましく、例えば400~450℃である。また、本実施形態で用いられる酸素含有ガスは、酸素に加えて不活性ガスを含有する混合ガスである。不活性ガスとしては、例えば、窒素、アルゴン、二酸化炭素、およびヘリウムが挙げられる。当該混合ガスの酸素濃度は、例えば1~35体積%である。 In the next oxygen oxidation step S3, the nanodiamond powder that has undergone the purification step S2 is heated in a gas atmosphere of a predetermined composition containing oxygen, using a gas atmosphere furnace. Specifically, nanodiamond powder is disposed in a gas atmosphere furnace, oxygen-containing gas is supplied or flowed to the furnace, and the temperature in the furnace is raised to the temperature condition set as the heating temperature. , Oxygen oxidation treatment is carried out. The temperature condition of this oxygen oxidation treatment is, for example, 250 to 500.degree. In order to realize a negative zeta potential for the ND particles contained in the ND dispersion to be produced, the temperature conditions of this oxygen oxidation treatment are preferably relatively high, for example, 400 to 450 ° C. . Further, the oxygen-containing gas used in the present embodiment is a mixed gas containing an inert gas in addition to oxygen. Inert gases include, for example, nitrogen, argon, carbon dioxide, and helium. The oxygen concentration of the mixed gas is, for example, 1 to 35% by volume.
作製されるND分散液に含まれるND粒子についてポジティブのゼータ電位を実現するためには、好ましくは、上述の酸素酸化工程S3の後に水素還元処理工程S3’を行う。水素還元処理工程S3’では、酸素酸化工程S3を経たナノダイヤモンドの粉体について、ガス雰囲気炉を使用して、水素を含有する所定組成のガス雰囲気下にて加熱する。具体的には、ナノダイヤモンド粉体が内部に配されているガス雰囲気炉に対して水素含有ガスが供給ないし通流され、加熱温度として設定された温度条件まで当該炉内が昇温されて、水素還元処理が実施される。この水素還元処理の温度条件は、例えば400~800℃である。また、本実施形態で用いられる水素含有ガスは、水素に加えて不活性ガスを含有する混合ガスである。不活性ガスとしては、例えば、窒素、アルゴン、二酸化炭素、およびヘリウムが挙げられる。当該混合ガスの水素濃度は、例えば1~50体積%である。作製されるND分散液に含まれるND粒子について、ネガティブのゼータ電位を実現するためには、このような水素還元処理工程を行わずに下記の解砕工程S4を行ってもよい。 In order to realize a positive zeta potential for the ND particles contained in the ND dispersion to be produced, preferably, a hydrogen reduction treatment step S3 'is performed after the above-described oxygen oxidation step S3. In the hydrogen reduction treatment step S3 ', the nanodiamond powder that has undergone the oxygen oxidation step S3 is heated in a gas atmosphere of a predetermined composition containing hydrogen using a gas atmosphere furnace. Specifically, a hydrogen-containing gas is supplied or flowed to a gas atmosphere furnace in which nanodiamond powder is disposed inside, and the temperature in the furnace is raised to the temperature condition set as the heating temperature, Hydrogen reduction treatment is performed. The temperature conditions of this hydrogen reduction treatment are, for example, 400 to 800.degree. The hydrogen-containing gas used in the present embodiment is a mixed gas containing an inert gas in addition to hydrogen. Inert gases include, for example, nitrogen, argon, carbon dioxide, and helium. The hydrogen concentration of the mixed gas is, for example, 1 to 50% by volume. In order to realize a negative zeta potential for the ND particles contained in the ND dispersion to be produced, the following crushing step S4 may be performed without performing such a hydrogen reduction treatment step.
以上のような一連の過程を経て精製等された後であっても、爆轟法ナノダイヤモンドは、凝着体(二次粒子)の形態をとる場合があり、更に凝着体から一次粒子を分離させるために、次に解砕工程S4が行われる。具体的には、まず、酸素酸化工程S3またはその後の水素還元処理工程S3’を経たナノダイヤモンドを純水に懸濁し、ナノダイヤモンドを含有するスラリーが調製される。スラリーの調製にあたっては、比較的に大きな集成体をナノダイヤモンド懸濁液から除去するために遠心分離処理を行ってもよいし、ナノダイヤモンド懸濁液に超音波処理を施してもよい。そして、当該スラリーが湿式の解砕処理に付される。解砕処理は、例えば、高剪断ミキサー、ハイシアーミキサー、ホモミキサー、ボールミル、ビーズミル、高圧ホモジナイザー、超音波ホモジナイザー、またはコロイドミルを使用して行うことができる。これらを組み合わせて解砕処理を実施してもよい。効率性の観点からはビーズミルを使用するのが好ましい。 Even after purification through a series of processes as described above, detonation nanodiamonds may take the form of an aggregate (secondary particles), and further primary particles from the aggregate. Next, a crushing step S4 is performed to separate. Specifically, first, nanodiamonds that have undergone the oxygen oxidation step S3 or the subsequent hydrogen reduction treatment step S3 'are suspended in pure water to prepare a slurry containing nanodiamonds. In preparing the slurry, centrifugation may be performed to remove relatively large assemblies from the nanodiamond suspension, or the nanodiamond suspension may be subjected to ultrasonication. Then, the slurry is subjected to a wet crushing process. The crushing process can be performed using, for example, a high shear mixer, a high shear mixer, a homomixer, a ball mill, a bead mill, a high pressure homogenizer, an ultrasonic homogenizer, or a colloid mill. The crushing process may be performed by combining these. From the viewpoint of efficiency, it is preferable to use a bead mill.
粉砕装置ないし分散機たるビーズミルは、例えば、円筒形状のミル容器と、ローターピンと、遠心分離機構と、原料タンクと、ポンプとを具備する。ローターピンは、ミル容器と共通の軸心を有してミル容器内部で高速回転可能に構成されている。遠心分離機構は、ミル容器内の上部に配されている。解砕工程におけるビーズミルによるビーズミリングでは、ミル容器内に所定量のビーズが充填され且つローターピンが当該ビーズを撹拌している状態で、ポンプの作用によって原料タンクからミル容器の下部に原料としての上記スラリー(ナノダイヤモンド凝着体を含む)が投入される。スラリーは、ミル容器内でビーズが高速撹拌されている中を通ってミル容器内の上部に到達する。この過程で、スラリーに含まれているナノダイヤモンド凝着体は、激しく運動しているビーズとの接触によって粉砕ないし分散化の作用を受ける。これにより、ナノダイヤモンドの凝着体(二次粒子)から一次粒子への解砕が進む。ミル容器内の上部の遠心分離機構に到達したスラリーとビーズは、稼働する遠心分離機構によって比重差を利用した遠心分離がなされ、ビーズはミル容器内に留まり、スラリーは、遠心分離機構に対して摺動可能に連結された中空ラインを経由してミル容器外に排出される。排出されたスラリーは、原料タンクに戻され、その後、ポンプの作用によって再びミル容器に投入される(循環運転)。このようなビーズミリングにおいて、使用される解砕メディアは例えばジルコニアビーズであり、ビーズの直径は、例えば15~500μmである。ミル容器内に充填されるビーズの量(見掛け体積)は、ミル容器の容積に対して、例えば50~80%である。ローターピンの周速は、例えば8~12m/分である。循環させるスラリーの量は例えば200~600mLであり、スラリーの流速は例えば5~15L/時間である。また、処理時間(循環運転時間)は、例えば30~300分間である。本実施形態においては、以上のような連続式のビーズミルに代えてバッチ式のビーズミルを使用してもよい。 The bead mill, which is a pulverizer or disperser, includes, for example, a cylindrical mill container, a rotor pin, a centrifugal separator, a raw material tank, and a pump. The rotor pin has a common axis with the mill container and is configured to be rotatable at high speed inside the mill container. The centrifuge system is disposed at the top in the mill vessel. In bead milling using a bead mill in the crushing step, as a predetermined amount of beads is filled in the mill container and the rotor pins are stirring the beads, the action of the pump acts as a raw material from the raw material tank to the lower part of the mill container. The above-mentioned slurry (including nano-diamond aggregates) is introduced. The slurry passes through the rapidly stirred beads in the mill vessel to reach the top in the mill vessel. In this process, the nano-diamond aggregates contained in the slurry are subjected to the action of crushing or dispersion by contact with the vigorously moving beads. As a result, the disintegration of the nano-diamond agglomerates (secondary particles) into primary particles proceeds. The slurry and the beads that reached the upper centrifuge in the mill vessel are centrifuged using the specific gravity difference by the operating centrifuge, the beads remain in the mill vessel, and the slurry It is discharged out of the mill container via a hollow line slidably connected. The discharged slurry is returned to the raw material tank and then introduced again into the mill container by the action of the pump (circulation operation). In such bead milling, the crushing media used is, for example, zirconia beads, and the diameter of the beads is, for example, 15 to 500 μm. The amount (apparent volume) of beads packed in the mill vessel is, for example, 50 to 80% of the volume of the mill vessel. The circumferential speed of the rotor pin is, for example, 8 to 12 m / min. The amount of slurry to be circulated is, for example, 200 to 600 mL, and the flow rate of the slurry is, for example, 5 to 15 L / hour. Further, the processing time (circulation operation time) is, for example, 30 to 300 minutes. In the present embodiment, a batch-type bead mill may be used instead of the continuous-type bead mill as described above.
このような解砕工程S4を経ることによって、ナノダイヤモンド一次粒子を含有するND分散液を得ることができる。解砕工程S4を経て得られる分散液については、粗大粒子を除去するための分級操作を行ってもよい。例えば分級装置を使用して、遠心分離を利用した分級操作によって分散液から粗大粒子を除去することができる。これにより、ナノダイヤモンドの一次粒子がコロイド粒子として分散する例えば黒色透明のND分散液が得られる。 Through such a crushing step S4, an ND dispersion containing nanodiamond primary particles can be obtained. The dispersion obtained through the crushing step S4 may be subjected to classification operation for removing coarse particles. For example, using a classifier, coarse particles can be removed from the dispersion by classification using centrifugation. Thereby, for example, a black transparent ND dispersion in which primary particles of nanodiamond are dispersed as colloidal particles is obtained.
初期なじみ剤および潤滑剤における潤滑基剤としては、極性溶媒または非極性溶媒が挙げられる。極性溶媒としては、水、メタノール、エタノール、プロパノール、ブタノール、多官能基アルコール(エチレングリコール、プロピレングリコール、ネオペンチルグリコール、トリメチロールプロパン、ペンタエリスリトール等)、およびこれらの混合溶媒などが挙げられる。また、非極性溶媒としては、合成油(ポリ-α-オレフィン、アルキルナフタレン、ポリブデンなど)、鉱物油、合成炭化水素油、エステル油(ポリオールエステル、ジエステル、コンプレックスエステルなど)、シリコーン油、フッ素油、ひまし油およびこれらの混合溶媒などが挙げられる。なかでも初期なじみ剤および潤滑剤における潤滑基剤としては、水が好ましい。 Lubricants in initial conformers and lubricants include polar solvents or nonpolar solvents. Examples of the polar solvent include water, methanol, ethanol, propanol, butanol, polyfunctional alcohols (ethylene glycol, propylene glycol, neopentyl glycol, trimethylolpropane, pentaerythritol and the like), mixed solvents thereof and the like. Moreover, as nonpolar solvents, synthetic oils (poly-α-olefin, alkyl naphthalene, polybuden etc.), mineral oils, synthetic hydrocarbon oils, ester oils (polyol esters, diesters, complex esters etc), silicone oils, fluorine oils And castor oil and mixed solvents thereof. Among them, water is preferred as a lubricant for the initial adjustor and lubricant.
初期なじみ剤における潤滑基剤の含有率は、本実施形態では例えば98質量%以上であり、好ましくは99質量%以上、より好ましくは99.5質量%以上、より好ましくは99.9質量%以上である。 In the embodiment, the content of the lubricant base in the initial fitting agent is, for example, 98% by mass or more, preferably 99% by mass or more, more preferably 99.5% by mass or more, and more preferably 99.9% by mass or more It is.
潤滑剤における潤滑基剤の含有率は、本実施形態では例えば99.9質量%以上であり、好ましくは99.95質量%以上、より好ましくは99.99質量%以上、より好ましくは99.999質量%以上である。 In the embodiment, the content of the lubricant base in the lubricant is, for example, 99.9% by mass or more, preferably 99.95% by mass or more, more preferably 99.99% by mass or more, and more preferably 99.999%. It is mass% or more.
初期なじみ剤および潤滑剤は、ND粒子および潤滑基剤に加えて他の成分を含有してもよい。他の成分としては、例えば、界面活性剤、増粘剤、カップリング剤、潤滑対象部材たる金属部材の錆止めのための防錆剤、潤滑対象部材たる非金属部材の腐食抑制のための腐食防止剤、凝固点降下剤、消泡剤、耐摩耗添加剤、防腐剤、着色料、およびND粒子以外の固体潤滑剤が挙げられる。 Initial conformers and lubricants may contain other components in addition to the ND particles and lubricant base. Other components include, for example, surfactants, thickeners, coupling agents, rust inhibitors for rusting of metal members to be lubricated, and corrosion prevention for suppressing corrosion of non-metal members to be lubricated. Agents, freezing point depressants, antifoam agents, antiwear additives, preservatives, colorants, and solid lubricants other than ND particles.
本発明の潤滑システムでは、初期なじみ剤をDLC摺動面に適量加え、あらかじめ摩擦(予滑り)をする。その後、潤滑剤の存在下、DLC摺動面を更に摺動(滑動)させる。本発明の潤滑システムは、例えば、機械における滑り軸受(ベアリング)等の摺動面における摩擦係数および摩耗を低減するのに適する。本発明の潤滑システムは、初期なじみ剤を使用したときのND粒子が作用する系でのトライボ化学反応により、DLC摺動面の濡れ性向上や平滑化が早期に進行するものと考えられ、DLC摺動面が早期に低摩擦化する傾向にある。また、潤滑剤を使用することにより、DLC摺動面の摩耗が抑制されつつ低摩擦性が維持される傾向にある。よって、本発明の潤滑システムは、DLC摺動面において低摩擦および低摩耗を実現するのに適するのである。相対的に高濃度のナノダイヤモンド粒子を含有する初期なじみ剤における粒子濃度は、好ましくは0.01~2質量%であり、相対的に低濃度のナノダイヤモンド粒子を含有する潤滑剤における粒子濃度は、好ましくは0.001質量%以下である。 In the lubrication system of the present invention, a suitable amount of initial welding agent is added to the DLC sliding surface, and friction (pre-slip) is performed in advance. Thereafter, the DLC sliding surface is further slid (sliding) in the presence of the lubricant. The lubrication system of the present invention is suitable, for example, to reduce the coefficient of friction and wear on sliding surfaces such as sliding bearings in machines. In the lubrication system of the present invention, it is considered that the wettability improvement and the smoothing of the DLC sliding surface proceed at an early stage due to the tribochemical reaction in the system where the ND particles act when the initial conformant is used. The sliding surface tends to reduce friction early. In addition, the use of a lubricant tends to maintain low friction while suppressing wear of the DLC sliding surface. Thus, the lubrication system of the present invention is suitable for achieving low friction and low wear on the DLC sliding surface. The particle concentration in the initial habituation agent containing relatively high concentration of nanodiamond particles is preferably 0.01 to 2% by mass, and the particle concentration in the lubricant containing relatively low concentration of nanodiamond particles is , Preferably 0.001 mass% or less.
下記の摩擦試験は、例えば、機械におけるDLC摺動面を有する滑り軸受(ベアリング)を模した試験である。下記摩擦試験で測定される摺動面の摩擦係数は0.05以下(より好ましくは0.03以下)であり、且つ摩擦試験後の下記摩耗量算出方法により求めるボール摩耗体積は1.0×10-4mm3以下(より好ましくは7.0×10-5mm3以下)であることが好ましい。
摩擦試験:まず、厚さ3μmのDLC膜がなすDLC摺動面を表面に有する直径30mmおよび厚さ4mmのディスクと、厚さ3μmのDLC膜がなすDLC摺動面を表面に有する直径8mmのボールとが取り付けられた、ボールオンディスク型の滑り摩擦試験機を使用して、ディスクのDLC摺動面に対し、1mLの初期なじみ剤を滴下したうえでボールを10Nの荷重で当接させつつディスク周方向に相対的に10mm/sの速度で10m滑動させ、滑り距離0~10mの当該滑動中、ディスクおよびボールのDLC摺動面間の摩擦係数を測定する。次に、ディスクおよびボールを、滑り摩擦試験機から取り外し、超音波洗浄する。洗浄後、ボールに付着したナノダイヤモンドを除去するためにアセトンを用いてボールを拭いてもよい。次に、ディスクおよびボールが取り付けられた滑り摩擦試験機を使用して、ディスクのDLC摺動面に対し、1mLの前記潤滑剤を滴下したうえで前記ボールを10Nの荷重で当接させつつディスク周方向に相対的に10mm/sの速度で更に90m滑動させ、滑り距離10~100mの当該滑動中、前記ディスクおよび前記ボールのDLC摺動面間の摩擦係数を測定する。
摩耗量算出方法:前記摩擦試験を経た前記ボールに形成されている円形状摩耗痕を共焦点顕微鏡を使用して観察し、当該観察像から、円形状摩耗痕について一様に滑らかな平面であると仮定したうえで直径r(mm)を求める。そして、下記の式(1)および式(2)によりボール摩耗体積V(mm3)を算出する。式(1)におけるhは、前記円形状摩耗痕の球冠の高さ(mm)であり、下記式(2)より求められる。式(2)におけるRは、前記ボールの半径であって4(mm)である。
Friction test: First, a disk with a diameter of 30 mm and a thickness of 4 mm having a DLC sliding surface formed by a 3 μm thick DLC film on the surface and a 8 mm diameter with a DLC sliding surface formed by a 3 μm thick DLC film on the surface Using a ball-on-disk sliding friction tester fitted with a ball, 1 mL of the initial bonding agent is dropped onto the DLC sliding surface of the disk and then the ball is brought into contact with a load of 10 N The disk is slid 10 m relatively at a velocity of 10 mm / s in the circumferential direction of the disk, and the coefficient of friction between the DLC sliding surface of the disk and the ball is measured during the sliding at a sliding distance of 0-10 m. The disc and ball are then removed from the sliding friction tester and ultrasonic cleaned. After washing, the ball may be wiped with acetone to remove nanodiamonds attached to the ball. Next, using a sliding friction tester fitted with a disk and a ball, 1 mL of the lubricant is dropped onto the DLC sliding surface of the disk and then the ball is abutted with a load of 10 N The sliding is further performed 90 m in the circumferential direction relatively at a speed of 10 mm / s, and the coefficient of friction between the disk and the DLC sliding surface of the ball is measured during the sliding at a sliding distance of 10 to 100 m.
Wear amount calculation method: A circular wear mark formed on the ball subjected to the friction test is observed using a confocal microscope, and from the observation image, it is a plane that is uniformly smooth about the circular wear mark. Assuming that the diameter r (mm) is determined. And ball wear volume V (mm < 3 >) is computed by following formula (1) and Formula (2). H in Formula (1) is height (mm) of the ball crown of the said circular shaped abrasion mark, and is calculated | required from following formula (2). R in Formula (2) is a radius of the said ball, and is 4 (mm).
DLC摺動面におけるダイヤモンドライクカーボン(DLC)膜は、主として炭化水素、あるいは、炭素の同素体から成る非晶質(アモルファス)の硬質膜である。DLCは、水素含有量の多少と、含まれる結晶質の電子軌道がダイヤモンド寄りかグラファイト寄りかによって、その性質を区別することができる。DLCとしては、例えば、アモルファス水素化カーボンであるa-C:H、アモルファスカーボンであるa-C、テトラヘドラルアモルファスカーボンであるta-C:H、および水素化テトラヘドラルアモルファスカーボンであるta-Cが挙げられる。 The diamond like carbon (DLC) film on the DLC sliding surface is an amorphous (amorphous) hard film mainly composed of a hydrocarbon or an allotrope of carbon. DLC can distinguish its properties depending on the hydrogen content and whether the crystalline electron orbits contained are close to diamond or close to graphite. As DLC, for example, amorphous hydrogenated carbon aC: H, amorphous carbon aC, tetrahedral amorphous carbon ta-C: H, and hydrogenated tetrahedral amorphous carbon ta -C is mentioned.
[ナノダイヤモンド水分散液の作製]
以下のような生成工程、精製工程、酸素酸化工程、および解砕工程を経て、ナノダイヤモンド水分散液X1(ND水分散液)を作製した。
[Preparation of nano diamond aqueous dispersion]
A nanodiamond aqueous dispersion X1 (ND aqueous dispersion) was produced through the following production steps, purification steps, oxygen oxidation steps, and crushing steps.
生成工程では、まず、成形された爆薬に電気雷管が装着されたものを爆轟用の耐圧性容器の内部に設置して容器を密閉した。容器は鉄製で、容器の容積は15m3である。爆薬としては、トリニトロトルエン(TNT)とシクロトリメチレントリニトロアミンすなわちヘキソーゲン(RDX)との混合物0.50kgを使用した。当該爆薬におけるTNTとRDXの質量比(TNT/RDX)は、50/50である。次に、電気雷管を起爆させ、容器内で爆薬を爆轟させた。次に、室温での24時間の放置により、容器およびその内部を降温させた。この放冷の後、容器の内壁に付着しているナノダイヤモンド粗生成物(上記爆轟法で生成したナノダイヤモンド粒子の凝着体と煤を含む)を回収した。上述の生成工程を複数回行うことによってナノダイヤモンド粗生成物を得た。 In the production step, first, a shaped explosive provided with an electric detonator was installed inside a pressure-resistant container for detonation to seal the container. The container is made of iron and the volume of the container is 15 m 3 . As an explosive, 0.50 kg of a mixture of trinitrotoluene (TNT) and cyclotrimethylene trinitroamine or hexogen (RDX) was used. The mass ratio of TNT to RDX (TNT / RDX) in the explosive is 50/50. Next, the electric detonator was detonated and the explosive was detonated in the container. Next, the container and its inside were cooled by leaving at room temperature for 24 hours. After this cooling, a crude nanodiamond product (including the agglomerates and wrinkles of nanodiamond particles produced by the above detonation method) attached to the inner wall of the vessel was recovered. The nanodiamond crude product was obtained by performing the above-mentioned production process a plurality of times.
次に、上記生成工程で得たナノダイヤモンド粗生成物に対して、精製工程の酸処理を行った。具体的には、当該ナノダイヤモンド粗生成物200gに6Lの10質量%塩酸を加えて得られたスラリーに対し、常圧条件での還流下で1時間の加熱処理を行った。この酸処理における加熱温度は85~100℃である。次に、冷却後、デカンテーションにより、固形分(ナノダイヤモンド凝着体と煤を含む)の水洗を行った。沈殿液のpHが低pH側から2に至るまで、デカンテーションによる当該固形分の水洗を反復して行った。次に、精製工程の溶液酸化処理としての混酸処理を行った。具体的には、酸処理後のデカンテーションを経て得た沈殿液(ナノダイヤモンド凝着体を含む)に、6Lの98質量%硫酸水溶液と1Lの69質量%硝酸水溶液とを加えてスラリーとした後、このスラリーに対し、常圧条件での還流下で48時間の加熱処理を行った。この酸化処理における加熱温度は、140~160℃である。次に、冷却後、デカンテーションにより、固形分(ナノダイヤモンド凝着体を含む)の水洗を行った。水洗当初の上澄み液は着色しているところ、上澄み液が目視で透明になるまで、デカンテーションによる当該固形分の水洗を反復して行った。次に、乾燥工程を行った。具体的には、上述の水洗処理を経て得られたナノダイヤモンド含有液1000mLを、噴霧乾燥装置(商品名「スプレードライヤー B-290」,日本ビュッヒ株式会社製)を使用して噴霧乾燥に付した。これにより、50gのナノダイヤモンド粉体を得た。 Next, acid treatment of the purification step was performed on the nanodiamond crude product obtained in the above generation step. Specifically, the slurry obtained by adding 6 L of 10% by mass hydrochloric acid to 200 g of the crude nanodiamond product was subjected to heat treatment under reflux under normal pressure conditions for 1 hour. The heating temperature in this acid treatment is 85 to 100.degree. Next, after cooling, decantation was performed to wash the solid content (including nano-diamond aggregates and soot) with water. The solid was repeatedly washed with water by decantation until the pH of the precipitate reached 2 from the low pH side. Next, mixed acid treatment was performed as solution oxidation treatment in the purification step. Specifically, 6 L of a 98 mass% aqueous sulfuric acid solution and a 1 L of 69 mass% aqueous nitric acid solution were added to a precipitation solution (including nanodiamond agglutinate) obtained through decantation after acid treatment to form a slurry Thereafter, the slurry was subjected to heat treatment for 48 hours under reflux under normal pressure conditions. The heating temperature in this oxidation treatment is 140 to 160.degree. Next, after cooling, the solid content (including nano-diamond aggregates) was washed with water by decantation. The supernatant liquid at the beginning of washing with water was colored, and the washing of the solid content by decantation was repeated until the supernatant was visually clear. Next, a drying step was performed. Specifically, 1000 mL of the nanodiamond-containing liquid obtained through the above-mentioned water washing treatment was subjected to spray drying using a spray dryer (trade name "SPRAY DRYER B-290, manufactured by Nippon Buchi Co., Ltd.) . This gave 50 g of nanodiamond powder.
次に、ガス雰囲気炉(商品名「ガス雰囲気チューブ炉 KTF045N1」,光洋サーモシステム株式会社製)を使用して酸素酸化工程を行った。具体的には、上述のようにして得られたナノダイヤモンド粉体4.5gをガス雰囲気炉の炉心管内に静置し、炉心管に窒素ガスを流速1L/分で30分間通流させ続けた後、通流ガスを窒素から酸素と窒素との混合ガスへと切り替えて当該混合ガスを流速1L/分で炉心管に通流させ続けた。混合ガス中の酸素濃度は4体積%である。混合ガスへの切り替えの後、炉内を加熱設定温度たる400℃まで昇温させた。昇温速度については、加熱設定温度より20℃低い380℃までは10℃/分とし、その後の380℃から400℃までは1℃/分とした。そして、炉内の温度条件を400℃に維持しつつ、炉内のナノダイヤモンド粉体について酸素酸化処理を行った。処理時間は3時間とした。 Next, an oxygen oxidation step was performed using a gas atmosphere furnace (trade name “gas atmosphere tube furnace KTF045N1” manufactured by Koyo Thermo System Co., Ltd.). Specifically, 4.5 g of nano diamond powder obtained as described above was allowed to stand still in the core tube of a gas atmosphere furnace, and nitrogen gas was allowed to flow through the core tube at a flow rate of 1 L / min for 30 minutes. Thereafter, the flow gas was switched from nitrogen to a mixed gas of oxygen and nitrogen, and the mixed gas was allowed to flow through the core tube at a flow rate of 1 L / min. The oxygen concentration in the mixed gas is 4% by volume. After switching to the mixed gas, the temperature in the furnace was raised to 400 ° C., which is the heating set temperature. The temperature rising rate was 10 ° C./min up to 380 ° C., which is 20 ° C. lower than the heating set temperature, and then 1 ° C./min from 380 ° C. to 400 ° C. Then, while maintaining the temperature condition in the furnace at 400 ° C., the oxygen oxidation treatment was performed on the nano diamond powder in the furnace. The processing time was 3 hours.
酸素酸化処理後、後記の方法でFT-IR分析により、ND粒子におけるカルボキシ基等の含酸素官能基の評価を行った。この分析で得られたスペクトルを図5に示す。図5より、C=O伸縮振動に帰属される1780cm-1付近に吸収P1がメインピークとして検出された。このピーク位置が1750cm-1以上になっていることで、ゼータ電位がネガティブのナノダイヤ分散液の原料になりうる。 After the oxygen oxidation treatment, evaluation of an oxygen-containing functional group such as a carboxy group in the ND particles was carried out by FT-IR analysis by the method described later. The spectrum obtained by this analysis is shown in FIG. From FIG. 5, C = O stretching absorption near 1780 cm -1 attributable to the vibration P 1 has been detected as a main peak. When the peak position is 1750 cm −1 or more, the zeta potential can be a raw material of the nanodiamond dispersion having a negative.
次に、解砕工程を行った。具体的には、まず、酸素酸化工程を経たナノダイヤモンド粉体1.8gと純水28.2mLとを50mLのサンプル瓶内で混合し、スラリー約30mLを得た。次に、当該スラリーについて、1Mの水酸化ナトリウム水溶液の添加によりpHを調整した後、超音波処理を施した。超音波処理においては、超音波照射器(商品名「超音波洗浄機 AS-3」,アズワン(AS ONE)社製)を使用して、当該スラリーに対して2時間の超音波照射を行った。この後、ビーズミリング装置(商品名「並列四筒式サンドグラインダー LSG-4U-2L型」,アイメックス株式会社製)を使用してビーズミリングを行った。具体的には、100mLのミル容器たるベッセル(アイメックス株式会社製)に対して超音波照射後のスラリー30mLと直径30μmのジルコニアビーズとを投入して封入し、装置を駆動させてビーズミリングを実行した。このビーズミリングにおいて、ジルコニアビーズの投入量は、ミル容器の容積に対して約33%であり、ミル容器の回転速度は2570rpmであり、ミリング時間は2時間である。次に、このような解砕工程を経たスラリーないし懸濁液について、遠心分離装置を使用して遠心分離処理を行った(分級操作)。この遠心分離処理における遠心力は20000×gとし、遠心時間は10分間とした。次に、当該遠心分離処理を経たナノダイヤモンド含有溶液の上清10mLを回収した。このようにして、初期なじみ剤組成物および潤滑剤の原液である、ナノダイヤモンドが純水に分散するND水分散液を得た。このND水分散液について、固形分濃度ないしナノダイヤモンド濃度は59.1g/L、pHは9.33であった。粒径D50(メディアン径)は3.97nm、粒径D90は7.20nm、ゼータ電位は-42mVであった。 Next, the crushing process was performed. Specifically, first, 1.8 g of nanodiamond powder that had undergone an oxygen oxidation step and 28.2 mL of pure water were mixed in a 50 mL sample bottle to obtain about 30 mL of a slurry. Next, the pH of the slurry was adjusted by the addition of a 1 M aqueous solution of sodium hydroxide, and then ultrasonication was applied. In the ultrasonic treatment, the slurry was subjected to ultrasonic irradiation for 2 hours using an ultrasonic irradiator (trade name “ultrasonic cleaner AS-3”, manufactured by AS ONE) . Thereafter, bead milling was performed using a bead milling apparatus (trade name “parallel four-cylinder sand grinder LSG-4U-2L type”, manufactured by Imex Co., Ltd.). Specifically, 30 mL of the slurry after ultrasonic wave irradiation and zirconia beads with a diameter of 30 μm are charged into 100 mL of a mill container, vessel (manufactured by IMEX Co., Ltd.), and sealed, and the device is driven to execute bead milling. did. In this bead milling, the input amount of zirconia beads is about 33% of the volume of the mill vessel, the rotation speed of the mill vessel is 2570 rpm, and the milling time is 2 hours. Next, the slurry or suspension subjected to such a crushing step was subjected to centrifugation using a centrifugal separator (classification operation). The centrifugal force in this centrifugation was 20000 × g, and the centrifugation time was 10 minutes. Next, 10 mL of the supernatant of the nanodiamond-containing solution subjected to the centrifugation treatment was collected. In this way, an ND aqueous dispersion in which nanodiamonds are dispersed in pure water, which is a stock solution of the initial adjustability composition and the lubricant, was obtained. With respect to this ND aqueous dispersion, the solid content concentration to the nanodiamond concentration was 59.1 g / L, and the pH was 9.33. The particle diameter D50 (median diameter) was 3.97 nm, the particle diameter D90 was 7.20 nm, and the zeta potential was -42 mV.
〈ナノダイヤモンド濃度〉
得られたND水分散液のナノダイヤモンド含有量(ND濃度)は、秤量した分散液3~5gの当該秤量値と、当該秤量分散液から加熱によって水分を蒸発させた後に残留する乾燥物(粉体)について精密天秤によって秤量した値とに基づき、算出した。
<Nano diamond concentration>
The nanodiamond content (ND concentration) of the obtained ND aqueous dispersion is the weighing value of 3 to 5 g of the weighed dispersion, and the dried product remaining after evaporation of the water from the weighing dispersion by heating (powder Body) was calculated based on the value measured by a precision balance.
〈粒径〉
得られたND水分散液に含まれるナノダイヤモンド粒子の粒径(メディアン径、D50ないしD90)は、Malvern社製の装置(商品名「ゼータサイザー ナノZS」)を使用して、動的光散乱法(非接触後方散乱法)によって測定した。測定に付されたND水分散液は、固形分濃度ないしナノダイヤモンド濃度が0.5~2.0質量%となるように超純水で希釈された後に超音波洗浄機による超音波照射を経たものである。
<Particle size>
The particle diameter (median diameter, D50 to D90) of the nanodiamond particles contained in the obtained ND aqueous dispersion is determined by dynamic light scattering using an apparatus manufactured by Malvern (trade name "Zetasizer Nano ZS"). It was measured by the method (noncontact backscattering method). The ND aqueous dispersion subjected to measurement was subjected to ultrasonic irradiation by an ultrasonic cleaner after being diluted with ultrapure water so that the solid content concentration or nano diamond concentration would be 0.5 to 2.0 mass%. It is a thing.
〈pH〉
得られたND水分散液のpHは、pH試験紙(商品名「スリーバンドpH試験紙」、アズワン株式会社製)を使用して測定した。
<PH>
The pH of the obtained ND aqueous dispersion was measured using pH test paper (trade name "Sleeve Band pH test paper", manufactured by As One Corporation).
〈ゼータ電位〉
得られたND水分散液に含まれるナノダイヤモンド粒子のゼータ電位は、Malvern社製の装置(商品名「ゼータサイザー ナノZS」)を使用して、レーザードップラー式電気泳動法によって測定した。測定に付されたND水分散液X1およびY1は、固形分濃度ないしナノダイヤモンド濃度が0.2質量%となるように超純水で希釈された後に超音波洗浄機による超音波照射を経たものであり、ゼータ電位測定温度は25℃である。
<Zeta potential>
The zeta potential of the nano diamond particles contained in the obtained ND aqueous dispersion was measured by a laser Doppler electrophoresis method using a device manufactured by Malvern (trade name "Zeta Sizer Nano ZS"). The ND aqueous dispersions X1 and Y1 subjected to the measurement were subjected to ultrasonic irradiation by an ultrasonic cleaner after being diluted with ultrapure water so that the solid content concentration to nano diamond concentration would be 0.2 mass%. And the zeta potential measurement temperature is 25.degree.
〈FT-IR分析〉
上述の酸素酸化処理後のナノダイヤモンド試料のそれぞれについて、FT-IR装置(商品名「Spectrum400型FT-IR」,株式会社パーキンエルマージャパン製)を使用して、フーリエ変換赤外分光分析(FT-IR)を行った。本測定においては、測定対象たる試料を真空雰囲気下で150℃に加熱しつつ赤外吸収スペクトルを測定した。真空雰囲気下の加熱は、エス・ティ・ジャパン社製のModel-HC900型Heat ChamberとTC-100WA型Thermo Controllerとを併用して実現した。
<FT-IR Analysis>
Fourier transform infrared spectroscopy (FT-IR) (FT-IR apparatus (trade name "Spectrum 400 type FT-IR", manufactured by PerkinElmer Japan Co., Ltd.) for each of the above-described oxygen-oxidized nano diamond samples using Fourier transform infrared spectroscopy (FT- IR) was done. In this measurement, the infrared absorption spectrum was measured while heating a sample to be measured at 150 ° C. in a vacuum atmosphere. Heating under a vacuum atmosphere was realized by using ST-Japan Japan Model-HC900 Heat Chamber and TC-100WA Thermo Controller in combination.
[初期なじみ剤および潤滑剤の作製]
上記で得られたND水分散液と、超純水とを混合して濃度調整することで、ND粒子を0.1質量%含む初期なじみ剤およびND粒子を0.0001質量%含む潤滑剤を作製した。
[Preparation of initial conformant and lubricant]
The ND aqueous dispersion obtained above and the ultrapure water are mixed to adjust the concentration, whereby an initial conformant containing 0.1% by mass of ND particles and a lubricant containing 0.0001% by mass of ND particles are mixed. Made.
[実施例1:摩擦試験]
摩擦試験には、ボールオンディスク型滑り摩擦試験機を用いた。直径8mmのSUJ2製のボール、および、直径30mm,厚さ4mmのSUJ2製のディスクを母材として、ボールおよびディスクの表面に東研サーモテック社のDLC膜を約3μm成膜した。試験開始時にディスク表面に上記初期なじみ剤を1mL滴下し、初期なじみ(予滑り)として、ディスク上でボールを10Nの荷重をかけながら、速度10mm/sで10m滑動させた。その後、ボールとディスクを摩擦試験機から取り外し、15分間精製水中で超音波洗浄を行った。洗浄後、アセトンでボールを拭くことにより、ボールに付着したナノダイヤモンドを除去した。その後、ボールとディスクを摩擦試験機に取り付け、上記潤滑剤を使用し、更に速度10mm/sで90m滑動させた。実施例1の摩擦試験について、滑り距離[m]を横軸、摩擦係数を縦軸としたグラフを図3に、滑り距離[m]を横軸、ボール摩耗体積(摩耗量)[mm3]を縦軸としたグラフを図4に示す。図3において、滑り距離10mに見られる摩擦係数0を下端とし、0.10付近を上端とする線は、潤滑剤を使用して滑動を再開したときのノイズであり、本試験で測定される摩擦係数には含まれないものとする。
Example 1: Friction Test
For the friction test, a ball-on-disk sliding friction tester was used. Using a SUJ2 ball of 8 mm in diameter and a SUJ2 disk of 30 mm in diameter and 4 mm in thickness as a base material, a DLC film of about 3 μm was formed on the surface of the ball and the disk. At the start of the test, 1 mL of the initial adhesion agent was dropped on the disc surface, and the ball was allowed to slide 10 m at a speed of 10 mm / s while applying a load of 10 N on the disc. The ball and disc were then removed from the friction tester and subjected to ultrasonic cleaning in purified water for 15 minutes. After washing, the nano diamond attached to the ball was removed by wiping the ball with acetone. After that, the ball and the disc were attached to a friction tester, and the above lubricant was used to slide 90 m at a speed of 10 mm / s. Friction test of Example 1, the horizontal axis sliding distance [m], a graph in which the ordinate the coefficient of friction in Figure 3, the horizontal axis sliding distance [m], Ball Wear volume (amount of wear) [mm 3] The graph which made y vertical axis | shaft is shown in FIG. In FIG. 3, the line with the lower end of the coefficient of
[比較例1:摩擦試験]
上記初期なじみ剤および潤滑剤の代わりに、ナノダイヤモンド粒子を含まない水を使用したこと以外は、実施例1と同様にして、摩擦試験を行った。比較例1の摩擦試験について、滑り距離[m]を横軸、摩擦係数を縦軸としたグラフを図2に、滑り距離[m]を横軸、上記の式(1)および式(2)から求められるボール摩耗体積(摩耗量)[mm3]を縦軸としたグラフを図4に示す。
Comparative Example 1: Friction Test
The friction test was conducted in the same manner as in Example 1 except that water containing no nanodiamond particles was used instead of the above-mentioned initial conformant and lubricant. In the friction test of Comparative Example 1, a graph in which the sliding distance [m] is taken along the horizontal axis and the friction coefficient is taken along the vertical axis is shown in FIG. 2; the sliding distance [m] is taken along the horizontal axis; The graph which made the vertical axis | shaft the ball | bowl wear volume (wear amount) [mm < 3 >] calculated | required from these is shown in FIG.
比較例1の摩擦試験(図2)では、滑り距離が増すにつれて徐々に摩擦係数が上昇することが分かる。一方、初期なじみ剤および潤滑剤を使用した実施例1の摩擦試験(図3)では、滑り距離100mにおいて比較例1ほどの摩擦係数の上昇は見られず、低摩擦を維持していることが分かる。つまり、初期なじみ剤を使用することで10mという短い予滑により、早期に低摩擦面を形成することができ、潤滑剤を使用することで、その後の90mの滑動において、低摩擦面を維持することができたことが分かる。また、図4より、水のみを使用した比較例1においては、摩耗量があまり上昇せず、摩耗が抑制できるが、ND粒子を用いている実施例1でも滑り距離10~90mにおいて、比較例1と同程度に摩耗を抑制できることが分かる。 In the friction test of Comparative Example 1 (FIG. 2), it can be seen that the coefficient of friction gradually increases as the sliding distance increases. On the other hand, in the friction test of Example 1 (FIG. 3) using the initial conformant and lubricant, no increase in the coefficient of friction as in Comparative Example 1 was observed at a sliding distance of 100 m, and low friction was maintained. I understand. In other words, the use of the initial conformer enables the early formation of a low friction surface with a short pre-slip of 10 m, and the use of a lubricant maintains the low friction surface in the subsequent 90 m of sliding motion. I know that I was able to do it. Further, according to FIG. 4, in Comparative Example 1 in which only water is used, the amount of wear does not increase so much and wear can be suppressed, but even in Example 1 in which ND particles are used, the sliding distance is 10 to 90 m. It can be seen that the wear can be suppressed to the same extent as 1.
以上のまとめとして、本発明の構成およびそのバリエーションを以下に付記として列記する。 As a summary of the above, the configuration of the present invention and the variations thereof are listed below as a supplementary note.
〔付記1〕
相対的に高濃度のナノダイヤモンド粒子を含有する初期なじみ剤を使用して低摩擦化されたDLC摺動面の潤滑に、相対的に低濃度のナノダイヤモンド粒子を含有する潤滑剤を使用する、潤滑システム。
〔付記2〕
前記初期なじみ剤のナノダイヤモンド粒子濃度は、0.01~2質量%である、付記1に記載の潤滑システム。
〔付記3〕
前記潤滑剤のナノダイヤモンド粒子濃度は、0.001質量%以下である、付記1または2に記載の潤滑システム。
〔付記4〕
下記摩擦試験で測定されるDLC摺動面の摩擦係数は0.05以下であり、且つ、下記摩擦試験後に摩耗量算出方法により求められるボール摩耗体積は1.0×10-4mm3以下である、付記1から3のいずれか一つに記載の潤滑システム(当該摩耗量算出方法は、本明細書に記載のとおりである)。
〔付記5〕
前記ナノダイヤモンド粒子の一次粒子の粒径は10nm以下である、付記1から4のいずれか一つに記載の潤滑システム
〔付記6〕
前記ナノダイヤモンド粒子は、爆轟法ナノダイヤモンド粒子の酸素酸化処理物である、付記1から5のいずれか一つに記載の潤滑システム。
〔付記7〕
前記ナノダイヤモンド粒子のゼータ電位はネガティブである、請求項1から6のいずれか一つに記載の潤滑システム。
〔付記8〕
前記ナノダイヤモンド粒子のゼータ電位は-60~-30mVである、付記7に記載の潤滑システム。
〔付記9〕
前記ナノダイヤモンド粒子のFT-IRにおけるC=O伸縮振動に帰属されるピーク位置が1750cm-1以上である、付記1から8のいずれか一つに記載の潤滑システム。
〔付記10〕
前記ナノダイヤモンド粒子は、爆轟法ナノダイヤモンド粒子の水素還元処理物である、請求項1から5のいずれか一つに記載の潤滑システム。
〔付記11〕
前記ナノダイヤモンド粒子のゼータ電位はポジティブである、付記1から5および10のいずれか一つに記載の潤滑システム。
〔付記12〕
前記ナノダイヤモンド粒子のゼータ電位は30~60mVである、付記11に記載の潤滑システム。
〔付記13〕
前記ナノダイヤモンド粒子のFT-IRにおけるC=O伸縮振動に帰属されるピーク位置が1750cm-1未満である、付記1から5および10から12のいずれか一つに記載の潤滑システム。
〔付記14〕
前記初期なじみ剤および前記潤滑剤における潤滑基剤は水である、付記1から13のいずれか一つに記載の潤滑システム。
〔付記15〕
濃度0.01~2質量%のナノダイヤモンド粒子を含有する初期なじみ剤と、濃度0.001質量%以下のナノダイヤモンド粒子を含有する潤滑剤とを備える、潤滑システム用液剤セット。
[Supplementary Note 1]
Use a lubricant containing a relatively low concentration of nanodiamond particles for the lubrication of a low friction DLC sliding surface using an initial fluxing agent containing a relatively high concentration of nanodiamond particles Lubrication system.
[Supplementary Note 2]
The lubrication system according to any of the preceding claims, wherein the concentration of nano diamond particles of said initial conformant is 0.01-2 wt%.
[Supplementary Note 3]
The lubrication system according to
[Supplementary Note 4]
The friction coefficient of the DLC sliding surface measured by the following friction test is 0.05 or less, and the ball wear volume determined by the wear amount calculation method after the following friction test is 1.0 × 10 -4 mm 3 or less The lubricating system according to any one of
[Supplementary Note 5]
The lubrication system according to any one of
The lubrication system according to any one of
[Supplementary Note 7]
The lubrication system according to any one of
[Supplementary Note 8]
8. The lubrication system of clause 7, wherein the zeta potential of the nanodiamond particles is -60 to -30 mV.
[Supplementary Note 9]
11. The lubrication system according to any one of
[Supplementary Note 10]
The lubrication system according to any one of
[Supplementary Note 11]
10. The lubrication system according to any one of
[Supplementary Note 12]
15. The lubrication system of clause 11, wherein the zeta potential of the nanodiamond particles is 30 to 60 mV.
[Supplementary Note 13]
10. The lubrication system according to any one of
[Supplementary Note 14]
15. A lubrication system according to any one of the preceding claims, wherein the lubricant in the initial conformant and the lubricant is water.
[Supplementary Note 15]
A liquid agent set for a lubrication system comprising: an initial blender containing nanodiamond particles in a concentration of 0.01 to 2% by mass; and a lubricant containing nanodiamond particles in a concentration of 0.001% by mass or less.
S1 生成工程
S2 精製工程
S3 酸素酸化工程
S3’ 水素還元処理工程
S4 解砕工程
S1 generation process S2 purification process S3 oxygen oxidation process S3 'hydrogen reduction treatment process S4 crushing process
Claims (12)
摩擦試験:まず、厚さ3μmのDLC膜がなすDLC摺動面を表面に有する直径30mmおよび厚さ4mmのディスクと、厚さ3μmのDLC膜がなすDLC摺動面を表面に有する直径8mmのボールとが取り付けられた、ボールオンディスク型の滑り摩擦試験機を使用して、前記ディスクのDLC摺動面に対し、1mLの前記初期なじみ剤を滴下したうえで前記ボールを10Nの荷重で当接させつつディスク周方向に相対的に10mm/sの速度で10m滑動させ、滑り距離0~10mの当該滑動中、前記ディスクおよび前記ボールのDLC摺動面間の摩擦係数を測定する。次に、前記ディスクおよび前記ボールを、前記滑り摩擦試験機から取り外し、超音波洗浄する。次に、洗浄後のディスクおよびボールが取り付けられた前記滑り摩擦試験機を使用して、前記ディスクのDLC摺動面に対し、1mLの前記潤滑剤を滴下したうえで前記ボールを10Nの荷重で当接させつつディスク周方向に相対的に10mm/sの速度で更に90m滑動させ、滑り距離10~100mの当該滑動中、前記ディスクおよび前記ボールのDLC摺動面間の摩擦係数を測定する。
摩耗量算出方法:前記摩擦試験を経た前記ボールに形成されている円形状摩耗痕を共焦点顕微鏡を使用して観察し、当該観察像から、前記円形状摩耗痕について一様に滑らかな平面であると仮定したうえで直径r(mm)を求める。そして、下記の式(1)および式(2)によりボール摩耗体積V(mm3)を算出する。式(1)におけるhは、前記円形状摩耗痕の球冠の高さ(mm)であり、下記式(2)より求められる。式(2)におけるRは、前記ボールの半径であって4(mm)である。
Friction test: First, a disk with a diameter of 30 mm and a thickness of 4 mm having a DLC sliding surface formed by a 3 μm thick DLC film on the surface and a 8 mm diameter with a DLC sliding surface formed by a 3 μm thick DLC film on the surface Using a ball-on-disk sliding friction tester equipped with a ball, 1 mL of the initial bonding agent was dropped onto the DLC sliding surface of the disk, and then the ball was loaded with a load of 10 N. The disc is slid 10 m relatively at a velocity of 10 mm / s in the circumferential direction of the disc while in contact with the disc, and the coefficient of friction between the disc and the DLC sliding surface of the ball is measured during the sliding of 0-10 m. The disc and the ball are then removed from the sliding friction tester and ultrasonic cleaned. Next, 1 mL of the lubricant is dropped onto the DLC sliding surface of the disk using the sliding friction tester with the cleaned disk and ball attached, and then the ball is loaded with a load of 10 N While making contact, slide 90 m relatively at a velocity of 10 mm / s in the circumferential direction of the disk, and measure the coefficient of friction between the DLC sliding surface of the disk and the ball during the sliding with a sliding distance of 10 to 100 m.
Wear amount calculation method: A circular wear mark formed on the ball subjected to the friction test is observed using a confocal microscope, and from the observation image, a uniformly smooth plane is obtained for the circular wear mark. Assuming that there is a diameter r (mm) is determined. And ball wear volume V (mm < 3 >) is computed by following formula (1) and Formula (2). H in Formula (1) is height (mm) of the ball crown of the said circular shaped abrasion mark, and is calculated | required from following formula (2). R in Formula (2) is a radius of the said ball, and is 4 (mm).
濃度0.001質量%以下のナノダイヤモンド粒子を含有する潤滑剤とを備える、潤滑システム用液剤セット。 An initial adjustor containing nanodiamond particles having a concentration of 0.01 to 2% by mass;
A liquid agent set for a lubrication system, comprising: a lubricant containing nanodiamond particles having a concentration of 0.001% by mass or less.
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| JPH0925110A (en) * | 1995-07-10 | 1997-01-28 | Ishizuka Kenkyusho:Kk | Hydrophilic diamond fine particles and method for producing the same |
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| JP3936724B1 (en) * | 2006-06-16 | 2007-06-27 | 有限会社アプライドダイヤモンド | Method for producing ultrafine diamond particle dispersion |
| JP2010255682A (en) * | 2009-04-22 | 2010-11-11 | Nsk Ltd | Method for preventing DLC film peeling of rolling sliding member, and method for using rolling support device |
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| WO2015163389A1 (en) * | 2014-04-24 | 2015-10-29 | 国立大学法人東北大学 | Sliding method, production method for sliding structure, sliding structure, and device |
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- 2018-10-25 JP JP2019552708A patent/JP7129068B2/en active Active
- 2018-10-25 WO PCT/JP2018/039647 patent/WO2019093142A1/en not_active Ceased
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| JPH0925110A (en) * | 1995-07-10 | 1997-01-28 | Ishizuka Kenkyusho:Kk | Hydrophilic diamond fine particles and method for producing the same |
| US5614477A (en) * | 1995-09-07 | 1997-03-25 | Kompan; Vladimir | Anti-friction additive and method for using same |
| JP3936724B1 (en) * | 2006-06-16 | 2007-06-27 | 有限会社アプライドダイヤモンド | Method for producing ultrafine diamond particle dispersion |
| JP2010255682A (en) * | 2009-04-22 | 2010-11-11 | Nsk Ltd | Method for preventing DLC film peeling of rolling sliding member, and method for using rolling support device |
| JP2013538274A (en) * | 2010-09-03 | 2013-10-10 | 株式会社ナノ炭素研究所 | Nano roller lubrication |
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| JP7129068B2 (en) | 2022-09-01 |
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