WO2007082299A2 - Nanoparticle compositions and methods for making and using the same - Google Patents

Nanoparticle compositions and methods for making and using the same Download PDF

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Publication number
WO2007082299A2
WO2007082299A2 PCT/US2007/060506 US2007060506W WO2007082299A2 WO 2007082299 A2 WO2007082299 A2 WO 2007082299A2 US 2007060506 W US2007060506 W US 2007060506W WO 2007082299 A2 WO2007082299 A2 WO 2007082299A2
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WIPO (PCT)
Prior art keywords
composition
milling
combination
oil
nanoparticles
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US2007/060506
Other languages
English (en)
French (fr)
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WO2007082299A3 (en
Inventor
Ajay P. Malshe
Arpana Verma
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
University of Arkansas at Fayetteville
University of Arkansas at Little Rock
Original Assignee
University of Arkansas at Fayetteville
University of Arkansas at Little Rock
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by University of Arkansas at Fayetteville, University of Arkansas at Little Rock filed Critical University of Arkansas at Fayetteville
Priority to US12/160,758 priority Critical patent/US8492319B2/en
Priority to CA2636932A priority patent/CA2636932C/en
Priority to EP07710113.7A priority patent/EP1973998B1/en
Priority to JP2008550538A priority patent/JP5603013B2/ja
Priority to MX2008009032A priority patent/MX2008009032A/es
Publication of WO2007082299A2 publication Critical patent/WO2007082299A2/en
Publication of WO2007082299A3 publication Critical patent/WO2007082299A3/en
Anticipated expiration legal-status Critical
Priority to US13/921,640 priority patent/US9499766B2/en
Priority to US14/173,369 priority patent/US9718967B2/en
Priority to US14/302,030 priority patent/US9902918B2/en
Priority to US14/816,546 priority patent/US9868920B2/en
Priority to US14/844,797 priority patent/US9650589B2/en
Priority to US15/675,231 priority patent/US10100266B2/en
Ceased legal-status Critical Current

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    • C10M169/04Mixtures of base-materials and additives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D3/00Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/08Groups 4 or 14
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/14Group 7
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2020/00Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01Physico-chemical properties
    • C10N2020/055Particles related characteristics
    • C10N2020/06Particles of special shape or size
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/06Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/56Boundary lubrication or thin film lubrication
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2050/00Form in which the lubricant is applied to the material being lubricated
    • C10N2050/023Multi-layer lubricant coatings
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2050/00Form in which the lubricant is applied to the material being lubricated
    • C10N2050/10Form in which the lubricant is applied to the material being lubricated semi-solid; greasy
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2070/00Specific manufacturing methods for lubricant compositions
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/29Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2982Particulate matter [e.g., sphere, flake, etc.]

Definitions

  • composition comprising solid lubricant nanoparticles and an organic medium.
  • nanoparticles comprising a layered material are disclosed.
  • a method of producing a nanoparticle comprising milling layered materials is provided.
  • a method of making a lubricant comprises milling layered materials to form nanoparticles and incorporating the nanoparticles into a base to form a lubricant.
  • Figure 1 is a diagram illustrating a method of producing solid lubricant nanoparticles.
  • Figure 2 is a diagram illustrating one method of preparing nanoparticle based lubricants.
  • Figure 3 shows transmission electron microscopy (TEM) micrographs of molybdenum disulphide particles.
  • Figure 3(A) shows molybdenum disulphide as it is available, typically from about a few microns to submicron size.
  • Figure 3(B) shows molybdenum disulphide that has been ball milled in air for 48 hours.
  • Figure 3(C) is a high resolution electron microscopy image that shows molybdenum disulphide that has been ball milled in air for 48 hours.
  • Figure 3(D) is a high-resolution transmission electron microscopy (HRTEM) image that shows molybdenum disulphide that has been ball milled in air for 48 hours followed by ball milling in oil for 48 hours.
  • HRTEM transmission electron microscopy
  • Figure 4 is a graph showing XRD spectra of molybdenum disulphide particles.
  • Figure 4(A) is the XRD spectra for molybdenum disulphide that has been ball milled in air for 48 hours followed by ball milling in oil for 48 hours.
  • Figure 4(B) is the XRD spectra for molybdenum disulphide that has been ball milled in air for 48 hours.
  • Figure 4(C) is the XRD spectra for molybdenum disulphide that has not been ball milled.
  • Figure 5 is a graph showing XPS spectra of molybdenum disulphide particles. The carbon peak for molybdenum disulphide that has not been ball milled is shown, as well as the carbon peak for molybdenum disulphide that has been ball milled in air for 48 hours, followed by ball milling in oil for 48 hours.
  • Figure 6 shows graphs and bar charts depicting tribological test data for different additives in paraffin oil.
  • Figure 6(A) shows the average wear scar diameter for a base oil (paraffin oil), paraffin oil with micron sized MoS 2 , paraffin oil with MoS 2 that was milled in air for 48 hours, and paraffin oil with MoS 2 that was milled in air for 48 hours followed by milling in canola oil for 48 hours.
  • Figure 6(B) shows the load wear index for paraffin oil without a nanoparticle additive, paraffin oil with micron sized MoS 2 , paraffin oil with MoS 2 that was milled in air for 48 hours, and paraffin oil with MoS 2 that was milled in air for 48 hours followed by milling in canola oil for 48 hours.
  • Figure 6(C) shows the COF for paraffin oil without a nanoparticle additive, paraffin oil with micron sized MoS 2 (C-MoS 2 ), paraffin oil with MoS 2 that was milled in air for 48 hours (d-MoS 2 ), and paraffin oil with MoS 2 that was milled in air for 48 hours followed by milling in canola oil for 48 hours (n- MoS 2 ).
  • Figure 6(D) shows the extreme pressure data for paraffin oil with micron sized MoS 2 (C-MoS 2 ), paraffin oil with MoS 2 that was milled in air for 48 hours (d-MoS 2 ), and paraffin oil with MoS 2 that was milled in air for 48 hours followed by milling in canola oil for 48 hours (n-MoS 2 ).
  • the solid lubricant nanoparticle additive was present in the amount of 1% by weight.
  • Figure 7 is a TEM image showing the architecture of molybdenum disulphide nanoparticles (15-70 nm average size).
  • Figure 7(A) shows the close caged dense oval shaped architecture of molybdenum disulphide nanoparticles that have been ball milled in air for 48 hours.
  • Figure 7(B) shows the open ended oval shaped architecture of molybdenum disulphide nanoparticles that have been ball milled in air for 48 hours followed by ball milling in canola oil for 48 hours.
  • Figure 8 is a graph depicting a comparison of wear scar diameters for different additives in paraffin oil.
  • One additive is crystalline molybdenum disulphide (C-MoS 2 ).
  • Another is molybdenum disulphide nanoparticles that were ball milled in air (n- MoS 2 ).
  • Another additive is molybdenum disulphide nanoparticles that were ball milled in air followed by ball milling in canola oil and to which a phospholipid emulsifier was added (n- MoS 2 + Emulsifier).
  • Figure 9 shows photographs and graphs produced using energy dispersive x-ray analysis (EDS) depicting the chemical analysis of wear scar diameters in four-ball tribological testing for nanoparticle based lubricants.
  • EDS energy dispersive x-ray analysis
  • Figure 9(A) shows paraffin oil without any nanoparticle composition additive.
  • Figure 9(B) shows paraffin oil with molybdenum disulphide nanoparticles that have been ball milled in air for 48 hours followed by ball milling in oil for 48 hours and treated with a phospholipid emulsifier.
  • any numerical range recited herein includes all values from the lower value to the upper value. For example, if a concentration range is stated as 1% to 50%, it is intended that values such as 2% to 40%, 10% to 30%, or 1% to 3%, etc., are expressly enumerated in this specification. These are only examples of what is specifically intended, and all possible combinations of numerical values between and including the lowest value and the highest value enumerated are to be considered to be expressly stated in this application.
  • compositions and methods for making compositions comprising solid lubricant nanoparticles and an organic medium are also described.
  • nanoparticles comprising layered materials.
  • the nanoparticles may be solid lubricant nanoparticles.
  • the nanoparticles may be made from starting materials or solid lubricant starting materials.
  • solid lubricants may include, but are not limited to, layered materials, suitably chalcogenides, more suitably, molybdenum disulphide, tungsten disulphide, or a combination thereof.
  • Another suitable layered material is graphite or intercalated graphite.
  • solid lubricants that may be used alone or in combination with the layered materials are polytetrafluoroethylene (Teflon ® ), boron nitride (suitably hexagonal boron nitride), soft metals (such as silver, lead, nickel, copper), cerium fluoride, zinc oxide, silver sulfate, cadmium iodide, lead iodide, barium fluoride, tin sulfide, zinc phosphate, zinc sulfide, mica, boron nitrate, borax, fluorinated carbon, zinc phosphide, boron, or a combination thereof.
  • Teflon ® polytetrafluoroethylene
  • boron nitride suitable hexagonal boron nitride
  • soft metals such as silver, lead, nickel, copper
  • cerium fluoride zinc oxide
  • silver sulfate cadmium iodide
  • lead iodide
  • Fluorinated carbons may be, without limitation, carbon-based materials such as graphite which has been fluorinated to improve its aesthetic characteristics. Such materials may include, for example, a material such as CF.sub.x wherein x ranges from about 0.05 to about 1.2. Such a material is produced by Allied Chemical under the trade name Accufluor. [0021]
  • the methods may include milling a solid lubricant feed.
  • the solid lubricant feed may be capable of being milled to particles comprising an average dimension of about 500 nanometers (submicron size) to about 10 nanometers.
  • the particles may have an average particle dimension of less than or equal to about 500 nanometers, suitably less than or equal to about 100 nanometers, suitably less than or equal to about 80 nanometers, and more suitably less than or equal to about 50 nanometers.
  • the ball milling may result in milled solid lubricant particles comprising a mixture, the mixture comprising particles having an average particle dimension of less than or equal to about 500 nanometers, plus larger particles.
  • Milling may include, among other things, ball milling and chemo mechanical milling. Examples of ball milling may include dry ball milling, wet ball milling, and combinations thereof.
  • Ball milling may refer to an impaction process that may include two interacting objects where one object maybe a ball, a rod, 4 pointed pins (jack shape), or other shapes.
  • Chemo mechanical milling may refer to an impaction process that may form a complex between an organic medium and a nanoparticle. As a result of chemo mechanical milling, the organic medium may coat, encapsulate, or intercalate the nanoparticles.
  • the solid lubricant feed may be dry milled and then wet milled.
  • An emulsifier may be mixed with a base and added to the wet milled particles. Dry milling may refer to particles that have been milled in the presence of a vacuum, a gas, or a combination thereof. Wet milling may refer to particles that have been milled in the presence of a liquid.
  • the solid lubricant nanoparticle composition may further comprise an organic medium.
  • organic mediums include, but are not limited to, oil mediums, grease mediums, alcohol mediums, or combinations thereof.
  • Specific examples of organic mediums include, but are not limited to, composite oil, canola oil, vegetable oils, soybean oil, corn oil, ethyl and methyl esters of rapeseed oil, distilled monoglycerides, monoglycerides, diglycerides, acetic acid esters of monoglycerides, organic acid esters of monoglycerides, sorbitan, sorbitan esters of fatty acids, propylene glycol esters of fatty acids, polyglycerol esters of fatty acids, n-hexadecane, hydrocarbon oils, phospholipids, or a combination thereof.
  • the composition may contain emulsifiers, surfactants, or dispersants.
  • emulsifiers may include, but are not limited to, emulsifiers having a hydrophilic-lipophilic balance (HLB) from about 2 to about 7; alternatively, a HLB from about 3 to about 5; or alternatively, a HLB of about 4.
  • HLB hydrophilic-lipophilic balance
  • emulsifiers may include, but are not limited to, lecithins, soy lecithins, phospholipids lecithins, detergents, distilled monoglycerides, monoglycerides, diglycerides, acetic acid esters of monoglycerides, organic acid esters of monoglycerides, sorbitan esters of fatty acids, propylene glycol esters of fatty acids, polyglycerol esters of fatty acids, compounds containing phosphorous, compounds containing sulfur, compounds containing nitrogen, or a combination thereof.
  • a method of making a lubricant is described.
  • the composition may be used as an additive dispersed in a base.
  • bases may include, but are not limited to, oils, greases, plastics, gels, sprays, or a combination thereof.
  • Specific examples of bases may include, but are not limited to, hydrocarbon oils, vegetable oils, corn oil, peanut oil, canola oil, soybean oil, mineral oil, paraffin oils, synthetic oils, petroleum gels, petroleum greases, hydrocarbon gels, hydrocarbon greases, lithium based greases, fluoroether based greases, ethylenebistearamide, waxes, silicones, or a combination thereof.
  • Described herein is a method of lubricating or coating an object that is part of an end application with a composition comprising at least one of solid lubricant nanoparticles and an organic medium. Further described is a method of lubricating an object by employing the composition comprising solid lubricant nanoparticles and an organic medium as a delivery mechanism.
  • FIG. 1 illustrates a method of preparing nanoparticle based lubricants or compositions.
  • a solid lubricant feed is introduced via line 210 to a ball milling processor 215. Ball milling is carried out in the processor 215 and the solid lubricant feed is milled to comprise particles having an average particle dimension of less than or equal to about 500 nanometers, suitably less than or equal to about 100 nanometers, suitably less than or equal to about 80 nanometers, and more suitably less than or equal to about 50 nanometers.
  • the ball milling may result in milled solid lubricant particles comprising a mixture, the mixture comprising particles having an average particle dimension of less than or equal to about 500 nanometers, plus larger particles.
  • the ball milling may be high energy ball milling, medium energy ball milling, or combinations thereof. Additionally, in various embodiments the ball milling may be carried out in a vacuum, in the presence of a gas, in the presence of a liquid, in the presence of a second solid, or combinations thereof.
  • the nanoparticle composition may be removed from the processor via line 220.
  • the nanoparticle composition may be a nanoparticle based lubricant.
  • the ball milling may comprise a first ball milling and at least one more subsequent ball millings, or ball milling and/or other processing as appropriate.
  • the ball milling may comprise dry milling followed by wet milling.
  • Figure 2 illustrates a further method 100 of preparing nanoparticle based lubricants where dry milling is followed by wet milling.
  • Feed 110 introduces a solid lubricant feed into a ball milling processor 115 where dry ball milling, such as in a vacuum or in air, reduces the solid lubricant feed to particles having an average dimension of the size described above.
  • Line 120 carries the dry milled particles to a wet milling processor 125.
  • the dry milled particles are combined with a composite oil or an organic medium prior to entering the wet milling processor 125.
  • the organic medium and dry milled particles may be combined in the wet milling processor 125.
  • the dry milling and wet milling may be carried out in a single processor where the organic medium is supplied to the single processor for wet milling after initially carrying out dry milling.
  • the balls in the ball milling apparatus may be coated with the organic medium to incorporate the organic medium in the solid lubricant nanoparticles.
  • line 130 carries the wet milled particles to a container 135, which may be a sonication device.
  • line 130 may carry a mixture comprising solid lubricant nanoparticles, organic medium, and a complex comprising the solid lubricant nanoparticles combined with an organic medium.
  • a base prior to introduction of the wet milled particles into the container 135, a base may be fed to the container 135 via line 150.
  • the base may be supplied to the wet milling processor 125 and the mixing, which may include sonicating, may be carried out in the wet milling processor 125.
  • the solid lubricant nanoparticle composition may be employed as an additive and dispersed in the base.
  • a base may be paired with a solid lubricant nanoparticle composition according to the ability of the base and the solid lubricant nanoparticle composition to blend appropriately. In such cases the solid lubricant nanoparticle composition may enhance performance of the base.
  • an emulsif ⁇ er may be mixed with the base. Emulsifiers may further enhance dispersion of the solid lubricant nanoparticle composition in the base. The emulsif ⁇ er may be selected to enhance the dispersion stability of a nanoparticle composition in a base. An emulsif ⁇ er may also be supplied to the container 135 via line 140. In many embodiments, the emulsif ⁇ er and base are combined in the container 135 prior to introduction of the wet milled particles.
  • Prior mixing of the emulsif ⁇ er with the base may enhance dispersion upon addition of complexes of solid lubricant nanoparticles and organic medium and/or solid lubricant nanoparticles by homogeneously dispersing/dissolving the complexes/nanoparticles.
  • the mixing of the emulsif ⁇ er and base may comprise sonicating.
  • the emulsifier may be supplied to the wet milling processor 125 and the mixing, which may include sonicating, may be carried out in the wet milling processor 125.
  • the lubricant removed from the container 135 via line 120 may be a blend comprising the wet milled particles, organic medium, and base.
  • the blend may further comprise an emulsifier.
  • additives may be added to the nanoparticle based lubricant during interaction with a mating surface.
  • antioxidants or anticorrosion agents may be milled with the solid lubricant nanoparticles.
  • antioxidants include, but are not limited to, hindered phenols, alkylated phenols, alkyl amines, aryl amines, 2,6-di-tert-butyl-4- methylphenol, 4,4'-di-tert-octyldiphenylamine, tert-Butyl hydroquinone, tris(2,4-di-tert- butylphenyl)phosphate, phosphites, thioesters, or a combination thereof.
  • anticorrosion agents include, but are not limited to, alkaline-earth, metal bisalkylphenolsulphonates, dithiophosphates, alkenylsuccinic acid half-amides, or a combination thereof.
  • biocidals may be milled with the solid lubricant nanoparticles.
  • biocidals may include, but are not limited to, alkyl or kydroxylamine benzotriazole, an amine salt of a partial alkyl ester of an alkyl, alkenyl succinic acid, or a combination thereof.
  • further processing of wet milled particles may comprise removal of oils that are not a part of a complex with the solid lubricant particles.
  • Such methods may be suitable for applications that benefit from use of dry particles of solid lubricant, such as coating applications. Oil and/or other liquids can be removed from wet milled particles to produce substantially dry solid lubricant particles and complexes. Such wet milling followed by drying may produce a solid lubricant with reduced tendency to agglomerate.
  • an agent such as acetone
  • acetone can be added that dissolves oils that are not a part of a complex, followed by a drying process such as supercritical drying, to produce a substantially dry solid lubricant comprising particles treated by milling in an organic medium.
  • Ball milling conditions may vary and, in particular, conditions such as temperature, milling time, and size and materials of the balls and vials may be manipulated.
  • ball milling may be carried out from about 12 hours to about 50 hours, suitably from about 36 hours to about 50 hours, suitably from about 40 hours to about 50 hours, and more suitably at about 48 hours.
  • ball milling is conducted at room temperature.
  • the benefits of increasing milling time may comprise at least one of increasing the time for the organic medium and solid lubricant nanoparticles to interact; and producing finer sizes, better yield of nanoparticles, more uniform shapes, and more passive surfaces.
  • An example of ball milling equipment suitable for carrying out the described milling includes the SPEX CertiPrep model 8000D, along with hardened stainless steel vials and hardened stainless steel grinding balls, but any type of ball milling apparatus may be used.
  • a stress of 600-650 MPa, a load of 14.9 N, and a strain of 10 "3 -10 "4 per sec may be used.
  • suitable ratios of solid lubricant nanoparticles to organic medium may be about 1 part particles to about 4 parts organic medium by weight, suitably, about 1 part particles to about 3 parts organic medium by weight, suitably, about 3 parts particles to about 8 parts organic medium by weight, suitably, about 2 parts particles to about 4 parts organic medium by weight, suitably, about 1 part particles to about 2 parts organic medium by weight, and suitably, about 1 part particles to about 1.5 parts organic medium by weight.
  • Suitable ratios of organic medium to emulsifier in a lubricant including the solid lubricant nanoparticles may be about 1 part organic medium to less than or equal to about 1 part emulsifier, suitably, about 1 part organic medium to about 0.5 parts emulsifier by weight, or suitably, from about 0.4 to about 1 part emulsifier for about 1 part organic medium by weight.
  • the amount of solid lubricant nanoparticle composition (by weight) sonicated or dispersed in the base may be from about 0.25% to about 5%, suitably 0.5% to about 3%, suitably 0.5% to about 2%, and more suitably 0.75% to about 2%.
  • the amount of emulsifier (by weight) sonicated or dissolved in the base may be from about 0.5% to about 10%, suitably from about 4% to about 8%, suitably from about 5% to about 6%, and suitably, from about 0.75% to about 2.25%.
  • the solid lubricant nanoparticle composition may be used, without limitation, as lubricants, coatings, delivery mechanisms, or a combination thereof.
  • the solid lubricant nanoparticle composition may be used, without limitation, as an additive dispersed in a base oil.
  • the composition may also be used, without limitation, to lubricate a boundary lubrication regime.
  • a boundary lubrication regime may be a lubrication regime where the average oil film thickness may be less than the composite surface roughness and the surface asperities may come into contact with each other under relative motion. During the relative motion of two surfaces with lubricants in various applications, three different lubrication stages may occur, and the boundary lubrication regime may be the most severe condition in terms of temperature, pressure and speed.
  • Mating parts may be exposed to severe contact conditions of high load, low velocity, extreme pressure (for example, 1-2 GPa), and high local temperature (for example, 150-300 degrees C).
  • the boundary lubrication regime may also exist under lower pressures and low sliding velocities or high temperatures. In the boundary lubrication regime, the mating surfaces may be in direct physical contact.
  • the composition may further be used, without limitation, as a lubricant or coating in machinery applications, manufacturing applications, mining applications, aerospace applications, automotive applications, pharmaceutical applications, medical applications, dental applications, cosmetic applications, food product applications, nutritional applications, health related applications, bio-fuel applications or a combination thereof.
  • uses in end applications include, without limitation, machine tools, bearings, gears, camshafts, pumps, transmissions, piston rings, engines, power generators, pin-joints, aerospace systems, mining equipment, manufacturing equipment, or a combination thereof.
  • Further specific examples of uses may be, without limitation, as an additive in lubricants, greases, gels, compounded plastic parts, pastes, powders, emulsions, dispersions, or combinations thereof.
  • the composition may also be used as a lubricant that employs the solid lubricant nanoparticle composition as a delivery mechanism in pharmaceutical applications, medical applications, dental applications, cosmetic applications, food product applications, nutritional applications, health related applications, bio-fuel applications, or a combination thereof.
  • compositions and methods may also be used, without limitation, in hybrid inorganic-organic materials.
  • applications using inorganic- organic materials include, but are not limited to, optics, electronics, ionics, mechanics, energy, environment, biology, medicine, smart membranes, separation devices, functional smart coatings, photovoltaic and fuel cells, photocatalysts, new catalysts, sensors, smart microelectronics, micro-optical and photonic components and systems for nanophotonics, innovative cosmetics, intelligent therapeutic vectors that combined targeting, imaging, therapy, and controlled release of active molecules, and nanoceramic-polymer composites for the automobile or packaging industries.
  • the ball milling process may create a close caged dense oval shaped architecture (similar to a football shape or fullerene type architecture). This may occur when molybdenum disulphide is milled in a gas or vacuum.
  • Figure 7(A) shows the close caged dense oval shaped architecture of molybdenum disulphide nanoparticles that have been ball milled in air for 48 hours.
  • the ball milling process may create an open ended oval shaped architecture (similar to a coconut shape) of molybdenum disulphide nanoparticles which are intercalated and encapsulated with an organic medium and phospholipids. This may occur when molybdenum disulphide is milled in a gas or vacuum followed by milling in an organic medium.
  • Figure 7(B) shows the open ended oval shaped architecture of molybdenum disulphide nanoparticles that have been ball milled in air for 48 hours followed by ball milling in canola oil for 48 hours.
  • the tribological performance of the nanoparticle based lubricant may be improved.
  • the tribological performance may be measured by evaluating different properties.
  • An anti-wear property may be a lubricating fluid property that has been measured using the industry standard Four-Ball Wear (ASTM D4172) Test.
  • the Four-Ball Wear Test may evaluate the protection provided by an oil under conditions of pressure and sliding motion. Placed in a bath of the test lubricant, three fixed steel balls may be put into contact with a fourth ball of the same grade in rotating contact at preset test conditions.
  • Lubricant wear protection properties may be measured by comparing the average wear scars on the three fixed balls. The smaller the average wear scar, the better the protection.
  • Extreme pressure properties may be lubricating fluid properties that have been measured using the industry standard Four-Ball Wear (ASTM D2783) Test. This test method may cover the determination of the load-carrying properties of lubricating fluids. The following two determinations may be made: 1) load-wear index (formerly Mean-Hertz load) and 2) weld load (kg).
  • the load-wear index may be the load-carrying property of a lubricant. It may be an index of the ability of a lubricant to minimize wear at applied loads.
  • the weld load may be the lowest applied load in kilograms at which the rotating ball welds to the three stationary balls, indicating the extreme pressure level that the lubricants can withstand.
  • the coefficient of friction may be a lubricating fluid property that has been measured using the industry standard Four-Ball Wear (ASTM D4172) Test.
  • COF may be a dimensionless scalar value which describes the ratio of the force of friction between two bodies and the force pressing them together.
  • the coefficient of friction may depend on the materials used. For example, ice on metal has a low COF, while rubber on pavement has a high COF.
  • a common way to reduce friction may be by using a lubricant, such as oil or water, which is placed between two surfaces, often dramatically lessening the COF.
  • the composition may have a wear scar diameter of about 0.4 mm to about 0.5 mm.
  • the composition may have a COF of about 0.06 to about 0.08.
  • the composition may have a weld load of about 150 kg to about 350 kg.
  • the composition may have a load wear index of about 20 to about 40. The values of these tribological properties may change depending on the amount of solid lubricant nanoparticle composition sonicated or dissolved in the base.
  • Ball milling was performed in a SPEX 8000D machine using hardened stainless steel vials and balls.
  • MoS 2 Alfa Aesar, 98% pure, 700 nm average particle size
  • canola oil canola oil
  • the ball to powder ratio was 2 to 1.
  • the ball weight in the container was 2% by weight and the weight of the MoS 2 sample was 1% by weight.
  • MoS 2 was ball milled for 48 hours in air followed by milling in canola oil for 48 hrs at room temperature. The nanop articles were about 50 nm after ball milling.
  • Table 1 summarizes milling conditions and resultant particle morphologies. It was observed that there was a strong effect of milling media on the shape of the ball milled nanoparticles. Dry milling showed buckling and folding of the planes when the particle size was reduced from micron size to nanometer size. However, the dry milling condition used here produced micro clusters embedding several nanoparticles. On the other hand, wet milling showed no buckling but saw de-agglomeration.
  • Figure 3 shows TEM micrographs of the as-available (700 nm), air milled and hybrid milled (48 hrs in air medium followed by 48 hours in oil medium) MoS 2 nanoparticles.
  • Figure 3(A) represents micron-sized particle chunks of the as-available MoS 2 sample off the shelf.
  • Figure 3(B) represent agglomerates of lubricant nanoparticles when milled in the air medium.
  • Figure 3(B) clearly demonstrates size reduction in air milled MoS 2 . Higher magnification (circular regions) revealed formation of the disc shaped nanoparticles after milling in the air medium.
  • the particle size was reduced to less than 30 nm after milling in air and hybrid conditions. Regardless of the occasionally observed clusters, the average size of the clusters is less than or equal to 200 nm.
  • Hybrid milled samples were dispersed in paraffin oil (from Walmart) and remained suspended without settling. However, the dispersion was not uniform after a few weeks. To stabilize the dispersion and extend the anti-wear properties, phospholipids were added. Around 2 % by weight of soy lecithin phospholipids (from American Lecithin) was added in the base oil.
  • Figures 4 and 5 show the XRD and XPS spectra OfMoS 2 before and after ball milling, respectively.
  • XRD spectra revealed no phase change as well as no observable amorphization in the MoS 2 after milling. This observation is consistent with the continuous platelets observed throughout the nanoparticle matrix in TEM analysis for milled material. Broadening of peaks (FWHM) was observed in XRD spectra OfMoS 2 ball milled in air and hybrid media, respectively. The peak broadening may be attributed to the reduction in particle size.
  • the estimated grain size is 6 nm. This follows the theme of ball milling where clusters consist of grains and sub-grains of the order of 10 nm.
  • XPS analysis was carried out to study the surface chemistry of the as-available and hybrid milled MoS 2 nanoparticles.
  • a carbon (C) peak observed at 285 eV in the as-available MoS 2 sample shifted to 286.7 eV.
  • Wear scar diameter (WSD, mm) of each stationary ball was quantified in both vertical and horizontal directions. The average value of WSD from 3 independent tests was reported within ⁇ 0.03 mm accuracy.
  • Figure 6(A) shows the average wear scar measurements for paraffin oil without a nanoparticle additive, paraffin oil with micron sized MoS 2 , paraffin oil with MoS 2 that was milled in air for 48 hours, and paraffin oil with MoS 2 that was milled in air for 48 hours followed by milling in canola oil for 48 hours.
  • Figure 6(B) shows the load wear index for paraffin oil without a nanoparticle additive, paraffin oil with micron sized MoS 2 , paraffin oil with MoS 2 that was milled in air for 48 hours, and paraffin oil with MoS 2 that was milled in air for 48 hours followed by milling in canola oil for 48 hours.
  • Figure 6(C) shows the COF for paraffin oil without a nanoparticle additive, paraffin oil with micron sized MoS 2 , paraffin oil with MoS 2 that was milled in air for 48 hours, and paraffin oil with MoS 2 that was milled in air for 48 hours followed by milling in canola oil for 48 hours.
  • Figure 6(D) shows the extreme pressure data for paraffin oil with micron sized MoS 2 , paraffin oil with MoS 2 that was milled in air for 48 hours, and paraffin oil with MoS 2 that was milled in air for 48 hours followed by milling in canola oil for 48 hours.
  • the nanoparticle additive was present in the amount of 1% by weight.
  • FIG. 9(a) depicts the base case of paraffin oil without a nanoparticle additive.
  • Figure 9(b) depicts paraffin oil with the molybdenum disulphide nanoparticles and the emulsifier. It shows the early evidences of molybdenum (Mo)-sulphur (S)-phosphorous (P) in the wear track.
  • Iron (Fe) is seen in Figures 9(a) and 9(b), as it is the material of the balls (52100 steel) in the four-ball test.
  • the molybdenum and sulphur peaks coincide and are not distinguishable because they have the same binding energy. Elemental mapping also showed similar results.
  • Examples 2-23 are made using a similar method as Example 1, unless specified otherwise.
  • MoS 2 Alfa Aesar, 98% pure, 700 nm average particle size
  • canola oil from ADM are used as the starting materials.
  • the MoS 2 powder is ball milled for various time conditions, variable ball/powder ratios, and under various ambient conditions, starting with air, canola oil and the subsequent combination of milling in air followed by milling in canola oil. It is also ball milled in different types of organic media.
  • one organic medium that is used is canola oil methyl ester. The processing of this will be similar to the above mentioned example.
  • the active EP-EA Extreme pressure - environmentally acceptable particles are treated with phospholipids that have been mixed with a base oil such as paraffin oil.
  • a base oil such as paraffin oil.
  • Molybdenum disulphide is ball milled with boron using a ratio of 1 part molybdenum disulphide to 1 part boron. This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil. An emulsif ⁇ er is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 - boron-canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • Molybdenum disulphide is ball milled with copper using a ratio of 1 part molybdenum disulphide to 1 part metal. This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil. An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 - copper-canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • a molybdenum disulphide/graphite (obtained from Alfa Aesar) mixture in the ratio of 1 : 1 is ball milled. This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil. An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -graphite-canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • a molybdenum disulphide/boron nitride (Alfa Aesar) mixture in the ratio of 1 : 1 mixture is ball milled. This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -boron nitride-canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • a molybdenum disulphide/graphite/boron nitride mixture in the ratio 1:1:1 is ball milled. This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -graphite-boron nitride-canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • a molybdenum disulphide/graphite mixture in the ratio of 1 : 1 : 1 is ball milled. This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -graphite-boron-canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • a molybdenum disulphide/graphite mixture in the ratio of 1 : 1 is ball milled with copper using a ratio of 1 part molybdenum disulphide/graphite to 1 part metal.
  • This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -graphite-copper-canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • a molybdenum disulphide/boron nitride mixture in the ratio of 1 : 1 is ball milled with boron using a ratio of 1 part molybdenum disulphide/boron nitride to 1 part metal.
  • This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -boron nitride-boron-canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • a molybdenum disulphide/boron nitride mixture in the ratio of 1 : 1 mixture is ball milled with copper using a ratio of 1 part molybdenum disulphide/boron nitride to 1 part metal.
  • This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -boron nitride-copper-canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • a molybdenum disulphide/boron nitride/graphite mixture in the ratio of 1 : 1 : 1 is ball milled with boron using a ratio of 1 part molybdenum disulphide/boron nitride/graphite to 1 part metal.
  • This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -boron mtride-graphite-boron- Canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • a molybdenum disulphide/boron nitride/graphite in the ratio of 1 : 1 : 1 is ball milled with copper using a ratio of 1 part molybdenum disulphide/boron nitride/graphite to 1 part metal.
  • This mixture is then ball milled with vegetable oil (canola oil) using a ratio of 1 part solid lubricant nanoparticles to 1.5 parts canola oil.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -boron nitride-graphite-copper- canola oil) to 2 parts emulsifier. This is added to the base oil (paraffin oil).
  • Molybdenum disulphide is ball milled with polytetrafluoroethylene (Teflon ® ) in a ration of 1 part molybdenum disulphide to 1 part Teflon ® . This mixture is then added to the base oil (paraffin oil) with a phospholipid emulsifier (soy lecithin).
  • Teflon ® polytetrafluoroethylene
  • Molybdenum disulphide is ball milled with polytetrafluoroethylene (Teflon ® ) in a ration of 1 part molybdenum disulphide to 1 part Teflon ® . This mixture is then added to the base oil (paraffin oil) with a phospholipid emulsifier (soy lecithin).
  • Teflon ® polytetrafluoroethylene
  • Molybdenum disulphide is ball milled with metal additives like copper, silver, lead etc. in a ratio of 1 part molybdenum disulphide to 1 part metal additive.
  • This mixture is further ball milled in vegetable oil based esters (canola oil methyl esters) in a ratio of 1 part solid lubricant nanoparticles to 1.5 parts esters.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -esters) to 2 parts phospholipid emulsifier. This is added to the base oil (paraffin oil).
  • Molybdenum disulphide is ball milled with metal additives like copper, silver, lead etc. in a ratio of 1 part molybdenum disulphide to 1 part metal additive. This mixture is further ball milled in vegetable oil based esters (canola oil methyl esters) in a ratio of 1 part solid lubricant nanoparticles to 1.5 parts esters. This is added to the base oil (paraffin oil).
  • Molybdenum disulphide is ball milled.
  • the solid lubricant nanoparticles are further ball milled in vegetable oil based esters (canola oil methyl esters) in a ratio of 1 part solid lubricant nanoparticles to 1.5 parts esters.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -esters) to 2 parts phospholipid emulsifier. This is added to the base oil (paraffin oil).
  • Molybdenum disulphide is ball milled.
  • the solid lubricant nanoparticles are further ball milled in vegetable oil based esters (canola oil methyl esters) in a ratio of 1 part solid lubricant nanoparticles to 1.5 parts esters. This is added to the base oil (paraffin oil).
  • vegetable oil based esters canola oil methyl esters
  • Molybdenum disulphide is ball milled with metal additives like copper, silver, lead etc. in a ratio of 1 part molybdenum disulphide to 1 part metal additive. This mixture is further ball milled in fatty acids (oleic acid) in a ratio of 1 part solid lubricant nanoparticles to 1.5 parts fatty acids. An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -oleic acid) to 2 parts phospholipid emulsifier. This is added to the base oil (paraffin oil).
  • Molybdenum disulphide is ball milled with metal additives like copper, silver, lead etc. in a ratio of 1 part molybdenum disulphide to 1 part metal additive. This mixture is further ball milled in fatty acids (oleic acid) in a ratio of 1 part solid lubricant nanoparticles to 1.5 parts fatty acids. This is added to the base oil (paraffin oil).
  • Molybdenum disulphide is ball milled.
  • the solid lubricant nanoparticles are further ball milled in fatty acids (oleic acid) in a ratio of 1 part solid lubricant nanoparticles to 1.5 parts fatty acids.
  • An emulsifier is added using a ratio of 1 part solid lubricant nanoparticle composition (MoS 2 -oleic acid) to 2 parts phospholipid emulsifier. This is added to the base oil (paraffin oil).
  • Molybdenum disulphide is ball milled.
  • the solid lubricant nanoparticles are further ball milled in fatty acids (oleic acid) in a ratio of 1 part solid lubricant nanoparticles to 1.5 parts fatty acids. This is added to the base oil (paraffin oil).

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