Classifications

• • 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
• • 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
  • C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
  • C10M2207/02—Hydroxy compounds
  • C10M2207/021—Hydroxy compounds having hydroxy groups bound to acyclic or cycloaliphatic carbon atoms
  • C10M2207/022—Hydroxy compounds having hydroxy groups bound to acyclic or cycloaliphatic carbon atoms containing at least two hydroxy groups
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  • 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
  • C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
  • C10M2207/28—Esters
  • C10M2207/283—Esters of polyhydroxy compounds
• • 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
  • C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
  • C10M2207/28—Esters
  • C10M2207/287—Partial esters
  • C10M2207/288—Partial esters containing free carboxyl groups
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  • 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
  • C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
  • C10M2207/28—Esters
  • C10M2207/287—Partial esters
  • C10M2207/289—Partial esters containing free hydroxy groups
• • 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
  • C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
  • C10M2209/10—Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
  • C10M2209/103—Polyethers, i.e. containing di- or higher polyoxyalkylene groups
  • C10M2209/104—Polyethers, i.e. containing di- or higher polyoxyalkylene groups of alkylene oxides containing two carbon atoms only
• • 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
  • C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
  • C10M2209/10—Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
  • C10M2209/103—Polyethers, i.e. containing di- or higher polyoxyalkylene groups
  • C10M2209/108—Polyethers, i.e. containing di- or higher polyoxyalkylene groups etherified
• • 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
  • C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant Compositions
  • C10M2215/08—Amides [having hydrocarbon substituents containing less than thirty carbon atoms]
• • 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
  • C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
  • C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
  • C10M2219/042—Sulfate esters
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
  • C10N2020/01—Physico-chemical properties
  • C10N2020/055—Particles related characteristics
  • C10N2020/06—Particles of special shape or size
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
  • C10N2030/06—Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
  • C10N2030/12—Inhibition of corrosion, e.g. anti-rust agents or anti-corrosives
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
  • C10N2030/18—Anti-foaming property
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
  • C10N2030/24—Emulsion properties
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2040/00—Specified use or application for which the lubricating composition is intended
  • C10N2040/20—Metal working
  • C10N2040/22—Metal working with essential removal of material, e.g. cutting, grinding or drilling
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2040/00—Specified use or application for which the lubricating composition is intended
  • C10N2040/20—Metal working
  • C10N2040/24—Metal working without essential removal of material, e.g. forming, gorging, drawing, pressing, stamping, rolling or extruding; Punching metal
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2050/00—Form in which the lubricant is applied to the material being lubricated
  • C10N2050/01—Emulsions, colloids, or micelles
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2050/00—Form in which the lubricant is applied to the material being lubricated
  • C10N2050/01—Emulsions, colloids, or micelles
  • C10N2050/011—Oil-in-water
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2050/00—Form in which the lubricant is applied to the material being lubricated
  • C10N2050/01—Emulsions, colloids, or micelles
  • C10N2050/013—Water-in-oil
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
  • C10N2070/00—Specific manufacturing methods for lubricant compositions

Definitions

• the present invention relates to a micellar emulsion, in particular a micellar emulsion comprising an oleaginous component, an aqueous component and a surfactant.
• Industrial fluids find many applications within industry, such as lubricating fluids, coolants and fuels. For example, these range from powering vehicles, cooling drilling apparatus, lubricating car engines and gear boxes, to subsea machinery, wind turbines, power generators and materials processing (cutting, grinding, rolling) to name but a few.
• Each of these industrial fluids has in common a basic composition of an oleaginous component, an aqueous component and a surfactant dispersed in the aqueous component to form an emulsion.
• oleaginous components are typically derived from hydrocarbon sources by, for example, the refining of crude oil or shale oil, or esterification.
• Including aqueous components into an oleaginous base or vice versa involves the use of emulsifiers to create an emulsion, since such aqueous and oleaginous materials are naturally immiscible.
• industrial fluids comprising aqueous emulsions include metalworking fluids and other water-based fluids.
• Surfactants are typically used to emulsify the aqueous and oleaginous components, with sufficient surfactant included to ensure that the emulsion forms completely. Ideally there should be no residual immiscible components, and the emulsion should be stable, such that the individual components do not separate out during storage or use.
• micellar emulsion comprising an emulsion of: an oleaginous component; an aqueous component; and a surfactant; wherein the oleaginous component forms micelles with the surfactant, each micelle having an average micelle diameter; and wherein a distribution of the average micelle diameters has at least one mode.
• the present invention provides a method of forming a micellar emulsion, comprising: forming a first micellar emulsion comprising micelles having a first average micelle diameter and a first distribution of average micelle diameters, forming a second micellar emulsion comprising micelles having a second average micelle diameter and a second distribution of average micelle diameters; and mixing the first and second micellar emulsions, wherein either: the first average micelle diameter and the second average micelle diameter are different; or the first distribution of average micelle diameters and the second distribution of average micelle diameters is different.
• the present invention provides a micellar emulsion made using such method.
• an industrial fluid may comprise a micellar emulsion having oleaginous components and aqueous components.
• Oleaginous components such as mineral oils and base oil stocks, may be emulsified with aqueous components, such as water, as long as there is a surfactant dispersed in the aqueous component.
• aqueous emulsions are used in various applications including lubrication and metalworking. These emulsions may be used undiluted or diluted using a diluent such as water.
• the emulsions may be used as an additive to impart various properties when mixed with a carrier fluid.
• the carrier fluid may be chosen from lubricating, energy dissipating or energy generating fluids, such that the micellar emulsion becomes an additive to these, with these fluids themselves comprising emulsions.
• substantially all of the surfactant is bound up in the micelle structure, substantially no unbound surfactant is present within the micellar emulsion. This removes the need to use insoluble defoamers and/or anti-foam compounds to compensate for foaming caused by excess surfactant, such that the micellar emulsion is substantially free of defoamers or anti-foam compounds.
• micellar emulsion is used as an additive to an emulsion or other carrier fluid.
• the micellar emulsion does not add to any foaming behaviour, and/or may have a tendency to reduce any foaming of the carrier fluid.
• a micelle is an aggregate of surfactant molecules dispersed in a colloid, where particles of a first material are suspended in a second material, creating a two-phase system. Unlike in a solution, the first material is insoluble or immiscible in the second material so becomes an emulsion.
• a micelle forms an aggregate with the hydrophobic tails of the surfactant molecules facing inwards and the hydrophilic heads of the surfactant molecules facing outwards. This forms a normal-phase micelle, leading to an oil-in-water phase mixture.
• An inverse-phase micelle has the inverse structure, where the hydrophilic heads of the surfactant molecules face inwards and the hydrophobic tails face outwards. This leads to a water-in-oil phase mixture.
• the packing behaviour of the surfactant molecules leads to a single layer of surfactant molecules around the core of the micelle, which, following surface energy considerations, typically forms a sphere.
• Further layers of surfactant may also be packed around the outside of the micelle. This will be the case when further surfactant is added to the mixture, as in the present invention.
• further surfactant is added to the mixture, as in the present invention.
• shear forces are applied to an oleaginous component this causes the molecules of the oleaginous component to stretch. This stretching causes the molecules to flatten out and tend towards a laminar structure, thus increasing the surface area any surfactant has available to be attracted to.
• the packing fraction of the surfactant increases from ⁇ 1/3 to >1/2.
• the molecule forms a spherical micelle due to surface energy considerations, unless, of course, the structure of the surfactant causes the minimum surface energy configuration of a micelle to be laminar or cylindrical.
• Gemini surfactants sometimes known as dimeric surfactants, have two hydrophobic tails, that distort the core of the micelle into an elongated ovoid shape.
• the surfactant packing fraction reduces back to ⁇ 1/3, such that any additional surfactant that had been attracted to the temporary laminar configuration of the molecule forms additional layers of surfactant around the micelle.
• the surfactant may comprise at least one ionic surfactant, at least one non-ionic surfactant or a mixture thereof.
• the surfactant is a non-ionic surfactant, since using an ionic surfactant may have an effect on the corrosion inhibition behaviour of the micellar emulsion.
• an ionic surfactant may be beneficial. Therefore whilst the main surfactant component within the surfactant layers may be a non-ionic surfactant, other ionic surfactants may be present within the layer, since this offers various advantages in terms of tailoring the surfactant performance.
• micellar emulsion embodiments in accordance with the present invention may be used undiluted, diluted or as an additive to a carrier fluid.
• the micellar emulsion can be taken directly from the manufacturing process and used as a neat emulsion.
• Water is used as a diluent in micellar emulsions used in lubrication and metalworking applications.
• An additive fluid is one that is added into a carrier fluid, such as another emulsion with lubricating properties.
• the carrier fluid will have a certain viscosity, and may also contain anti-foam or defoamer compounds, which may be soluble or insoluble within the emulsion.
• anti-foam or defoamer compounds which may be soluble or insoluble within the emulsion.
• micellar emulsion it is important that it does not make any foaming behaviour worse than in the original emulsion, otherwise additional anti-foam or defoamer compounds will be required to ensure the performance of the carrier fluid and micellar emulsion mix.
• embodiments of the present invention are very useful, since their surfactant content is bound up in the micelles of the oleaginous component in the aqueous component.
• This dilution step may be carried out more than once, effectively forming a series of fluids with the micellar emulsion diluted further and further to create certain performance behaviour. For example, it may be desirable to take an amount of the micellar emulsion and dilute it using water in order to create a custom lubrication fluid with known surfactant behaviour and viscosity. In this situation, the micellar emulsion may be used to improve viscosity and/or to reduce foaming behaviour.
• Use of the method of the present invention to create a micellar emulsion also enables materials with high viscosities to be emulsified into a stable emulsion.
• Using existing techniques it is difficult to emulsify fluids having a viscosity of greater than approximately 100 - 150 cSt at 40°C.
• Using the method of the present invention it is possible to emulsify fluids having a viscosity of 8,000 - 12,000 cSt and solids at various temperatures. The actual limit is dependent upon the temperature of the various components of the emulsification. For example, it may be necessary to heat up components to around 90°C in order to emulsify such viscosities.
• Anti-foam and defoaming compounds are those materials whose primary action is to defoam (compensate for any foam created by the micellar emulsion), and are available in various forms.
• a popular class of compounds for use with lubricants or metalworking fluids are those having a silicon component. These compounds also have in common that they are insoluble in the fluid used to either form the micellar emulsion or to dilute the micellar emulsion - typically being water insoluble.
• the components themselves can create solubility issues in a final emulsion.
• the above description is based upon an oleaginous in aqueous emulsion, but the same considerations apply for the inverse situation of an aqueous in oleaginous emulsion.
• the oleaginous component may comprise a single component, a group of components or a fully formulated fluid.
• micellar emulsion having substantially all of the surfactant in the fluid bound up in the micelle structures can be achieved.
• the use of the micelle structure in micellar emulsions and some benefits thereof are described in more detail below.
• Industrial fluids typically comprise an oleaginous component, that is, a material that is oily, oil-based or oil-containing in nature. Taking the example of a lubricating fluid, these oleaginous components may be referred to as lubricating compositions.
• Lubricating compositions may be a fully formulated lubricant or a blend of components, at least one of which has lubricating properties.
• a fully formulated lubricant is typically based on a lubricating base oil stock.
• Many different lubricating base oils are known, including synthetic oils, natural oils or a mixture of both, which may be used in both refined or unrefined states (with or without at least one purification step).
• Natural oils include mineral oils of paraffinic, naphthenic or mixed paraffinic-naphthenic natures, based upon the nature of their source. Synthetic oils include hydrocarbon oils (olefins such as polybutylenes and polypropylenes, for example) and Polyalphaolefins (PAOs). Base oil stock categories have been defined by the American Petroleum Institute (API Publication 1509) providing a set of guidelines for all lubricant base oils.
• API Publication 1509 providing a set of guidelines for all lubricant base oils.
• Table 1 Base Oil Stocks Saturates Sulphur Viscosity Index (VI) Group I ⁇ 90 and/or >0.03% and ⁇ 80 and ⁇ 120 Group II ⁇ 90 and ⁇ 0.03% and ⁇ 80 and ⁇ 120 Group III ⁇ 90 and ⁇ 0.03% and ⁇ 120 Group IV Includes Polyalphaolefins (PAO) and GTL (gas-to-liquid) products Group V All other base oils not included in Groups I, II, III or IV
• Group II and/or Group III base oils such as hydrocracked and hydroprocessed base oils, as well as synthetic oils such as polyalphaolefins, alkyl aromatics and synthetic esters are wells known base oils.
• Group III oil base stock tends to be highly paraffinic with saturates higher than 90%, a viscosity index over 125, low aromatic content (less than 3%) and an aniline point of at least 118.
• Synthetic oils include hydrocarbon oils such as polymerised and interpolymerised olefins, such as polybutylenes, polypropylenes, propylene isobutylene copolymers and ethylene alphaolefin copolymers.
• PAOs Polyalphaolefins
• PAOs are typically derived from C 6 , C 8 , C 10 , C 12 , C 14 and C 16 olefins or mixtures thereof.
• Such PAOs typically have a viscosity index greater than 135.
• PAOs can be manufactured by catalytic oligomerisation (polymerisation to low molecular weight products) of linear ⁇ -olefin (otherwise known as LAO) monomers.
• PAOs high viscosity index PAOs
• HVI-PAOs high viscosity index PAOs
• PAOs being formed in the presence of a catalyst such as AlCl 3 or BF 3
• HVI-PAOs being formed using a Friedel-Crafts catalyst or a reduced chromium catalyst.
• Esters also form a useful base oil stock, including synthetic esters, as do GTL (gas-to-liquid) materials, particularly those derived from a hydrocarbon source.
• GTL gas-to-liquid
• the esters of dibasic acids with monoalcohols, or the polyol esters of monocarboxyilic acid may be useful.
• Such esters should typically have a viscosity of less than 10,000 cSt at - 35°C, in accordance with ASTM D5293.
• the actual choice of suitable lubricating composition will depend upon the end application for the micellar emulsion. For example, some metalworking applications will be based upon mineral oils and/or ester combinations, and some automotive applications will be based upon Group III, IV or V oils.
• Micellar emulsions in accordance with embodiments of the present invention may also be used as additives into synthetic lubricants that carry no emulsified components. This is because the components of a synthetic lubricant product are water soluble, including salts of mixed amine and carboxylic acids and ethylene/propylene oxide block copolymers. Examples of these include Syntilo 9913 and Syntilo 81 BF, available from Castrol Limited.
• a suitable method of forming a micelle structure for use in micellar emulsions is described in US2013/0201785 , concerning an apparatus for mixing oleaginous and aqueous materials under a shear force and laminar flow to create either an oil-in-water or a water-in-oil fluid.
• the basis of the method is as follows: a first fluid comprising an aqueous solution of a surfactant and a second fluid comprising an oleaginous compound are mixed under a shear force to produce an intermediate fluid.
• This intermediate fluid is in the form of a colloidal emulsion, has a greater viscosity than either the first or second fluids, and may be free-flowing or gel-like.
• This intermediate fluid comprises micelles of either the oleaginous fluid in aqueous emulsion or the aqueous fluid in oleaginous emulsion.
• Both the first and the second fluids are added to a chamber in which stirrers are used to mix the two fluids together under shear force by rotating at a rotational speed of 1200 to 1600rpm.
• the shape of the chamber and size of the stirrers are chosen to ensure that a region around the walls of the chamber is devoid of turbulent flow.
• an aqueous suspension of a surfactant can flow around the chamber in this region, producing a laminar flow.
• a third fluid to the intermediate fluid under laminar flow, for example, increasing the water content of the aqueous fluid to decrease the viscosity of the resulting micellar emulsion.
• micellar emulsion being substantially free of defoamers or anti-foam compounds, since these are no longer required to compensate for any foaming of an oleaginous/aqueous emulsion.
• the point at which the micellar emulsion becomes nominally free of excess surfactant can be determined by measuring the surface tension of the emulsion. Once the critical micelle concentration has been reached, and no more surfactant molecules are included in the surface layer(s), the surface tension of the emulsion exhibits a discontinuity. This may be detected by surface tension measurement techniques known to those skilled in the art. Other techniques for determining this point include NMR (nuclear magnetic resonance) techniques and optical scattering techniques.
• micellar emulsion is a lubricating fluid, of which a metalworking fluid is an exemplary form. This is considered in more detail below.
• the present invention provides a method of making a micellar emulsion, using the method described above, and a micellar emulsion made using that process.
• the following non-limiting examples are in relation to micellar emulsions used in metalworking processes.
• Metalworking fluid is a lubricant used in either a destructive metalworking process (one where chips are produced, such as milling) or a deformation metalworking process (one where a material is deformed or shaped such that no chips are produced, for example such as steel rolling).
• Metalworking fluids are formulated both for the specific type of metal they are used on (such as steel) and for the process they are used for (such as wire drawing).
• a typical metalworking fluid composition suitable for a destructive process (milling) is characterised by the illustrative composition:
• micellar emulsion in accordance with embodiments of the present invention may comprise all of the above elements except for water, creating an emulsion that requires water in order to be diluted for use, or the micellar emulsion may be created as a final emulsion and used in an undiluted form.
• Suitable surfactants include, but are not limited to, C 16 - C 18 fatty alcohol ethoxylates - with an ethoxylation range of 0-9 moles (fatty alcohol polyglycol ethers); C 16 -C 18 fatty alcohol ethoxylate and propoxylate; C 6 /C 8 /C 16-18 alkyl polyoxyethylene ether carboxylic acids with a 2 to 9 mole ethoxylation range; alkyl ether ethoxylate mono phosphate esters - alkyl chain C 18 , with a 2 to 5 mole ethoxylation range; ethoxylated oleine with a 6/9 mole ethoxylation range; and polyethylene glycol esters of C 16 -C 18 fatty acids. Combinations of various surfactants, as mentioned above, may be particularly advantageous.
• Suitable corrosion inhibitors include, but are not limited to amine/alkali salts of short chain carboxylic mono acids, di acids and tri acids, short chain acidic phosphate esters, including alkoxylated esters, semi-succinate half esters, amide-carboxylic acid salts, fatty amides, and amine and alkali sulphonates or their derivatives.
• Yellow metals include benzotriazole or its derivatives and tolutriazole or its derivatives.
• Suitable esters include, but are not limited to TMP (trimethylol propane) mono, di and tri esters of C 8 - C1 8 fatty acids, glycol esters of predominantly olely fatty acids, methyl or isopropyl esters of predominantly olely fatty acids or triglycerides, natural triglycerides , such as rapeseed, and modified natural oils such as blown rapeseed. Biocides (typically amine compounds) may also be included if desired.
• TMP trimethylol propane
• di and tri esters of C 8 - C1 8 fatty acids glycol esters of predominantly olely fatty acids, methyl or isopropyl esters of predominantly olely fatty acids or triglycerides
• natural triglycerides such as rapeseed
• modified natural oils such as blown rapeseed.
• Biocides typically amine compounds
• formaldehyde releasing agents including ortho-formal, hexahydratriazine and derivatives, methylene bis morpholene, oxazoladine and derivatives, isothiazolinones and derivatives, and iodo propyl butyl carbamate-fungicide.
• NanoGel CCT comprises caprylic/capri triglyceride, water, glycerine. Laureth-23, sodium dicocoylethlyenediamine PEG-15 sulfate, sodium lauroyl lactylate, behenyl alcohol, glyceryl stearate and glyceryl stearate citrate.
• the oleaginous components are comprised within micelles each having three surface layers of surfactant, accounting for substantially all of the surfactant within the emulsion.
• Sample 1 comprised 10wt% NanoGel CCT and 90wt% water
• Sample 2 comprised 5wt% NanoGel CCT and 95% water. These were evaluated against a Control Sample 1 comprising 10wt% Alusol 41 BF metalworking lubricant (available from Castrol Limited) and 90wt% water.
• a tapping torque test under ASTM 5619 - 00 (2011) was carried out to compare Sample 1, Sample 2 and the Control Sample 1. This test determines the amount of torque required to form a thread in a pre-drilled hole in an aluminium alloy (AlZnMgCu0.5). Results were as in Table 2, taking the performance of the Control Sample 1 as a performance index of 100: Table 2 - Tapping Torque Test Sample Control Sample 1 Sample 1 Sample 2 Performance Index 100 93.5 99.4 As can be seen, the inclusion of 5wt% of NanoGel CCT in water offers a small reduction in torque compared with the Control Sample. However, the inclusion of 10wt% in water offers a significant reduction in torque compared with the Control Sample.
• the above examples involve the use of normal-phase micelles, that is, where the surfactant forms a surface layer where the hydrophilic heads of the surfactant molecules face outwards; forming an oil-in-water mixture (the oleaginous component is in emulsion in the aqueous component).
• an inverse-phase micelle structure forming a water-in-oil mixture (the aqueous component is in emulsion in the oleaginous component).
• the size distribution of the average diameters of the micelles follows a generally bell-shaped profile, with a mean ⁇ and a standard deviation ⁇ .
• this may be a Gaussian distribution.
• the standard deviation ⁇ is particularly advantageous for the standard deviation ⁇ to be less than or equal to 0.2 ⁇ .
• the standard deviation of the average micelle diameter is 0.08 ⁇ m or less.
• the average micelle diameter is an average of various diameter measurements take for a micelle, which in the case of spherical micelles is approximately equal to the micelle diameter (since there is little or no variation of the diameter regardless of where the measurement is taken).
• the average micelle diameter is ⁇ 0.4 ⁇ m.
• Suitable measurement techniques to determine both the average micelle diameter and the distribution of average micelle diameters include, but are not limited to, optical measurement techniques - for example, laser particle size analysis using a Beckman Coulter Laser Diffraction PS Analyzer (LS 13 320), and flow cytometry techniques.
• the advantage of having a narrow range of average micelle diameters lies in the ability of the micellar emulsion to cover a surface fully.
• a further embodiment of the present invention requires the combination of at least two micellar emulsions to create a fluid having a bi-modal or multi-modal average micelle diameter distribution.
• the embodiment above describes a distribution with a single mode i.e. a single peak in the curve presenting average micelle diameter. Both the median and mode values may be close to the mean of these distributions, for example within ⁇ 0.05 ⁇ m, indicating that such size distributions are typically narrow.
• the bi-modal or multi-modal distribution micellar emulsions may be formed by mixing two micellar emulsions together, or by incorporating sold materials, such as paraffin wax, of differing diameters in a single micellar emulsion.
• a micellar emulsion may comprise a first micellar emulsion having micelles with a first average micelle diameter and a first distribution of average micelle diameters, and a second micellar emulsion having micelles with a second average micelle diameter and a second distribution of average micelle diameters.
• a bi-modal or multi-modal distribution of average micelle diameters either the first average micelle diameter and the second average micelle diameter are different, or the first distribution of average micelle diameters is different to the second distribution of average micelle diameters.
• the viscosity index (VI) of various base oils stocks is given in Table 1 above.
• the kinematic viscosity of an oil base stock will also have an effect on whether or not the oil can be emulsified to create an aqueous emulsion.
• oils suitable for use in the micellar emulsions described above will have a kinematic viscosity of less than or equal to 20cst at 40°C.
• oils may also be used having a higher kinematic viscosity than this, for example, up to 100cst at 40°C.
• micelles in oleaginous and aqueous emulsions to form lubricating fluids finds use in many applications.
• such fluids may be used in an automotive application (including but not limited to engine or gearbox/drivetrain lubrication), an industrial process (including but not limited to gear lubrication, cutting applications, power generation and machinery lubrication) or a marine or subsea process (lubrication of drilling and cutting tools).
• an automotive application including but not limited to engine or gearbox/drivetrain lubrication
• an industrial process including but not limited to gear lubrication, cutting applications, power generation and machinery lubrication
• a marine or subsea process lubrication of drilling and cutting tools.
• Micellar emulsions include lubricating, energy dissipating, energy generating, or energy transmission fluids and additives thereof.
• Energy dissipating fluids may include cooling fluids (such as drilling fluids used in subsea and terrestrial applications and industrial coolants), and energy generating fluids may include, but not be limited to fuels such as gasoline, diesel and kerosene.
• Energy transmission fluids include hydraulic and transformer fluids.
• the micellar emulsion may also find used as an additive to any of these fluids, in a similar manner to which additives are included in automotive lubricants and fuels. Such additives improve the performance, lifetime or operation of such fluids.
• micellar emulsions Various embodiments and other examples of micellar emulsions will be apparent to the skilled person based upon the appended claims.

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• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• Organic Chemistry (AREA)
• Lubricants (AREA)
• Colloid Chemistry (AREA)

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Citations (6)

• 2018
  • 2018-01-05 EP EP18150508.2A patent/EP3508562A1/fr not_active Withdrawn
• 2019
  • 2019-01-07 WO PCT/EP2019/050259 patent/WO2019135000A1/fr not_active Ceased

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