SE415107B - METAL WORKING EMULSION CONTAINING TRIGLYCERID OIL - Google Patents

METAL WORKING EMULSION CONTAINING TRIGLYCERID OIL

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Publication number
SE415107B
SE415107B SE7802533A SE7802533A SE415107B SE 415107 B SE415107 B SE 415107B SE 7802533 A SE7802533 A SE 7802533A SE 7802533 A SE7802533 A SE 7802533A SE 415107 B SE415107 B SE 415107B
Authority
SE
Sweden
Prior art keywords
weight
parts
oil
fatty
fatty acid
Prior art date
Application number
SE7802533A
Other languages
Swedish (sv)
Other versions
SE7802533L (en
Inventor
S Andlid
L Linden
Original Assignee
Karlshamns Oljefabriker Ab
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 Karlshamns Oljefabriker Ab filed Critical Karlshamns Oljefabriker Ab
Priority to SE7802533A priority Critical patent/SE415107B/en
Priority to NL7901522A priority patent/NL7901522A/en
Priority to FR7904947A priority patent/FR2419317A1/en
Priority to IT20594/79A priority patent/IT1113413B/en
Priority to DE2907863A priority patent/DE2907863C2/en
Priority to LU80993A priority patent/LU80993A1/en
Priority to FI790735A priority patent/FI62680C/en
Priority to CA322,726A priority patent/CA1115684A/en
Priority to PT69306A priority patent/PT69306A/en
Priority to ES478364A priority patent/ES478364A1/en
Priority to AT0168279A priority patent/AT365630B/en
Priority to DD79211404A priority patent/DD142204A5/en
Priority to NO790748A priority patent/NO145622C/en
Priority to DK93079A priority patent/DK93079A/en
Priority to PL1979213922A priority patent/PL117140B1/en
Priority to BE0/193878A priority patent/BE874665A/en
Priority to CH221979A priority patent/CH639687A5/en
Priority to CS791538A priority patent/CS212712B2/en
Priority to GB7908077A priority patent/GB2016516B/en
Publication of SE7802533L publication Critical patent/SE7802533L/en
Publication of SE415107B publication Critical patent/SE415107B/en
Priority to US06/285,295 priority patent/USRE31242E/en

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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M173/00Lubricating compositions containing more than 10% water
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    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/02Water
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/125Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of eight up to twenty-nine carbon atoms, i.e. fatty acids
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/129Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of thirty or more carbon atoms
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    • C10M2207/404Fatty vegetable or animal oils obtained from genetically modified species
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    • C10M2211/04Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions containing carbon, hydrogen, halogen, and oxygen
    • C10M2211/044Acids; Salts or esters thereof
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    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
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    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
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    • C10M2219/00Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/02Sulfur-containing compounds obtained by sulfurisation with sulfur or sulfur-containing compounds
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    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/22Metal working with essential removal of material, e.g. cutting, grinding or drilling
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    • C10N2040/20Metal working
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    • C10N2040/241Manufacturing joint-less pipes
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    • C10N2050/00Form in which the lubricant is applied to the material being lubricated
    • C10N2050/01Emulsions, colloids, or micelles

Description

'7802533-5 'I ..- hudkontakt och risk för lungskador föreligger vid inandning av den oljebemängda luften. De Senaste åren har rapporterats från flera håll om förekomst av cancerogena ämnen i skärvätskor. Mineralolja inne- håller polyaromatiska kolväten, t.ex. benspyrener. Dessutom är det på grund av de höga temperaturer som råder i skärzonen sannolikt att polyaromater bildas när produkterna används. '7802533-5' I ..- skin contact and risk of lung damage if inhaled oily air. In recent years, the presence of carcinogenic substances in cutting fluids has been reported from several sources. Mineral oil contains polyaromatic hydrocarbons, e.g. bone spurs. In addition, due to the high temperatures prevailing in the cutting zone, it is likely that polyaromatics will be formed when the products are used.

Miljölagstiftningen ställer stora krav på verkstadsindustrins avfalls- vattenhantering. Tekniken för rening av förbrukade emulsioner och av- fettningsbad har blivit komplicerad, på grund av att produktutveck- lingen medfört allt fler additiver och allt stabilare tensidsystem.Environmental legislation places great demands on the engineering industry's wastewater management. The technology for purifying spent emulsions and degreasing baths has become complicated, due to the fact that product development has led to more and more additives and increasingly stable surfactant systems.

Detta har medfört, att omhändertagandet av förbrukade skärvätskor, främst emulsioner, blivit mycket besvärligt och kostsamt.This has meant that the disposal of consumed cutting fluids, mainly emulsions, has become very cumbersome and expensive.

De mindre företagen måste härvid utnyttja specialiserade destruktions- företag, och endast de största företagen har egna emulsionsspräck- ningsanläggningar, vilka emellertid inte alltid fungerar tillfreds- ställande. Separationen resulterar i en vattenfas, som måste behandlas vidare i ett konventionellt reningsverk, samt ett oljehaltigt slam, som måste deponeras, eller i bästa fall är användbart som bränsle. En återanvändning av oljan är otänkbar.The smaller companies have to use specialized destruction companies, and only the largest companies have their own emulsion fracturing plants, which, however, do not always work satisfactorily. The separation results in an aqueous phase, which must be further treated in a conventional treatment plant, as well as an oily sludge, which must be deposited, or is at best useful as fuel. A reuse of the oil is unthinkable.

Från industrins sida är således intresset för en ny typ av skärvätska mycket stort, och kraven på en sådan omfattande: - vara minimalt skadlig på människa och miljö' - ge minimal bildning av oljerök och oljedimma - möjliggöra en enkel avfallshantering utan deponeríngsproblem - vara enkelt uppbyggd med få additiver - vara resistent mot angrepp av mikroorganismer.From the industry's point of view, there is thus a great deal of interest in a new type of cutting fluid, and the requirements for such a comprehensive: - be minimally harmful to humans and the environment '- provide minimal formation of oil fumes and oil mist - enable simple waste management without disposal problems - be simple with few additives - be resistant to attack by microorganisms.

Feta oljor, d.v.s. vegetabiliska eller animaliska oljor och fetter, är funktionellt lämpliga råvaror för smörjmedel, och har tidigare an- vänts i stor omfattning, innan de billigare mineraloljorna helt kom att dominera marknaden. I motsats till mineraloljor är feta oljor för- nyelsebara, miljövänliga och biologiskt nedbrytbara.Feta oils, i.e. vegetable or animal oils and fats, are functionally suitable raw materials for lubricants, and have previously been used extensively, before the cheaper mineral oils came to completely dominate the market. In contrast to mineral oils, fatty oils are renewable, environmentally friendly and biodegradable.

Vid skärande bearbetning av metall är det oftast mest fördelaktigt att använda en skärvätska i form av en vattenhaltig emulsion, av ty- pen olja-i-vatten, varigenom man uppnår on bättre kylande effekt, sam- tidigt som oljcdelens smörjeffokt kvarstår. Ur ekonomisk synpunkt 7802533-5 'ut u ställer sig dessutom användningen av en vattenhaltig emulsion betyd- 1 ligt gynnsammare{ Dessa emulsioner kan visserligen beredas i bruksfärdigt skick, men ur transport- och hanteríngssynpunkt är det lämpligare att först be- reda ett koncentrat, som sedan enkelt kan spädas med vatten hos an- vändaren - verkstadsindustrin. U Kraven på en dylik koncentrerad emulsion är, att stabiliteten skall vara mycket god, samtidigt som den skall vara lätt och obegränsat spädbar med vatten, och stabil som emulsion även i utspätt skick. För att kunna framställa en sådan emulsion måste man använda sig av spe- ciella emulgatorer (ytaktiva ämnen). Man kan härvid använda sig av kraftiga syntetiska tensider, men på grund av de hälso- och miljö- problem, som inledningsvis berörts, vill man undvika detta.When cutting metal, it is usually most advantageous to use a cutting fluid in the form of an aqueous emulsion, of the type oil-in-water, whereby a better cooling effect is achieved, while the lubricating moisture of the oil part remains. In addition, from an economic point of view, the use of an aqueous emulsion is considerably more favorable. Although these emulsions can be prepared in a ready-to-use condition, from the point of view of transport and handling it is more convenient to first prepare a concentrate which can then be easily diluted with water at the user - the engineering industry. U The requirements for such a concentrated emulsion are that the stability should be very good, at the same time as it should be easily and indefinitely dilutable with water, and stable as an emulsion even in diluted condition. In order to be able to prepare such an emulsion, special emulsifiers (surfactants) must be used. You can use strong synthetic surfactants, but due to the health and environmental problems that were initially touched on, you want to avoid this.

Uppgiften för föreliggande uppfinning har således varit att framställa en metallbearbetningsemulsion av typen olja-i-vatten, baserad på tri- glyceridoljor, som uppfyller kraven på stabilitet och spädbarhet, och som samtidigt har tillräckligt goda och smörjande egenskaper, liksom r dag använda, men ur miljö- och hälsosynpunkt icke önskvärda, produk- ter.The object of the present invention has thus been to prepare a metal-working emulsion of the type oil-in-water, based on triglyceride oils, which meets the requirements for stability and dilutability, and which at the same time has sufficiently good and lubricating properties, as used today, but from environmental and health point of view undesirable, products.

Det har nu överraskande visat sig, att man utgående från triglycerid- oljor kan framställa en emulsion, som uppfyller stabilítets- och späd- barhetskruvon, med hjälp av ett emulgatorsystom bestående av fettsyra- monoglycerider och alkalítvålar av fettsyror. Genom att endast "natur- liga" och helt ofarliga komponenter används uppfylles de krav, som ställes på produkten ur miljö- och hälsosynpunkt.It has now surprisingly been found that, from triglyceride oils, an emulsion which satisfies the stability and diluence screw can be prepared by means of an emulsifier system consisting of fatty acid monoglycerides and alkali metal soaps of fatty acids. By using only "natural" and completely harmless components, the requirements placed on the product from an environmental and health point of view are met.

För att emulsionens smörjande och kylande egenskaper skall komma i paritet med de mineraloljebaserade produkternas erfordras emellertid införandet av ytterligare komponenter.However, in order for the lubricating and cooling properties of the emulsion to be on a par with the mineral oil-based products, the introduction of additional components is required.

Det har sålunda visat sig, att användandet av en organisk amin, såsom en alkanolamin, t.ex. trietanolamin eller en fettamín, betydligt ökar emulsionens vätande egenskaper, och därmed dess kylande effekt. Det har vidare visat sig, att en tillsats av fri fettsyra till triglyce- ridoljnn ökar dennas smörjandc egenskaper. I själva verket föreligger amin och fettsyra till övervägande delen i sultform, d.v.s. som tvål m 7802533-5 Uppfinningen kännetecknas sålunda därav, att metallbearbetníngsemul- sionen innehåller en oljefas och en vattenfas, och att oljefasen, som består av: ' 0,5 -50 viktsdelar triglyceridolja, 0,1 -10 víktsdelar fettsyramonoglycerid, 0,05-10 viktsdelar fettsyra och 0,05-10 viktsdelar alkanolamin eller fettamin, emulgeras in i vattenfasen, som består av: 0,05- 3 viktsdelar alkalitvålar av fettsyror och 45 -98 viktsdelar vatten.Thus, it has been found that the use of an organic amine, such as an alkanolamine, e.g. triethanolamine or a fatty amine, significantly increases the wetting properties of the emulsion, and thus its cooling effect. It has further been found that the addition of free fatty acid to triglyceride oil increases its lubricating properties. In fact, amine and fatty acid are predominantly in starvation form, i.e. The invention is thus characterized in that the metalworking emulsion contains an oil phase and an aqueous phase, and that the oil phase, which consists of: 0.5 -50 parts by weight of triglyceride oil, 0.1 -10 parts by weight of fatty acid monoglyceride, 0.05 -10 parts by weight of fatty acid and 0.05-10 parts by weight of alkanolamine or fatty amine are emulsified into the aqueous phase, which consists of: 0.05-3 parts by weight of alkali soaps of fatty acids and 45 -98 parts by weight of water.

De högre mängderna av fettkomponenter användes vid beredning av de emulsionskoncentrat, som, enligt vad som tidigare omtalats, vanligtvis framställes av tillverkaren, medan de lägre mängderna användes vid framställning av bruksfärdiga emulsioner.The higher amounts of fat components are used in the preparation of the emulsion concentrates which, as previously mentioned, are usually prepared by the manufacturer, while the lower amounts are used in the preparation of ready-to-use emulsions.

Vid beredningen av oljefasen löses fettsyramonoglyceriden, fettsyran och aminen i triglyceridoljan vid en temperatur av 40-70°C.In the preparation of the oil phase, the fatty acid monoglyceride, fatty acid and amine are dissolved in the triglyceride oil at a temperature of 40-70 ° C.

Vattenfasen beredes genom att alkalitvålarna upplöses vid en tempera- tur av zo-7o°c, förenradesivs zo-4o°c.The aqueous phase is prepared by dissolving the alkali soaps at a temperature of zo-70 ° C, combined with zo-40 ° C.

Oljefasen iblandas långsamt i vattenfasen under omrörning vid en tem- peratur av 20-50°C.The oil phase is slowly mixed into the aqueous phase with stirring at a temperature of 20-50 ° C.

Vid framställning av bruksfärdíga emulsioner är det därefter tillräck- ligt med en kraftigare omrörning för att erhålla en stabil emulsion, medan det vid framställning av emulsionskoncentrat som regel erfordras en homogenisering av produkten. Homogeniseringen utföres lämpligen vid en temperatur av 40-60°C i konventionell homogeniseringsutrustning.In the preparation of ready-to-use emulsions, a more vigorous stirring is then sufficient to obtain a stable emulsion, while in the preparation of emulsion concentrate a homogenization of the product is usually required. The homogenization is conveniently carried out at a temperature of 40-60 ° C in conventional homogenization equipment.

Triglyceridoljan kan utgöras av vilken som helst animalisk eller vege- tabilisk olja, eller oljeblandning, som har en tillräckligt låg stel- ningspunkt, för att tillåta en säker hantering av emulsionen i såväl koncentrerad, som bruksfärdig form, men som samtidigt är någorlunda fri från främst linolensyra, som annars kan vålla oxidations- och polymerisationsproblem. Oljan bör sålunda företrädesvis vara flytande vid rumstemperatur, och ha en oljesyrahalt på minst 40%. Särskilt lämpliga oljor ur funktionalitetssympunkt utgör olivolja, jordnötsolja 7802533-5 och lobraolja (rapsolja med låg erukasyrahalt). Även bottenfraktioner- na av fraktionerade fetter, såsom t.ex. "palmolein" har visat sig ypperliga för ändamålet.The triglyceride oil can be any animal or vegetable oil, or oil mixture, which has a sufficiently low solidification point, to allow a safe handling of the emulsion in both concentrated and ready-to-use form, but which is at the same time reasonably free from mainly linolenic acid, which can otherwise cause oxidation and polymerization problems. Thus, the oil should preferably be liquid at room temperature, and have an oleic acid content of at least 40%. Particularly suitable oils from a functional point of view are olive oil, peanut oil 7802533-5 and lobra oil (rapeseed oil with a low erucic acid content). Also the bottom fractions of fractionated fats, such as e.g. "palmolein" has proven excellent for the purpose.

Fettsyramonoglyceriden bör vara av den "mjuka typen" (soft product), d.v.s. ha en smältpunkt under 60°C. Den bästa produkten är ren olje- syramonoglycerid (monooleoglycerol), men även andra kommersiella pro- dukter kan användas, såsom t.ex. Dimodan S, en molekylardestillerad monoglycerid, framställd av Grindstedvaerket, Danmark, ur ätligt, raffinerat ister, med en approximativ fettsyrasammansättning av 30% palmitinsyra, 18% stearinsyra och 40% oljesyra.The fatty acid monoglyceride should be of the "soft product", i.e. have a melting point below 60 ° C. The best product is pure oleic acid monoglyceride (monooleoglycerol), but other commercial products can also be used, such as e.g. Dimodan S, a molecularly distilled monoglyceride, produced by Grindstedvaerket, Denmark, from edible, refined lard, having an approximate fatty acid composition of 30% palmitic acid, 18% stearic acid and 40% oleic acid.

Det är även möjligt att använda s.k. tekniska monoglycerider, fram- ställda genom glycerolys (glycerolförestring) av t.ex. lobraolja.It is also possible to use so-called technical monoglycerides, produced by glycerolysis (glycerol esterification) of e.g. lobra oil.

Dylika produkter, med en halt av 40-60% monoglycerid, är lätta att framställa utan invecklad apparatur, och därmed attraktiva. Givetvis måste, om sådana produkter användas, mängdförhållandet triglycerid- oljazglycerolysprodukt justeras så, att halten monoglycerid i emul- sionen blir den rätta.Such products, with a content of 40-60% monoglyceride, are easy to produce without complicated equipment, and thus attractive. Of course, if such products are used, the amount ratio of triglyceride-oil to glycerolysis product must be adjusted so that the content of monoglyceride in the emulsion is correct.

Den oljelösliga monoglyceríden användes, i första hand på grund av sina ytaktiva egenskaper, som lipofil komponen^ . emulgatorsystemet.The oil-soluble monoglyceride was used, primarily because of its surfactant properties, as the lipophilic component. the emulsifier system.

Ytaktiviteten medför emellertid även en vätande effekt, varigenom oljans smörjande effekt ökar.However, the surface activity also has a wetting effect, whereby the lubricating effect of the oil increases.

Fettsyran utgöres lämpligen av oljesyra. Kraven på denna komponent är desamma som för oljan och monoglyceríden, nämligen att den är flytande vid rumstemperatur, alltså har en titer lägre än Z5°C, samt att den inte innehåller väsentliga kvantiteter av mera omättade homologer.The fatty acid is suitably constituted by oleic acid. The requirements for this component are the same as for the oil and monoglyceride, namely that it is liquid at room temperature, ie has a titer lower than Z5 ° C, and that it does not contain significant quantities of more unsaturated homologues.

Fettsyran har visat sig väsentligt bidra till en ökad smörjeffekt.The fatty acid has been shown to significantly contribute to an increased lubricating effect.

Närvaron av fettsyra förhindrar uppkomst av lukt vid hårdare bearbet- ningsoperationer, vilket dels kan antas bero på fettsyrans förbätt- ring av smörjeffekten, dels sammanhänga med bildningen av tvålar av amin och fettsyra.The presence of fatty acid prevents the appearance of odor during harder processing operations, which can partly be assumed to be due to the fatty acid's improvement of the lubricating effect, and partly related to the formation of soaps of amine and fatty acid.

Som alkanolamin användes lämpligen en amin med 2-4 kolatomer i alka- nolen. Särskilt lämplig ställer sig trietanolamin, som förutom sina goda vätande och rostskyddande egenskaper även har fördelen att vara dermatologiskt ofarlíg, vilket också visas av dess utbredda använd- ning i kosmetiska preparat. 7802533-5 6 Även aminen kan baseras på fettrâvara; varvid samma goda vätande och rostskyddande egenskaper kan uppnås. Lämpligen kan härvid en fettamin med 8 till 18 kolatomer i kedjan användas, och som särskilt lämplig anses dodecylamin vara. I Fettsyratvålen utgöres lämpligen av ett natríum- eller kalium-salt av en fettsyra med 12-22 kolatomer, vanligtvis 16 eller 18 kolatomer (palmitin- eller stearinsyra). Kaliumstearat ger något bättre resultat än natriumstearat, men överhuvudtaget gäller, att om stearintvålar skall användas, måste avjoníserat vatten användas, för att förhindra utflockníng av calcium- och magnesiumtvålar. Vid användning av olje- syratvålar (natrium eller kalium) undvikes detta problem helt, ehuru det vid framställning av koncentratet är lämpligast att använda av- joniserat vatten.As the alkanolamine, an amine having 2-4 carbon atoms in the alkanol is suitably used. Particularly suitable is triethanolamine, which in addition to its good wetting and anti-corrosion properties also has the advantage of being dermatologically harmless, which is also shown by its widespread use in cosmetic preparations. 7802533-5 6 The amine can also be based on fat raw material; whereby the same good wetting and anti-corrosion properties can be achieved. Suitably a fatty amine having 8 to 18 carbon atoms in the chain can be used, and dodecylamine is considered to be particularly suitable. The fatty acid soap is suitably a sodium or potassium salt of a fatty acid having 12-22 carbon atoms, usually 16 or 18 carbon atoms (palmitic or stearic acid). Potassium stearate gives slightly better results than sodium stearate, but in general, if stearin soaps are to be used, deionized water must be used to prevent the accumulation of calcium and magnesium soaps. When using oleic acid soaps (sodium or potassium) this problem is completely avoided, although it is most convenient to use deionized water when preparing the concentrate.

Vid bearbetningsoperationer med speciellt höga kontakttryck kan me- tallbearbetningsemulsíonens smörjande egenskaper om så erfordras yt- terligare förstärkas genom tillsats av lätt klorerade och/eller ' sulfurerade tríglyceridoljor. Dessa medel är väl kompatibla med me- tallbearbetningsemulsionen enligt uppfinningen. Företrädesvis ersättes, vid speciellt krävande bearbetningar 20-40% av triglyceridoljan med sådana medel.In machining operations with particularly high contact pressures, the lubricating properties of the metal working emulsion can, if necessary, be further enhanced by the addition of lightly chlorinated and / or sulfurized triglyceride oils. These agents are well compatible with the metalworking emulsion of the invention. Preferably, in particularly demanding processes, 20-40% of the triglyceride oil is replaced with such agents.

För att förebygga oxidations- och polymerisatíonsproblem kan even- tuellt ett antioxidatíonsmedel tillsättas. Lämpliga antioxidanter är butylhydroxianisol, BHA, och butylhydroxitoluen, BHT. Med fördel kan t.eX. Eastman Kodaks produkter Tenox 2 eller Tenox 6 användas. Dessa medel tillsättes lämpligen i en mängd av 0,1-1,0 viktsprocent i den koncentrerade emulsionen.To prevent oxidation and polymerization problems, an antioxidant may be added. Suitable antioxidants are butylhydroxyanisole, BHA, and butylhydroxytoluene, BHT. Advantageously, e.g. Eastman Kodak's products Tenox 2 or Tenox 6 are used. These agents are suitably added in an amount of 0.1-1.0% by weight in the concentrated emulsion.

Under de ogynnsamma betingelser, som verkstadsmiljön innebär, kan lätt angrepp av mikroorganismer äga rum. Får dessa mikroorganismer utveck- las ohämmat under en längre tid kan en obehaglig lukt utvecklas, sam- tidigt som emulsionens korrosionshämmande egenskaper nedsättes, genom bildningen av sura nedbrytningsprodukter, i likhet med vad som äger rum vid användningen av traditionella mineraloljebaserade produkter.Under the adverse conditions of the workshop environment, micro-organisms can be easily attacked. If these microorganisms develop uninhibited for a long time, an unpleasant odor can develop, at the same time as the emulsion's corrosion-inhibiting properties are reduced, through the formation of acidic decomposition products, similar to what takes place when using traditional mineral oil-based products.

Detta undvikes genom att ett bakteriekontrollerande medel sättes till metallbearbetningsemulsionen. Med fördel kan ett formaldehydavspjälk- ande medel användas, t.ex. Grotan BK, som tillverkas av Schülke & Mayr GmbH. l I 7802533-s L Den enligt uppfinningen framställda produkten erbjuder således ur an- vändarens synpunkt en lång rad fördelar: Produkten har i sin helhet baserats på feta oljor eller beståndsdelar i dessa. Dessa oljor är förnyelsebara, miljövänliga och biologiskt nedbrytbara.This is avoided by adding a bactericidal agent to the metalworking emulsion. Advantageously, a formaldehyde cleaving agent can be used, e.g. Grotan BK, manufactured by Schülke & Mayr GmbH. I I 7802533-s L The product produced according to the invention thus offers from the user's point of view a wide range of advantages: The product has been based in its entirety on fatty oils or constituents thereof. These oils are renewable, environmentally friendly and biodegradable.

Förekomsten av hudirritationer, eksem och allergier kan väsentligen elimineras, och risken för cancer undanröjas.The presence of skin irritations, eczema and allergies can be significantly eliminated, and the risk of cancer eliminated.

På grund av triglyceridoljornas större molekylvikt, och därmed sam- manhängande betydligt högre ångtryck kommer någon besvärande oljerök icke att uppstå. Rent allmänt innebär detta en avsevärt renare arbets- miljö. ' Produkter baserade på feta oljor erbjuder ur avfallshantoringssyn- punkt inga svårigheter. Med rätt vald separationsteknik kan den feta delen lätt avskiljas, och vattendelen kräver ingen särskild rening före utsläpp. Den feta delen kan lätt med känd teknik spaltas hydro- lytiskt, och de därvid utvunna fettsyrorna återanvändas.Due to the greater molecular weight of the triglyceride oils, and the associated significantly higher vapor pressure, no troublesome oil fumes will occur. In general, this means a considerably cleaner working environment. 'Products based on fatty oils do not present any difficulties from a waste management point of view. With the right separation technique chosen, the oily part can be easily separated, and the water part does not require any special treatment before discharge. The fatty part can be easily hydrolytically decomposed with known technology, and the fatty acids thus obtained are reused.

Jppfinningen åskådliggöres närmare i följande exempel: Exempel 1. Framställning av en metallbearbetningsemulsion i koncent- rerad form.The invention is further illustrated in the following examples: Example 1. Preparation of a metalworking emulsion in concentrated form.

Oljefasz 34,7 viktsdelar palmolein 4,9 viktsdelar monoglycerid, Dimodan S 2,7 viktsdelar rapsfettsyror 2,7 viktsdelar trietanolamín Vattenfas: 1,1 viktsdelar natriumoleat 55,0 viktsdelar avjoniserat vatten.Oil phase 34.7 parts by weight palmolein 4.9 parts by weight of monoglyceride, Dimodan S 2.7 parts by weight of rapeseed fatty acids 2.7 parts by weight of triethanolamine Aqueous phase: 1.1 parts by weight of sodium oleate 55.0 parts by weight of deionized water.

Palmoleinet utgjordes av en bottenfraktíon från palmoljefraktionering.The palm oil consisted of a bottom fraction from palm oil fractionation.

Palmoleinets halt av oljesyra var 50%.The palm oil content of oleic acid was 50%.

Oljefasens komponenter blandades vid 60-7006. Tvålen upplöstes i vatt- net vid ZSOC, varefter oljefasen långsamt och under omrörning tillsat- tes vattenfasen. Den så erhållna dispersion homogeniserades därefter vid 50°C i en homogenisator av konventionell typ. '7802533-5 e Emulsionskoncentratet var lätt och obegränsat spädbart med vatten av skiftande hârdhetsgrad (0-12 dH). Både emulsionskoncentratet och de utspädda emulsionerna visade sig vara lagringsstabila utan tendenser till oljeseparation.The components of the oil phase were mixed at 60-7006. The soap was dissolved in the water at ZSOC, after which the oil phase was slowly and with stirring the aqueous phase was added. The dispersion thus obtained was then homogenized at 50 ° C in a conventional type homogenizer. '7802533-5 e The emulsion concentrate was easily and indefinitely dilutable with water of varying hardness (0-12 dH). Both the emulsion concentrate and the diluted emulsions were found to be storage stable with no tendency to oil separation.

Produkten provades i spädning 1:10 i en flerspindlíg borrmaskin i pro- duktionsdrift där arbetsoperationen var gängníng i aluminium. Efter l månads drift var emulsionens funktion oförändrad, och helt jämförbar med funktionen hos en konventionell mineraloljebaserad emulsion.The product was tested in dilution 1:10 in a multi-spindle drilling machine in production operation where the work operation was threading in aluminum. After 1 month of operation, the function of the emulsion was unchanged, and completely comparable to the function of a conventional mineral oil-based emulsion.

Exempel 2. En metallbearbetningsemulsíon framställdes för provning i en hårt belastad, numeriskt styrd automatsvarv. Bearbetníngen skedde med hårdmetallskär i ett flertal järnmetaller såsom t.ex. gjutjärn och härdat verktygsstâl. Metallbearbetningsemulsionen framställdes enligt följande: Oljefasz 27,9 viktsdelar rapsolja 11,7 viktsdelar teknisk monoglycerid av rapsolja 2,7 viktsdelar rapsfettsyra 2,7 viktsdelar trietanolamín 0,4 viktsdelar antioxidant, Tenox 6 Vattenfas: 1,1 viktsdelar natriumoleat 55,0 víktsdelar avjoniserat vatten.Example 2. A metalworking emulsion was prepared for testing in a heavily loaded, numerically controlled automatic lathe. The machining took place with cemented carbide inserts in a number of ferrous metals such as e.g. cast iron and hardened tool steel. The metalworking emulsion was prepared as follows: Oil phase 27.9 parts by weight of rapeseed oil 11.7 parts by weight technical monoglyceride of rapeseed oil 2.7 parts by weight of rapeseed fatty acid 2.7 parts by weight of triethanolamine 0.4 parts by weight of antioxidant, Tenox 6 Aqueous phase: 1.1 parts by weight of sodium part .

Rapsoljan var av lågerukasyratyp med en oljesyrahalt av 52%.The rapeseed oil was of the lower uka acid type with an oleic acid content of 52%.

Den tekniska monoglyceríden hade en halt av 40% monoglycerid.The technical monoglyceride had a content of 40% monoglyceride.

Komponenterna i oljefasen blandades vid en temperatur av 40-50°C, och natriumoleatet upplöstes i vattnet vid en temperatur av 25-SOOC. Där- efter tillsattes oljefasen långsamt, och under omrörning till vatten- fasen. Den erhållna díspersionen homogeniserades vid 50°C i konven- tionell homogeniseringsutrustning.The components of the oil phase were mixed at a temperature of 40-50 ° C, and the sodium oleate was dissolved in the water at a temperature of 25-SOOC. Then the oil phase was added slowly, and with stirring to the water phase. The resulting dispersion was homogenized at 50 ° C in conventional homogenization equipment.

Det på detta sätt erhållna emulsionskoncentratet späddes l:l5 i van- ligt stadsvatten och provades i en automatsvarv. Efter 3 månaders drift var metallbearbetningsemulsionens funktion oförändrad. De bear- betade detaljerna uppvísade inga som helst korrosionstendenser. Me- tallbearbetningsemulsionen gav inga torkande beläggníngar, tvärtom var t.ex. maskinytorna mycket lätta att hälla rena. '7802533-5 u Exempel 3. Exemplet avser att visa fettsyrans smörjförbättrande funk- tion i emulsionen.The emulsion concentrate thus obtained was diluted 1: 15 in ordinary city water and tested in an automatic lathe. After 3 months of operation, the function of the metalworking emulsion was unchanged. The machined details did not show any corrosion tendencies. The metalworking emulsion did not give drying coatings, on the contrary, e.g. machine surfaces very easy to pour clean. '7802533-5 u Example 3. The example is intended to show the lubricating function of the fatty acid in the emulsion.

Två metallbearbetningsemulsioner i bruksfärdig koncentration bereddes för testning i en rundslipmaskin. Metallbearbetningsemulsionerna till- verkades av följande komponenter: Prov A viktsdelar Prov B viktsdelar Oljefasz Oljefas: rapsolja 2,00 rapsolja 1,80 teknisk monoglycerid teknisk monoglycerid av rapsolja 0,78 av rapsolja 0,78 trietanolamín 0,18 rapsfettsyror 0,20 Z tríetanolamin 0,18 Vattenfas: Vattenfas: natriumstearat 0,10 natríumstearat 0,10 avjoniserat vatten 97 avjoniserat vatten 97 Rapsoljan var av lågerukasyratyp med en oljesyrahalt av 60%.Two metalworking emulsions in ready-to-use concentration were prepared for testing in a circular grinder. The metalworking emulsions were made from the following components: Sample A parts by weight Sample B parts by weight Oil phase Oil phase: rapeseed oil 2.00 rapeseed oil 1.80 technical monoglyceride technical monoglyceride of rapeseed oil 0.78 of rapeseed oil 0.78 triethanolamine 0.18 rapeseed fatty acids 0.20 Z triethanolamine .18 Aqueous phase: Aqueous phase: sodium stearate 0.10 sodium stearate 0.10 deionized water 97 deionized water 97 Rapeseed oil was of the lower uka acid type with an oleic acid content of 60%.

Den tekniska monoglyceriden hade en halt av 40% monoglycerid.The technical monoglyceride had a content of 40% monoglyceride.

Komponenterna i oljefasen blandades vid 40-S0°C och na.riumstearatet upplöstes i vattenfasen vid 60-70°C. Därefter tillsattes oljefasen långsamt vattenfasen under intensiv omrörning varvid en stabil emul- sion erhölls.The components of the oil phase were mixed at 40-50 ° C and the sodium stearate was dissolved in the aqueous phase at 60-70 ° C. Thereafter, the oil phase was slowly added to the aqueous phase with vigorous stirring to obtain a stable emulsion.

De på detta sätt framställda metallbearbetningsemulsionerna provades i en rundslipmaskin genom insticksslipning i härdat verktygsstål.The metalworking emulsions prepared in this way were tested in a circular grinder by insert grinding in hardened tool steel.

Härvid befanns att vad beträffar det bearbetade materialets ytfinhet, samt relativa slipskíveförslitningar, prov B (med fettsyratillsats) gav bättre resultat än prov A (utan fettsyratíllsats). Genomsnittligt var ytfinheten 10% bättre och relativa slipskiveförslitningen 30% lägre med prov B än med prov A. Resultaten var helt jämförbara med vad som erhålles då konventionella mineraloljebaserade emulsioner utan EP-additiv används.It was found that with regard to the surface finish of the processed material, as well as relative grinding wheel wear, sample B (with fatty acid addition) gave better results than sample A (without fatty acid addition). On average, the surface finish was 10% better and the relative grinding wheel wear was 30% lower with sample B than with sample A. The results were completely comparable to those obtained when conventional mineral oil-based emulsions without EP additives are used.

Exempel 4. Exemplet avser att visa trietanolaminens vätningsförbätt- rande funktion i emulsionen.Example 4. The example is intended to show the wetting-improving function of triethanolamine in the emulsion.

Två emulsionsprover framställdes enligt samma förfarande som i exem- pel 3. ' 7802533-5 10 Prov A viktsdclar Prov B viktsdelar Oljcfas: Oljcfusz rapsolja 3,50 rapsolja 4,00 monoglycerid av olje- monoglycerid av olje- syra 1,00 syra 1,00 trietanolamin 0,50 Vattenfas: ~ Vattenfas: natriumstearat 0,10 natriumstearat 0,10 avjoniserat vatten 95 avjoniserat vatten 95 Rapsoljan var av lågerukasyratyp med en oljesyrahalt av 60%.Two emulsion samples were prepared according to the same procedure as in Example 3. '7802533-5 Sample A parts by weight Sample B parts by weight Oil phase: Oilfusz rapeseed oil 3.50 rapeseed oil 4.00 monoglyceride of oil monoglyceride of oleic acid 1.00 acid 1, 00 triethanolamine 0.50 Aqueous phase: ~ Aqueous phase: sodium stearate 0.10 sodium stearate 0.10 deionized water 95 deionized water 95 Rapeseed oil was of the lower uka acid type with an oleic acid content of 60%.

Mätningar gjordes av dessa emulsionsßrovers vätning av stålytor. Här- vid befanns emulsionsprov B (utan trietanolamin) ge en vätningsvinkel av 40-450, och emulsionsprov A (med tríetanolamín) ge en vätningsvin- kel av 15-ZOO. Detta sistnämnda resultat var t.o.m. något bättre än vad som erhålles med konventionella mineraloljebaserade emulsioner.Measurements were made of these emulsion-massive wetting of steel surfaces. Emulsion sample B (without triethanolamine) was found to give a wetting angle of 40-450, and emulsion sample A (with triethanolamine) to give a wetting angle of 15-ZOO. This latter result was t.o.m. slightly better than that obtained with conventional mineral oil-based emulsions.

Exemgel 5. En metallbearbetningsemulsíon framställdes enligt exempel l med följande ingredienser: Oljefasz 34.3 viktsdelar palmoleín 4.8 viksdelar monoglycerid Dimodan S 2 7 viktsdelar rapsfettsyror 5.4 viktsdelar trietanolamin Vattenfas: l.l viksdelar natrinmoleat 55.0 viksdelar avjoniserat vatten Skäremulsionen provades en längre tid i en numeriskt styrd verktygsmaskin för borrning och gängning. I maskinen bearbetades seghärdat stål med snabbstålsverktyg. Bearbetningsresültaten jäm- fördes med vad som erhölls då en traditionell skärvätska av emul- sionstyp med tillsats av EP-additíver användes. Den traditionella skärvätskan var speciellt avsedd för tung bearbetning såsom borrning, gängning, gängskärning och dragning í olika järnmateríal.Example 5. A metalworking emulsion was prepared according to Example 1 with the following ingredients: Oil phase 34.3 parts by weight of palmolein 4.8 parts by weight of monoglyceride Dimodan S 2 7 parts by weight of rapeseed fatty acids 5.4 parts by weight of triethanolamine Water phase: 11 parts by weight of sodium molar and threading. In the machine, toughened steel was machined with high-speed steel tools. The processing results were compared with those obtained when a traditional emulsion-type cutting fluid with the addition of EP additives was used. The traditional cutting fluid was especially intended for heavy machining such as drilling, threading, thread cutting and drawing in various iron materials.

Båda skärvätskorna användes i samma spädning, ca 15 ggr, med vanligt kranvatten. 7802533-5 ll l Det bearbetade materialets ytjämnhet var samma för den traditio- nella skärvätskan och för skärvätskan enligt uppfinningen. Verktygs- livslängden var vid borrning lika bra och vid gängníng t.o.m. något bättre med skärvätskan enligt uppfinningen än med den traditionella skärvätskan.Both cutting fluids were used in the same dilution, about 15 times, with ordinary tap water. The surface smoothness of the processed material was the same for the traditional cutting fluid and for the cutting fluid according to the invention. The tool life was as good when drilling and when threading up to and including slightly better with the cutting fluid according to the invention than with the traditional cutting fluid.

Claims (1)

1. a 7802533-5 12 Patentkrav Metallbearbetníngsemulsion av typen olja i vatten, med god stabilitet och obegränsad spädbarhet, baserad på triglyceridoljor, vilken emulsíon är avsedd att an- vändas vid deformerande metallbearbetning, främst spån- avskiljande bearbetning, men även lämplig för pressning och valsning, k ä n n e t e c k n a d d ä r a v, att den består av en oljefas dispergerad i en kontinuerlig vattenfas och att oljefasen består av: 0.5 -50 viktsdelar triglyceridolja 0.1 -10 víktsdelar fettsyramonoglyceríd 0.05-10 víktsdelar fettsyra, och 0.05-10 viktsdelar alkanolamin eller fettamín, Samt att Vâttèflfaâen b6SïåT QVI -v 0.05- J víktsdelar alkalitvålar av fettsyror, och 45 -98 viktsdelar vatten. Metallbearbetningsemulsion enligt krav 1, i koncentrerad form, k ä n n e t e c k n a d d ä r a v, att oljefasen består av: 1' St víktsdelar triglyceridolja, 2-10 viktsdelar fettsyramonoglyceríd, l-10 víktsdelar fettsyra och 1-10 viktsdelar alkanolamin eller fettamin, *och vattenfasen består av: 0.5- 3 viktsdelar alkalitvål av fettsyror och 45 -60 víktsdelar vatten. Metallbearbetníngsemulsion enligt krav 1 i bruksfärdig form, k ä n n e t e c k n a d d ä r a v, att oljefasen består av: 0.5 -10 viktsdelar triglyceridolja, 0.1 - Z viktsdelar fettsyramonoglycerid, 0.05- Z víktsdelar fettsyra och 0.05- l viktsdelar alkanolamin eller fettamín OCh V8tt6nfaS6n B8Står 8V2 0.05- 0.5 viktsdelar alkalítvål av fettsyror och 90 -98 viktsdelar vatten. 10. 13 7802533-5 Metallbearbetningsemulsion enligt krav l, k ä n n e t e c k n a d d ä r a v, att triglyceridoljan utgöres av en fet olja, flytande vid rumstemperatur, och med en cljesyrahalt (Cl8:l) på lägst 45 víkts%, såsom t.ex.: olivolja, jordnötsolja och lâgerukasyra- haltig rapsolja, samt bottenfraktionerna av fraktionerade fetter, såsom palmolein eller animaliska oleiner. Metallbearbetníngsemulsíon enligt krav l, k ä n n e t e c k n a d d ä r a v, att fettsyrorna i fettsyramonoglyceriden utgöres av fettsyror med 16 och/eller 18 kolatomer, varav minst 40 viktsä utgöres av oljesyra (Cl8:l), företrädesvis ren oljesyramonogly- cerid. Metallbearbetningsemulsion enligt krav 1, k ä n n e t e c k n a d d ä r a v, att som fettsyramonoglycerid användes en teknisk pro- dukt, erhâllen genom glyccrolförcstring av en triglyceridolja _enligt krav 4. Metallbearbetningsemulsíon enligt krav l, k ä n n e t e c k n a d d ä r a v, att fettsyran har en titer lägre än 25°C, och före- trädesvis utgöres av oljesyra. Metallbearbetningsemulsion enligt krav 1, k ä n n e t e c k n a d d ä r a v, att alkanolaminen företrädesvis utgöres av trietanol- amin, eller att fettaminen företrädesvis utgöres av en dodecyl- amin. Metallbearbetningsemulsion enligt krav 1, k ä n n e t e c k n a d d ä r a v, att alkalitvålen av fettsyror utgöres av natrium- eller kalium-tvål av fettsyror med en títer lägre än ZSOC, och företrä- desvis utgöres av natrium- eller kaliumoleat. Metallbearbetningsemulsion enligt krav 1, k ä n n e t e c k n a d d ä r a v, att eventuellt 20-40 víkts% av triglyceridoljan har ersatts av ett medel för högt kontakttryck, som utgöres av en lätt klorerad eller sulfurerad triglycerídolja. ANFÖRDA PUBLIKATIONER: Sverige 384 523 (c1om 1/40) Storbritannien 1 025 240 (23 c:1/04) us 2 258 552 (252-49.3)Claims Metal working emulsion of the oil in water type, with good stability and unlimited dilutability, based on triglyceride oils, which emulsion is intended to be used in deforming metal working, mainly chip-separating processing, but also suitable for pressing and rolling, characterized in that it consists of an oil phase dispersed in a continuous aqueous phase and that the oil phase consists of: 0.5 -50 parts by weight of triglyceride oil 0.1 -10 parts by weight of fatty acid monoglyceride 0.05-10 parts by weight of fatty acid, and 0.05-10 parts by weight of alkanolamine or fatty amine, And that Vâttè fl get b6SïåT QVI -v 0.05- J parts by weight of alkali soaps of fatty acids, and 45 -98 parts by weight of water. Metalworking emulsion according to claim 1, in concentrated form, characterized in that the oil phase consists of: 1 'parts by weight of triglyceride oil, 2-10 parts by weight of fatty acid monoglyceride, 1-10 parts by weight of fatty acid and 1-10 parts by weight of alkanolamine or fatty amine, * and aqueous of: 0.5- 3 parts by weight of alkali soap of fatty acids and 45-60 parts by weight of water. Metalworking emulsion according to claim 1 in ready-to-use form, characterized in that the oil phase consists of: 0.5 -10 parts by weight of triglyceride oil, 0.1 - 2 parts by weight of fatty acid monoglyceride, 0.05- 2 parts by weight of fatty acid and 0.05- 1 parts by weight of alkanolamine or 8 0.5 parts by weight of alkali soap of fatty acids and 90 -98 parts by weight of water. Metal processing emulsion according to claim 1, characterized in that the triglyceride oil consists of a fatty oil, liquid at room temperature, and with a cleic acid content (Cl8: 1) of at least 45% by weight, such as: olive oil, peanut oil and camphoric acid rapeseed oil, and the bottom fractions of fractionated fats, such as palmolein or animal oleins. Metalworking emulsion according to claim 1, characterized in that the fatty acids in the fatty acid monoglyceride consist of fatty acids having 16 and / or 18 carbon atoms, of which at least 40% by weight consist of oleic acid (C18: 1), preferably pure oleic acid monoglyceride. A metalworking emulsion according to claim 1, characterized in that a technical product obtained by fatty acid monoglyceride is obtained, obtained by glycrole esterification of a triglyceride oil according to claim 4. A metalworking emulsion according to claim 1, characterized in that a fatty acid ° C, and preferably consists of oleic acid. Metalworking emulsion according to claim 1, characterized in that the alkanolamine is preferably triethanolamine, or that the fatty amine is preferably a dodecylamine. Metalworking emulsion according to claim 1, characterized in that the alkali soap of fatty acids consists of sodium or potassium soap of fatty acids with a titer lower than ZSOC, and preferably consists of sodium or potassium oleate. Metalworking emulsion according to claim 1, characterized in that possibly 20-40% by weight of the triglyceride oil has been replaced by an agent for high contact pressure, which consists of a lightly chlorinated or sulfurized triglyceride oil. STATED PUBLICATIONS: Sweden 384 523 (c1om 1/40) Great Britain 1,025 240 (23 c: 1/04) us 2 258 552 (252-49.3)
SE7802533A 1978-03-07 1978-03-07 METAL WORKING EMULSION CONTAINING TRIGLYCERID OIL SE415107B (en)

Priority Applications (20)

Application Number Priority Date Filing Date Title
SE7802533A SE415107B (en) 1978-03-07 1978-03-07 METAL WORKING EMULSION CONTAINING TRIGLYCERID OIL
NL7901522A NL7901522A (en) 1978-03-07 1979-02-26 METALWORKING EMULSION.
FR7904947A FR2419317A1 (en) 1978-03-07 1979-02-27 EMULSION FOR METAL WORKING
IT20594/79A IT1113413B (en) 1978-03-07 1979-02-27 EMULSION FOR METAL WORKING
DE2907863A DE2907863C2 (en) 1978-03-07 1979-03-01 Metal working emulsion
LU80993A LU80993A1 (en) 1978-03-07 1979-03-05 EMULSION FOR METAL WORKING
FI790735A FI62680C (en) 1978-03-07 1979-03-05 METALLBEARBETNINGSEMULSION
CA322,726A CA1115684A (en) 1978-03-07 1979-03-05 Metal working emulsion
PT69306A PT69306A (en) 1978-03-07 1979-03-05 Metal working emulsion
ES478364A ES478364A1 (en) 1978-03-07 1979-03-06 Metal working emulsion
AT0168279A AT365630B (en) 1978-03-07 1979-03-06 METAL WORKING EMULSION
DD79211404A DD142204A5 (en) 1978-03-07 1979-03-06 METALLBEARBEITUNG EMULSION
NO790748A NO145622C (en) 1978-03-07 1979-03-06 METALLBEARBEIDNINGSEMULSJON.
DK93079A DK93079A (en) 1978-03-07 1979-03-06 METALWORKING EMULSION
PL1979213922A PL117140B1 (en) 1978-03-07 1979-03-06 Metalworking emulsion
BE0/193878A BE874665A (en) 1978-03-07 1979-03-07 EMULSION FOR METAL WORKING
CH221979A CH639687A5 (en) 1978-03-07 1979-03-07 EMULSION FOR METAL WORKING.
CS791538A CS212712B2 (en) 1978-03-07 1979-03-07 Emulsion for metal machining processes
GB7908077A GB2016516B (en) 1978-03-07 1979-03-07 Metal working lubricant and cooling emulsion
US06/285,295 USRE31242E (en) 1978-03-07 1981-07-20 Metal working emulsion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE7802533A SE415107B (en) 1978-03-07 1978-03-07 METAL WORKING EMULSION CONTAINING TRIGLYCERID OIL

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SE415107B true SE415107B (en) 1980-09-08

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US (1) USRE31242E (en)
AT (1) AT365630B (en)
BE (1) BE874665A (en)
CA (1) CA1115684A (en)
CH (1) CH639687A5 (en)
CS (1) CS212712B2 (en)
DD (1) DD142204A5 (en)
DE (1) DE2907863C2 (en)
DK (1) DK93079A (en)
ES (1) ES478364A1 (en)
FI (1) FI62680C (en)
FR (1) FR2419317A1 (en)
GB (1) GB2016516B (en)
IT (1) IT1113413B (en)
LU (1) LU80993A1 (en)
NL (1) NL7901522A (en)
NO (1) NO145622C (en)
PL (1) PL117140B1 (en)
PT (1) PT69306A (en)
SE (1) SE415107B (en)

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Also Published As

Publication number Publication date
AT365630B (en) 1982-02-10
LU80993A1 (en) 1979-06-18
NO145622B (en) 1982-01-18
NO790748L (en) 1979-09-10
CA1115684A (en) 1982-01-05
NO145622C (en) 1982-04-28
USRE31242E (en) 1983-05-17
IT1113413B (en) 1986-01-20
BE874665A (en) 1979-07-02
SE7802533L (en) 1979-09-08
PL213922A1 (en) 1979-11-05
FI790735A (en) 1979-09-08
GB2016516A (en) 1979-09-26
DD142204A5 (en) 1980-06-11
CS212712B2 (en) 1982-03-26
CH639687A5 (en) 1983-11-30
FI62680C (en) 1983-02-10
FI62680B (en) 1982-10-29
GB2016516B (en) 1982-08-18
PL117140B1 (en) 1981-07-31
IT7920594A0 (en) 1979-02-27
FR2419317B1 (en) 1984-03-09
ATA168279A (en) 1981-06-15
DE2907863A1 (en) 1979-09-13
DE2907863C2 (en) 1982-10-28
FR2419317A1 (en) 1979-10-05
NL7901522A (en) 1979-09-11
PT69306A (en) 1979-04-01
ES478364A1 (en) 1980-01-01
DK93079A (en) 1979-09-08

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