EP0807010A1 - Procede de preparation d'emulsions d'huile dans l'eau contenant des alcools liquides - Google Patents

Procede de preparation d'emulsions d'huile dans l'eau contenant des alcools liquides

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Publication number
EP0807010A1
EP0807010A1 EP96901316A EP96901316A EP0807010A1 EP 0807010 A1 EP0807010 A1 EP 0807010A1 EP 96901316 A EP96901316 A EP 96901316A EP 96901316 A EP96901316 A EP 96901316A EP 0807010 A1 EP0807010 A1 EP 0807010A1
Authority
EP
European Patent Office
Prior art keywords
alcohols
water
carbon atoms
weight
atoms
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
EP96901316A
Other languages
German (de)
English (en)
Inventor
Thomas Förster
Marcus Claas
Ingo Wegener
Stephan Heck
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.)
BASF Personal Care and Nutrition GmbH
Original Assignee
Henkel AG and Co KGaA
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 Henkel AG and Co KGaA filed Critical Henkel AG and Co KGaA
Publication of EP0807010A1 publication Critical patent/EP0807010A1/fr
Ceased legal-status Critical Current

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Definitions

  • the invention relates to a process for the preparation of oil-in-water emulsions containing liquid alcohols and their use as release agents for hydraulic binders.
  • DE-A-38 19 193 discloses liquid oil-in-water emulsions of polar oil components which have been produced at a temperature in the range of the phase inversion temperature interval or above and are therefore low viscosity, finely divided and very stable.
  • emulsifiers and co-emulsifiers such emulsions are so finely divided that their particles are no longer visually visible.
  • Such emulsions, which have a transparent, bluish opalescent appearance, are also referred to as microemulsions.
  • fatty alcohols as mold release agents for hydraulic binders.
  • GB 1 294 038 describes mold release agents based on aliphatic, saturated or unsaturated alcohols and a cationic emulsifier.
  • EP-A 561 465 proposes emulsifiable mold release agents for hydraulic binders based on fatty acid esters of polyols which do not carry any HI atoms in the ⁇ position to the OH group. Higher aliphatic monofunctional alcohols can also be added to the esters.
  • the emulsions are prepared by emulsifying the mold release agents in water with stirrers.
  • This method has several disadvantages; e.g. problems with emulsion stability occur.
  • the viscosity of the emulsions can increase during storage, for example, or the oil component can be separated by creaming.
  • Some of these disadvantages can be avoided by using special emulsifying units which make it possible to produce particularly fine-particle emulsions. However, the operation of such units is time-consuming and costly.
  • the object of the invention was to provide a process which avoids the disadvantages mentioned above and allows stable, liquid alcohols to be used as emulsions containing oil components To be available that can be used as mold release agents for hydraulic binders.
  • stability means that the emulsion neither creams nor thickens at least 1/2 year, better 1 year at room temperature. Temperature fluctuations occur during storage and transport of the emulsions, which likewise must not impair stability. It is therefore desirable that the emulsions are stable against short-term temperature fluctuations between 5 and 40 ° C, that is, neither cream nor thicken.
  • the invention relates to a process for the preparation of oil-in-water emulsions by using a mixture of
  • a co-emulsifier from the group of saturated fatty alcohols with 16-22 C atoms or the partial esters of polyols with 3-6 C atoms with saturated fatty acids with 14-22 C atoms and
  • Another object of the invention is the use of emulsions produced by the process according to the invention for the treatment of formwork material in concrete construction.
  • water-immiscible alcohols are understood to mean those whose solubility in water at 20 ° C. is below 5% by weight.
  • Liquid at temperatures of 5 to 15 ° C. means that the alcohols or mixtures of alcohols according to the invention are mobile, flowable liquids at these temperatures.
  • the unsaturated fatty alcohols used are known compounds which can be obtained by partial hydrogenation of fats or fatty acid methyl esters.
  • the fats and oils used as raw materials are not purely chemical compounds, but their fatty acids have a C chain distribution and can be in saturated, mono- or polyunsaturated form. Accordingly, the fatty alcohols produced from them also have a C chain distribution and can contain saturated, mono- or polyunsaturated species.
  • the unsaturated fatty alcohols can consist of 12 to 22, preferably 16 to 18, carbon atoms and iodine numbers in the range from 40 to 170, preferably from 70 to 100.
  • Fats are used as the raw material base and oils of vegetable and animal origin are used, for example palm kernel oil, coconut oil, tallow, rapeseed oil, soybean oil, palm oil and sunflower oil. It is particularly preferred to use an unsaturated fatty alcohol based on tallow, sunflower oil with an oil acidity> 80% by weight and / or rapeseed oil, which can also be used without distillation.
  • Guerbet alcohols can also be used. Guerbet alcohols can be obtained by the known alkali-catalyzed condensation of aliphatic alcohols at temperatures of around 200 ° C. Alcohols with 8 to 22 carbon atoms can be used in the condensation reaction. Linear alcohols with 8 to 14 carbon atoms are preferably used for the condensation, which leads to the Guerbet alcohols with 16 to 28 carbon atoms which are preferably used.
  • oxo alcohols can also be used. These are mostly primary, partially branched higher alcohols, which are obtained in oxo synthesis. In this synthesis, aldehydes obtained by adding carbon monoxide to olefins are reduced with hydrogen to alcohols having, for example, 8 to 15 carbon atoms.
  • the proportion of alcohols in the oil component is at most 70% by weight, preferably at most 50% by weight, based on the oil component.
  • all water-insoluble, water-insoluble at room temperature (20 ° C.) branched or linear hydrocarbons, ethers or esters and fatty oils (triglycerides) can be used.
  • solid or higher-melting paraffins, esters, waxes or fats can also be used in such quantities that the mixture with the liquid oil components remains liquid at 20 ° C.
  • Mineral oils and synthetically produced hydrocarbons e.g. B. liquid polyolefins or defined hydrocarbons, for. B. alkylcyclohexanes such. B. 1,3-diisooctylcyclohexane.
  • R 'and R 2 are alkyl groups with 1 - 22 C atoms or alkenyl groups with 8 - 22 C atoms and R 3 are alkylene groups with 2 - 16 C atoms, and which contain at least 10 C atoms, and / or fatty acid triglycerides of Fatty acids with 8 - 22 carbon atoms.
  • Oil components of the type of the mono- and diesters of the formulas I, II and III are known as cosmetic and pharmaceutical oil components and as lubricants and lubricants.
  • the products that are liquid at room temperature (20 ° C.) are of the greatest importance.
  • esters of saturated and unsaturated fatty acids with 12-22 C atoms and polyols of the neopentyl type such as neopentyl glycol, trimethylolpropane, trimethylolethane, pentaerythritol, ditrimethylpropane, dipentaerythritol and tripentaerythritol, can also be used.
  • the ethers of alcohols with more than 6 C atoms preferably up to 18 C atoms, such as e.g. Di-n-hexyl ether, di-n-octyl ether or di-n-decyl ether.
  • Suitable dicarboxylic acids (II) are e.g. B. di-n-butyl adipate, di-n-butyl sebacate, di- (2-ethylhexyl) adipate, di- (2-hexyldecyl) succinate and di-isotridecylvestate.
  • Suitable diasters (III) are e.g. B. ethylene glycol dioleate, ethylene glycol di-isotridecanoate, propylene glycol di- (2-ethylhexanoate), butanediol di-isostearate and neopentyl glycol di-caprylate.
  • the proportion of the other, water-immiscible organic compound in the oil component is at least 30% by weight, preferably at least 50% by weight, based on the oil component.
  • Nonionic emulsifiers suitable as emulsifiers (b1) are characterized by a lipophilic, preferably linear alkyl or acyl group and a hydrophilic group formed from low molecular weight glycol, glucose and polyol ethers. Ethoxylated castor oils are also suitable nonionic emulsifiers.
  • Nonionic ethylene oxide addition products onto fatty alcohols with 16-22 C atoms which are suitable as emulsifiers (b1) are commercially available.
  • the technical products are mixtures of homologous polyglycol ethers of the starting fatty alcohols, the average degree of oxyethylation of which corresponds to the molar amount of ethylene oxide added.
  • emulsifiers (b2) it is also possible to use ethylene oxide adducts on partial esters of a polyol having 3 to 6 carbon atoms and fatty acids having 14 to 22 carbon atoms. Such products are e.g. B.
  • glycerol monostearate glycerol monopalmitate
  • mono- and di-fatty acid esters of sorbitan e.g. B. made of sorbitan monostearate or sorbitan sesquioleate.
  • the emulsifiers suitable for the process according to the invention should have an HLB value of 11-15.
  • the HLB value hydrophile-lipophile balance
  • the HLB value is to be understood as a value that can be calculated according to
  • a coemulsifier (b2) can be used in amounts of up to 0.2, preferably from 0.1 to 0.2 parts by weight to prepare the oil-in-water emulsions by the process according to the invention. Due to its hydrophilicity, the co-emulsifier is not itself suitable for the production of oil-in-water emulsions, but together with the emulsifiers defined above, particularly stable and finely divided emulsions of the polar oil components can be produced.
  • Coemulsifiers according to the invention are those of the type of saturated fatty alcohols with 16-22 carbon atoms, e.g. B. cetyl alcohol, stearyl alcohol, arachidyl alcohol or behenyl alcohol or mixtures of these alcohols, as are obtained in the technical hydrogenation of vegetable and animal fatty acids with 16-22 carbon atoms or the corresponding fatty acid methyl ester.
  • co-emulsifiers are partial esters composed of a polyol having 3 to 6 carbon atoms and saturated and / or unsaturated fatty acids having 14 to 22 carbon atoms. Such partial esters are e.g. B.
  • Technical monoesters which are obtained by esterification of 1 mol of polyol with 1 mol of fatty acid and which are a mixture of monoesters, diesters, triesters and, if appropriate, unesterified polyol are also understood as monoesters.
  • an emulsion is first formed which is so finely divided that the emulsion droplets are submicroscopically fine and the emulsion has a transparent, bluish opalescent appearance.
  • emulsions are also called microemulsions.
  • Microemulsions are obtained when the type and proportions of oil components Emulsifiers and co-emulsifiers are coordinated with one another in the preferred manner.
  • addition products of 8-16 moles of ethylene oxide with saturated fatty alcohols with 16-22 C atoms are used as nonionic emulsifiers (b1).
  • the nonionic emulsifiers used are ethoxylated castor oils which have been obtained by adding 5 to 50, preferably 5 to 20, mol of ethylene oxide (EO) per mol of triglyceride.
  • non-ionic emulsifiers with polyfunctional alcohols preferably ethylene glycol, ring-opened ⁇ -epoxides having 8 to 18, preferably 12 to 14, carbon atoms, which subsequently contain 5 to 25, preferably 7 to 15, mol of ethylene oxide per mol ⁇ -epoxy were used.
  • the nonionic emulsifiers with 5 to 50, preferably 7 to 15, mol of ethylene oxide reacted with saturated or unsaturated fatty alcohols with 8 to 18, preferably 10 to 14, carbon atoms.
  • non-ionic emulsifiers with mixtures of 1 to 10, preferably 3 to 7 mol of ethylene oxide and 1 to 5, preferably 1 to 3 mol of propylene oxide (PO) reacted fatty alcohols with 8 to 18, preferably 10 to 14 C. Atoms, used.
  • fatty acids reacted with 5 to 15 mol ethylene oxide and having 8 to 22, preferably 10 to 18, carbon atoms are used as nonionic emulsifiers.
  • fatty acid alkanolamides having 8 to 22, preferably 10 to 18, carbon atoms reacted with 5 to 15 mol of ethylene oxide are used as nonionic emulsifiers.
  • nonionic emulsifiers are esters of sorbitan or of up to 40 mol ethoxylated sorbitan with fatty acids having 12 to 22 carbon atoms.
  • the method according to the invention can be carried out by first determining the phase inversion temperature by heating a sample of the emulsion prepared in the customary manner using a conductivity meter and determining the temperature at which the conductivity decreases sharply.
  • the specific conductivity of the oil-in-water emulsion initially present usually decreases over a temperature range of 2 - 8 ° C from initially over 1 millisiemens per cm (mS / cm) to values below 0.1 mS / cm. This temperature range is referred to here as the phase inversion temperature range.
  • the process according to the invention can be carried out either by subsequently heating the emulsion initially prepared as usual to a temperature which is within or above the phase inversion temperature range, or in that Way that one selects a temperature which is within or above the phase inversion temperature range already during the preparation of the emulsion.
  • the emulsions produced from the release agents for hydraulic binders according to the invention can have a solids content of 5 to 55% by weight, preferably 20 to 40% by weight.
  • the emulsions produced in this way are thin to viscous and have water as a continuous phase.
  • the emulsions can also contain customary auxiliaries customary in mold release agents for hydraulic binders, such as rust inhibitors, antioxidants, anti-porosity agents, preservatives, protective colloids, stabilizers, wetting agents, defoamers and adhesives in amounts of up to 15% by weight, based on the all means without water - included.
  • customary auxiliaries customary in mold release agents for hydraulic binders such as rust inhibitors, antioxidants, anti-porosity agents, preservatives, protective colloids, stabilizers, wetting agents, defoamers and adhesives in amounts of up to 15% by weight, based on the all means without water - included.
  • release agents according to the invention are to be used for hydraulic binders for formwork materials made of steel, the use of an anti-rust agent is recommended as an additive in order to avoid signs of corrosion on the formwork materials.
  • a number of compounds can be used as rust inhibitors or corrosion inhibitors.
  • a group of rust inhibitors according to the invention are, for example, the amines, for example octylamine, tridecylamine, dibutylamine, tributylamine, dimethylalkylamines having 8 to 18 carbon atoms in the alkyl chain or diamines such as ethylenediamine, 1,2-propylenediamine, diethylenetriamine and - preferably - Alkanolamines such as ethanolamine, diethanolamine, triethanoiamine, 1-amino-2-propanol, diisopropanolamine, triisopropanolamine, methylethanolamine, dimethylethanolamine, aminoethylethanolamine, ethylethanolamine, and diethylethanolamine, which have a corrosion-inhibiting effect, in particular on iron or iron-containing alloys.
  • the amines for example octylamine, tridecylamine, dibutylamine, tributylamine, dimethylalkylamine
  • Another group of active compounds are anionic compounds such as sodium, potassium or amine soaps from fatty acids, preferably having 6 to 10 carbon atoms, from dimer fatty acid or the corresponding compounds from aromatic mono- or dicarboxylic acids, such as benzoic or Phthalic acid.
  • anionic compounds such as sodium, potassium or amine soaps from fatty acids, preferably having 6 to 10 carbon atoms, from dimer fatty acid or the corresponding compounds from aromatic mono- or dicarboxylic acids, such as benzoic or Phthalic acid.
  • the alkali metal or amine salts of acidic phosphoric acid esters with alcohols having 6 to 18 carbon atoms or phosphoric acid salts such as trisodium phosphate are anticorrosive agents within the meaning of the invention.
  • Another group of corrosion-inhibiting compounds which can be used according to the invention are the amides of fatty acids or dimeric fatty acids with alkanolamines such as monoethanolamine or diethanolamine, monopropanolamine or dipropanolamine, or diamines such as ethylenediamine, 1,3-propylenediamine, 1,2-propylenediamine or diethylenetriamine.
  • alkanolamines such as monoethanolamine or diethanolamine, monopropanolamine or dipropanolamine, or diamines such as ethylenediamine, 1,3-propylenediamine, 1,2-propylenediamine or diethylenetriamine.
  • the last-mentioned amidoamines can be in a form neutralized with acids such as lactic acid be used.
  • the monoethanolamides of saturated and unsaturated fatty acids with 16 to 20 C atoms are preferably used, particularly preferably the ethanolamide of oleic acid or linoleic acid or technical mixtures of these
  • the amounts of added rust preventive are from 0.01 to 2% by weight, preferably from 0.1 to 1.0% by weight, based on the total agent without water.
  • the rust preventives can be incorporated into the oil component if they are soluble in it. It is also possible to add the rust preventive to the water required to emulsify the release agents for hydraulic binders or, after the emulsification has taken place, to the finished emulsion.
  • Hydraulic binders are mineral substances that harden like stones under water absorption and are water-resistant after hardening.
  • the preferred hydraulic binder is concrete.
  • the emulsions can be applied to the formwork surfaces, for example by spraying, spraying, brushing, brushing or brushing.
  • low-viscosity emulsions are so stable that they can be sprayed without problems.
  • the emulsions can be used to treat steel, plastic or wooden formwork in concrete construction.
  • the application can be done with the usual aggregates.
  • the oil components, emulsifiers and co-emulsifiers were mixed and heated to a temperature above the melting point of the mixture and homogenized.
  • the melt was then added to the water, which had been heated to approximately the same temperature, with stirring and then briefly (approx. 1 minute) heated to a temperature in the phase inversion temperature range or slightly above (95 ° C. in all examples) .
  • the emulsions were then cooled rapidly, ie at a cooling rate of about 2 ° C. per minute, to room temperature with stirring. After 24 hours, the flowability and the flow limit were determined. All of the microemulsions prepared according to Table I, Example 1.1-1.8, were liquid, ie mobile under the action of gravity. The yield point was well below 0.1 Pa (20 ⁇ C).
  • composition of the emulsions can be found in Table 1.
  • Alcohol component 1 2 222,, 55 2 222,, 55 22.5
  • the electrical conductivity of the emulsions as a function of the temperature was determined using a conductivity measuring bridge (Radiometer, Copenhagen). For this purpose, the emulsion was first cooled to + 20 ° C. At this temperature, the emulsions showed a conductivity of over 1 millisiemens per cm (mS / cm), ie they were in the form of oil-in-water emulsions. By slow heating with a heating rate of approx. 0.5 ⁇ C / min, which is controlled with the help of a temperature programmer in conjunction with a cryostat a conductivity diagram was created. The temperature range within which the conductivity dropped below 0.1 mS / cm was noted as the phase inversion temperature range. For all emulsions listed in Table 1, this temperature range was below 100 ° C (Table 1, phase inversion).

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Abstract

Afin de préparer des émulsions stables d'huile dans l'eau contenant des alcools liquides, on transforme un mélange à une température se situant dans la plage de températures d'inversion des phases ou supérieure à celle-ci en une émulsion d'huile dans l'eau finement dispersée de faible viscosité. Le mélange contient (a) 1 partie en poids d'un constituant huileux composé de (i) au maximum 70 parties en poids d'alcools monofonctionnels ayant 6 à 30 atomes de carbone non miscibles avec de l'eau et liquides à des températures comprises entre 5 et 15 °C et (ii) au moins 30 parties en poids d'un autre composé organique non miscible avec de l'eau; (b1) 0,1 à 0,5 parties en poids d'un émulsifiant non ionique ayant un équilibre hydrophile-lipophile compris entre 11 et 15; le cas échéant (b2) jusqu'à 0,2 parties en poids d'un co-émulsifiant du groupe des alcools gras saturés ayant 16 à 22 atomes de carbone ou des esters partiels de polyols ayant 3 à 6 atomes de carbone avec des acides gras saturés ayant 14 à 22 atomes de carbone; (c) 1 à 6 parties en poids d'eau; et le cas échéant (d) d'autres adjuvants usuels de démoulage de liants hydrauliques.
EP96901316A 1995-01-30 1996-01-22 Procede de preparation d'emulsions d'huile dans l'eau contenant des alcools liquides Ceased EP0807010A1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE19502892A DE19502892A1 (de) 1995-01-30 1995-01-30 Verfahren zur Herstellung von flüssige Alkohole enthaltenden Öl-in-Wasser-Emulsionen
DE19502892 1995-01-30
PCT/EP1996/000238 WO1996023638A1 (fr) 1995-01-30 1996-01-22 Procede de preparation d'emulsions d'huile dans l'eau contenant des alcools liquides

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EP0807010A1 true EP0807010A1 (fr) 1997-11-19

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DE10031917B4 (de) * 2000-06-07 2005-08-04 H. Hiendl Gmbh & Co. Kg Verwendung einer Wasser-in-Öl-Emulsion als Betontrennmittel
RU2656630C1 (ru) * 2017-06-05 2018-06-06 Игорь Викторович Столяров Способ удаления высола и восстановления поверхностей изделий из декоративного бетона

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JPS56162608A (en) * 1980-05-21 1981-12-14 Kindai Kagaku Kogyo Kk Release agent in case of manufacture of construction material
JPS5720309A (en) * 1980-07-10 1982-02-02 Dai Ichi Kogyo Seiyaku Co Ltd Aqueous parting agent for concrete
DK216984D0 (da) * 1984-05-01 1984-05-01 Koege Kemisk Vaerk Fremgangsmaade til forbedring af frigoerelse af beton fra stoebeforme
SU1608051A1 (ru) * 1988-12-23 1990-11-23 Центральный Научно-Исследовательский Экспериментальный И Проектный Институт По Сельскому Строительству Смазка дл металлических форм
JP3007470B2 (ja) * 1992-03-24 2000-02-07 花王株式会社 コンクリート用型枠剥離剤
JP2951796B2 (ja) * 1992-04-20 1999-09-20 花王株式会社 コンクリート用型枠剥離剤
FR2717731B1 (fr) * 1994-03-24 1996-05-15 Chryso Sa Concentré pour émulsion de démoulage des liants hydrauliques, émulsion de démoulage et utilisation.

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See references of WO9623638A1 *

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