Glycosiduronic acids (Preparation process)

Abstract: Glycosiduronic acids, such as alkyl glycosiduronic acids or alkenyl glycosiduronic acids, which may be used in the preparation of surfactant compositions, such as detergents and cleansers, are prepared by reacting an oxidised mono-, oligo-, or polysaccharide with up to 10 monomer units with one or more fatty alcohols having 8-22 carbon atoms in the presence of a catalyst, preferably in bulk, and after acetalisation removing the excess alcohol. Preferably the oxidised monosaccharide used is glucuronic acid and/or glucuronic acid-3,6-lactone.

Description: The invention relates to a process for the preparation of glycosiduronic acids, such as alkyl glycosiduronic acids or alkenyl glycosiduronic acids. For some time now it has not only been endeavoured to use biodegradable substances in mass-produced articles such as detergents and cleansers in order to protect the environment, but also, since raw material sources such as crude oil or mineral coal are exhaustible, attempts are being made to prepare these compounds on the basis of regenerating raw materials. Thus, e.g., alkyl glycosides, such as alkyl monosaccharides and alkyl oligosaccharides, according to US 3 839 318 are obtained from aldose sugars and higher alcohols and used as nonionic surfactants. According to EP-A-0 415 192, alkyl glycosides can be prepared by reacting mono-, oligo-, or polysaccharides with a fatty alcohol in the presence of sulphosuccinic acid. Due to their limited solubility, the use of these products as mass-produced surfactants is subject to restrictions. Efforts have been made to increase the hydrophilic nature of these substances by oxidising such alkyl glucosides to alkyl glucuronic acids, as is described, e.g., in EP-A-0 326 673. Because of their hydrophilic and hydrophobic structural elements these compounds are highly suitable for use as detergents and cleansers both by themselves and in combination with other surfactants. A drawback to this preparative process is that a comparatively large amount of catalyst is needed, that despite the use of large amounts of catalyst the yield is unsatisfactory, and that, furthermore, long reaction periods are required. Therefore, there is still need for an improved process for the preparation of glycosiduronic acids such as alkyl glycosiduronic acids or alkenyl glycosiduronic acids. Hence the object of the invention is to provide a process for the preparation of glycosiduronic acids which does not have the drawbacks listed hereinbefore, has above all economic advantages and operates with good yields. This object is attained by means of a process for the preparation of glycosiduronic acids, such as alkyl glycosiduronic acids or alkenyl glycosiduronic acids, having a) at least one glycoside unit carrying a carboxyl function directly attached to the glycoside ring, and b) at least one glycoside unit carrying an acetalically bound hydrocarbon group, such as an alkyl or alkenyl group with 8-22 carbon atoms, the unit defined under a) and b) optionally being the same unit, which is characterised in that an oxidised mono-, oligo-, or polysaccharide with up to 10 monomer units is reacted with one or more fatty alcohols having 8-22 carbon atoms in the presence of a catalyst, preferably in bulk, and after acetalisation the non-reacted alcohol is removed. The use of a stoichiometric excess of the fatty alcohol is preferred. Preferably, the catalysts used are acid catalysts, more particularly p-toluene sulphonic acid, sulphosuccinic acid, methane sulphonic acid and C 14/16 -olefin sulphonic acid. It is advantageous to use 1-6, preferably 1-3 moles of fatty alcohol per mole of oxidised saccharide. In a preferred embodiment of the process according to the invention the oxidised saccharide is reacted, in a first step, with an excess of the fatty alcohol, and after the first step, further oxidised saccharide is added in one or more portion. After acetalisation the excess fatty alcohol can be removed at best by one of the following two general procedures. The first procedure comprises the distillation of the excess alcohol, more particularly the distillation of the alcohol from thin films of the reaction mixture at a temperature of 100° to 190°C, preferably 150°-180°C, preference being given in this procedure to molecular distillation. The second procedure comprises a process which may be called a liquid/solid separation process. Herein the reaction mixture is treated with an organic solvent, preferably lower aliphatic alcohols such as ethanol or isopropanol, containing a base thus precipitating the alkyl glycosiduronic acid as salt. The excess fatty alcohol remains in solution. Whereas the distillation is preferred at higher fatty alcohol/oxidised saccharide ratios, the liquid/solid separation process is preferably used at lower fatty alcohol/oxidised saccharides ratios. In one especially advantageous embodiment of the process according to the invention the oxidised monosaccharide used is glucuronic acid and/or glucuronic acid-3,6-lactone. The glycosiduronic acids have as their bases monosaccharides or polysaccharides containing up to 10 monomer units, which have at least one glycoside unit carrying a carboxyl function - optionally in the form of a lactone - that is directly attached to the sugar ring. The basis of these carboxyl-functional mono-, oligo-, and polysaccharides is formed, in its turn, by mono-, oligo-, and polysaccharides of which the glycoside units are present in the α- or β-form 1,2-, 1,3-, 1,4-, or 1,6-linked. These saccharides may be composed of hexoses which in the non-oxidised form carry primary glycosidic hydroxyl groups, such as glucose, galactose, and mannose. The preferred component is glucose. The preferably obtained glycosiduronic acids contain at least one glucuronic acid unit of the structure In addition, also other glycoside units, more particularly glycoside units of the structure may be comprised. The hydrocarbon group is acetalically bound and preferably lies in the structure wherein R = C 8-22 alkyl. Alternatively, the acetalically bound hydrocarbon group may be present in the form of other glycoside units, more particularly glycoside units of the structure Particularly preferred glycosiduronic acids are alkyl glucuronic acids of the structure wherein R = C 8-18 alkyl. The glycosiduronic acids are prepared by reacting the described oxidised mono-, oligo-, or polysaccharides with a fatty alcohol in the presence of a catalyst at elevated temperature. It is also possible for mixtures to be used. For acetalising preferably use is made of oxidised monosaccharides, more particularly glucuronic acid and glucuronic acid-3,6-lactone. The fatty alcohols contain an alkyl group with 8-22 carbon atoms. In addition, the alkyl group may be linear or branched. In the primary reaction fatty alcohols are employed in stoichiometric excess, more particularly in an amount of 3-6 moles (calculated on 1 mole of oxidised saccharide). With regard to additional dosage of oxidised saccharide the overall molar ratio of fatty alcohol and oxidised saccharide is about 1-6:1. Instead of an alkyl group some other, e.g. unsaturated hydrocarbon group, such as an alkenyl group, may be present. As an example the oleyl group is mentioned. By fatty alcohols are meant both alcohols of natural origin and synthetically prepared alcohols. The alcohol's hydrocarbon group may carry substituents, e.g. hydroxyl groups; alternatively, the hydrocarbon chain may be interrupted by heteroatoms, such as oxygen. Suitable as catalyst are conventional acetalisation catalysts, such as p-toluene sulphonic acid, sulphosuccinic acid, and sulphuric acid. The catalysts are added in an amount of 0.2-5 wt.% (calculated on oxidised glycoside), preferably in an amount of 0.5-2 wt.%. The reaction is carried out at a temperature of 70°-110°C, preferably 80°-100°C. To accelerate the reaction the removal of the formed water is supported by applying a vacuum. If the reaction affords additional dosage of oxidised saccharide each further portion can be added when the previous portion has been dissolved in the reaction mixture. The reaction is proceeded for about 0.5-3 hours, preferably 1-2 hours, after the last portion of oxidised saccharide has been dissolved. The excess fatty alcohol can be removed by vacuum distillation, preferably by distilling the excess alcohol from thin films of the reaction mixture at a temperature of 100-190°C, more particularly 150-180°C. The removal by distillation is preferably applied to reaction mixtures with higher fatty alcohol/oxidised saccharide ratios. By treatment with bases, such as alkali metal hydroxides, ammonia, and amines, the thus prepared glycosiduronic acids can be converted to their water-soluble salts. Alternatively, the reaction mixture can be treated with an organic solvent, such as ethanol and isopropanol containing a base. The organic solvent dissolves the fatty alcohol and the base forms the corresponding salt of the glycosiduronic acid which precipitates from the organic phase. The glycosiduronic acid salts show surface active properties and can be used for the preparation of detergents and cleansers. They can be combined with other surfactants and with other substances used in the preparation of detergents and cleansers. The invention will be further elucidated with reference to the following examples Example 1 790 g of a C 12/14 fatty alcohol mixture are charged to a distillation apparatus and heated to 90°C. Subsequently, 1,8 g of p-toluene sulphonic acid are added. After the catalyst has dissolved, 176 g of finely powdered glucuronic acid-3,6-lactone are added and a water jet vacuum is applied. After 2.5 hours the glucuronic acid lactone has dissolved. Stirring is continued for another hour. After this time the reaction water is virtually completely separated. Then the reaction mixture is subjected to molecular distillation in an oil pump vacuum at 170°C to separate the excess fatty alcohol. Example 2 395 g of a C 12/14 -fatty alcohol mixture is charged to a distillation apparatus and heated to 95°C while stirring. Then, 0.9 g of p-toluene sulphonic acid are added. After the catalyst has dissolved, 88 g of finely powdered glucuronic acid-3,6-lactone are added and a water jet vacuum is applied. After about 2 hours the glucuronic acid-3,6-lactone has dissolved. Then, the water jet vacuum is interrupted and another portion comprising 88 g of finely powdered glucuronic acid-3,6-lactone and 0.9 g p-toluene sulphonic acid is added. After 1-1.5 hours the additional portion lactone has dissolved. The last step is repeated once more. After a subsequent stirring of about 1 hour the reaction water is virtually completely separated. The reaction mixture is poured within 30 min into a well-stirred solution of 80 g sodium hydroxide in 3 l ethanol of 60°C. After complete addition, the reaction mixture is refluxed for 30 min. The suspension is cooled, and filtered at room temperature. The filter cake is washed with ethanol and dried in vacuum. The sodium salt of C 12-14 -alkylglucuronic acid is recovered as yellowish powder (bleachable, e.g. by means of hydrogen peroxide). It was particularly surprising that with the process according to the invention it was not only possible to reduce the reaction times in comparison with the acetalization of non-oxidized saccharides, but also that good yields were obtained. It is also possible to work at lower temperatures. This difference renders the process considerably more economical. The raw materials used are renewable and the biodegradability of the products is very good. The products are eminently suited to be used for the preparation of detergents and cleansers. If the amounts of fatty alcohol required for acetalising glucose are compared with the amounts of fatty alcohol needed in the process according to the invention for the acetalisation of equal molar quantities of glucuronic acid or glucuronic acid lactone, a notable reduction in the amount of alcohol needed will result in the case of the process according to the invention.

Claims: A process for the preparation of glycosiduronic acids having a) at least one glycoside unit carrying a carboxyl function directly attached to the glycoside ring, and b) at least one glycoside unit carrying an acetalically bound hydrocarbon group with 8-22 carbon atoms, the unit defined under a) and b) optionally being the same unit, characterised in that an oxidised mono-, oligo-, or polysaccharide with up to 10 monomer units is reacted with one or more fatty alcohols having 8-22 carbon atoms in the presence of a catalyst, and after acetalisation the non-reacted alcohol is removed. A process according to claim 1, characterised in that a stoichiometric excess of the fatty alcohol is used. A process according to claim 1 or 2, characterised in that the reaction is carried out in bulk. A process according to one or more of claims 1-3, characterised in that use is made of acid catalysts. A process according to claim 4, characterised in that the catalyst used is selected from the group consisting of p-toluene sulphonic acid, methane sulphonic acid, C 14/16 -olefinsulphonic acid and sulphosuccinic acid. A process according to one or more of claims 1-5, characterised in that per mole of oxidised saccharide 1-6 moles of alcohol are employed. A process according to one or more of the claims 1-6, characterised in that per mole of oxidised saccharide 1-3 moles of alcohol are employed. A process according to one or more of claims 1-7, characterised in that in a first step the oxidised saccharide is reacted with an excess of fatty alcohol and after the first step a further oxidised saccharide is added in one or more portions. A process according to claim 8, characterised in that for the primary step per mole of oxidised saccharide 3-6 moles of fatty alcohol are employed. A process according to claim 9, characterised in that for the primary step per mole of oxidised saccharide 3-4 moles of fatty alcohol are employed. A process according to one or more of claims 1-10, characterised in that the non-reacted alcohol is removed by means of distillation. A process according to claim 11, characterised in that the alcohol is removed by distillation from thin films of the reaction mixture at a temperature of 100° to 190°C. A process according to claim 12, characterised in that the distillation is carried out at a temperature of 150°-180°C. A process according to claim 12 or 13, characterised in that a molecular distillation is carried out. A process according to one or more of claims 1-10, characterised in that the reaction mixture is treated'with an organic solvent containing a base and in that the precipitated alkyl glycosiduronic acid salt is separated. A process according to claim 15, characterised in that the solvent used is a lower aliphatic alcohol. A process according to claim 16, characterised in that the lower aliphatic alcohol is selected from the group consisting of ethanol and isopropanol. A process according to one or more of claims 1-17, characterised in that the oxidised monosaccharide used is glucuronic acid and/or glucuronic acid-3,6-lactone. A process according to any one of claims 1-18, characterised in that the hydrocarbon group is an alkyl group. A process according to any one of claims 1-19, characterised in that the hydrocarbon group is an alkenyl group.

Inventors: SCHATTSCHNEIDER MANFRED, WEISSEN HANS JOACHIM, WEUSTE BURKHARD, SCHATTSCHNEIDER, MANFRED, WEISSEN, HANS JOACHIM, WEUSTE, BURKHARD
Applicants: AKZO NOBEL NV, AKZO NOBEL N.V.
Application year: 1992
Main classification: C07H15
IPC codes: C11D1, B01J31, C07H15, C07B61, C08B37