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Publication numberUS2719858 A
Publication typeGrant
Publication dateOct 4, 1955
Filing dateJul 31, 1952
Priority dateJul 31, 1952
Publication numberUS 2719858 A, US 2719858A, US-A-2719858, US2719858 A, US2719858A
InventorsHill Eugene F
Original AssigneeEthyl Corp
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
High molecular weight alcohols
US 2719858 A
Abstract  available in
Images(4)
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Claims  available in
Description  (OCR text may contain errors)

United States Patent ce HIGH MOLECULAR WEIGHT ALCOHOLS Eugene F. Hill, Detroit, Micln, ass'ignor to Ethyl Corporation, New York, N. Y., a corporation of Delaware No Drawing. Application July 31, 1952,

Serial No. 301,977

3 Claims. '(Cl. 260-39715) The present invention relates to high molecular weight alcohols, and more particularly to novel mixtures of alcohols derived from sugar cane oil and a process for their preparation.

In processing sugar cane to obtain raw or refined sugar, a by-product filter residue or mud is obtained which contains sugar cane wax plus an oil composed essentially of glycerol esters of saturated and unsaturated fatty acids. The sugar cane wax, which is a valuable commercial product useful in formulating various wax and polish compositions, is extracted from thisfilter residue or mud by processes well known in the art. The wax extraction process leaves the sugar cane oil as a residue. Heretofore this sugar cane oil has been considered a waste product in that no economical and satisfactory method for converting it to useful commercial products was known. As a result of my investigations, however, I have discovered that sugar cane oil can be processed to produce novel and usefulmixtures of high molecular weight alcohols.

Accordingly, it is an object of my invention to provide new compositions of matter consisting essentially of novel and useful mixtures of high molecular weight alcohols. A more specific object of my invention is to provide a mixture of high molecular weight alcohols corresponding in number of carbon atoms to' the fatty acids contained in sugar cane oil. Still another object of my invention isto provide a process for preparing these novel alcohol mixtures. Other objects of my-invention will become apparent from a considerationof the following description and the appended claims wherein the novel features of my invention are specifically pointed out.

The above and other objects of my invention are accomplished by converting the sugar cane oil acids into the corresponding mixtures of high molecular weight alcohols. The mixture of alcohols obtained by my process can be utilized as such in the preparation of detergents, lubricant additives, and the like, and because of their unsaturated character are admirably suited for use in formulating drying oils. My novel alcohol mixtures are prepared from sugar cane oil by simultaneously treating the oil with an alkali metal and reducing alcohol. The reduction mixture is then hydrolyzed and the alcohols recovered from the mixture.

As previously indicated, the starting material for pre paring my alcohol mixtures is sugar cane oil. Although sugar cane oils vary in composition, a typical oil will analyze as follows:

2,7 l 9,8 58 Patented Oct. 4, v1955 2 The major portion of sugar cane'oil thus consists of saturated and unsaturated fattyacids, and these acids occur both as glycerol estersand free acids. The sugar cane oils are further characterized by the folowing typical analyses:

In accordance with my invention, 'rnixtures of high molecular weight alcohols are preparedfroin' such sugar cane oils by simultaneously treating the oil with alkali metal'and reducing alcohol, followed 'by hydrolysis of the reduced mixture. The chemicalre'act-ions involved canbedepicted as follows: i

where R is a carbon chain having from 10 to 30 carbon atoms, R is a lower alkyl radical, and M is an alkali metal. In carrying out the above reactions 'to prepare the alcohol mixtures, a preferred method utilizes alkali metal in the form'of subdivided particles.v Alkali metal dispersions, which are well known to the art, are there fore admirably suited for this purpose. Such dispersions are prepared by fusing alkali. metal in an inert hydro carbon and subjecting the entire mixture to vigorous agi= tation. The temperature of' the mixture is maintained at above the melting point of the alkali metal during the agitation, and the resulting product 'is a dispersion or suspension of finely divided particles of alkali metal. A variety ;of inert liquids are suitable for use as dispersing media in preparing such dispersions. Examples of typical dispersing media include toluene, xylene, benzene, petroleum fractions, heavy alkylate, and the like. Still other dispersing media can be employed, the above merely representing a list'of those most commonly used. The ratio of alkali metal to dispersing medium employed in forming dispersions can vary, and dispersions having metallic concentrations from trace amounts up to 60 per cent by weight are common. For use in my invention, however, it is preferred to utilize a dispersion having a metal concentration of between about 20 and 50 per cent by weight.

In carrying out the reduction reaction to prepare high molecular weight alcohol mixtures from sugar cane oil, it is preferred to utilize about 5 per cent excess of alkali metal over that theoretically required to accomplish the reduction. Although any of the alkali metals such as potassium, sodium, lithium, and the hke can be used, I prefer sodium. The quantity of alkali metal required to give a 5 per cent stoichiometric excess can readily be calculated and is a sum of the following three quantities:

( =lbs. metal for ester ?w=lbs metal for free acid is) v 1g =lbs. metal for hydroxyl compounds where A=Ester number of'oil B=Acid number of oil C=Hydroxyl value of oil M =Atomic weight of alkali metal W=Weight of oil used (lbs.) D=Molecular weight KOH E=Molecular weight OH As previously indicated, the reduction reaction is carried out using alkali metal and a reducing or hydrolytic alcohol. In general, the lower aliphatic secondary and tertiary alcohols are best suited for this purpose and include such alcohols as tertiary or secondary butyl alcohol, methyl isobutyl carbinol, and the like, these alcohols merely representing those mostly commonly used. The amount of hydrolytic alcohol employed in my reaction is preferably 5 per cent in excess over the stoichiometric amount, and this amount can be calculated as follows:

where F=molecular weight of reducing alcohol, and A, W, and D are as designated above.

As can be seen from the foregoing equations illustrating the chemical reactions involved, alcoholates are produced in the reduction reaction. In order that these alcoholates be kept in solution, the reaction should be carried out in an inert solvent medium; that is, a medium inert to the alkali metal. In general, aromatic hydrocarbons such as toluene and xylene are well suited for this purpose, although other materials such as petroleum fractions, dibutyl ether, and tertiary amine compounds and the like can be employed. The amount of inert solvent used can vary, although it is generally preferred =lbs. reducing alcohol to utilize a solvent-to-oil ratio from between about 1 to 1 and 5 to 1.

In accordance with one embodiment of my invention, the reactants are brought together by initially preparing in a suitable vessel an alkali metal dispersion of the type described above, utilizing the calculated amount of alkali metal. This dispersion is then heated sufiiciently so as to maintain a vigorous reflux. The heating is then discontinued, and a solution of sugar cane oil, reducing alcohol, and solvent is added to the dispersion at a rate sufiicient to maintain steady reflux. The addition is continued for a period of from one-half hour to two hours, after which time the mixture is heated for an additional period of from 15 minutes to an hour so as to insure complete reaction. This reduction mixture is then hydrolyzed by adding the mixture to a hydrolysis flask charged with a weight of water calculated to produce about a 20 per cent caustic solution. For example, when using sodium as the reducing metal, this amount of water is calculated as follows:

'174 wi. Na 5 Wt. rho- O.96 )(Wt. Na

4 solution of sodium chloride. The solvent and reducing alcohol are then removed from the alcohol products by distillation.

The following examples, in which all parts and percentages are on weight basis, will serve to further illustrate my invention.

Example I A reduction solution was prepared from 150 parts sugar cane oil (sample A described above), 72.8 parts methyl isobutyl carbinol, and 476 parts toluene. A sodium dispersion was prepared in a reaction flask equipped with a stirring mechanism and refiux condenser by fusing 38.5 parts sodium in 173 parts toluene and subjecting the mixture to vigorous agitation for a period of about 30 minutes. After the dispersion was formed, heat was applied sufiicient to establish a vigorous reflux. While maintaining reflux temperature, the reduction solution was added to the dispersion over a 30-minute period and the entire mixture cooked at reflux for a period of one hour. Following this cook period the mixture was hydrolyzed by addition to 272 parts water. Since the starting material contained an unusually high concentration of free fatty acid, an emulsion was encountered upon hydrolysis. In order to break this emulsion and effect a phase separation, the toluene-water azeotrope was distilled ofi and the emulsion broken when a total of 560 parts toluene and 118 parts water was removed. During the azeotropic distillation, 50 parts of water was added. When the emulsion was broken, the mixture separated into two clear liquid layers. The organic layer containing the product alcohols was decanted and washed with about parts of a 0.5 per cent sodium chloride solution. The remaining toluene and methyl isobutyl carbinol were then removed by heating to C. atlS mm. Approximately parts product consisting essentially of a mixture of high molecular weight saturatedand unsaturated alcohols was obtained representing a yield of approximately 99 per cent of theoretical.

As can be seen from the above example, in carrying out the process the presence of free fatty acids in the starting material somewhat complicates the hydrolysis step in that emulsions may be encountered. This can be minimized to a great extent by initially esterifying the Example II Two hundred parts of sugar cane oil (sample A) was mixed with 15 parts methanol and 0.5 part sulfuric acid and refluxed for a period of two hours. After treatment the excess methanol was removed by fractionation and the treated oil found to have the following analysis:

Saponification No. 144

Acid No 5 Ester No. 139 Hydroxyl value 1.5

A reduction solution was then prepared by adding 112 parts methyl isobutyl carbinol and 476 parts toluene to the methanol treated oil. This reduction solution was then added to 56.8 parts sodium dispersed in 215 parts toluene, and the reaction carried out as described in Example I. In this case, since the free acid had been largely esterified, the emulsion which formed upon hy drolysis was quickly broken by means of the azeotropic distillation described in Example I. The product was worked up as in Example I, and approximately 181 parts of alcohol mixture was obtained, representing a 97 per cent yield.

The crude .sugar cane oil obtained. by conventional processes normally contains a residual amount of wax, generally of the order of per cent by weight. Although it is not necessary in my process that this residual wax be removed prior to treating the oil with alkali metal, this can be done by merely treating the oil with a wax solvent such as acetone, and allowing the solution to stand for a period sufficient "to permit complete extraction. The solution of the oil is then decanted from the wax. The following example will serve to further illustrate this embodiment of my invention.

Example III Approximately 400 parts of sugar cane oil (sample B) containing about 10 per cent wax was mixed with 1280 parts of acetone and the mixture vigorously agitated. After standing for a period of 24 hours the acetone solution of the oil was decanted and the acetone removed by heating to 130 C. at mm. pressure. By this process a yield of 341 parts of wax-free sugar cane oil was obtained. This wax-free oil was then treated with methanol as described in Example II. The reduction solution was then prepared utilizing this wax-free methanol-treated oil and 114.8 parts methyl isobutyl carbinol and 650 parts toluene. This reduction solution was reacted with 57.8 parts sodium dispersed in 215 parts toluene in the manner described in the preceding examples. The reduction mixture was hydrolyzed and the product worked up in the manner identical to that described in Example I. A yield of approximately 181 parts alcohol mixture was obtained, representing a yield of 97 per cent theoretical.

The product obtained in each of the above three examples was a brown liquid when hot and had the appearance of a wax at room temperature. This product contains essentially high molecular weight alcohols, both saturated and unsaturated, having from about 10 to 30 carbon atoms. The sterols originally present in the sugar cane oil are substantially unaffected by the foregoing reduction process and are also present in the product mixture. Such a mixture can be utilized as such in the preparation of detergents, drying oils, and the like, although for some applications it may be desirable to effect a partial separation of the product into various fractions. For example, the sterols can be separated from the product mixture if desired. Although in practice it may be convenient to cut out somewhat different fractions of alcohols from the crude product, I have found it convenient to separate the above products into two fractions, one consisting essentially of C10 to C alcohols and the other consisting essentially of C20 to C alcohols, including the sterols. The C10 to C20 fraction has an average molecular weight of 260, this weight being slightly higher than that of a C17 alcohol. The iodine number of this fraction indicates an average of about 1.5 double bonds per molecule. The C20 to C30 fraction has an average molecular weight of 400 (about that of a C27 alcohol) and an average of 2.9 double bonds per molecule.

The above separation of the crude product into the C10 to C20 and C20 to C30 fractions can be conveniently accomplished by distillation carried out at about 225 C. and 1 mm. pressure. The distillate will consist of the C10 to C20 fraction, and the residue will contain the C20 to C30 fraction. This residue is then extracted with boiling acetonitrile, the extract decanted from the insoluble material, cooled to crystallize the C20 to C30 alcohols, and the C20 to C30 alcohols separated by filtration or some equivalent means.

The following examples will serve to illustrate this embodiment of my invention. The parts and proportions given are on weight basis.

Example IV Approximately 123 parts of the product obtained in Example II above was distilled at a temperature of 225 :6 C. and a pressure of .1 mm. Approximately 73 parts of distillate was obtained consisting essentially of Cru-to C20 alcohols having the following analysis:

Saponification No- 2 Acid No 0 Ester No 2 Hydroxyl value 6.3 Iodine No Saponification No 3 Acid No- 0 Ester No 3' Hydroxyl value 4.1 Iodine number 173 Melting point C 70-100 Example V One hundred forty parts of the product obtained in Example III above was treated in the manner described in Example IV. A yield of 81 parts of the C10 to C20 alcohol mixture was obtained having the following analysis:

Saponification No 2 Acid No 1 Ester No 1 Hydroxyl value" 6.7 Iodine No- 153 Twenty-two parts of C20 to C20 alcohols was obtained and had the following analysis:

Saponification No 7 Acid No 1 Ester No 6 Hydroxyl value 4.5 Iodine number 194 It can therefore be seen that by my invention I have provided new and useful mixtures of high molecular weight alcohols characterized by a relatively high degree of unsaturation. I have also provided a novel process for obtaining these alcohols using as a starting material sugar cane oil which has heretofore been generally considered waste material. An important embodiment of my process is that the unsaturation present in the starting material is preserved, thereby rendering the resulting products highly useful in applications suchas in formulating drying oils and resins which require high molecular weight unsaturated materials. The sugar can oil alcohols of my invention can also be used to prepare novel high molecular weight wax compositions by esterifying these alcohols with high molecular weight fatty acids. For example, one method of preparing such a wax consists of esterifying the sugar cane oil alcohols with sugar cane oil fatty acids.

It is to be understood that the above examples are given only by way of illustrating specific embodiments, and I intend by the appended claims to cover all modifi cations which fall within the spirit and scope of my invention.

I claim:

1. A new composition of matter comprising essentially a mixture of higher molecular weight alcohols derived from sugar cane oil by a process which comprises reducing sugar cane oil with an alkali metal and a hydrolytic alcohol and hydrolyzing the resulting reduction mixture.

2. A new composition of matter comprising a mixture consisting essentially of sterols derived from sugar cane oil and alcohols corresponding to the fatty acid radicals of sugar cane oil obtained by a process which comprises reducing sugar cane oil with an alkali metal and a References Cited in the file of this patent UNITED STATES PATENTS 868,252 Bouveault Oct. 15, 1907 Balch, Wax and Fatty By-Products From Sugar Cane,

8 Bertsch Aug. '28, 1934 Bertsch Aug. 28, 1934 Scott Oct. 29, 1935 Henke Feb. 16, 1937 Balch Aug. 7, 1945 Blinoif Feb. 8, 1949 OTHER REFERENCES 10 Oct. 1947, pp. 39-51.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US868252 *Jan 23, 1904Oct 15, 1907Louis BouveaultAlcohol and process of obtaining the same from carboxylic compounds.
US1971742 *Aug 2, 1930Aug 28, 1934American Hyalsol CorpProduction of primary alcohols
US1971743 *Nov 13, 1930Aug 28, 1934American Hyalsol CorpProcess of reducing organic compounds
US2019022 *Jun 9, 1934Oct 29, 1935Du PontPreparation of high molecular weight alcohols
US2070597 *Nov 14, 1934Feb 16, 1937Du PontProcess for producing alcohols
US2381420 *Jul 25, 1942Aug 7, 1945Claude R WickardHard waxes and fatty products derived from crude sugar cane waxes
US2460969 *Dec 11, 1946Feb 8, 1949Innovations Chimiques SinnovaMethod for producing higher molecular alcohols
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2809206 *Apr 21, 1954Oct 8, 1957Ethyl CorpTreatment of fatty acid esters and production of high molecular weight alcohols therefrom
US2824143 *Jan 13, 1955Feb 18, 1958Abner EisnerProduction of lanolin alcohols
US2865968 *May 6, 1955Dec 23, 1958Nat Distillers Chem CorpProduction of fatty alcohols
US2915564 *Apr 15, 1955Dec 1, 1959Nat Distillers Chem CorpReduction of fatty acid esters to produce alcohols
US4371470 *Feb 18, 1981Feb 1, 1983Lion CorporationMethod for manufacturing high quality fatty acid esters
US5663156 *Feb 25, 1993Sep 2, 1997Laboratorios Dalmer SaMixture of higher primary aliphatic alcohols, its obtention from sugar cane wax and its pharmaceutical uses
US5856316 *Dec 23, 1996Jan 5, 1999Laboratorios Dalmer SaMixture of higher primary aliphatic alcohols, its obtention from sugar cane wax and its pharmaceutical uses
US7192524 *Jan 21, 2005Mar 20, 2007Rafael AlmagroMethod for processing sugar cane filter cake mud and extracting component products
Classifications
U.S. Classification552/545, 568/884, 568/923, 568/851, 568/919, 568/864
International ClassificationC07C29/00, C07C29/147
Cooperative ClassificationC07C29/147
European ClassificationC07C29/147