US2547208A

US2547208A - Method for the refining of tall oil soap

Info

Publication number: US2547208A
Application number: US757329A
Authority: US
Inventors: Hasselstrom Torsten; Stoll Michael
Original assignee: Us Ind Chemicals Inc
Current assignee: U S Ind Chemicals Inc
Priority date: 1947-06-26
Filing date: 1947-06-26
Publication date: 1951-04-03
Anticipated expiration: 1968-04-03

Description

Patented Apr. 3, 1951 UNITED STATES METHOD FOR THE REFINING OF TALL OIL SOAP ware No Drawing. Application June 26, 1947, Q

, Serial No. 757,329

6 Claims. 1

This invention relates to a .method for the refining of an aqueous tall oil soap containing undesirable non-saponifiable components and color bodies to effect a substantial removal of such undesirable constituents.

Tall oil soap (skimmings) is obtained in quantity in the manufacture ofpine wood pulp by the sulfate process, and is composed primarily of an aqueous solution of the sodium salts of various fatty and resin acids, together with a minor but appreciable proportion of non-saponifiables and color bodies. For the tall oil released by the acidification of such a tall oil soap to be of the greatest utility in the manufacture of esters, alkyd resins, etc., it is necessary that the tall oil be substantially free from the aforementioned non-saponifiables and color bodies. Many processes have been. suggested for the refining of tall oil as such (e. .g., distillation, contacting with adsorbent or mineral acids, etc.), but such processes do not result in an effective separation of the aforementioned undesirable components from the tall oil. For example, distillation at temperatures in excess of about 100 C. of a tall oil containing non-saponifiables results in the formation of nondistillable esters by a combination of the tall oil fatty acids and the non-saponifiables, thus reducing the amount of commercially useful fatty acids in such distilled tall oil.

The foregoing being briefly the state of the art, it is an object of this invention to provide a method for the refining of a crude tall oil soap containing non-saponifiable components and color bodies toeffect a substantial removal of such undesirable materials.

It is also an object of this invention to provide a tall oil soap from which there may be released by acidification a tall oil which may be more advantageously processed inaccordance with known procedures to provide an improved and further refined tall oil.

The foregoing and other objects are accomplis'hecl in accordance with this invention by d1:- solving in certain ketones an aqueous solution of a tall oil soap containing undesirable non-saponiv fiables and color bodies, and thereafter diluting the ketone solution with water to form a ketone layer and an aqueous tall oil soap layer containing reduced quantities of non-saponi'fiables and color bodies.

The examples which follow illustrate specific embodiments of the method of this invention, and are to be considered not limitative thereof.

Example I .139 parts by weight of acrude tall oil soap containing 65% solids was dissolved in 839 parts by weight of methyl isobutyl ketone while the solvent was being refluxed. The solution was then refluxed for 15-20 minutes, and was then cooled to (3., after which 800 parts by weight water was added. The mixture separated into two layers after a period of about '15 minutes. Analyses of the talloil soap before and after having been subjected to the foregoing treatment showed that the non-saponifiable content thereof had been reduced from 5.4 to 0.9%, based upon the total solids content of the tall oil soap, and also that the color of the tall oil soap had been substantially decreased.

The aqueous tall oil soap layer prepared as just described contains a small amount of methyl isobutyl ketone, which assists in the retention of the aforementioned 0.9% of non-saponifiables in that layer. However, such residual non-saponifiable content may be easily furthenreduced by contacting the aqueous tall oil soap layer with fresh portions of the lretone. Thus, by mixing the aqueous tall oil soap layer at reflux temperature with an equal volume of methyl isobutyl ketone, cooling the mixture, separating the aqueous tall oil soap layer from the methyl isobutyl ketone layer, and repeating this process three times more, the nonsaponifiable content of the aqueous tall oil soap layer furtl'ier reduced to (3.3%, based upon the total solids content of the tall oil soap.

Example II 10 parts by weight of a crude tall oil soap containing solids was dissolved in 200 parts by weight ofinethyl isobutyl ketone by stirring them together at room temperature for a period of about 30 minutes. The insoluble portion of the tall oil soap, representing 1.7% of the total solids content thereof, was filtered off. To 252 parts by volume of the filtered methyl isobutyl ketone solution was added at room temperature parts by volume of water. Upon standing, the mixture separated into two layers, viz., an upper methyl isobutyl lcetone layer amounting to about 235 parts by volume and containing a substantial proportion of the non-saponifiable constituentsof the crude tail oil, and a lower aqueous layer amounting to about lei parts by volume and containing the refined tall oil soap, which was substantially lighter in color than the crude tall oil soap subjected to the aforementioned refining treatment.

The illustrate the method f this invention the reduction of the conent of noihsaponifiables and color bodies in an ion of a tail oil soap by dissolving the s ion 1 a ketone, thereafter diluting the lzetone solution with water tcform a ketone produced procedure are valuable compositions of matter.

layer, and an aqueous tall oil soap layer containing reduced quantities of non'saponifiables and color bodies. Although methyl isobutyl ketone was employed as a solvent for the aqueous tall oil soap in the examples, there may be sub- .stituted for such ketone any ketone which is a liquid at ordinary temperatures and which at ordinary temperatures is soluble in water to the pe centage is not critical. in general, the aqueous tall oil soap to be refined in accordance with the method described herein should preferably contain from about 39 to about 75% by weight of solids in order that the refining may be effected most economically. The upper limit of concentration of the tall oil soap in the aqueous solution treated is determined by the ease or handling such solution as a liquid.

In addition, the amount of ketone used to dissolve the aqueous solution of the tall oil soap will depend upon various factors, such as the particular ketone used, the concentration of tall oil soap in the aqueous solution thereof, upon the temperature at which the solution is effected, etc.

However, the volume of ketone employed is gen erally from about 8 to about 60, and preferably from about 10 to about 20, times the volume of the water contained in the aqueous tall oil soap solution to be refined. Solution of the aqueous tall oil soap in the ketone results in a precipitation of the sodium salts of certain acidic color bodies and a portion of the sodium salt of lignoceric acid contained in the tall oil soap being treated, and the precipitate thus formed should preferably be separated from the remainder of the ketone solution at this stage of the procedure.

As is seen from the examples, the addition of sufficient water to the solution of aqueous tall oil and ketone results in the formation of two layers, one of which is the ketone substantially free from tall oil soap but containing a substantial proportion of the non-saponifiaoles and color bodies originally present in the crude tall oil soap, and the other of which is an aqueous solu- 7 tion of the tall oil soap having a reduced content of non-saponifiables and color bodies. The partition constant greatly favors the ketone phase with respect to the non-saponifiable materials. When a crude aqueous tall oil soap containing 65% of solids is refined, the most effective separation of the two layers is in general accomplished by the addition to the solution of aqueous tall oil soap in the ketone or at least four volumes of water, based upon the volume of crude aqueous tall oil soap present, followed by a settling period of at least minutes. Residual amounts of the ketone dissolved in the aqueous phase may be removed therefrom and recovered for further use by heating such aqueous phase and distilling the ketone therefrom.

Both the aqueous layer and the ketone layer in accordance with. the foregoing Thus, acidification of the aqueous layer results in the separation of a tall oil of improved properties for the preparation of esters, alkyd resins, etc. The tall oil produced by such acidification may also be further refined in accordance with known methods, such as distillation, contacting with adsorbents, etc. The ketone layer, on the other hand, may be stripped of solvent, leaving a residue having a high content of beta sitosterol.

We claim:

1. The method of refining an aqueous solution of a tall oil soap comprising 25% to 70% water and also containing undesirable non-saponiflabios and color bodies, which method comprises dissolving said aqueous solution to form a single phase in a dialkyl ketone which is liquid at ordinary temperatures and which, at ordinary temperatures, is soluble in water to the extent of about 0.2% to about 113% by weight and thereafter separating the setone solution into a ketone layer con; ning the niaior portion of the nonsaponifiables and color bodies and an aqueous layer containing the major portion of the tall oil soap by adding further water to the said ketone solution.

2. The method of refinin an aqueous solution of a tall oil soap comprising from about 30% to about 75% by Weight of solids and containing undesirable non-saponifiables and color bodies, which method corn-prises dissolving said aqueous solution to form a single phase in a dialkyl kctone which is liquid at ordinary temperatures and which, at ordinary temperatures, is soluble in Water to the extent of 0.2% to about 10% by weight and thereafter separating the ketone solution into a ketone layer containing the major portion of the non-saponifiables and color bodies and an aqueous layer containing the major portion of the tall oil soap by adding further Water to the said ketone solution.

3. The method of refining an aqueous solution of a tall oil soap comprising 22% to 70% water and also containing undesirable non-saponifiabios and color bodies, which method comprises dissolving said aqueou solution in methyl isobutyl ketone to form a single phase and thereafter separating the ketone solution into a ketone layer containing the major portion of the non-saponifiables and color bodies and an aqueone layer containing the major portion of the tall oil soap by adding further water to such ketone solution.

l. The method or" refining an aqueous solution of tall oil soap comprising from about 30% to about 75% by weight of solids and also containing undesirable non-saponifiables and color bodies, which method comprises dissolving said aqueous solution in methyl isobutyl ketone to form a single phase and thereafter separating the ketone solution into a ketone layer containing the major portion or the non-saponifiables and color bodies in an aqueous layer containing the major portion of the tall oil soap by adding further water to the said ketone solution.

5. The method of refining an aqueous solution of a tall oil soap comprising 25% to 70% water and also containing undesirable non-saponifiables and color bodies, which method comprises dissolving said aqueous solution to form a single phase in a dialkyl ketone which at ordinary temperature is soluble in water to the extent of 0.2% to about 10% by weight, at a temperature within the range from about room temperature to the boiling point of the lzetone and thereafter-separating the ketone solution into a ketone layer containin" the major portion of the non-saponifiables and color bodies and an -aqueous layer containing the major portion ofgthe tall oil soap by adding further water to the said ketone solution.

6. The method of refining an aqueous solution of a tall oil soap comprising 25 to 70% water and also containing undesirable fInon-saponifiables and color bodies, whichniethod comprises dissolving said aqueous solutionin a dialkyl ketone which at ordinary temperature is soluble in waterito the extent of aboutg0.2% to about 10% by weight, at a temperature within the range ifrqin' about room temperature to the boiling point of the ketone, separating any precipitated s ids from the solution and thereafter the ketone solution ,iiinto a ketone aining the major portipn of the nonsaponifiables and color bodies and an aqueous REFERENCES CITED The following references are of record in the file or this patent:

V UNITED STATES PATENT Nurnber Name Date 2,399,483 Turck Lari, 26, 1943 Lovas et a1. Feb. 19, 1946 OTHER REFERENCES 2 @Cihemioal Abstracts, vol. 38, page 281 9, citing Bufiiazhnaya Prom. 19, No. 2, 18-21 (1941);

Claims

1. THE METHOD OF REFINING AN AQUEOUS SOLUTION OF A TALL OIL SOAP COMPRISING 25% TO 70% WATER AND ALSO CONTAINING UNDESIRABLE NON-SAPONIFLABLES AND COLOR BODIES, WHICH METHOD COMPRISES DISSOLVING SAID AQUEOUS SOLUTION TO FORM A SINGLE PHASE IN A DIALKYL KETONE WHICH IS LIQUID AT ORDINARY TEMPERATURES AND WHICH, AT ORDINARY TEMPERATURES, IS SOLUBLE IN WATER TO THE EXTENT OF ABOUT 0.2% TO ABOUT 10% BY WEIGHT AND THEREAFTER SEPARATING THE KETONE SOLUTION INTO A KETONE LAYER CONTAINING THE MAJOR PORTION OF THE NONSAPONIFIABLES AND COLOR BODIES AND AN AQUEOUS LAYER CONTAINING MAJOR PORTION OF THE TALL OIL SOAP BY ADDING FURTHER WATER TO THE SAID KETONE SOLUTION.