US1781772A - Process of manufacturing color lakes from petroleum - Google Patents

Description

Patented Nov. 18, 1930 UNITED STATES PATENT OFFICE GELLERT ALLEMAN, OP SWARTHMORE, PENNSYLVANIA, ASSIGNOR TO SUN OIL COH- PANY, F PHILADELPHIA, PENNSYLVANIA, A CORPORATION OF NEW JERSEY PROCESS OF UFACTURING COLOR LAKES FROM PETROLEUM- No Drawing. Original application filed February 6, 1924, Serial No., 691,023. Divided and this application filed August 24, 1926. Serial No. 131,311.

The object of my invention is to produce color lakes by the treatment, with water- Y fatty acid soap. I start with the alkali precipitate or soda sludge resulting from the treatment, with caustic soda or other alkali, of acid-treated lubricating stock. A typical composition comprises fatty acid soap, 11.6%; inert material similar to fossil res ins, 17.1%; sodium sulfate, 2.3%, mineral oil, 46%; water, 23%. To-this composition I add water until the water content is approximately fitty-eight per cent. I then heat'the composition to a steam pressure of about sixty pounds for about two hours, and cool it while applying compressed air under pressure of about sixty pounds. .The oil separates out as a top layer. A solution of soap and resin, containing no mineral oil but containing a little sodium sulfate, separates out as a middle layer. The bottom layer is an aqueous solution of sodium sulfate. If the cooling be carried down to 5 C. or below, the separation of the sodium sulfate solution from the solution of soap and resin is practically complete. It is unnecessary, however, to effect a complete elimination of the sodium sulfate, but if a complete separation is desired, it is preferred to concentrate the solution of soap and resin by driving off half ofthe water, more or less, and then cooling to 5 (3., or below, the separation being hastened by low temperatures. Aside from the desirability of completely removing the sodium sulfate, concentration of the soap and water solution is desirable, thereby producing a soap and resin solution that solidifies to a pasty mass. The product is free from mineral oil. The process above described is also set forth in applications filed by me sludge so as to eliminate a large part of the Water and most of the sodium sulfate and to reduce the percentage. of mineral oil. Instead of starting my process with the untreated alkali precipitate, I may start the process with the product of the Maitland patents. In either case, after the described heating and cooling under pressure, I produce a product comprising a fatty acid soap derivative frompetroleum containing petroleum resins and substantially free from mineral oil.

If it be desired to obtain a productcomprising a fatty acid soap derivative from specified Maitland patents. If I start with an emulsion, or colloidal suspension, resulting from the treatment with caustic soda of acid-treated mineral oil lubricating stock having the approximate composition hereinbefore given, I proceed as follows:

To the emulsion I add gasoline and also a small amount of lithium sulfate, sodium sulfate or potassium sulfate, or a small amount of lithium chloride, sodium chloride or potassium chloride. An immediate separation takes place of the gasoline and mineral oil, with most of the resins dissolved therein, from the soap, water and a minor proportion of the resins.- The sulfates are found to be superior to the chlorides, the double negative charge on the sulfate ion being more effective than the single negative charge on the chloride ion in neutralizing and precipitating the positively charged emulsion particles. Lithium salts are superior to sodium salts, and sodium salts superior to those of potassium. This is a function of surface tension lithium salts increasing 1e surface tension more than sodium or potassium salts, and hence tending to break the emulsion more readily. From a commercial standpoint, so-

dium chloride (common salt), because of its suspended colloidal particles.

abundance and low cost, seems to be the most desirable substance to elliectthe separation of the gasoline and oil, with dissolved resins, from the soap, water and a minor proportion of resins. A saturated aqueous solution of the salt is used, being added to the amount of ten per cent. of the total volume. The salt solution may be added before the introduction of the gasoline or it may be added after the gasoline has been distilled into the soapoil-water emulsion. Instead of using a saturated solution of salt in water, solid sodium chloride (salt) may be added.

It is best to allow the gasoline to enter the crude soap tank, at the bottom, as a vapor. This stirs the mixture. and probably also aids in neutralizing the electrical charges on the Larger surfaces are exposedto the gasoline, in this manner.

The apparatus employed is conveniently arranged as follows: An upright, cylindrical container is employed to hold the oilsoap-water emulsion, which should fill the container to about onethird its capacity, This is conveniently connected to a gasoline still. The bottom of the first mentioned container should be above the level of the gasoline still. Vapors of gasoline are passed through appropriate pipes, from the still, to the bottom of the container holding the soapoil-water emulsion. A saturated solution of common salt, equivalent in volume to about one-tenth of the soap-oil'gasoline emulsion is added. Gasoline vapor is introduced at the bottom until the container is almost filled by the condensed gasoline. tion of gasoline into this container is then discontinued and the mixture allowed toseparate. The gasoline-oil layer on top is siphoned back into the gasoline still and the process repeated. After about three extractions, the soap-water solution which remains in the bottom of the container is substantially free of mineral oil, but contains such petroleum resins asmay not have been dissolved by the gasoline.

The purified soap contains the original sulfur compounds, wholly or principally sodium sulfate, which were in the crude soap. These can be largely removed by known methods if their removal be desirable. For example, the soap solution maybe concentrated by first evaporating some of the Water (to expedite the operation) and then cooling in order to separate the soap from the sodium sulfate, which remains in solution in the water. The separation begins to take place at about 5 C. and is hastened by lower temperatures. The sodium sulfate remains in solution in the water.

The soap may be converted into fatty acids,

in any known manner, as, for example, by

decomposing the soap with sulfuric, hydrochlor1c or other mineral acids. These fatty The introducacids have an acid number of about 103.5. (The original crude soap before treatment yields fatty acids having an acid number of 30.)

The fatty. acids are now subjected to distillation at an absolute pressure of 4 mm., yielding distillates which are free from resins. Up to a temperature of 180 C. a fraction is obtained having an acid number of 187.06. The next fraction boiling off between 180 and 190 C. has an acid number of 174.4. The next fraction boiling off between l9.0 and 200 C. has an acid number of 160. The residue, containing most of the resins, present before distillation, has an acid number of 61. The distillates contain very little of the resins, the lower boiling distillate being almost free of resin. The last described process is set forth in an application filed by me July 18, 1925, Serial No. 44,629. To manufacture my improved color lakes, I may utilize the. soap produced by the first described process, which is free of mineral 7 oil but contains the original resins; or I may utilize the soap produced by the last described process, which is also free of mineral oil and contains only a minor proportion of the original resins; or I may saponify any of the fatty acid distillates, or any mixture of the fatty acid. distillates, produced by the last described process, by any known means of saponifying fatty acids and use the soap thereby produced, which soap is also free of mineral oil and contains a still smaller proportion of the original resins or substantially none of the original resins.

To any one of the described soaps I add a water-soluble dyestufi, and then add a water-soluble metal salt to effect an exchange of the metallic ion of the added salt for the .metallic ion of the water-soluble soap.

The following is a specific example of the steps of my process followingthe production of the soap.

An oil-free soap produced by the first of the described processes will have a variable acid value, averaging, perhaps, approximately 85. Assuming the soap to have this acid value, I take 1 kg. of the anhydrous soap and dissolve it in about 4 litres of water. To this soap solution is added 15 gms., more or less, Lithosol Rubine B Powder. Alternatively, the dyestufl may be dissolved in water and added to the anhydrous oil-free soap. gms. of anhydrous calcium chloride are. dissolved in about 500 cc. .'of water. It is decidedly advantageous, although unnecessary, to add the calcium chloride solution gradually, while stirring the soap solution.

The calcium derivative of the soap separates I out as an extremely sticky, tenacious redcolored mass. The dyestuif is absorbed by the calcium derivative, thus forming a color lake insoluble in water; or some chemical reaction, the nature of which is-not understood, takes place between the dyestuif and the calcium derivative. The sticky mass, which flows at a temperature of about 60 F is next washed with cold water, during which process it is agitated by means of a mechanical stirrer or by means of air. The mechanical stirrer seems to be more desirable for this purpose, as fine fibres of the calcium derivative are pulled through the water, thus gaining greater surface for washing. After washing with water, it may be partly dried by the application of heat.

. all, other salts.

In place of the dyestufi' mentioned, any other water-soluble dyestufi' may be used, dependent on the color desired.

In place of calcium chloride, I may use another water-soluble salt of calcium, or any otherwater-soluble metallic salt, as for example, salts of barium, zinc, lead, manganese, copper, chromium, cobalt, nickel, aluminum and magnesium. Color lakes made with salts of barium and calcium give better colors and give more desirable physical properties to the color lakes than most, or possibly As is well understood, when using certain dyestuffs, the precipitates with certain salts are of one color and those with. another salt are another color.

An oil-free soap produced by the second of the described processes will have, due to the reduced content or substantial elimina-' tion of petroleum resins, a substantially higher acid value than 85. It may have an acid value varying from 103.5 to, as high as 187,

or-eyen higher. If such a soap be employed,

while'the process of adding a water-soluble dyestuffand. a water solution of a watersoluble salt may be the same as that above described, it will be understood that a larger amount of a water-soluble metal salt, such as calcium chloride, will be required.

The novelty of the process and of the color lakes themselves do not depend on any novelty in the method of adding the dyestuff and the water-soluble metal salt, the novelty of the process and product depending on the production from petroleum of a fatty acid soap that-may or may not contain a substant1al proportion of petroleum resins but from which the mineral oil has been substantially but remains sticky. When mixed with cal cium carbonate, it forms a non-drying, non- -hardening, .pastfy-like mass which sticks to g1ass, wo0d -0 1"1I0I-l with greater tenacity.

It is non-brittle or (perhaps more accurately stated) not of a cheesy constituency and accommodates itself without cracking to the differences in volume due to the contraction by cold and expansionby heat.

While these color lakes are adapted to manifold uses, they are especially valuable in themanufacture of varnishes, paints and printing, lithographing, and wall paper inks. It will-be understood that the. proportion of dyestuff will vary with the strength of the dye and the intensity of the color desired and that the proportion of the metal salt will vary with the particular metal salt that is used'as well as with the. acid value of the soap. For example, if barium chloride is the salt used, and if the oil-free soap used has an acid value of 85, it willrequire 185 gms. ofbarium chloride to one kg. of the soap.

Having now fully described my invention,

what I claim and desire to protect by Letters Patent is:

1. The process, of manufacturing color lakes which comprises adding to a watersoluble fatty acid soap derived from petroleum, a water-soluble dyestufl and a water solution of a water-soluble metal salt adapted to precipitate said soap.

2. The process of manufacturing color lakes which comprises adding to an emulsion of a water-soluble fatty acid soap derived from petroleum and containing petroleum resins, a water-soluble dyestuff and a water solution of a water-soluble metalsalt adapted to precipitate, said, soap.

3. The process of manufacturing color lakes which comprises adding to a watersoluble fatty acid soap derived from petrolerum, a water-soluble dyestufl and a water solution of a water-soluble metal salt adapted to precipitate said soap, said soap being distinguished from the emulsion of soap, mineral oil and petroleum resins produced by treating mineral lubricating oil successively with a mineral acid and an alkali by the fact that it is substantially devoid of mineral D11.

4. The process of manufacturing color lakes which comprises adding to an emulsion of a water-soluble fatty acid soap derived from petroleum and containing petroleum resins, a water-soluble dyestuff and a water solution-of a water-soluble metal salt adapted to precipitate said soap, said emulsionbeing distinguished from the emulsion of soap, mineral oil and petroleum resins produced by treating mineral lubricating'oil successively with a mineral acid and an alkali by the fact that it is substantially devoid of mineral oil.

5. A color lake comprising the reaction products of a water-soluble fatty acid soap derived from petroleum, a water-soluble soap-precipitating metal salt and a watersoluble dyestufi.

6. A color lake comprising the reaction products of a water-soluble fatty acid soap derived from petroleum and petroleum resins, a Water-soluble soap-precipitating metal salt and a water-soluble dyestufi.

7. A color lake comprising the reaction products of a Water-soluble soap-precipitating metal salt, a water-soluble dyestufi' and a water-soluble fatty acid soap derived from petroleum, said soap being distinguished from the emulsion of soap, mineral oiland petroleum resins produced by treating mineral lubricating oil successively With a mineral acid and an alkali by the fact that it is' substantially devoid of mineral oil.

8. A color lake comprising the reaction products, a water-soluble soap-precipitating metal salt, a water-soluble dyestufi' and an emulsion of a water-soluble fatty acid soap derived from petroleum and petroleum resins, said emulsion being distinguished from the emulsion of soap, mineral oil and petroleum resins produced by treating mineral lubricating oil successively with the mineral acid and an alkali by the fact that it is substantially devoid of mineral oil.

In testimony of which invention, I have hereunto set my hand at Swarthmore, Penna,

on this 19th day of August, 1926.

GELLERT ALLEMAN.