US2530042A

US2530042A - Separating higher molecular alcohols from the soaps obtained in the preparation of the same

Info

Publication number: US2530042A
Application number: US779384A
Authority: US
Inventors: Blinoff Vsevolod
Original assignee: INNOVATIONS CHIMIQUES SINNOVA
Current assignee: D'innovations Chimiques Dite Sinnova Ou Sadic SA Ste; INNOVATIONS CHIMIQUES SINNOVA
Priority date: 1947-03-11
Filing date: 1947-10-11
Publication date: 1950-11-14
Anticipated expiration: 1967-11-14
Also published as: NL83671C; DE970983C; FR944199A; BE480277A

Description

Nov. 14, 1950 Filed Oct. 11, 1947 V BLINOFF Fig .1

SEPARATING HIGHER MOLECULAR ALCOHOLS FROM THE SOAPS OBTAINED IN THE PREPARATIQN OF THE SAME Sheets-Shae: 1

Jam n51 Nov. 14, 1950 Filed Oct. 11, 1947 V BLINO F F SEPARATING HIGHER MOLECULAR ALCOHOLS FROM THE SOAPS OBTAINED IN THE PREPARATION OF THE SAME 2 Sheets-Sheet 2 Patented Nov. 14, 1950 SEPARATING HIGHER MOLECULAR ALCO- HOLS FROM THE SOAPS OBTAINED IN THE PREPARATION OF THE SAME Vsevolod Blinoff, Paris, France, assignor to Socit Anonyme dite:

Chimiques dite: Beauval, France Societe DInncvations Sinnova ou Sadie, Manx,

Application October 11, 1947, Serial No. 779,384 In France March 11, 1947 4 Claims. 1

It is well known that it is difiicult and sometimes impossible to separate fatty alcohols by distillation from the soaps obtained in the preparation of the same.

Effectively, even if a good vacuum is employed, the higher alcohols will distill off at high temperature and in these conditions the soap is liable to react with said alcohols and form such decomposition products as unsaturated hydrocarbons, resin, tar, etc. Moreover, depending on the soap-content of the mixture, abundant and persistent froths are formed which make distillation quite difficult. Finally, there always remains a certain percentage of undistilled fatty alcohols in the residual soap.

It has been attempted to eliminate these inconveniences by using other methods of separation than distillation, for instance by Washing the mixture of soap and fatty alcohols with water while taking advantage of the insolubility of heavy alcohols in water to separate same from the water-soluble soap.

However, it is found then that in order to carry out such a separation such large amounts of water must be used that the separation proves to be almost impossible; effectively, within quite Wide limits, soaps will act as emulsifiers, and emulsions of alcohols in soap water are obtained which it is almost impossible to resolve.

Applicant has now found, according to the present invention, that all the aforesaid inconveniences can be eliminated by dissolving the mixture of soap and heavy alcohols in a suitable solvent and then washing the solution with water. Under these conditions, with suitable amounts of water added to the solution in,the solvent, there are obtained two layers: a layer more particularly loaded with solvent and which contains the alcohols and an aqueous layer enriched in soap.

It will be appreciated that by repeating the operation several times it is possible in this manner to separate all the heavy alcohols from the soaps.

It will also be appreciated that the performance of the said separation in continuous operation becomes quite easy since it is only necessary to run the soap and heavy alcohol solution and the wash water in opposite directions.

It is advantageous to use a low-boiling solvent in order that it can be separated easily by distillation from the heavy alcohols or the aqueous soap solution.

As solvents for the fatty alcohols there may be-used such aliphatic or cyclic alcohols as propyl 2 alcohol, butyl alcohol, amyl alcohol, lauryl alcohol, eyclohexanol, aliphatic or cyclic hydrocarbons, gasoline, benzene, toluene, cyclohexane, ketones, etc, or mixtures of such solvents.

On the whole, the present invention has for its object a method of separating heavy alcohols from their mixture with the soap obtained in preparing the same by causing the heavy alcohols to pass into a water-insoluble solvent in which soap is less soluble than in water.

The invention is applicable to all alcohols and alcohol mixtures Whose molecular Weights are higher than C5, and in particular to alcohols obtained by reducing cocoanut oil, palm oil, sperm oil, fish oils and to synthetic alcohols.

Various examples of the application of this invention are given hereinafter for the purpose of illustrating and by no means of limiting the invention.

(l). The product from the reduction in a butyl alcoholic medium of 250 kg. of fatty acids derived from palm oil or cocoanut oil, that is, about 1500 kg, is first of all Washed with 300 litres of water in order to remove the sodium hydroxide.

The material resulting from this washing step is admixed with 600 kg. of benzene and 600 kg. of water. The mixture breaks up into two layers,

An upper layer weighing about 1000 kg.

A lower layer weighing about 1100 kg.

About 2% of soap are contained in the upper layer, and 7.4% in the aqueous layer.

In this case the coeflicient of separation related to the soap comes out as 3.7 and. it will be appreciated that by repeating the washing operation several times it is possible to completely separate the soap from the heavy alcohols.

Thus, by using another 600 litres of water in a further washing of the alcohol-containing layer, the amount of soap would become 19 times larger in the water than in the alcohol-containing layer.

Since the variation of the coefiicient of separa- I tion then makes the washing the easier as the amount of soap is lower, practically after three times, no soap is present any longer in the alcohol-containing layer and the heavy alcohols are stripped therefrom.

(2). 3.7 parts by weight of spermaceti are saponified with .5 part by weight of potassium hydroxide dissolved in 5 parts by Weight of butanol. 1

To the solution there are added parts by volume of butanol and parts by volume of xylene and to the mixture there are admixed 100 parts by volume of water.

The mixture breaks up into two layers and. the coefiicient of division of the soap amongst the two layers is 2.6 to the advantage of the aqueous layer.

The washing operation is repeated several times until the soap is completely separated from the heavy alcohols. After three Washes there remains no soap in the alcoholic layer; the alcohols are stripped therefrom.

(3) 9 parts by weight of lanolin are saponified with two parts by weight of potassium hydroxide dissolved in parts by weight of butanol.

The product obtained is admixed with 80 parts by volume of butanol, parts by volume of toluone and to the whole there are added 280 parts by volume of water.

The coefficient of division of the soap amongst either layer is then 1. The operation is continued in the same manner as in the preceding examples.

The same saponification product as above, if admixed with a mixture of 100 parts by volume of acetone and 10 parts by volume of xylene will give a coefiicient of division of 1.9.

(4) 5 parts by weight of beeswax are treated with 5 :parts by weight of potassium hydroxide in 10 parts by volume of amyl alcohol and then admixed with 100 parts by volume of amyl alcohol and 20 parts by volume of xylene and then with 100 parts by volume of water.

The coefficient of division amongst either layer is 1.1. The operation is continued thereafter in the same manner as in the preceding examples.

(5) parts by weight of palm oil dissolved in 100 parts by weight of lauryl alcohol are reduced with sodium.

The raw product is washed with water in order to eliminate the sodium hydroxide as a 36 B. solution; the remaining oil, that is, about 150 parts by volume, is admixed with 100 parts by volume of water.

The soap content of the oily portion is four times less than that of the aqueous portion. The operation is continued like in the preceding examples.

(6) 250 parts by weight of palm oil dissolved in butanol 2 containing 10% of a 100-140 C. gasoline fraction are reduced with sodium. After washing with water to eliminate the sodium hydroxide as a 36 B. solution the remaining oil is admixed with an equal volume of water.

The amount of soap present in the oil is then 14 times less than the amount contained in the water. The operation is continued in the same manner as in the preceding examples.

(7) 250 parts by weight of sperm oil are saponified with 25 parts by weight of potassium hydroxide in 1250 parts by weight of butanol.

100 parts by weight of xylene are added. A sufiicient amount of water is added to remove the excess sodium hydroxide as e. g. a 36 B'.

solution and the remaining oil is admixed with an equal volume of water.

It will then be found that the amount of soap [present in the water is three times larger than the amount of soap in the oil.

The operation is then continued in the same manner as in the preceding examples.

It is particularly advantageous to perform the method according to this invention in an apparatus designed for continuous operation equipped with one or several columns and to combine the washing with the necessary distillation apparatus so that the solvent or solvent mixture can be used in a closed circuit.

Two examples of apparatus enabling to carry out the present invention are shown diagrammatically for the purpose of illustration and by no means of limitation in Figs. 1 and 2 of the appended drawing.

In the embodiment illustrated in Fig. 1, a tank B is fed through a pipe l with the mixture of heavy alcohols and soap which are to be separated. The solvent recovered in the continuous operation flows into the tank through a pipe [4.

The mixture of solvent, soap and alcohol is flowed through a pipe 2 into a washing column L. The water necessary for separating the soap is fed into the column through a ,pipe 3.

Said water flows out through the pipe 1 as an aqueous soap solution that contains solvent and it is led into a distillation column D2 in which the soap solution is to be separated from the solvent and from which the solvent recovered is led into the tank B through the pipe line 9 and the condenser C.

The soap solution flows out at 8.

The solution of heavy alcohols in the solvent is discharged from the washing column L at 5 and is led into a column D1 in which said heavy alcohols are separated from the solvent.

The heavy alcohols are discharged at 6 while the solvent recovered flows out at [0, is condensed in the condenser C and is led back into the tank B through the pipe it. However, a portion of said solvent is used: on one hand by means of a pipe 4 to remove the last traces of heavy alcohols from the soap in the solution discharged through pipe 7, on the other hand to provide for the retrogradations necessary for the operation of the columns D1 and D2, and this, through the pipes I2 and I3. Besides, this system may be equipped with automatic regulators.

Another way of carrying the invention into effect consists in separating the alcohols from the soaps and to continuously regenerate the fatty acids present therein so that the apparatus will deliver the alcohols to be separated and the regenerated fatty acids. This can be accomplished in the apparatus shown in Fig. 2.

The tank B is supplied through a pipe I with the mixture of heavy alcohols and soap to be separated. Said tank is fed through a pipe I4 with the solvent reclaimed in the continuous operation. Said mixture of solvent, soap and a1- cohol is led through a pipe 2 into a washing column L1.

The water necessary for separating the soap is fed into the column through a pipe 3. Said water flows out through a pipe 1 as an aqueous solvent-containing soap solution which is fed into a washing column L2.

A mineral or organic acid is fed into said column L2 through a pipe IE to wash the soap solution and set free the fatty acid; it flows out as an aqueous solution of sodium salts. The solvent-containing fatty acid is discharged at I! and led to a distillation column D2 in which the solvent is separated from the fatty acids and then recycled as in the preceding example while the fatty acid recovered is discharged at l 8. A return of the said acids to the bottom of column L2 (pipe I9) is provided in order to strip the salt solution discharged at I6 from any solvent that might remain dissolved therein.

As to the solvent that contains the heavy alcohols and that is discharged from the column L, its circuit is the same as in the former case.

The solvent containing the heavy alcohol is discharged at 5 and led to a distillation column D1. The heavy alcohol flows out at 6 and the solvent at 10. It is condensed in a condenser C from which it is discharged through the pipes I4 and H to perform the same function as in diagram No. 1, that is, washing in the bottom of column L, retrogradation in the distillation apparatus, the solvent being returned to tank B.

It is quite evident that an other suitable layout might be used; in particular, the columns I and 2 might be divided into two sections each of which would do the work that is effected in the upper and the lower portions of each of said columns.

What I claim is:

1. A continuous method for the separation of high molecular fatty alcohols from their mixtures with soap obtained in the preparation of the same comprising admixing a high molecular alcohol and soap mixtures with a solvent for the high molecular alcohol in which the soap is less soluble than in water and introducing the resulting mixture into the middle portion of a washingtower, introducing wash-water into the top portion of said tower, discharging aqueous soap solution containing a small quantity of the solvent from the bottom of the tower, feeding the same into the top part of a first distillation column, condensing solvent vapors that escape from the top of the said first distillation column, tapping solution of high molecular alcohol from the top of the aforesaid washing tower, leading said last named solution into a second distillation column in which the solvent is separated from the high molecular alcohol, condensing solvent vapors that escape from the top of the said second distillation column, and re-using the solvent condensate from the first and the second distillation columns to treat further amounts of the high molecular alcohol and soap mixture.

2. A continuous method for the separation of high molecular fatty alcohols from their mixtures with soap obtained in the preparation of the same comprising admixing a high molecular alcohol and soap mixtures with a solvent for the high molecular alcohol in which the soap is less soluble thanin water and introducin the resulting mixture into the middle portion of a washing tower, introducing wash-water into the top portion of said tower, introducing a smaller amount of the same solvent into the lower portion of said tower, discharging aqueous soap solution containing a small quantity of the solvent from the bottom of the tower, feeding the same into the top part of a first distillation column, condensing solvent vapors that escape from the top of the said first distillation column, tapping solution of high molecular alcohol from the top of the aforesaid washing tower, leading said last named solution into a second distillation column in which the solvent is separated from the high molecular alcohol, condensing solvent vapors that escape from the top of the said second distillation column, and re-using the solvent condensate from the columns to treat further amounts of the high molecular alcohol and soap mixture.

3. A continuous method for the separation of high molecular fatty alcohols from their mixtures with soap obtained in the preparation of the same comprising admixing a high molecular fatty alcohol and soap mixture with a solvent for the high molecular fatty alcohol in which the soap is less soluble than in water and introducing the resulting mixture into the middle portion of a main Washing tower, introducing wash-water into the top portion of said main washing tower, tapping the high molecular fatty alcohol solution from the top of said main washing tower, feeding said solution into a first distillation column in which the solvent is separated from the high molecular fatty alcohol, condensing solvent vapors that escape from the top of said column, discharging aqueous soap solution containing a small quantity of the solvent from the bottom of the main washing-tower, introducing said last named solution into an additional washing-tower, feeding an acid into the top thereof, tapping the thus formed aqueous alkali salt solution from the bottom of said additional washing-tower, tapping the solvent solution of fatty acid from the top of said tower, separating the fatty acid from the solvent in a second distillation column, condensing the solvent vapors that escape from the top of said second distillation column, and re-using the solvent condensate from the columns to treat further amounts of the high molecular fatty alcohol and soap mixtures.

4. A continuous method for the separation of high molecular fatty alcohols from their mixtures with soap obtained in the preparation of the same comprising admixing a high molecular fatty alcohol and soap mixture with a solvent for the high molecular fatty alcohol in which the soap is less soluble than in water and introducing the resulting mixture into the middle portion of a main washing-tower, introducing wash-water into the top portion of said main washing tower, tapping the high molecular fatty alcohol solution from the top of said main washing tower, feeding said solution into a first distillation column in which the solvent is separated from the high molecular fatty alcohol, condensing solvent vapors that escape from the top of said column, introducing a smaller flow of the same solvent into the lower portion of said washing-tower, discharging aqueous soap solution containing a small quantity of the solvent from the bottom of the main washing-tower, introducing said last named solution into an additional washing-tower, introducing an acid into the top of said washing tower tapping the thus formed aqueous alkali salt solution from the bottom of said additional Washingtower, tapping the solvent solution of fatty acid from the top of said lower, and separating the fatty acid from the solvent in a second distillation column, condensin solvent vapors that escape from the top of the same, and re-using the solvent condensate from the columns to treat further amounts of the high molecular fatty alcohol and soap mixtures.

VSEVOLOD BLINOFF.

REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 1,814,654 Youtz July 14, 1931 2,019,022 Scott et a1. Oct. 29,1935 2,070,318 Rosser et al Feb. 9, 1937 2,080,111 Bump May 11, 1937 2,148,846 Von Retze et a1 Feb. 28, 1939 2,193,321 Liethe Mar. 12, 1940 2,287,128 Pirkle June 23, 1942 2,421,040 Shields et a1 May 27, 1947

Claims

1. A CONTINUOUS METHOD FOR THE SEPARATION OF HIGH MOLOCULAR FATTY ALCHOLS FROM THEIR MIXTURES WITH SOAP OBTAINED IN THE PREPARATION OF THE SAME COMPRISING ADMIXING A HIGH MOLECULAR ALCOHOL AND SOAP MIXTURES WITH A SOLVENT FOR THE HIGH MOLECULAR ALCOHOL IN WHICH THE SOAP IS LESS SOLUBLE THAN IN WATER AND INTRODUCING THE RESULTING MIXTURE INTO THE MIDDLE PORTION OF A WASHINGTOWER, INTRODUCING WAST-WATER INTO THE TOP PORTION OF SAID TOWER, DISCHARGING AQUEOUS SOAP SOLUTION CONTAINING A SMALL QUANTITY OF THE SOLVENT FROM THE BOTTOM OF THE TOWER, FEEDING THE SAME INTO THE TOP PART OF A FIRST DISTILLATION COLUMN, CONDENSING SOLVENT VAPORS THAT ESCAPE FROM THE TOP OF THE SAID FIRST COLUMN, TAPPING SOLUTION OF HIGH MOLECULAR ALCOHOL FROM THE TOP OF THE AFORESAID WASHING TOWER, LEADING SAID LAST NAMED SOLUTION INTO A SECOND DISTILLATION COLUMN IN WHICH THE SOLVENT IS SEPARATED FROM THE HIGH MOLECULAR ALCOHOL, CONDENSING SOLVENT VAPORS THAT ESCAPE FROM THE TOP OF THE SAID, SECOND DISTILLATION COLUMN, AND RE-USING THE SOLVENT CONDENSATE FROM THE FIRST AND THE SECOND DISTILLATION COLUMNS TO TREAT FURTHER AMOUNTS OF THE HIGH MOLECULAR ALCOHOL AND SOAP MIXTURE.