US1964641A - Foam prevention - Google Patents
Foam prevention Download PDFInfo
- Publication number
- US1964641A US1964641A US620298A US62029832A US1964641A US 1964641 A US1964641 A US 1964641A US 620298 A US620298 A US 620298A US 62029832 A US62029832 A US 62029832A US 1964641 A US1964641 A US 1964641A
- Authority
- US
- United States
- Prior art keywords
- oil
- foam
- volatile
- sulfonated
- soap
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
- C13B30/002—Evaporating or boiling sugar juice
- C13B30/005—Evaporating or boiling sugar juice using chemicals
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S159/00—Concentrating evaporators
- Y10S159/04—Foam
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S435/00—Chemistry: molecular biology and microbiology
- Y10S435/812—Foam control
Definitions
- This invention relates to a method and to a composition for reducing or preventing the formation of foam, particularlyin the beet sugar refining industry.
- the extracted or lixiviated juice is defecated with lime, subjected to a carbonation process for removing the excess lime, concentrated in triple-efiect evaporators and finally introduced into a strikepan or vacuum crystallization pan.
- a carbonation process for removing the excess lime
- concentration and the introduction into the vacuum pans there is a tendency for the solution to foam. This tendency is most persistent in evaporators and it is quite serious because the froth or foam not only impairs the efiiciency of the evaporation but it carries overthe juices by entrainment, resulting in loss of valuable sugar.
- An object of my invention is to provide a de-foaming composition which will be watersoluble and which will therefore not separate out in the form of scale and which at the same time will more effectively retard or prevent the forma-' tion of foam for a longer period of time than has been heretofore possible.
- I may employ sulfonated vegetable oil, such as sulfonated castor oil, or a sulfonated animal oil as my dispersing agent, but I prefer to use sulfonated mineral oil compositions, especially preferentially oil soluble sulfonates or sulfonic acids produced from mineral oil as described in Humphreys U. S. Patent No. 1,286,179. Briefly," they are produced by sulfonation of viscous petroleum oils with concentrated or fuming sulfuric acid.
- Preferentially oil-soluble sulfonates may be extracted from the oil phase (after sludge separation and afterneu- 55 tralization) by means of a 50% aqueous alcohol solution and they may be purified by extraction with about 70% to 80% alcohol, as describedin Too Pat. No. 1,493,111; these compounds are generallyreferred to as mahogany soaps be- I cause of their characteristic color. They may bepurified'by removal of salt impurities such as sodium sulfate by means of high proof alcohol, as above stated. but they are not necessarily separated from oil because they are used in admixture with oil. Green. acid (preferentially watersoluble) soaps may also be used, either alone or in admixture with mahogany soaps. v
- the petroleum oil is preferably a non-volatile viscous highly treated oil.
- the so-called white oils or medicinal oils have proved to be satisfactory, but I prefer to use a so-called white Vaseline oil or a highly treated residual oil or bright stock which is less volatile than the refined distillates which are used in the manufacture of many technical white oils.
- the treatment of oil with acid shall be sufficient to remove colors,'odors and tastes which might contaminate the product.
- My improved anti-foaming composition is employed in about the same proportions as the vegetable oils which have heretofore been used,-- about four ounces being sufficient for treating several thousand gallons of juice.
- I add to 3,600 gallons of juice in beet sugar concentrators, four ounces of a composition consisting of 3% mahogany soap and 97% viscous white oil (upwards of 80 seconds Saybolt at 100 F.).
- This composition will suppress the foam in the evaporators for about an hour, more 100 than twice as long as an equal amount of the corn oil which has been previously used for this purpose.
- the above de-forming agent is added to the vacuum pans, it is immediately effective in breaking the foam,corn oil requires a period of five minutes to efiect a similar result.
- the method of retarding formation of foam in a liquid characterized by calcium alkalinity which comprises dispersing a non-volatile petro- 'oiland a sulfonated mineral oil composition;
- the method of retarding formation of foam in a liquid characterized by calcium alkalinity comprises dispersinga non-volatile petroleum oil thereon by means of a mineral oil sulfonic acid soap.
- the method of retarding formation of foam in a liquid characterized by calcium alkalinity which comprises dispersing a non-volatile petroleum oil thereon by means of a mahogany soap.
- the method of de-i'oaming beet sugar solutions which comprises adding thereto a small amount of a highly purified non-volatile mineral 011, containing about 1% to 6% of an oil-soluble sulfonic acid compound of the class which consists of a sulfonatedvegetable oil, a sulfonated foam in industrial solution of the type encoun-' tered in the beet sugar refining industry, which comprises contacting the surface of said solutions with a mixture of a non-volatile'oil and a small amount of a sulfonic acid compound of the class which consists ofa sulfonated vegetable oil, a
- the methodof retarding the formation of foam in industrial solutions of the type encountered in the beet sugar refining industry which comprises contacting the surface ofsaid solutions with a mixture of non-volatile oils with mineral oil sulfonic acid soaps.
- 'L'I'he method of retarding the formation of foam in an aqueous industrial solution having a tendency to foam which comprises contacting said aqueous solution with a mixture of a nonvolatile petroleum oil with a small amountof a sulfonic acid soap prepared from a sulfonated oil whereby the concentration of adsorbed materials in the gas-liquid interface of the solution is regulated.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Edible Oils And Fats (AREA)
Description
Patented June 26, 1934 1.964.641 FOAM PREVENTION:
Henry a. Mathias, Highland Park, 111., assignor to Standard Oil Company, Chicago, 111., a corpo'ration of Indiana No Drawing. Application June 30, 1932,
Serial No. 620,298 1 'zclaims. (01. 127-46) This invention relates to a method and to a composition for reducing or preventing the formation of foam, particularlyin the beet sugar refining industry.
I In the process of refining beet sugar, the extracted or lixiviated juice is defecated with lime, subjected to a carbonation process for removing the excess lime, concentrated in triple-efiect evaporators and finally introduced into a strikepan or vacuum crystallization pan. In three of these phases, namely the defecation, the concentration and the introduction into the vacuum pans, there is a tendency for the solution to foam. This tendency is most persistent in evaporators and it is quite serious because the froth or foam not only impairs the efiiciency of the evaporation but it carries overthe juices by entrainment, resulting in loss of valuable sugar. Heretofore, many efforts have been made to prevent or retard the formation of foam under these circumstances,-the most generally used reagent being a vegetable oil such as corn oil or cotton seed oil. These anti-foam agents are objectionable because the calcium soaps which are formed are insoluble in aqueous solutions and they therefore separate out in the apparatus in the form of calcium soap scale. An object of my invention is to provide a de-foaming composition which will be watersoluble and which will therefore not separate out in the form of scale and which at the same time will more effectively retard or prevent the forma-' tion of foam for a longer period of time than has been heretofore possible.
I have discovered that heavy, non-volatile mineral oils form excellent de-foaming agents if they can be thoroughly dispersed over the surface of an aqueous solution. I have also found that a small amount of a sulfonic compound is an excellent dispersing agent under these particular conditions. Both the sodium and the calcium soaps of sulfonic acids are water-soluble, at least to the degree necessary for the complete dispersion of the mineral oil with which they are used. I may employ sulfonated vegetable oil, such as sulfonated castor oil, or a sulfonated animal oil as my dispersing agent, but I prefer to use sulfonated mineral oil compositions, especially preferentially oil soluble sulfonates or sulfonic acids produced from mineral oil as described in Humphreys U. S. Patent No. 1,286,179. Briefly," they are produced by sulfonation of viscous petroleum oils with concentrated or fuming sulfuric acid. Preferentially oil-soluble sulfonates may be extracted from the oil phase (after sludge separation and afterneu- 55 tralization) by means of a 50% aqueous alcohol solution and they may be purified by extraction with about 70% to 80% alcohol, as describedin Divine Pat. No. 1,493,111; these compounds are generallyreferred to as mahogany soaps be- I cause of their characteristic color. They may bepurified'by removal of salt impurities such as sodium sulfate by means of high proof alcohol, as above stated. but they are not necessarily separated from oil because they are used in admixture with oil. Green. acid (preferentially watersoluble) soaps may also be used, either alone or in admixture with mahogany soaps. v
The petroleum oil is preferably a non-volatile viscous highly treated oil. The so-called white oils or medicinal oils have proved to be satisfactory, but I prefer to use a so-called white Vaseline oil or a highly treated residual oil or bright stock which is less volatile than the refined distillates which are used in the manufacture of many technical white oils. The treatment of oil with acid shall be sufficient to remove colors,'odors and tastes which might contaminate the product.
' Theproportion of mahogany soap to oil should be kept within certain limits and I have found that excellent results are obtained by using about 1% to 6% of mahogany soap, the rest of the composition consisting of non-volatile oil. If 20% or more of mahogany soap is employed, I have found that foaming may actually be increased instead of being prevented or retarded; The phenomenon is apparently one of surface tension and although it is not thoroughly understood I believe that the proportion of soap to oil has an important bearing in its determination.
My improved anti-foaming composition is employed in about the same proportions as the vegetable oils which have heretofore been used,-- about four ounces being sufficient for treating several thousand gallons of juice. As a specific example, I add to 3,600 gallons of juice in beet sugar concentrators, four ounces of a composition consisting of 3% mahogany soap and 97% viscous white oil (upwards of 80 seconds Saybolt at 100 F.). This composition will suppress the foam in the evaporators for about an hour, more 100 than twice as long as an equal amount of the corn oil which has been previously used for this purpose. -When the above de-forming agent is added to the vacuum pans, it is immediately effective in breaking the foam,corn oil requires a period of five minutes to efiect a similar result.
While I have described the use of mahogany soaps as dispersing agents for mineral oils, it should be understood that equivalent dispersing means maybe employed. The invention is not limited to the sugar refining industry, but may be useful in any case where foaming must be prevented, and particularly where the foam is due to surface tension phenomena in the presence of cal- 'cium alkalinity. Foam prevention is not neces- .lar or colloidal substances positively or; negatively adsorbed in a gas-liquid interface. Since positively absorbed substances lower the surface tension and negatively adsorbed substances raise the surface tension it is seen that there is no correlation between foaming and surface tension (C. W. Foulk A theory of liquid film formation", Industrial 8: Engineering Chemistry, vol. 21, page 815). The eifectiveness of antifoam agents is therefore probably due to their eflect on the concentration of adsorbed materials in the gas-liquid interface rather than to a raising or lowering of the surface tension. While I have described a preferred embodiment of my invention, it should be understood I do not limit myself to' any of I the details hereinabove set forth except as defined by the following claims which should be construed as broadly as the prior art will permit.
I claim:
1. The method of retarding formation of foam in a liquid characterized by calcium alkalinity" which comprises dispersing a non-volatile petro- 'oiland a sulfonated mineral oil composition;
2. The method of retarding formation of foam in a liquid characterized by calcium alkalinity which comprises dispersinga non-volatile petroleum oil thereon by means of a mineral oil sulfonic acid soap.
3. The method of retarding formation of foam in a liquid characterized by calcium alkalinity which comprises dispersing a non-volatile petroleum oil thereon by means of a mahogany soap. 4. The method of de-i'oaming beet sugar solutions which comprises adding thereto a small amount of a highly purified non-volatile mineral 011, containing about 1% to 6% of an oil-soluble sulfonic acid compound of the class which consists of a sulfonatedvegetable oil, a sulfonated foam in industrial solution of the type encoun-' tered in the beet sugar refining industry, which comprises contacting the surface of said solutions with a mixture of a non-volatile'oil and a small amount of a sulfonic acid compound of the class which consists ofa sulfonated vegetable oil, a
sulfonated animal oil and a suli'onated mineral oil composition.
'6. The methodof retarding the formation of foam in industrial solutions of the type encountered in the beet sugar refining industry, which comprises contacting the surface ofsaid solutions with a mixture of non-volatile oils with mineral oil sulfonic acid soaps.
'L'I'he method of retarding the formation of foam in an aqueous industrial solution having a tendency to foam, which comprises contacting said aqueous solution with a mixture of a nonvolatile petroleum oil with a small amountof a sulfonic acid soap prepared from a sulfonated oil whereby the concentration of adsorbed materials in the gas-liquid interface of the solution is regulated.
, HENRY R. MATHIAS.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US620298A US1964641A (en) | 1932-06-30 | 1932-06-30 | Foam prevention |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US620298A US1964641A (en) | 1932-06-30 | 1932-06-30 | Foam prevention |
Publications (1)
Publication Number | Publication Date |
---|---|
US1964641A true US1964641A (en) | 1934-06-26 |
Family
ID=24485379
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US620298A Expired - Lifetime US1964641A (en) | 1932-06-30 | 1932-06-30 | Foam prevention |
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US (1) | US1964641A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2423214A (en) * | 1944-03-16 | 1947-07-01 | Paper Chemistry Inst | Foam prevention |
US2426088A (en) * | 1945-06-04 | 1947-08-19 | Standard Oil Dev Co | Method for eliminating foaming in the recovery of sulfuric acid from an olefin recovery operation |
US2426082A (en) * | 1945-06-04 | 1947-08-19 | Standard Oil Dev Co | Method for eliminating foaming in the recovery of sulfuric acid from an olefin recovery operation |
US2442789A (en) * | 1944-11-11 | 1948-06-08 | Doughnut Corp | Conversion of wheat starch |
US2442768A (en) * | 1939-11-24 | 1948-06-08 | Dearborn Chemicals Co | Method of conditioning water |
US2453352A (en) * | 1945-07-26 | 1948-11-09 | Wyandotte Chemicals Corp | Composition for inhibiting foam |
US2475485A (en) * | 1948-12-15 | 1949-07-05 | Oil Well Chemical And Material | Treatment of drilling fluids |
US2716610A (en) * | 1951-01-26 | 1955-08-30 | Exxon Research Engineering Co | Automobile polish compositions |
US2727002A (en) * | 1952-12-31 | 1955-12-13 | Sun Oil Co | Non-foaming drilling fluid |
US3249515A (en) * | 1960-06-20 | 1966-05-03 | Vogelbusch Gmbh | Method of destroying foam in fermenters |
-
1932
- 1932-06-30 US US620298A patent/US1964641A/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2442768A (en) * | 1939-11-24 | 1948-06-08 | Dearborn Chemicals Co | Method of conditioning water |
US2423214A (en) * | 1944-03-16 | 1947-07-01 | Paper Chemistry Inst | Foam prevention |
US2442789A (en) * | 1944-11-11 | 1948-06-08 | Doughnut Corp | Conversion of wheat starch |
US2426088A (en) * | 1945-06-04 | 1947-08-19 | Standard Oil Dev Co | Method for eliminating foaming in the recovery of sulfuric acid from an olefin recovery operation |
US2426082A (en) * | 1945-06-04 | 1947-08-19 | Standard Oil Dev Co | Method for eliminating foaming in the recovery of sulfuric acid from an olefin recovery operation |
US2453352A (en) * | 1945-07-26 | 1948-11-09 | Wyandotte Chemicals Corp | Composition for inhibiting foam |
US2475485A (en) * | 1948-12-15 | 1949-07-05 | Oil Well Chemical And Material | Treatment of drilling fluids |
US2716610A (en) * | 1951-01-26 | 1955-08-30 | Exxon Research Engineering Co | Automobile polish compositions |
US2727002A (en) * | 1952-12-31 | 1955-12-13 | Sun Oil Co | Non-foaming drilling fluid |
US3249515A (en) * | 1960-06-20 | 1966-05-03 | Vogelbusch Gmbh | Method of destroying foam in fermenters |
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