US2043378A - Apparatus for manufacturing a fibrous soap - Google Patents
Apparatus for manufacturing a fibrous soap Download PDFInfo
- Publication number
- US2043378A US2043378A US685532A US68553233A US2043378A US 2043378 A US2043378 A US 2043378A US 685532 A US685532 A US 685532A US 68553233 A US68553233 A US 68553233A US 2043378 A US2043378 A US 2043378A
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- US
- United States
- Prior art keywords
- soap
- chamber
- manufacturing
- fibrous
- vessel
- 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
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D13/00—Making of soap or soap solutions in general; Apparatus therefor
- C11D13/14—Shaping
- C11D13/20—Shaping in the form of small particles, e.g. powder or flakes
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- 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
- Y10S159/14—Soap
Definitions
- This invention relates to means for manufacturing a fibrous soap, which consists in pouring a stream of melted ground soap into a meshed or perforated vessel rotating rapidly in a closed chamber, subjecting it to centrifugal force by introducing air into the lower peripheral portion of the chamber; suspending in a heated atmosphere the melted liquor of the soap scattered from the meshed or perforated vessel and thereby solidifying it in a fibrous shape.
- the object thereof is to obtain a soap of beautiful appearance easy to dissolve and free from any danger of crumbling and scattering as loose particles.
- the annexed drawing shows diagrammatically an example ofthe apparatus embodying the present invention in practice.
- the powdered, granular and flaky soaps have hitherto been known as the class of soaps having comparatively good solubility.
- the powdered soap does not dissolve so quickly in spite of the area of its contact surface being comparatively great, because the particles stick together due to the adhesiveness of their surfaces.
- the powder there is the ever present tendency of the powder to float on the surface of the water in an agglomerated form.
- the granular and flaky soaps they have so small an exposed surface area that it takes them a pretty long time to dissolve completely.
- the melted ground soap manufactured by the present method is poured in a continuous stream into a perforated vessel rotating quickly in a closed chamber and is subjected to centrifugal force by passing heated air or the like into the lower peripheral portion of the chamber. Then, the melted liquor of the soap projected through the apertures of the vessel is suspended in a dehydrating heated atmosphere and solidified in a fibrous form.
- a closed chamber 3 the conical inner walls 2 pierced with numerous small holes I, are attached, put one upon another in spaced relation in the form of a staircase, so as to form an annular space H at the seam.
- Chamber 3 is provided at the ceiling with a rotatable vessel 5 which has a wire net 4 stretched around it.
- the vessel is connected to the shaft l3 of an electric motor 6 so as to be rotated thereby very quickly.
- a fixed leading pipe 8 is connected with the bottom 5 of a tank I, which has a stirrer Ill operated together with said shaft, opens in the rotatable vessel 5, the tank being equipped with an electric heater or other heating devices.
- Melted soap is supplied to the tank 1 from an 10 inlet pipe 9 and delivered into the quickly rotating vessel 5 through the leading pipe 8, stirring it with the stirrer l0, operated by the said motor so that said melted soap may be projected through the wire net 4 by centrifugal force.
- a current of cooled or heated air is introduced into the chamber from a lower peripheral portion thereof with a fan l4 and projected in the form of jets through the holes l of the perforated conical wall 2, so that a spray of melted soap is 0 suspended in the atmosphere in the conical chamber to be solidified in a fibrous form.
- the shape of the product may be changed suitably by regulating the adhesive quality, water content and quantity of the melted soap introduced into the rotatable 35 vessel, the speed of rotation and the size of the meshes of the rotatable vessel Having now fully described our invention, we claim:--
- apparatus for manufacturing fibrous soap, 40 having a chamber provided at the upper portion thereof with a rotatable means for c'entrifugally projecting soap in fluid form into said chamber and at the lower portion of the sides thereof a peripherally disposed air supply means, the combination of a perforate conical apron occupying the lower portion of said chamber and the major portion of the sides thereof over said air supply means and reaching upwardly toward the level of said rotatable soap projecting means in order to cause the incoming air from said air supply means to pass inwardly through the perforations in the form of a plurality of obliquely directed air jets, and a perforate member fixedly associated with a portion of said rotatable means so as to rotate 55 therewith and-rapidly project the soap centrifugally into said chamber toward the sides and perforated conical apron in the form of a large number of simultaneously formed soap fibres.
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Detergent Compositions (AREA)
Description
June 9, 1936. M. IGARASHI ET AL.
vAPPARATUS FOR MANUFACTURING A FIBROUS SOAP Filed Aug. 17, 1955 v w I MASAJI. IGARASHI TOSHIRO HATTA INVENTORS BYMNMMCVZ ATTORNEYS Patented June 9, 1936 UNITED STATES APPARATUS FOR MANUFACTURING A FIBROUS SOAP Masaji Igarashi and Toshiro Hatta, Tokyo, Japan, assignors to Kao Sekken Kabushiki Kaisha Nagase Shokai, Tokyo, Japan, a corporation of Japan Application August 17, 1933, Serial No. 685,532
In Japan January 11, 1933 2 Claims.
This invention relates to means for manufacturing a fibrous soap, which consists in pouring a stream of melted ground soap into a meshed or perforated vessel rotating rapidly in a closed chamber, subjecting it to centrifugal force by introducing air into the lower peripheral portion of the chamber; suspending in a heated atmosphere the melted liquor of the soap scattered from the meshed or perforated vessel and thereby solidifying it in a fibrous shape. The object thereof is to obtain a soap of beautiful appearance easy to dissolve and free from any danger of crumbling and scattering as loose particles.
The annexed drawing shows diagrammatically an example ofthe apparatus embodying the present invention in practice.
The powdered, granular and flaky soaps have hitherto been known as the class of soaps having comparatively good solubility. However, the powdered soap does not dissolve so quickly in spite of the area of its contact surface being comparatively great, because the particles stick together due to the adhesiveness of their surfaces. Moreover, there is the ever present tendency of the powder to float on the surface of the water in an agglomerated form. As to the granular and flaky soaps, they have so small an exposed surface area that it takes them a pretty long time to dissolve completely. In the present invention, the melted ground soap manufactured by the present method is poured in a continuous stream into a perforated vessel rotating quickly in a closed chamber and is subjected to centrifugal force by passing heated air or the like into the lower peripheral portion of the chamber. Then, the melted liquor of the soap projected through the apertures of the vessel is suspended in a dehydrating heated atmosphere and solidified in a fibrous form. Thus, by removing the abovementioned defect it is possible to produce simply in a short time by continuous operation a soap which has a beautiful appearance and such good solubility as not to crumble or be scattered as loose particles, without any fear of the particles affecting the health of an operator as in the practice of the method of manufacturing powdered soap.
The following is the explanation of an example of using this invention in actual practice with reference to the drawing:--
In a closed chamber 3 the conical inner walls 2 pierced with numerous small holes I, are attached, put one upon another in spaced relation in the form of a staircase, so as to form an annular space H at the seam. Chamber 3 is provided at the ceiling with a rotatable vessel 5 which has a wire net 4 stretched around it. The vessel is connected to the shaft l3 of an electric motor 6 so as to be rotated thereby very quickly. A fixed leading pipe 8 is connected with the bottom 5 of a tank I, which has a stirrer Ill operated together with said shaft, opens in the rotatable vessel 5, the tank being equipped with an electric heater or other heating devices.
Melted soap is supplied to the tank 1 from an 10 inlet pipe 9 and delivered into the quickly rotating vessel 5 through the leading pipe 8, stirring it with the stirrer l0, operated by the said motor so that said melted soap may be projected through the wire net 4 by centrifugal force. At the same 15 time, a current of cooled or heated air is introduced into the chamber from a lower peripheral portion thereof with a fan l4 and projected in the form of jets through the holes l of the perforated conical wall 2, so that a spray of melted soap is 0 suspended in the atmosphere in the conical chamber to be solidified in a fibrous form. Then, it is swept downward by the air current entering from the annular space H and conducted to a transportation chamber l5 of channel form pro- 25 vided with a screw conveyer l2. A wire net l6 or coarse cloth is stretched over the upper part of said transportation chamber to carry the soap outward by projecting air through the meshes. The same result may be obtained by the cyclone 30 separator system.
With this invention, the shape of the product may be changed suitably by regulating the adhesive quality, water content and quantity of the melted soap introduced into the rotatable 35 vessel, the speed of rotation and the size of the meshes of the rotatable vessel Having now fully described our invention, we claim:--
1. In apparatus for manufacturing fibrous soap, 40 having a chamber provided at the upper portion thereof with a rotatable means for c'entrifugally projecting soap in fluid form into said chamber and at the lower portion of the sides thereof a peripherally disposed air supply means, the combination of a perforate conical apron occupying the lower portion of said chamber and the major portion of the sides thereof over said air supply means and reaching upwardly toward the level of said rotatable soap projecting means in order to cause the incoming air from said air supply means to pass inwardly through the perforations in the form of a plurality of obliquely directed air jets, and a perforate member fixedly associated with a portion of said rotatable means so as to rotate 55 therewith and-rapidly project the soap centrifugally into said chamber toward the sides and perforated conical apron in the form of a large number of simultaneously formed soap fibres.
2. Apparatus for manufacturing fibrous soap according to claim 1, whereinthe perforate conical apron is provided in the form of a plurality o! stepped concentric and perforated conical membemgoastocauseawhirlingandchurning throughout the. chamber of the air currents introduced'through thepertorations of said stepped and perforated conical members.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2043378X | 1933-01-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
US2043378A true US2043378A (en) | 1936-06-09 |
Family
ID=16488823
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US685532A Expired - Lifetime US2043378A (en) | 1933-01-11 | 1933-08-17 | Apparatus for manufacturing a fibrous soap |
Country Status (1)
Country | Link |
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US (1) | US2043378A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2467470A (en) * | 1945-05-25 | 1949-04-19 | Universal Oil Prod Co | Manufacture of spherical particles |
US2555516A (en) * | 1949-01-24 | 1951-06-05 | Purex Corp Ltd | Spray drier |
US2733961A (en) * | 1956-02-07 | Atomizer | ||
US2747659A (en) * | 1950-04-27 | 1956-05-29 | Panmetals And Processes Inc | Method and apparatus for concentrating scale-forming phosphoric acid solutions and the like |
US2836464A (en) * | 1954-10-26 | 1958-05-27 | Gen Eng Radcliffe | Apparatus for atomizing a liquid in a vacuum |
US2851097A (en) * | 1950-11-10 | 1958-09-09 | Colgate Palmolive Co | Apparatus for and method of separating gas from solids |
US2911036A (en) * | 1955-01-03 | 1959-11-03 | Melvin E Lazar | Spray-drying apparatus |
US3442317A (en) * | 1965-10-19 | 1969-05-06 | Du Pont | Process for isolating elastomers from intimate mixtures thereof with volatile liquids |
DE2725754A1 (en) * | 1976-06-09 | 1977-12-22 | Armour Pharma | MACROSPHERICAL PARTICLES, METHOD AND DEVICE FOR THEIR PRODUCTION |
US4430155A (en) | 1981-01-21 | 1984-02-07 | Armour Pharmaceutical Company | Production of macrospherical particles |
-
1933
- 1933-08-17 US US685532A patent/US2043378A/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2733961A (en) * | 1956-02-07 | Atomizer | ||
US2467470A (en) * | 1945-05-25 | 1949-04-19 | Universal Oil Prod Co | Manufacture of spherical particles |
US2555516A (en) * | 1949-01-24 | 1951-06-05 | Purex Corp Ltd | Spray drier |
US2747659A (en) * | 1950-04-27 | 1956-05-29 | Panmetals And Processes Inc | Method and apparatus for concentrating scale-forming phosphoric acid solutions and the like |
US2851097A (en) * | 1950-11-10 | 1958-09-09 | Colgate Palmolive Co | Apparatus for and method of separating gas from solids |
US2836464A (en) * | 1954-10-26 | 1958-05-27 | Gen Eng Radcliffe | Apparatus for atomizing a liquid in a vacuum |
US2911036A (en) * | 1955-01-03 | 1959-11-03 | Melvin E Lazar | Spray-drying apparatus |
US3442317A (en) * | 1965-10-19 | 1969-05-06 | Du Pont | Process for isolating elastomers from intimate mixtures thereof with volatile liquids |
DE2725754A1 (en) * | 1976-06-09 | 1977-12-22 | Armour Pharma | MACROSPHERICAL PARTICLES, METHOD AND DEVICE FOR THEIR PRODUCTION |
US4430155A (en) | 1981-01-21 | 1984-02-07 | Armour Pharmaceutical Company | Production of macrospherical particles |
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