+

US2102849A - Method of making soap beads or the like - Google Patents

Method of making soap beads or the like Download PDF

Info

Publication number
US2102849A
US2102849A US39552A US3955235A US2102849A US 2102849 A US2102849 A US 2102849A US 39552 A US39552 A US 39552A US 3955235 A US3955235 A US 3955235A US 2102849 A US2102849 A US 2102849A
Authority
US
United States
Prior art keywords
gel
soap
solvent
beads
solute
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
Application number
US39552A
Inventor
Vaman R Kokatnur
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
AUTOXYGEN Inc
Original Assignee
AUTOXYGEN Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by AUTOXYGEN Inc filed Critical AUTOXYGEN Inc
Priority to US39552A priority Critical patent/US2102849A/en
Application granted granted Critical
Publication of US2102849A publication Critical patent/US2102849A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D13/00Making of soap or soap solutions in general; Apparatus therefor
    • C11D13/14Shaping
    • C11D13/20Shaping in the form of small particles, e.g. powder or flakes

Definitions

  • An object of the present invention is to provide a process of producing soap beads, flakes or the like which may be either solid or hollow, and consisting of pure soap or of soap combined with any other material, the process involving no spraying or spray drying and being far simpler, and less expensive than spray process and involving no complex apparatus and no problems of temperature and humidity control.
  • Another object is to provide a process by which I can produce soap beads devoid of "iiller material, but having any suitable type of detergent material incorporated in them.
  • My present invention is based partially on the discovery that minute drops of a soap gel falling into a bath of material which is a solvent for the material which has gelled with the soap, is -effective not only to case harden or set the droplets to form heads but to partially or completely replace the original petroleum or other base of the gel so that the resultant beads are composed of pure soap or of soap containing part of the original petroleum of the gel or part of the gel solvent or both.
  • the bath of solvent into which the droplets of gel fail serves the two-told function of promptly case-hardening the droplets and of eliminating (to any desired extent) the solute from the soap.
  • Factors which enter into the shape assumed 20 by the solidified soap particles involve the temperature of the molten gel, the temperature of the solvent into which the molten gel is poured, the nature of the nozzle or other discharge device :trom which the molten gel drops 25 are emitted, and the method of agitating the solvent into which the molten gel falls (where agitation is resorted to).
  • the bath of solvent is maintained at a temperature at which the solute in the soap gel will partially vaporize, the drops upon falling into the bath have the solute on their outside surfaces almost instantaneously dissolved and since the outside surfaces are simultaneously cooled the solute within the beads tends to expand and pull the beads up. Later, as cooling of the beads be- 5 comes complete and the gasifled solvent at the interior of the beads is liquefied, it will be absorbed back into the material and the resultant Product will be a hollow head. If this material is left in the solvent long enough the solute will be so completely replaced by the solvent and when the beads are removed from the bath, this solvent completely evaporates leaving hollow beads of pure soap.
  • the invention may perhaps be best understood i .irom certain typical examples of the manner in which the'process is carried out commercially.
  • the liquefied gel is delivered drop by drop into a tank containing another petroleum solvent such as gasoline solvent, naphtha, carbon tetrachloride etc., the introduction of the droplets into the tank being preferably unaccompanied by agitation.
  • another petroleum solvent such as gasoline solvent, naphtha, carbon tetrachloride etc.
  • the first action of the solvent is to take up all of the petroleum solute on the surface of the droplet and by cooling to case-harden the droplet. If we assume that the surface tensions of the molten gel and of the solvent are approximately similar, the grannice or beads of soap will be approximately of regular form. If these beads are quickly removed from the solvent they will still retain some of the original solute present in the gel because the solvent will not have had sumcient time to completely permeate the beads and entirely displace the original solute. If the beads are left long enough in the solvent, the solvent of course replaces all of the original gel solute.
  • the beads may be removed and dried in any suitable fashion to completely dr ve petroleum oi the solvent the'characteristics of saponified body may be 'If a petroleum soap gel is poured into solventout all 0! the solvent and leave pure soap. If
  • this solvent is not volatilethe soap beads will be I in the form of pure soap combined with thesolvent oi. the bath.
  • This latter may be of any suitable detergent material capable of dissolving I
  • Also'the' i I I ,non-volatile'solvents maybe used to replace only part oi. the original solute of the gel in which case I I produce soap beads combining mixed detergent materials consisting of the solute and the solvent.
  • thesolvent in the bath is 'a'mixed solmediate the'flaky 'orspheroid, that'is, a somewhat oblate or egg-shaped granule. 'By merely varying the solvents used the shape of the bead,
  • Alcoholic soap gel is prepared by neutralizing any fatty acid in alcohol. Desirably about 50% ofiatty acid is dissolved in the alcohol. 'To this the required amount of alkali solution, either of hydroxide or of carbonate is added. The hydroxide or carbonate is preferably added at an elevated temperature. On cooling an alcohol gel or soap is formed in which the proportion of alcohol to soap is roughly 1 to 1. This gel is subject to liquefaction upon heating.
  • the liquid gel containing water in the case noted above or made by any other process with or without water content is liquefied and poured into a tank containing a more volatile solvent of alcohol such as wood alcohol, acetone, ether, etc.
  • the droplets assume a generally spheroidalshape. If the alcohol solvent is heated the beads occur. The solute at the ou'ter'surfaces of the beads is immediately boiled oil and the embedded I to other solvents having different surface tensioiis from the gel such as petroleum compounds,
  • the droplets will assume shapes varying from the spheroid to the as: flake, these variations being apparently primarily determined by the extent of difference in the surface tensions of the solvent and the molten gel and also influenced to some extent by other factors as noted above.
  • soap gel made from any organic diluent. This includes petroleum compounds, coal tars, alcohols, ketones. In fact, even esters and chlorine or nitrp compounds may be used in the soap gels. Similarly pure soap beads, either solid or hollow water-containing soap beads, flakes, elongated granules, or
  • a method or producing soap beads or the like which includes the step of dropping a normally solid or gelled soapy substance in molten condition into a bathoi non-aqueous organic volatile cooling liquid to efiect rapid cooling and case hardening oi the drops into the form of beads or the like.
  • a method of forming beads of soap which consists in melting a soap gel including a soapy material and a solute, and introducing it in the form of small drops intoan organic non-aqueous liquid solvent for the solute which is suiiiciently cool to harden the soapy material in the liquefied gel.
  • a method of making soap beads/or the like which includesthe steps of melting an anhydrous petroleum soap gel and introducing drops of the liquefied gel into a solvent, for the petroleum in the tank containing a petroleum gel.
  • a method of making soap beads, or the like which includes the steps of melting an anhydrous petroleum soap gel, and introducing drops of the liquefied gel into a tank containing a petroleum solvent, for the petroleum in the gel, while maintaining said solvent at a temperature low enough to eflect case hardening of the drops of molten gel.
  • a method of making soap beads, or the like which includes the steps of melting an anhydrous petroleum soap gel, including a hydrocarbon solute, such as benzene, and dropping this melted gel into a bath containing a petroleum solvent for the solute.
  • a method of making soap beads, or the like whichincludes the steps of melting an anhydrous petroleum soap gel, including a hydrocarhon solute, such as benzene, dropping this melted gel into a bath containing a petroleum solvent for the solute, and maintaining such bath at a temperature low enough to etfect hardening of the drops of gel.
  • a hydrocarhon solute such as benzene
  • a method of producing beads of soap, or the like which includes the steps of liquefying an anhydrous petroleum soap gel, in which there is less petroleum solute than soap in the gel and dropping this liquefied gel into a hardening bath consisting of a solvent for the solute.
  • a method of producing soap in the form of beads, flakes, or the like which includes the steps of introducing drop by drop a liquefied soap solute, into a hardening bath consisting of a volatile solvent for the solute.
  • a method of producing soap in the form of beads, flakes, or the like which includes the steps of introducing drop by drop a liquefied soap gel, which gel includes soap and a solute into a hardening bath consisting of a volatile solvent'for the solute, and aiter the solvent has displaced the solute evaporating the solvent to leave pure soap.
  • a method of preparing soap beads from an alcoholic soap gel which includes the steps of liqueiying the gel, and dropping the gel into a tank containing a more volatile solvent of alcohol than any solvent present in the gel.
  • a method of preparing soap beads from an alcoholic soap gel which includes the steps of liqueiying the gel, and dropping the gel into a tank containing a more volatile solvent-of alcohol than any solvent present in the gel, said volatile solvent having a surface tension. approximately equivalent to the surface tension of the molten gel.
  • a method of preparing soap beads from an alcoholic soap gel which includes the steps of liquefying the gel and dropping the gel into a tank containing a more volatile solvent of alcohol, said volatile solvent having a surface tension approximately equivalent to the surface tension of the molten gel, and being at a temperature to efi'ect case hardening of the drops as they fall

Landscapes

  • 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)
  • Cosmetics (AREA)

Description

Patented Dec. 21, 1937 I ammo METHOD or mmc soar nuns on m Vaman R. Kokatnnr, New York, N. It, to Autoxygen Ina, New York, N. Y a corporation of New Yo No Drawing. Application September 7, 1935,
Serial No. 39,552
18 Claims. (01. 87-16) The advantage of preparing soap in the form of hollow or solid beads or spheroids is well recognized, since soap in this form presents a large surface exposure, whereby its solubility is enhanced and a profuse lather may be quickly produced. Until about a decade ago, the only type of soap beads available were solid beads or balls which were not even of relatively pure soap, but included a considerable amount of non-soapy l0 and non-saponified material, known to the art as filler material.
Present methods of producing the relatively pure soap beads which are extensively commercially used, involve what is known as the spray drying process, in which the minute droplets of soap are sprayed into the air and air-dried to cause them to assume the desired approximately spheroidal form. In all variations of the spray process, due to the fact that the soap is only molten at high temperature and due further to the fact that the sprayed molten droplets must not only be solidified but also dried in the air, careful control must be maintained over both the temperature and the humidity of the air in which the spheroidal particles are formed. This has heretofore involved many complexities in the construction of the apparatus for handling the soap as well as in the construction of the control mechanism for maintaining the desired tempera- 39 ture and humidity within a processing plant.
An object of the present invention is to provide a process of producing soap beads, flakes or the like which may be either solid or hollow, and consisting of pure soap or of soap combined with any other material, the process involving no spraying or spray drying and being far simpler, and less expensive than spray process and involving no complex apparatus and no problems of temperature and humidity control.
Another object is to provide a process by which I can produce soap beads devoid of "iiller material, but having any suitable type of detergent material incorporated in them.
My present invention is based partially on the discovery that minute drops of a soap gel falling into a bath of material which is a solvent for the material which has gelled with the soap, is -effective not only to case harden or set the droplets to form heads but to partially or completely replace the original petroleum or other base of the gel so that the resultant beads are composed of pure soap or of soap containing part of the original petroleum of the gel or part of the gel solvent or both.
56 The bath of solvent into which the droplets of gel fail serves the two-told function of promptly case-hardening the droplets and of eliminating (to any desired extent) the solute from the soap.
I shall have occasion in the specification and 5 claims to refer to two solvents (1) the solvent material which combined with the soap produces the soap gel, and (2) the solvent into which the droplets of molten gel are poured. To avoid confusion in terminology I shall refer, throughout 10 the specification and claims, to the solvent originally present in the gel as a "solute and to the bath of material into which the molten gel falls as a "solvent.
In practice, if a solvent is used having substanl5 tially the same or higher surface tension as the molten droplets of gel which fall into it, the soap beads upon case-hardening assume an almost perfect spherical form.
Factors which enter into the shape assumed 20 by the solidified soap particles, however, involve the temperature of the molten gel, the temperature of the solvent into which the molten gel is poured, the nature of the nozzle or other discharge device :trom which the molten gel drops 25 are emitted, and the method of agitating the solvent into which the molten gel falls (where agitation is resorted to).
One further important factor which seems to bear a definite relation to the shape assumed 80 by the drops as they fall into the solvent is the relative surface tensions of the gel and the solvent. Bygproperly regulating these relative surface tensions I am able to produce not only beads, but flakes or shapes intermediate flakes and 35 beads, such for instance as generally fiat elongated ovoids or granules.
If the bath of solvent is maintained at a temperature at which the solute in the soap gel will partially vaporize, the drops upon falling into the bath have the solute on their outside surfaces almost instantaneously dissolved and since the outside surfaces are simultaneously cooled the solute within the beads tends to expand and pull the beads up. Later, as cooling of the beads be- 5 comes complete and the gasifled solvent at the interior of the beads is liquefied, it will be absorbed back into the material and the resultant Product will be a hollow head. If this material is left in the solvent long enough the solute will be so completely replaced by the solvent and when the beads are removed from the bath, this solvent completely evaporates leaving hollow beads of pure soap.
In the event that the molten particles of gel identical with the original gel.
are dropped into a bath of solvent which is identical in nature with the solute intbe Iel. the beads which are formed will be chemically substantially To illustrate, this point-ii a petroleum soap gel formed in accordance with my prior Patent No. 1,753,859 is melted and dropped into a petrolsum solvent whichis identical with the petroleum in the gel, the solvent willserve to cool the drop lets with suillcient rapiditys'o that they are case- I the form of minute spheroidal petroleum soap It may desirable in many places to replace theoriginal solute of the gel with some other detergent material which is a solvent oithe solute [in which eventsuch'detergent solvent is used, in
the bath and by leaving the soap bath long enough the original solute will beads in the be replaced by the other detergent solvent and the original soap gel may be converted into soap beads 'having'radically different characteristics from the gel. v I
- The invention may perhaps be best understood i .irom certain typical examples of the manner in which the'process is carried out commercially.
I I I 7 Example 1 An anhydrous petroleum soap gel formed in accordance with the process disclosed in my Pati eat 1,753,659ahd including typically a hydrocarebon solute, such, for instance,'as *kerowne, is
heated until liquefaction thereof occurs, this tem-v i Q 'peratureapproximating, in the case of benzene,
roughlyi50-2009C. I
The liquefied gel is delivered drop by drop into a tank containing another petroleum solvent such as gasoline solvent, naphtha, carbon tetrachloride etc., the introduction of the droplets into the tank being preferably unaccompanied by agitation.
I have. found it desirable to prepare a gel in which the proportions of petroleum solute to the soap is not in excess of 1 to 1. If the proportion of the petroleum solute in the molten gel is less than 1, the granules assume more nearly spheroidal shape and the wall structures of the granules are substantial. If the proportion of the petroleum solute in the gel is more than 1 to l the walls of the granules are thinner and their structure is irregular.
Assuming that the melted petroleum gel con-.
taining somewhat less petroleum than soap is poured into the petroleum solvent, the first action of the solvent is to take up all of the petroleum solute on the surface of the droplet and by cooling to case-harden the droplet. If we assume that the surface tensions of the molten gel and of the solvent are approximately similar, the grannice or beads of soap will be approximately of regular form. If these beads are quickly removed from the solvent they will still retain some of the original solute present in the gel because the solvent will not have had sumcient time to completely permeate the beads and entirely displace the original solute. If the beads are left long enough in the solvent, the solvent of course replaces all of the original gel solute. If-the solvent is highly volatile the beads may be removed and dried in any suitable fashion to completely dr ve petroleum oi the solvent the'characteristics of saponified body may be 'If a petroleum soap gel is poured into solventout all 0! the solvent and leave pure soap. If
this solvent is not volatilethe soap beads will be I in the form of pure soap combined with thesolvent oi. the bath. This latter may be of any suitable detergent material capable of dissolving I Also'the' i I I ,non-volatile'solvents maybe used to replace only part oi. the original solute of the gel in which case I I produce soap beads combining mixed detergent materials consisting of the solute and the solvent.
' If a molten petroleum, gel is into anon- I hydrocarbon solvent, such for, instance asalcohol,
out the solute in. the original soap'gel.
acetone, etc., which has considerable less surface form. n thesolvent in the bath is 'a'mixed solmediate the'flaky 'orspheroid, that'is, a somewhat oblate or egg-shaped granule. 'By merely varying the solvents used the shape of the bead,
granule, flake or other minute ,self sustaining varied at will. w
tension'than the molten gel itself. the soap does I not assume a granular form but assumes a flaky naphthawhich has been heated to a temperature I I suiilclent to partially or completely vaporize the petroleum in the gel, certain interesting-results and still'heated solvent in the beads tends to swell them. Upon cooling and drying these swol- I let: beads are ,iound .to be hollow. Apparently some of the petroleum within the beads is vapor, 'ized almost simultaneously with case-hardening of the beads, but being unable to scape merely expanded thebeads and any excess liquid-petroleum at the center point of the heads is subsequently absorbed by their walls. If these beads are maintained submerged in the solvent naphtha or equivalent solvent for a' sufllcient length of f time to dry out all the petroleum, then subsequently exposed to the air to permit complete Where anhydrous gels are used-the beads will be anhydrous. If however, a petroleum gel made by other processes and containing a certain amount of water is used, the soap beads themselves may retain at least part of this original water.
Example 2 Alcoholic soap gel is prepared by neutralizing any fatty acid in alcohol. Desirably about 50% ofiatty acid is dissolved in the alcohol. 'To this the required amount of alkali solution, either of hydroxide or of carbonate is added. The hydroxide or carbonate is preferably added at an elevated temperature. On cooling an alcohol gel or soap is formed in which the proportion of alcohol to soap is roughly 1 to 1. This gel is subject to liquefaction upon heating. The liquid gel containing water in the case noted above or made by any other process with or without water content is liquefied and poured into a tank containing a more volatile solvent of alcohol such as wood alcohol, acetone, ether, etc. The surface tension of the gel in the solvent being substantially identical, the droplets assume a generally spheroidalshape. If the alcohol solvent is heated the beads occur. The solute at the ou'ter'surfaces of the beads is immediately boiled oil and the embedded I to other solvents having different surface tensioiis from the gel such as petroleum compounds,
benzene, carbon tetrachloride, etc. the droplets will assume shapes varying from the spheroid to the as: flake, these variations being apparently primarily determined by the extent of difference in the surface tensions of the solvent and the molten gel and also influenced to some extent by other factors as noted above.
In the above examples -I have described two types of gels, but it is understoodthat it is within the spirit of the invention to use a soap gel made from any organic diluent. This includes petroleum compounds, coal tars, alcohols, ketones. In fact, even esters and chlorine or nitrp compounds may be used in the soap gels. Similarly pure soap beads, either solid or hollow water-containing soap beads, flakes, elongated granules, or
other particles exposing a large surface area and containing naphtha, alcohols, ketones or other useful or detergent materials may be made within the spirit and scope of the appended claims.
It will be more or less .seli -evident that when the solvent for the gel solute becomes saturated or has taken up an undesirable "amount of solute, the solvent and solute may be readily separated by a standard fractional distillation process.
Having thus described my invention, what I claim as new and desire to secure by Letters Pat- I out is:-
i. A method or producing soap beads or the like, which includes the step of dropping a normally solid or gelled soapy substance in molten condition into a bathoi non-aqueous organic volatile cooling liquid to efiect rapid cooling and case hardening oi the drops into the form of beads or the like.
2. A method of forming beads of soap which consists in melting a soap gel including a soapy material and a solute, and introducing it in the form of small drops intoan organic non-aqueous liquid solvent for the solute which is suiiiciently cool to harden the soapy material in the liquefied gel.
3. A method as set forth in claim 2 wherein the solvent is eflcctive to quickly vaporize the solute on the outer surfaces of the drops.
4. Amethod as set forth in claim 2 wherein the solvent is volatile and substantially evaporates from the soap beads upon air drying of the latter.
5. A method as set forth in claim 1 wherein the surface tension of the molten gel and of the bath are substantially identical.
6. A method as set forth in claim 1 wherein the temperature dill'erential between the bath and the droplets of molten gel is sumcient to cause swelling of the droplets as they fall into the bath and the production of resultant hollow beads.
7. A method of making soap beads/or the like, which includesthe steps of melting an anhydrous petroleum soap gel and introducing drops of the liquefied gel into a solvent, for the petroleum in the tank containing a petroleum gel.
8. A method of making soap beads, or the like, which includes the steps of melting an anhydrous petroleum soap gel, and introducing drops of the liquefied gel into a tank containing a petroleum solvent, for the petroleum in the gel, while maintaining said solvent at a temperature low enough to eflect case hardening of the drops of molten gel.
9. A method of making soap beads, or the like, which includes the steps of melting an anhydrous petroleum soap gel, including a hydrocarbon solute, such as benzene, and dropping this melted gel into a bath containing a petroleum solvent for the solute.
10. A method of making soap beads, or the like, whichincludes the steps of melting an anhydrous petroleum soap gel, including a hydrocarhon solute, such as benzene, dropping this melted gel into a bath containing a petroleum solvent for the solute, and maintaining such bath at a temperature low enough to etfect hardening of the drops of gel.
11. A method of producing beads of soap, or the like, which includes the steps of liquefying an anhydrous petroleum soap gel, in which there is less petroleum solute than soap in the gel and dropping this liquefied gel into a hardening bath consisting of a solvent for the solute.
12. A method of producing soap in the form of beads, flakes, or the like, which includes the steps of introducing drop by drop a liquefied soap solute, into a hardening bath consisting of a volatile solvent for the solute.
13. A method of producing soap in the form of beads, flakes, or the like, which includes the steps of introducing drop by drop a liquefied soap gel, which gel includes soap and a solute into a hardening bath consisting of a volatile solvent'for the solute, and aiter the solvent has displaced the solute evaporating the solvent to leave pure soap.
14. A method of preparing soap beads from an alcoholic soap gel, which includes the steps of liqueiying the gel, and dropping the gel into a tank containing a more volatile solvent of alcohol than any solvent present in the gel.
15. A method of preparing soap beads from an alcoholic soap gel, which includes the steps of liqueiying the gel, and dropping the gel into a tank containing a more volatile solvent-of alcohol than any solvent present in the gel, said volatile solvent having a surface tension. approximately equivalent to the surface tension of the molten gel.
16. A method of preparing soap beads from an alcoholic soap gel, which includes the steps of liquefying the gel and dropping the gel into a tank containing a more volatile solvent of alcohol, said volatile solvent having a surface tension approximately equivalent to the surface tension of the molten gel, and being at a temperature to efi'ect case hardening of the drops as they fall
US39552A 1935-09-07 1935-09-07 Method of making soap beads or the like Expired - Lifetime US2102849A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US39552A US2102849A (en) 1935-09-07 1935-09-07 Method of making soap beads or the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US39552A US2102849A (en) 1935-09-07 1935-09-07 Method of making soap beads or the like

Publications (1)

Publication Number Publication Date
US2102849A true US2102849A (en) 1937-12-21

Family

ID=21906076

Family Applications (1)

Application Number Title Priority Date Filing Date
US39552A Expired - Lifetime US2102849A (en) 1935-09-07 1935-09-07 Method of making soap beads or the like

Country Status (1)

Country Link
US (1) US2102849A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2448280A (en) * 1946-02-09 1948-08-31 Socony Vacuum Oil Co Inc Insulating gel
US2448439A (en) * 1944-03-11 1948-08-31 Standard Oil Dev Co Process of preparing an inorganic hydrogel
US2449253A (en) * 1945-06-23 1948-09-14 Socony Vacuum Oil Co Inc Preparation of hollow gel spheroids
US2474911A (en) * 1944-03-11 1949-07-05 Standard Oil Dev Co Preparation of spherical gel particles
US2503913A (en) * 1944-06-21 1950-04-11 Standard Oil Dev Co Process of drying inorganic hydrogel particles
US2584286A (en) * 1944-03-11 1952-02-05 Standard Oil Dev Co Preparation and drying of catalytic hydrogel beads
US2801220A (en) * 1954-07-06 1957-07-30 Baker Castor Oil Co Production of lubricating greases from monohydric alcohol esters of hydroxy fatty acids
US20040106536A1 (en) * 2000-03-20 2004-06-03 Jean Mane Solid perfumed preparation in the form of microbeads and the use thereof

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2448439A (en) * 1944-03-11 1948-08-31 Standard Oil Dev Co Process of preparing an inorganic hydrogel
US2474911A (en) * 1944-03-11 1949-07-05 Standard Oil Dev Co Preparation of spherical gel particles
US2584286A (en) * 1944-03-11 1952-02-05 Standard Oil Dev Co Preparation and drying of catalytic hydrogel beads
US2503913A (en) * 1944-06-21 1950-04-11 Standard Oil Dev Co Process of drying inorganic hydrogel particles
US2449253A (en) * 1945-06-23 1948-09-14 Socony Vacuum Oil Co Inc Preparation of hollow gel spheroids
US2448280A (en) * 1946-02-09 1948-08-31 Socony Vacuum Oil Co Inc Insulating gel
US2801220A (en) * 1954-07-06 1957-07-30 Baker Castor Oil Co Production of lubricating greases from monohydric alcohol esters of hydroxy fatty acids
US20040106536A1 (en) * 2000-03-20 2004-06-03 Jean Mane Solid perfumed preparation in the form of microbeads and the use thereof
US7723284B2 (en) * 2000-03-20 2010-05-25 V. Mane Fils Solid perfumed preparation in the form of microbeads and the use thereof

Similar Documents

Publication Publication Date Title
DE876838C (en) Process for the manufacture of non-caking and hardening ammonium nitrate
US2102849A (en) Method of making soap beads or the like
US3240712A (en) Process for manufacturing a detergent briquette
US2372402A (en) Interstitially coated compound and method of making the same
US2089945A (en) Process of producing ammonium nitrate and other fusible compounds
US2423452A (en) Process for treating sprayed dried organic detergents
US2115851A (en) Process for producing ammonium nitrate
US2834770A (en) Water-soluble shellac powder
US2933526A (en) Process for the manufacture of urea in granular form
US2189772A (en) The manufacture of modified
US1954596A (en) Material for high emission cathodes
US2304133A (en) Production of anhydrous aluminum sulphate
US3055835A (en) Drying process for detergents
US2206916A (en) Manufacture of smokeless powders
US2622090A (en) Method of neutralizing sulphonic products
US1971634A (en) Of producing an oxidized
US2830064A (en) Solid sarcosinate particles and method of preparation thereof
US2129919A (en) Solid starch and method of preparing the same
US2075025A (en) Coating compositions and processes of preparing the same
US1475492A (en) Hydrated calcium nitrate and method of making same
US2944977A (en) Process for preparing aqueous soapsynthetic detergent mixtures in ribbon form
US2135365A (en) Method of and agent for producing fire extinguishing foam
US1873262A (en) Preparing bentonite compositions
US2174238A (en) Manufacture of ammonium nitrate
DE869209C (en) Process for neutralizing sulfonation products
点击 这是indexloc提供的php浏览器服务,不要输入任何密码和下载