US2846401A - Granular detergent compositions - Google Patents
Granular detergent compositions Download PDFInfo
- Publication number
- US2846401A US2846401A US594365A US59436556A US2846401A US 2846401 A US2846401 A US 2846401A US 594365 A US594365 A US 594365A US 59436556 A US59436556 A US 59436556A US 2846401 A US2846401 A US 2846401A
- Authority
- US
- United States
- Prior art keywords
- spray dried
- granules
- sulfate
- sodium
- amount
- 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
Links
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
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/02—Inorganic compounds ; Elemental compounds
- C11D3/04—Water-soluble compounds
- C11D3/046—Salts
-
- 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
- C11D11/00—Special methods for preparing compositions containing mixtures of detergents
- C11D11/02—Preparation in the form of powder by spray drying
-
- 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
- C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
- C11D17/0039—Coated compositions or coated components in the compositions, (micro)capsules
-
- 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
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/02—Inorganic compounds ; Elemental compounds
- C11D3/04—Water-soluble compounds
- C11D3/06—Phosphates, including polyphosphates
Definitions
- the present invention relates to anionic detergent compositions which are free-flowing and resistant to caking, and more particularly to spray dried, heavy-duty,
- the invention also relates to the process of producing suchdetergent compositions.
- detergent compositions for example, are spray dried mixtures of water soluble anionic syntheticv detergents of the 1 sulfuric reaction product type with massive amounts of alkali metal tripolyphosphate.
- Such detergent compositions for example, are disclosed in vdetail in U. S. Patent 2,486,922 to Strain.
- Particularly efiicient compositions for example, are the spray dried products which are based on the sodium salt of alkyl sulfuric acid esters of higher alcohols obtained by the reduction of tallow and coconut oil and those which are based on sodium polypropylene phenyl sulfonate with 9-18, and preferably with 12-15 carbon atoms in the polypropylene chain, and.
- compositions are commercially available in the form of solid spray dried granules whose components fall within the following percentage ranges: from about 20% to about 40% by weight ,ofactive synthetic from about 10% to about 60% by.
- weightvofalkali metal phosphates such as sodium tripolyphosphate,;. pyrophosphate and orthophosphate, the.
- whichjcan include, for example, moisture, perfume,
- organic builders sodium silicate, 'and other inorganic alkaline salts.
- Another object is to provide heavy-dutyfsynthetic detergent phosphate-containing washing compositions'which have superior resistance to change in caking and freeflowing characteristics when subjected to storage for pro-'-- longed: periods of time 'at relatively high temperature and high humidity.
- Another object is to provide animproved heavy-duty synthetic detergent composition which does not require expensive moisture-proof containers for storage under humid atmospheric conditions. i r
- a further objectof the invention is toprovide a-process Y duty detergent compositions.
- the present invention is directed for the production of the above noted improvedheavycomprises agitating spray dried particles of heavy-duty synthetic detergent compositions 'hereinbefore referred to andzsimultaneously'applying to the surface thereof an aqueous'solution of a' sulfate of magnesium, 'zinc,"alumi-':” num, or mixtures ofsuch salts.
- Theamountof solution"? applied to the particles is selected so that the concentration of inorganic sulfate salt applied to the" granules. ranges from about 1% to about 10% of the'weight of the granulesitr'eated;preferably from about 2% to about 4%.
- the concentration of the inorganic sulfate in the solution) applied to the granules is not critical, and can be adjusted 70 coastal areas where high temperature and high humidity; prevail forextended periods of time, the'prior art methods within a range of 10% by weight to saturation, a concen tration of about 18% to 22%"by'weight being preferred,
- the temperature conditions under which the aqueous solution of sulfate salt is applied to the granules is not critical, but of course reasonable limits should be observed.
- the amount of moisture evaporation that may take place during transfer or cooling. of the granules by airlift will bear consideration.
- mag nesium, zinc, or aluminum sulfate, or mixture of such salts in accordance with the invention not only imparts marked resistance to the development of free-flow reluctance in the granular product, but also surprisingly achieves a resistance to true caking that is far superior to that noted in products whose granules have been treated with water alone.
- the inorganic sulfate salt enters into chemical reaction with granular components at substantially the surface of the particles, thereby, for example, forming low or nonhydrating double salts with the phosphates, and especially those phosphates resulting, from the reversion or hydrolysis of tripolyphosphate, i. e., orthophosphates and pyrophosphates.
- tripolyphosphate i. e., orthophosphates and pyrophosphates.
- the specific method whereby the inorganic salt solution is applied to the spray dried granules does not constitute a part of the invention and the solutions may be applied continuously or batchwise as may be desired.
- the dried and cooled granules are usually passed continuously through a rotating drum Where they are tumbled.
- the drum may be equipped with plates or batfies afiixed to the inner wall thereof to provide more effective tumbling. It is conventional to mix the spray dried granules in such a rotating drum apparatus with ingredients such as perfume, organic builder, or other desirable adjuncts that might be volatilized or thermally decomposed under the more elevated temperature conditions occurring within the spray-drying tower.
- Magnesium, zinc, or'aluminum sulfate solution designed for treatment of the spray dried particles in accordance with the present invention can be applied to the particles in such conventional rotating drums, either simultaneously or-sequentially with the application of other constituents by spray-on procedure.
- Other methods of application of the-solution to the granular particles are known in the art and can be employed without departing from the spirit of the invention.
- Example I 100 parts of spray dried detergent granules containing 28% sodium polypropylene benzene sulfonate in which the polypropylene radical averaged about 12 carbon atoms, about 19.5% sodium tripolyphosphate, and'about 13% sodium pyrophosphates, about 1.5% sodium orthophosphates, about 6% sodium silicate solids having a ratio of SiO Na O of 2: 1, about 7.2% moisture, about 2.4% ethanolamide of mixed coconut oil fatty acids, and the balance being mainly sodium sulfate with minor amounts of carboxymethyl cellulose, fluorescent dyes and perfume, were agitated in a rotating drum and sprayed with a water solution of magnesium sulfate having a concentration of approximately 20%.
- the amount of anhydrous magnesium sulfate applied to the granules amounted to about 2.5% and the moisture content. of the treated product was increased to about 17.3%.
- This product was packaged and stored under temperature and humidity conditions which were known to promote freefiow reluctance and'caking. The product was found to be resistant to the development of free-flow reluctance and even after fourteen days of storage was as free-flowing and free from caking as the initial product.
- the magnesium sulfate in the solution sprayed on the granules reacts with the pyroand orthophosphates at or near the surface of the granules to form low hydrating or nonhydrating magnesium-sodium phosphates. which indicates that the equilibrium moisture of the granules containing the sprayed-on magnesium sulfate decreases with increasing amounts of magnesium sulfate. If, in the product of this example, the magnesium sulfate did not react with any component of the granules, it would form its heptahydrate and an increase in equilibrium moisture would be expected.
- the product of this example and the products of the invention in general are characterized by a coating comprising hydrated double salts of the phosphates formed from sodium and from the magnesium (or zinc or aluminum) of the magnesium sulfate solution applied.
- Example [I In the manner described in Example I, parts of the same spray dried detergent granules were treated with a solution of aluminum sulfate of approximately 20% concentration so as to coat the particles with about 2% anhydrous aluminum sulfate and to increase the moisture content to about 14.1%.
- the product so treated was packaged and stored under humidity and temperature conditions known to cause the development of freefiow reluctance and caking. The product was entirely resistant against the development of free-flow reluctance and was outstandingly resistant to caking.
- a solution containing a mixture of aluminum sulfate and magnesium sulfate at about 20% concentration can also be employed in the place of the aluminum sulfate solution of Example 11 to yield a product having superior stability against caking and the development of free-flow reluctance.
- Example III The process of Example II was repeated using a solution of zinc sulfate of about 20% concentration.
- Example IV The treatment of detergent granules as specified in Example II is followed using a magnesium sulfate solution of approximately 20% concentration and a spray dried synthetic detergent composition containing about 35% sodium polypropylene benzene sulfonate in which the polypropylene radical averaged 12 carbon atoms, about 15.0% sodium tripolyphosphate, about 22% sodium pyrophosphates, about 2% sodium orthophosphates, about 6% sodium silicate solids having a sio zNa O
- This belief has been supported by evidenceratio of 2:1, about 8% moisture, and the balance being mainly sodium sulfate with minor amounts of carboxymethyl cellulose, fluorescent dyes, and perfume.
- Example IV Treatment of the granules so as to apply thereto approximately 2% anhydrous magnesium sulfate and to increase the moisture content to about 15% renders the product especially stable against caking and the development of free-flow reluctance during storage under atmospheric conditions of high temperature and high humidity.
- the process of Example IV can also be applied to spray dried synthetic detergent granules which contain substantially greater amounts of sodium tripolyphosphate, such as from '1 to 1% times the amount of active synthetic' detergent and with smaller proportions of other phosphates, and the superiority of the products against the development of free-flow reluctance and caking under humid storage conditions is readily apparent.
- the sodium salt of the alkyl sulfuric-acid esters of higher alcohols derived by the reduction of coconut oil or tallow can be substituted in whole or in part to yield products having superior characteristics as regards caking and freedom of flow.
- thetic detergent is, at least in substantial part, sodium polypropylene benzene sulfonate in which the polypropyl'ene radicals average about 12 carbon atoms.
- a spray dried heavy-duty synthetic detergent granule possessing improved resistance to change, during storage under humid atmospheric conditions, in the free-flowing and non-caking character of the freshly 'spray dried granule detergent compositions consisting essentially from about 20% to about 40% by weight of water soluble anionic synthetic detergent of the sulfuric reaction product type, from about 10% to about by weight of alkali metal phosphates including sodium tripolyphosphate and the pyrophosphate and orthophosphate reversion products thereof, from about 12% toabout' 25% moisture, and from about 10% to about 30% by weight of sodium sulfate, said granules being characterized by a coating comprising hydrated double salts of said phosphates formed from sodium and from at least one polyvalent metal selected from the group consisting of magnesium, zinc, and aluminum, the amount of polyvalent metal present being equivalent to an amount of anhydrous sulfate of said metal within the range of about 1% to about 10%.
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)
- Inorganic Chemistry (AREA)
- Detergent Compositions (AREA)
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BE557881D BE557881A (enExample) | 1956-06-28 | ||
| US594365A US2846401A (en) | 1956-06-28 | 1956-06-28 | Granular detergent compositions |
| DEP18600A DE1076866B (de) | 1956-06-28 | 1957-05-21 | Wasch- und Reinigungsmittel und Verfahren zu seiner Herstellung |
| FR1176379D FR1176379A (fr) | 1956-06-28 | 1957-05-31 | Nouvelles compositions détersives et leur procédé de fabrication |
| GB19872/57A GB806340A (en) | 1956-06-28 | 1957-06-24 | Improved detergent compositions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US594365A US2846401A (en) | 1956-06-28 | 1956-06-28 | Granular detergent compositions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2846401A true US2846401A (en) | 1958-08-05 |
Family
ID=24378578
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US594365A Expired - Lifetime US2846401A (en) | 1956-06-28 | 1956-06-28 | Granular detergent compositions |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US2846401A (enExample) |
| BE (1) | BE557881A (enExample) |
| DE (1) | DE1076866B (enExample) |
| FR (1) | FR1176379A (enExample) |
| GB (1) | GB806340A (enExample) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3288858A (en) * | 1962-12-21 | 1966-11-29 | Procter & Gamble | Sulfoxides and syntheses thereof |
| US3336230A (en) * | 1962-12-21 | 1967-08-15 | Procter & Gamble | Built detergent compositions containing dialkyl sulfoxides |
| US3355494A (en) * | 1965-03-30 | 1967-11-28 | Procter & Gamble | Preparation of ketosulfoxides |
| US3615185A (en) * | 1968-11-22 | 1971-10-26 | Fmc Corp | Process for the production of trisodium phosphate |
| US3925230A (en) * | 1973-12-26 | 1975-12-09 | Procter & Gamble | Non-caking laundry sour |
| US3989635A (en) * | 1973-09-10 | 1976-11-02 | Lion Fat & Oil Co., Ltd. | Process for improving granular detergents |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB0922649D0 (en) | 2009-12-29 | 2010-02-10 | Unilever Plc | Low TMF extruded soap bars having reduced cracking |
| DE102012203688A1 (de) | 2012-03-08 | 2013-09-12 | Henkel Ag & Co. Kgaa | Geformte Seifenprodukte mit einem verringerten Gehalt an Fettsäureseifen |
| WO2022258605A1 (en) | 2021-06-10 | 2022-12-15 | Unilever Ip Holdings B.V. | High moisture silica gel soap bars and process for preparing the same |
| WO2025056485A1 (en) | 2023-09-11 | 2025-03-20 | Unilever Ip Holdings B.V. | Low tfm high moisture polymeric silica soap bars |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR974713A (fr) * | 1947-11-07 | 1951-02-26 | Unilever Ltd | Perfectionnements aux détergents non-savonneux |
| GB676449A (en) * | 1948-10-12 | 1952-07-30 | Bataafsche Petroleum | Improvements in and relating to detergent compositions |
| US2768095A (en) * | 1952-05-30 | 1956-10-23 | Shell Dev | Process of coating finely divided solid material |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2480579A (en) * | 1943-10-21 | 1949-08-30 | Colgate Palmolive Peet Co | Detergent products and their preparation |
| US2456437A (en) * | 1943-11-24 | 1948-12-14 | Colgate Palmolive Peet Co | Nondusting soap composition and method for making same |
-
0
- BE BE557881D patent/BE557881A/xx unknown
-
1956
- 1956-06-28 US US594365A patent/US2846401A/en not_active Expired - Lifetime
-
1957
- 1957-05-21 DE DEP18600A patent/DE1076866B/de active Pending
- 1957-05-31 FR FR1176379D patent/FR1176379A/fr not_active Expired
- 1957-06-24 GB GB19872/57A patent/GB806340A/en not_active Expired
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR974713A (fr) * | 1947-11-07 | 1951-02-26 | Unilever Ltd | Perfectionnements aux détergents non-savonneux |
| GB676449A (en) * | 1948-10-12 | 1952-07-30 | Bataafsche Petroleum | Improvements in and relating to detergent compositions |
| US2768095A (en) * | 1952-05-30 | 1956-10-23 | Shell Dev | Process of coating finely divided solid material |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3288858A (en) * | 1962-12-21 | 1966-11-29 | Procter & Gamble | Sulfoxides and syntheses thereof |
| US3336230A (en) * | 1962-12-21 | 1967-08-15 | Procter & Gamble | Built detergent compositions containing dialkyl sulfoxides |
| US3355494A (en) * | 1965-03-30 | 1967-11-28 | Procter & Gamble | Preparation of ketosulfoxides |
| US3615185A (en) * | 1968-11-22 | 1971-10-26 | Fmc Corp | Process for the production of trisodium phosphate |
| US3989635A (en) * | 1973-09-10 | 1976-11-02 | Lion Fat & Oil Co., Ltd. | Process for improving granular detergents |
| US3925230A (en) * | 1973-12-26 | 1975-12-09 | Procter & Gamble | Non-caking laundry sour |
Also Published As
| Publication number | Publication date |
|---|---|
| DE1076866B (de) | 1960-03-03 |
| FR1176379A (fr) | 1959-04-09 |
| GB806340A (en) | 1958-12-23 |
| BE557881A (enExample) |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2846401A (en) | Granular detergent compositions | |
| US4000094A (en) | Water-insoluble aluminosilicate-containing detergent composition | |
| US4091544A (en) | Drying process | |
| IE43415B1 (en) | Process for preparation of per salts | |
| US2712529A (en) | Detergent composition | |
| JPS59196396A (ja) | 洗剤組成物の製造方法 | |
| AU643206B2 (en) | Agglomerated peroxyacid bleach granule and process for making same | |
| EP0451893B1 (en) | Particulate bleaching detergent composition | |
| US4131558A (en) | Process for preparing an orthophosphate-silicate detergent product | |
| CA1137258A (en) | Stabilized alkali metal percarbonate powder bleach | |
| US2863835A (en) | Perborate composition | |
| US4497757A (en) | Energy efficient hydration process | |
| US3290254A (en) | Methyl-beta-hydroxydodecyl sulfoxide containing detergent compositions | |
| CA1227100A (en) | Detergent compositions | |
| US4162236A (en) | Detergent compositions containing mixtures of alkylbenzene sulfonates as the detergent active | |
| US4427567A (en) | Method for reconditioning of poorly flowing or caked detergent powders | |
| US2536833A (en) | Recovery of naphthoquinone | |
| US2175781A (en) | Process for the manufacture of sodium silicate detergents | |
| US2897155A (en) | Process for preparing a detergent composition containing anhydrous form 11 tripolyphosphate | |
| US3056652A (en) | Modification of the hydration characteristics of form ii sodium tripolyphosphate prior to detegent processing | |
| US3965169A (en) | Crystalline trisodium carboxymethyloxysuccinate monohydrate | |
| US3520817A (en) | Process for making fast hydrating tripolyphosphates and detergents containing said phosphates | |
| US3455834A (en) | Process for production of detergent tablets | |
| US3753930A (en) | Process for preparing spray dried blended detergents | |
| US3227517A (en) | Potassium-ammonium permonosulphate compounds and method of their preparation |