|Publication number||US3888781 A|
|Publication date||Jun 10, 1975|
|Filing date||Sep 5, 1972|
|Priority date||Sep 5, 1972|
|Publication number||US 3888781 A, US 3888781A, US-A-3888781, US3888781 A, US3888781A|
|Inventors||Kingry Gary W, Lahrman Frank H|
|Original Assignee||Procter & Gamble|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (8), Referenced by (25), Classifications (14)|
|External Links: USPTO, USPTO Assignment, Espacenet|
United States Patent Kingry et al.
PROCESS FOR PREPARING A GRANULAR AUTOMATIC DISI-IWASHING DETERGENT COMPOSITION Inventors: Gary W. Kingry; Frank H.
Lahrman, both of Cincinnati, Ohio Assignee: The Procter & Gamble Company,
Cincinnati, Ohio Filed: Sept. 5, 1972 Appl. No.: 286,654
US. Cl. 252/99; 252/ 135; 252/ 174 Int. Cl Clld 7/54 Field of Search 252/99, 135, 174
References Cited UNITED STATES PATENTS 4/1966 Matthaei 252/99 12/1967 Kancko et a]... 252/99 8/1971 Coates 252/99 11/1971 Corliss et 252/135 X Fairs 252/99 Primary Examiner-Benjamin R. Padgett Assistant Examiner-E. A. Miller Attorney, Agent, or Firm-Charles R. Wilson; Julius P.
Filcik; Richard C. Witte  ABSTRACT A method of producing an automatic dishwasher detergent composition comprising the steps of charging a particulate alkaline builder salt to a mixture zone, agi- Q tating the particulate matter and spraying thereon a i mixture of liquid silicate and nonionic detergent. The resultant composition is in the form of crisp, free- Y flowing agglomerated granules. In a preferred aspect,
a high level of nonionic detergent is included in the formulation without destroying the crispness of th granular product.
10 Claims, No Drawings PROCESS FOR PREPARING A GRANULAR AUTOMATIC DISHWASI-IING DETERGENT COMPOSITION BACKGROUND OF THE INVENTION The present invention relates to a process of producing an automatic dishwasher detergent composition. In a preferred aspect, it relates to a process of producing a dishwasher detergent composition which is crisp and free flowing and contains a high level of nonionic deterent. g Automatic dishwasher detergent compositions generally contain an alkaline builder salt, a bleach, an alkali metal silicate and a small level of water-soluble organic synthetic nonionic detergent. The alkaline builder salt sequesters or ties up hardness ions normally found in tap water thus allowing the therein included detergent to more satisfactorily perform its function. The
purpose of the bleach component is to break up food particles into a form which is more easily dissolvable and, hence, more easily removable from tableware. An alkali metal silicate is included in the known compositions for its corrosion inhibiting effect. The generally included nonionic detergent performs a cleaning function as well as providing a water sheeting" effect. The latter function is important in that it allows for water to more easily drain from tableware thus leaving the tableware with a spotless appearance. Such known compositions are generally found in the form of agglomerates. The dry components are normally admixed and thereafter sprayed with water or a liquid silicate. The sprayon liquid material has the effect of causing the agglomeration of the small particulate matter into larger forms.
Preferably, a relatively high level of nonionic detergent is desired in a dishwasher detergent composition. Unfortunately, nonionic detergents when included in a granular detergent composition by prior art methods tend to make the total composition tacky and non-free flowing. For this reason, generally less than 3% by weight nonionic detergent is included in dishwasher detergent compositions. Various processes and additive materials have been used in an attempt to overcome the caking problem inherent with high levels of nonionic detergents in such compositions. While some prior art attempts have been successful to a limited degree, there is still a need to include higher levels of nonionic detergents in dishwashing detergent compositions without experiencing a caking effect.
An object of the present invention is the production of an automatic dishwasher detergent composition by an economical process.
Another object of this invention is to produce a noncaking automatic dishwasher detergent composition.
A still further object is to produce an automatic dish washer detergent composition that contains a high level of nonionic detergent and is non-caking.
These and other objects will become apparent from the description and the examples to follow.
As used herein, all percentages are by weight unless otherwise specified.
SUMMARY OF THE INVENTION A process for producing a crisp, free-flowing, agglomerated granular automatic dishwasher detergent composition comprising the steps of:
a. charging to a mixing zone particulate matter comand wherein the liquid mixture is sprayed on at a level of from 25% to 50% based on the total com position to form said agglomerated granules.
DETAILED DESCRIPTION OF THE INVENTION The process of the present invention comprises initially charging particulate matter comprising an alkaline builder salt to a mixing zone. The particulate matter is then agitated and while being agitated has sprayed thereon a mixture of liquid silicate and a nonionic de- 5 tergent. As a result of the spray-on of the liquid mixture, the particulate solids form agglomerates which are crisp and free flowing.
The alkaline builder salts that form a part of the composition of this invention are included therein in the range of from 10% to preferably 25% to 50%, based on the total final composition. The particular builder salts that form a part of this invention are any of the well-known sequestering type or precipitating type builder salts commonly used in automatic dishwasher detergent composition. Particularly preferred builder salts are sodium tripolyphosphate, alkali metal garbona tes, and alkali metal citrates.
Additional particulate components that can be included with the alkaline builder salts include sodium sulfate, a chlorine-yielding bleach as more fully described hereinafter, various known suds suppressors, coloring matter and dyes.
The particulate matter may have a wide range of particle sizes. Preferably, all the particles will pass through a Tyler No. 8 screen.
As the first step of the process of this invention above, particulate matter is charged to a mixing zone. Any suitable mixing device such as an inclined pan granulator, a rotating drum, or any other vessel with suitable means of agitation may be used. Methods of agitating the particulate components of this invention are well known to those skilled in the art. With continuous agitation, a liquid alkali metal silicate and nonionic detergent mixture is sprayed onto the particulate mixture. The al,kgismetal s iliga,te has an SiO :alkali metal oxide ratio of from 3.6:1 to 05:1, preferably 3.2:1 to 2.521. The liquid silicates used herein contain from 45% to 70%, preferably 55% to 65%, water.
The nonionic detergents found most useful in the instant detergent composition are the low -fo arning nonromqgompounds. Compounds which meet the above 1 criteria and which are advantageously employed in the composition of this invention include, but are not limited to, the following polyoxyalkylene nonionic detergents: C C normal fatty alcohol-ethylene oxide condensates, i.e., condensation products of one mole of a 5 fatty alcohol containing from eight to 22 carbon atoms with from 3 to 20 moles of ethylene oxide; polyoxy- I hydrophobic chains together consitututing 31% to 39% by weight of the product, the linking hydrophilic chains together constituting 31% to 35% by weight of the product, the intrinsic viscosity of the product being from 0.06 to 0.09 and the molecular weight being from about 3,000 to 5,000 (all as described in us. Pat. No.
3,048,548); butylene oxide capped alcohol ethoxylates having the formula R oc,H. common where R I is a C -C alkyl group and y is an integer from about 3.5 to 10 and x is an integer from about 0.5 to 1.5; benzyl ethers of polyoxyethylene condensates of alkyl phenols having the formula where R is a C -C alkyl group and x is an integer from 5 to 40; and alkyl phenoxy polyoxyethylene ethanols having the formula R Q (oc n on where R is a Cg-Cgo alkyl group and x is an integer from 3 to 20. Other nonionic detergents are suitable for use in the herein-disclosed dishwashing compositions and it is not intended to exclude any detergent possessing the desired attributes.
The amount of liquid mixture sprayed onto the particulate mixture is sufficient to cause the particulate mixture to form a bed of agglomerated granules but not so great that its particulate nature is destroyed. From 25% to 50%, preferably 35% to 45% of the liquid mixture based on the total composition wherein the ratio of liquid silicate to nonionic detergent is from 2.511 to 20:], preferably 3:1 to 6:1, is sprayed onto the particulate mixture.
The liquid mixture is preferably agitated continuously prior to spray-on so as to prevent any separation of the alkali metal silicate and nonionic detergent. The
temperature of the liquid mixture is maintained at a temperature of from 110F. to 200F., preferably 140F. to 160F. At these temperatures proper atomization is achieved as well as the formation of agglomerates having an optimum particle size.
Spraying of liquid silicate and nonionic detergent separately onto the dry particulate mixture does not give a product as crisp or free flowing as the product resulting from the process of this invention. It is not known exactly why the spray-on of the mixture in accord with this invention gives a more crisp, free-flowing product than does the separate spray-on of the same components at the same weight level. It is believed that the resultant product is crisp and free flowing due to either the tacky nonionic detergent being enclosed within the silicate matrix as the agglomerated particles cool or hydrogen bonding existing between the nonionic detergent and silicate.
The agglomerated granules resulting from the abovedescribed spray-on may next be subjected to a drying operation and thereafter a grinding and classification operation to achieve a product having substantial uniformity in particle size. Preferably the resultant final product has a particle size such that allthe particles will pass through a Tyler No. 8 screen.
As a result of the process of this invention a level of nonionic detergent can be used in excess of that normally used without destroying the crispness and flow properties of the final product. As previously discussed, such is desirable from a performance standpoint. In this preferred aspect of the invention from 5% to 10% of the nonionic is added to the composition by way of the present process. The resultant product is crisp, freeflowing and performs very satisfactorily with respect to cleaning and spotting/filming.
The bleach component previously mentioned that may be a part of the particulate matter is a chlorineyielding bleach. Such bleach is included in the composition at a level sufficient to give the detergent composition an available chlorine content of from 0.5% to 10%, preferably 1% to 5%. As used herein, the term available chlorine indicates the amount of chlorine in the composition which is equivalent to elemental chlorine in terms of oxidizing power. Active chlorine is oftentimes used instead of available chlorine. The same type of chlorine is designated by the two terms, but when expressed quantitatively active chlorine indicates the chlorine actually present. The numerical value for available chlorine content is twice that for active chlorine. Available chlorine contents below 0.5% fail to give proper cleaning performance, while amounts in excess of 10% do not result in any added cleaning ability. Any of many known chlorine bleaches can be used in the present detergent composition. Examples of such bleach compounds are: chlorinated trisodium phosphate; dichlorocyanuric acid; salts of chlorine substituted cyanuric acid; l,3-dichloro-5,5- dimethylhydantoin; N,N-dichlorobenzoylene urea; paratoluene sulfodichloroamide; trichloromelamine; N-chloroammeline; N-chlorosuccinimide; N,N'- dichloroazodicarbonamide; N-chloroacetyl urea; N,N- dichlorobiuret; chlorinated dicyandiamide; sodium hypochlorite; calcium hypochlorite; and lithium hypochlorite. The preferred bleach is an alkalimfita salt of dichlorocyanuricjfii, e.g. potassium or sodium dichlorocyanurate. Depending on the particular bleach utilized, the bleach may be included with the particulate alkaline builder salt prior to the liquid mixture spray-on or may be admixed with the agglomerated granules of alkaline builder salt, nonionic detergent and silicate. That is, a bleach that is susceptible to high levels of water and/or heat must be admixed with the agglomerated granules. Similarly a bleach that is not susceptible to water or heat degradation but is of a particle size smaller than desired in the final product must be included with the particulate alkaline builder salt.
The following examples are illustrative of the invention.
EXAMPLE I A particulate mixture 55 parts by weight of sodium citrate dihydrate and 15 parts by weight of sodium carbonate was charged to a pan agglomerater. The particle size of this mixture was such that all the particles passed through a Tyler No. 8 screen. A liquid mixture of 20.5 parts by weight of liquid sodium silicate having a SiO :Na O ratio of 2.58: 1, 20.5 parts by weight of liquid sodium silicate having a SiO zNa o ratio of 3.2011,
and 9.5 parts by weight of a polyoxyalkylene nonionic detergent (Pluradot PIA-433 nonionic detergent supplied by the Wyandotte Corp.) was prepared. The liquid mixture contained 50% water. The liquid mixture was agitated and heated to a temperature of 140F. As the citrate and carbonate mixture was being agitated, the liquid mixture of sodium silicate and nonionic detergent was sprayed thereon. Agglomeration of the particulate mixture began as the spray droplets contacted it. After completion of the spray-on, the agglomerated particles were dried to a moisture content of 10%. The agglomerates were thereafter ground and classified so that all the agglomerates passed through a Tyler No. 8 screen and more than 10% passed through a Tyler No. 100 screen.
For purposes of comparison, products having the above formulation were prepared by different processes. In one process, the liquid sodium silicate was first sprayed onto the particulate mixture, followed by the spray-on of the nonionic detergent. In another process, the nonionic detergent was first sprayed onto the particulate mixture, followed by the spray-on of the liquid sodium silicate. All the other steps of the processes were the same. The product produced by the process of this invention was crisp and free-flowing. Products produced by the two processes described immediately above were noticeably less crisp and less free-flowing. When each of the above three products were stored in containers, pools of liquid were seen forming in the containers that contained the products produced by the separate spray-on of the liquid silicate and nonionic detergent. No such pools of liquid were noticed in the container containing the product of the process of this invention.
EXAMPLE II An agglomerated automatic dishwasher machine detergent composition having the following formulation was produced by the process of this invention as described in Example I Sodium citrate dihydrate 28% Sodium carbonate 12% Pluradot PIA-433 8% Sodium silicate sio,:Na,o 2.58: l) 17% Sodium silicate sio,=Na,o 3.20) 17% Sodium sulfate l8% The above product was crisp and free-flowing despite containing a high level of nonionic detergent.
When the process of this invention described in Example I is repeated using other nonionic detergents in place of the Pluradot I-lA-433 substantially the same I results are obtained.
The addition of 3.5 parts by weight of potassium dichlorocyanurate to the agglomerates of Example I re- 1 sults in a product that cleans satisfactorily and has ex- 5 cellent spotting and filming characteristics. Similar performance results are obtained when 20 parts by weight of chlorinated trisodium polyphosphate is included with the sodium citrate and carbonate prior to spray-on of the liquid mixture.
What is claimed is:
1. A process for producing a crisp, free-flowing agglomerated granular detergent composition comprising i the steps of: I
a. charging to a mixing zone particulate matter comprising an alkaline builder salt; r b. agitating the particulate matter in the zone; and c. with continuous agitation spraying onto the particulate matter a liquid mixture having a temperature of from F. to 200F. of an alkali metal silicate having a siO zalkali metal oxide ratio of from 3.2:1 to 2.5:1 and a nonionic detergent wherein the ratio of liquid alkali metal silicate to nonionic detergent 1 ranges from 3:1 to 6:1 and wherein the liquid mixj ture is sprayed on at a level of from 25% to 50% based on the total composition to form said agglomerated granules.
2. The process of claim 1 wherein the nonionic detergent is sprayed on at a level sufficient to give the prod- I uct a level of nonionic detergent of from 5% to 10%..
3. The process of claim 1 further comprising the step of adding a chlorine-yielding bleach to the composition in an amount sufficient to give the detergent composition an available chlorine content of from 0.1% to 10%.
4. The process of claim 3 wherein the chlorineyielding bleach is added after the liquid mixture has been sprayed onto the particulate mixture.
5. The process of claim 4 wherein thev chlorineyielding bleach is a water-soluble salt of a dichlorocyanuric acid.
6. The process of claim 1 wherein the alkaline builder salt is an alkali metal salt of citric acid.
7. The process of claim 6 wherein the nonionic detergent is a polyoxyalkylene nonionic detergent.
8. The process of claim 7 wherein the liquid alkali metal silicate contains from 45% to 70% water.
9. The process of claim 8 wherein the liquid mixture is continuously agitated prior to being sprayed onto the particulate matter.
10. The process of claim 9 wherein the liquid mixture is maintained at a temperature of from F. to F.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US3247118 *||Feb 25, 1963||Apr 19, 1966||Lever Brothers Ltd||Method for preparing detergent compositions|
|US3359207 *||Jun 18, 1965||Dec 19, 1967||Wyandotte Chemicals Corp||Chlorine-stable detergent compositions and process for the preparation thereof|
|US3598743 *||Jul 23, 1969||Aug 10, 1971||Procter & Gamble||Preparation of granular detergent compositions for automatic dishwashers|
|US3620979 *||Apr 24, 1968||Nov 16, 1971||Fmc Corp||Process of forming free-flowing, particulate mixtures of phosphates and silicates|
|US3630928 *||Jan 8, 1968||Dec 28, 1971||Fmc Corp||Particles containing mixtures of polyphosphates and silicates|
|US3701736 *||Apr 12, 1971||Oct 31, 1972||Colgate Palmolive Co||Means to inhibit overglaze damage by automatic dishwashing detergents|
|US3708427 *||Dec 8, 1970||Jan 2, 1973||Henkel & Cie Gmbh||Washing and cleansing compositions|
|US3763047 *||May 3, 1971||Oct 2, 1973||Procter & Gamble||Detergent compositions|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US4077897 *||Feb 13, 1976||Mar 7, 1978||The Procter & Gamble Company||Process for preparing detergent compositions|
|US4123375 *||Nov 19, 1976||Oct 31, 1978||Henkel Kommanditgesellschaft Auf Aktien||Dishwasher detergent with clear rinsing effect and method of machine washing dishes|
|US4136045 *||Oct 11, 1977||Jan 23, 1979||The Procter & Gamble Company||Detergent compositions containing ethoxylated nonionic surfactants and silicone containing suds suppressing agents|
|US4169806 *||Aug 9, 1978||Oct 2, 1979||The Procter & Gamble Company||Agglomeration process for making granular detergents|
|US4182683 *||Apr 17, 1978||Jan 8, 1980||Berk Gunter H||Process for the manufacture of a dishwashing detergent|
|US4207197 *||Aug 9, 1978||Jun 10, 1980||The Procter & Gamble Company||Agglomeration process for making granular detergents|
|US4228025 *||Jun 29, 1979||Oct 14, 1980||The Procter & Gamble Company||Agglomeration process for making granular detergents|
|US4237024 *||Jun 16, 1978||Dec 2, 1980||Certified Chemicals, Inc.||Dishwashing composition and method of making the same|
|US4244832 *||Jul 27, 1979||Jan 13, 1981||Basf Wyandotte Corporation||Phosphate-free machine dishwashing detergents useful at low temperatures|
|US4259199 *||Sep 18, 1979||Mar 31, 1981||The Procter & Gamble Company||Alkaline dishwasher detergent|
|US4306987 *||Dec 29, 1980||Dec 22, 1981||Basf Wyandotte Corporation||Low-foaming nonionic surfactant for machine dishwashing detergent|
|US4374058 *||Oct 26, 1981||Feb 15, 1983||The Chemithon Corporation||Method for producing powdered detergent containing alpha olefin sulfonate|
|US4637891 *||Jan 28, 1985||Jan 20, 1987||Lever Brothers Company||Process for the manufacture of detergent compositions containing sodium aluminosilicate|
|US4996001 *||Jan 23, 1989||Feb 26, 1991||Capital City Products Company||Puffed borax as an agglomerating aid|
|US5279756 *||Aug 27, 1992||Jan 18, 1994||Church & Dwight Co., Inc.||Non-phosphate machine dishwashing detergents|
|US5281352 *||Aug 27, 1992||Jan 25, 1994||Church & Dwight Co., Inc.||Low-phosphate machine dishwashing detergents|
|US5458799 *||Aug 3, 1993||Oct 17, 1995||Amway Corporation||Mix process for formulating detergents|
|US5612305 *||Jan 12, 1995||Mar 18, 1997||Huntsman Petrochemical Corporation||Mixed surfactant systems for low foam applications|
|US5614485 *||Jun 7, 1996||Mar 25, 1997||The Procter & Gamble Company||Process for making a granular dishwashing composition by agglomerating ingredients and admixing solid alkali metal silicate|
|US5616277 *||Jun 25, 1996||Apr 1, 1997||The Procter & Gamble Company||Incorporating nonionic surfactant into silicate for granular automatic dishwashing detergent composition|
|US5958865 *||Jun 20, 1997||Sep 28, 1999||Fmc Corporation||Single pass process for making an increased surfactant loaded detergent using an agglomerator|
|US5997764 *||Dec 4, 1997||Dec 7, 1999||The B.F. Goodrich Company||Thickened bleach compositions|
|US6083422 *||Sep 2, 1999||Jul 4, 2000||The B.F. Goodrich Company||Thickened bleach compositions|
|EP0551670A1 *||Nov 27, 1992||Jul 21, 1993||Unilever N.V.||Processes for preparing powdered detergent compositions|
|EP0651050A1 *||Nov 3, 1993||May 3, 1995||THE PROCTER & GAMBLE COMPANY||Surfactant agglomerate particle|
|U.S. Classification||510/229, 510/444, 510/381, 510/506, 510/477|
|International Classification||C11D11/00, C11D1/66, C11D3/08|
|Cooperative Classification||C11D11/0088, C11D3/08, C11D1/66|
|European Classification||C11D11/00D4, C11D1/66, C11D3/08|