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US4260651A Expired / Lapsed US ⏱️ 0.0 years remaining

Phosphate-free concentrated particulate heavy duty laundry detergent

Assignee: Colgate Palmolive Co
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Filing: 1976-12-02
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Granted: 1981-04-07
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Expires: 1996-12-02
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Abstract

Abstract A free flowing phosphate-free particulate heavy duty laundry detergent is comprised of particles of a mixture of sodium carbonate and sodium bicarbonate having nonionic detergent in the interior and on the surface thereof, to which is adhered a coating of smaller particles of ion exchanging zeolite. The product made is exceptionally free flowing and, although the particles are relatively large, is also of high bulk density (over 0.6 g./cc.). Also within the invention is a method of making such products by contacting the particles of mixed sodium carbonate and sodium bicarbonate with a normally liquid or pasty nonionic detergent in the liquid state so that the detergent is largely absorbed by the particles and coats the surfaces thereof, which are then coated with powdered zeolite which adheres to the surface nonionic of the particles and makes them free flowing.

Inventors

  • 👤 Harold E. Wixon

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 11:18
CPC Classifications
C; C11; C11D; C11D17/00; C11D17/0039; C11D1/00; C11D1/66; C11D1/72; C11D17/06; C11D17/065; C11D3/00; C11D3/02; C11D3/04; C11D3/10; C11D3/12; C11D3/124; C11D3/1246; C11D3/128

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 307 words
A method of making a free-flowing particulate heavy duty laundry detergent having a bulk density of at least about 0.6 gm/c.c. comprising mixing together from about 20 to 40% of a mixture of sodium carbonate and sodium bicarbonate particles in a weight ratio in the range of from about 1:10 to 10:1, with from about 10 to 30% by weight of a nonionic detergent so that said nonionic detergent is absorbed by and coats the particles, and admixing with said nonionic detergent coated particles from about 40 to 60% by weight of zeolite particles such that said zeolite particles adhere to the detergent on the surfaces of the particles to provide a first formed particle; and applying a second coating of nonionic detergent to said first formed particle and then applying to said second nonionic detergent coating a coating of zeolite particles to render said particle free flowing; wherein the ratio of said second nonionic deterent coating to zeolite particles post-applied to said first formed particle is in the range of from about 1:6 to about 3:4, said zeolite being a crystalline zeolite, amorphous zeolite or a mixture of crystalline and amorphous zeolites wherein the exchange rate and capacity of said zeolite is such that when about 375 ppm of said zeolite on an anhydrous basis is placed in water at 45° C. containing about 40 ppm of dissolved calcium ion while vigorously stirring the dissolved calcium ion content of the water is reduced to below about 8 ppm in about 5 minutes, said zeolite particles having ultimate particle diameters in the range of from about 0.01 to 20 microns; said nonionic detergent being a fatty-alcohol polyethylene oxide condensate which is a 10 to 18 carbon atom higher fatty alcohol alkoxylated with about 3 to 15 moles of ethylene oxide per mole of the higher fatty alcohol.
Claim 2
Independent Claim 307 words
A method of making a free-flowing particulate heavy duty laundry detergent having a bulk density of at least about 0.6 gm/c.c. comprising mixing together from about 20 to 40% of a mixture of sodium carbonate and sodium bicarbonate particles in a weight ratio in the range of from about 1:10 to 10:1, with from about 10 to 30% by weight of a nonionic detergent so that said nonionic detergent is absorbed by and coats the particles, and admixing with said nonionic detergent coated particles from about 40 to 60% by weight of zeolite particles such that said zeolite particles adhere to the detergent on the surfaces of the particles to provide a first formed particle; and applying a second coating of nonionic detergent to said first formed particle and then applying to said second nonionic detergent coating a coating of zeolite particles to render said particle free flowing; wherein the ratio of said second nonionic deterent coating to zeolite particles post-applied to said first formed particle is in the range of from about 1:6 to about 3:4, said zeolite being a crystalline zeolite, amorphous zeolite or a mixture of crystalline and amorphous zeolites wherein the exchange rate and capacity of said zeolite is such that when about 375 ppm of said zeolite on an anhydrous basis is placed in water at 45° C. containing about 40 ppm of dissolved calcium ion while vigorously stirring the dissolved calcium ion content of the water is reduced to below about 8 ppm in about 5 minutes, said zeolite particles having ultimate particle diameters in the range of from about 0.01 to 20 microns; said nonionic detergent being a fatty-alcohol polyethylene oxide condensate which is a 10 to 18 carbon atom higher fatty alcohol alkoxylated with about 3 to 15 moles of ethylene oxide per mole of the higher fatty alcohol.
Claim 3
Dependent Claim 25 words
The method according to claim 1 wherein said zeolite is a crystalline zeolite selected from the group consisting of zeolite types 4A, X, and Y.
Claim 4
Dependent Claim 18 words
The method according to claim 1 wherein the ratio of sodium bicarbonate to sodium carbonate is about 1:2.
Claim 5
Dependent Claim 19 words
The method according to claim 1 wherein said first formed particle is sequentially coated from 2 to 5 times.
Claim 6
Dependent Claim 56 words
The method according to claim 1 wherein the rate and capacity of said zeolite are such that when 375 ppm of said zeolite is placed in water at 45° C. containing 40 ppm of dissolved calcium ion while vigorously stirring, the dissolved calcium ion content is reduced to below about 3 ppm within about 5 minutes.
Claim 7
Independent Claim 47 words
The method according to claims 1 or 2 wherein the amount of zeolite and nonionic detergent post-applied to said first formed particle is about 5 parts by weight nonionic detergent and 10 parts by weight zeolite based on 100 parts by weight of said first formed particle.
Claim 8
Dependent Claim 61 words
The method according to claim 1 wherein said zeolite is a type 4A zeolite, said nonionic detergent is a fatty alcohol-polyethylene oxide condensate wherein the fatty alcohol is a C 12 to C 15 fatty alcohol with an average of 7 moles of ethylene oxide per mole of fatty alcohol; and the ratio of sodium carbonate to sodium bicarbonate is 1:2.
Claim 9
Independent Claim 59 words
The method according to claims 1 or 2 wherein the amount of nonionic detergent coated onto said first formed particle is about one-half of the amount of nonionic detergent in said first formed particle, and wherein the amount of zeolite applied to said second nonionic detergent coating is about one-half the amount of zeolite in said first formed particle.
Claim 10
Independent Claim 60 words
The method according to claims 1 or 2 wherein the amount of nonionic detergent coated onto said first formed particle is about equivalent to the amount of nonionic detergent in said first formed particle, and wherein the amount of zeolite applied to said second nonionic detergent coating is about equivalent to the amount of zeolite in said first formed particle.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-04-06 1984-10-06 1985-04-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-04-06 1988-10-06 1989-04-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-04-06 1992-10-06 1993-04-07 $7700.00 Window Closed / Lapsed

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