Spray-dried detergent compositions

Claim 2

A granular detergent composition comprising: (a) from about 5% to about 40% of a water-soluble organic surface active agent selected from the group consisting of linear alkyl benzene sulfonate, alkyl sulfate, alkyl ethoxy ether sulfate, and mixtures thereof, said alkyl groups containing from about 10 to about 20 carbon atoms and said alkyl ethoxy ether sulfate having an average degree of ethoxylation of from about 1 to about 4 moles of ethylene oxide per mole of alkyl sulfate; (b) from about 10% to about 60% of a finely divided water-insoluble aluminosilicate ion exchange material selected from the group consisting of: (1) crystalline aluminosilicate material of the formula Na.sub.z [(AlO.sub.2).sub.z.(SiO.sub.2).sub.y ].xH.sub.2 O wherein z and y are at least 6, the molar ratio of z to y is from 1.0 to 0.5 and x is from 10 to 264, said material having a particle size diameter of from about 0.1 micron to about 10 microns, a calcium ion exchange capacity of at least about 200 mg. CaCO 3 eq./g. and a calcium ion exchange rate of at least about 2 grains Ca ++ /gallon/minute/gram; (2) amorphous hydrated aluminosilicate material of the empirical formula M z (zAlO 2 .ySiO 2 ) wherein M is sodium, potassium, ammonium, or substituted ammonium, z is from about 0.5 to about 2, y is 1, said material having a particle size diameter of less than about 100 microns, a magnesium ion exchange capacity of at least about 50 milligrams equivalent of CaCO 3 hardness per gram of anhydrous aluminosilicate and a Mg ++ exchange rate of at least about 1 grain/gallon/minute/gram/gallon and (3) mixtures thereof; (c) from about 5% to about 30% of an alkali metal oxide silicate solid having a weight ratio of SiO 2 :alkali metal oxide of about 1.6, and (d) from about 0.5 to about 20% of a water-soluble salt of acetic acid, said granular detergent having been prepared by mixing the above components with water to form a slurry, and then removing water from the slurry by drying.

Claim 3

The composition of claim 1 wherein the aluminosilicate ion exchange material has the formula Na 12 [(AlO 2 ) 12 (SiO 2 ) 12 ].xH 2 O wherein x is from about 20 to about 30.

Claim 4

The composition of claim 1 which additionally comprises from about 5% to about 30% of sodium carbonate.

Claim 5

The composition of claim 1 which additionally comprises from about 5% to about 15% of a polyphosphate salt selected from the group consisting of sodium pyrophosphate, sodium tripolyphosphate and mixtures thereof.

Claim 6

The composition of claim 3 which additionally comprises 0.1% to about 5% of an anti-caking agent selected from the group consisting of a polyethylene glycol with a molecular weight of at least about 2000, an alkali metal toluene sulfonate, and an alkali metal sulfosuccinate.

Claim 7

A process for producing crisp, free-flowing detergent granules comprising the steps of: (1) forming an aqueous slurry comprising: (a) from about 3.5% to about 30% of a water-soluble organic surface active agent selected from the group consisting of linear alkyl benzene sulfonate, alkyl sulfate, alkyl ethoxy ether sulfate, and mixtures thereof, said alkyl groups containing from about 10 to about 20 carbon atoms and said alkyl ethoxy ether sulfate having an average degree of ethoxylation of from about 1 to about 4 moles of ethylene oxide per mole of alkyl sulfate; (b) from about 7% to about 45% of a finely divided water-insoluble aluminosilicate ion exchange material selected from the group consisting of: (1) crystalline aluminosilicate material of the formula: Na.sub.z [(AlO.sub.2).sub.z.(SiO.sub.2).sub.y ].xH.sub.2 O wherein z and y are at least 6, the molar ratio of z to y is from 1.0 to 0.5 and x is from 10 to 264, said material having a particle size diameter of from about 0.1 micron to about 10 microns, a calcium ion exchange capacity of at least about 200 mg. CaCO 3 eq./g. and a calcium ion exchange rate of at least about 2 grains Ca ++ /gallon/minute/gram; and (2) amorphous hydrated aluminosilicate material of the empirical formula M z (zAlO 2 .ySiO 2 ) wherein M is sodium, potassium, ammonium, or substituted ammonium, z is from about 0.5 to about 2, y is 1 and said material having a particle size diameter of less than about 100 microns, a magnesium ion exchange capacity of at least about 50 milligrams equivalent of CaCO 3 hardness per gram of anhydrous aluminosilicate and a Mg ++ exchange rate of at least about 1 grain/gallon/minute/gram/gallon and (3) mixtures thereof; (c) from about 3.5% to about 20% of an alkali metal oxide silicate solid having a weight ratio of SiO 2 :alkali metal oxide of about 1.6; (d) from about 0.4% to about 15% of a water-soluble salt of acetic acid; and (e) from about 25% to about 50% water; (2) drying the slurry to form crisp, free-flowing detergent granules.

Claim 8

A process for producing crisp, free-flowing detergent granules comprising the steps of: (1) forming an aqueous slurry comprising: (a) from about 3.5% to about 30% of a water-soluble organic surface active agent selected from the group consisting of linear alkyl benzene sulfonate, alkyl sulfate, alkyl ethoxy ether sulfate, and mixtures thereof, said alkyl groups containing from about 10 to about 20 carbon atoms and said alkyl ethoxy ether sulfate having an average degree of ethoxylation of from about 1 to about 4 moles of ethylene oxide per mole of alkyl sulfate; (b) from about 7% to about 45% of a finely divided water-insoluble aluminosilicate ion exchange material selected from the group consisting of: (1) crystalline aluminosilicate material of the formula: Na.sub.z [(AlO.sub.2).sub.z.(SiO.sub.2).sub.y ].xH.sub.2 O wherein z and y are at least 6, the molar ratio of z to y is from 1.0 to 0.5 and x is from 10 to 264, said material having a particle size diameter of from about 0.1 micron to about 10 microns, a calcium ion exchange capacity of at least about 200 mg. CaCO 3 eq./g. and a calcium ion exchange rate of at least about 2 grains Ca ++ /gallon/minute/gram; and (2) amorphous hydrated aluminosilicate material of the empirical formula M z (zAlO 2 .ySiO 2 ) wherein M is sodium, potassium, ammonium, or substituted ammonium, z is from about 0.5 to about 2, y is 1 and said material having a particle size diameter of less than about 100 microns, a magnesium ion exchange capacity of at least about 50 milligrams equivalent of CaCO 3 hardness per gram of anhydrous aluminosilicate and a Mg ++ exchange rate of at least about 1 grain/gallon/minute/gram/gallon and (3) mixtures thereof; (c) from about 3.5% to about 20% of an alkali metal oxide silicate solid having a weight ratio of SiO 2 :alkali metal oxide of about 1.6; (d) from about 0.4% to about 15% of a water-soluble salt of acetic acid; and (e) from about 25% to about 50% water; (2) drying the slurry to form crisp, free-flowing detergent granules.

Claim 9

The process of claim 6 wherein the slurry is dried by spray-drying.

Claim 10

The process of claim 7 wherein the aluminosilicate ion exchange material has the formula Na 12 [(AlO 2 ) 12 (SiO 2 ) 12 ].xH 2 O wherein x is from about 20 to about 30.

Claim 11

The process of claim 7 wherein the aqueous slurry additionally comprises from about 3.5% to about 20% of sodium carbonate.