Macroscopic aggregates of microcrystalline zeolites for static water softening applications
AssigneeEngelhard Corporation
InventorsSteven M. Kuznicki, Tadeusz W. Langner, Jacqueline S. Curran, Valerie A. Bell
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AssigneeEngelhard Corporation
InventorsSteven M. Kuznicki, Tadeusz W. Langner, Jacqueline S. Curran, Valerie A. Bell
Estimating the term…
Novel morphologies are provided for aluminosilicate zeolite ion-exchange materials useful for static water softening. The zeolites are provided in the form of large aggregates composed of submicron zeolite crystals. Rapid exchange rates, high hardness ion capacity and increased attrition resistance characterize the zeolite ion exchangers.
An aluminosilicate zeolite composition comprising macroscopic aggregates having an average size of greater than 5 microns consisting essentially of a plurality of smaller crystals of said zeolite, said zeolite containing positive amounts up to 40% by weight relative to the total SiO2 content of the zeolite as occluded silicate which is not part of the framework of said zeolite crystals.
An aluminosilicate zeolite composition comprising in-situ formed macroscopic aggregates of a plurality of submicron zeolite crystals, said aggregates having an average size of greater than 5 microns, said zeolite containing positive amounts up to 40% by weight relative to the total SiO2 content of the zeolite as occluded silicate which is not part of the framework of said zeolite crystals.
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Treatment of water, waste water, or sewage: by ion-exchange
Use of material as cation exchangers; Treatment of material for improving the cation exchange properties: base exchange silicates, e.g. zeolites
Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange…
Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange…
Term ended 3 Nov 2021 (estimated)
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The present invention is directed to novel aluminosilicate zeolite structures useful as water softening materials. The unique zeolite materials of this invention can be used to form both regenerable as well as disposable static water softening devices.
Water softening is a process of water treatment by which undesirable cations, in particular, calcium and magnesium, are removed. Water, which contains such cations, is considered hard, wherein hardness is usually expressed as calcium carbonate equivalents in parts per million. The presence of these cations in water is undesirable for household purposes, such as for bathing, cleaning, and laundry, as well as for industrial purposes, such as boiler feed, food processing and chemical processing, because of reactions which form soap scum, boiler scale, and unwanted byproducts. Hard waters have been softened by precipitation processes which involved the use of hydrated lime or cation-exchange processes which involved the use of sodium-cation exchangers such as aluminosilicate zeolites or hydrogen cation-exchangers such as in the form of resins in bead form.
Water softening with ion exchange material such as resin particles or the like is well-known in the art. During the softening process, or service cycle, the ion exchange resin particles acquire hardness inducing ions (Ca2+, Mg2+) from the water in exchange for soft ions, (H+, Na+, K+) which do not induce hardness. After prolonged contact of the resin particles with raw water, the ion exchange capacity of the resin is diminished considerably and periodic regeneration of the resin particles must be accomplished, conventionally by contacting the resin particles with a brine solution, i.e., an aqueous solution of sodium chloride or potassium chloride or the like.
Microspheres of microcrystalline Zeolite A were prepared by combining 125 grams of Luminex®-derived 40 micron microsphere metakaolin with a solution containing 22 grams N-Brand sodium silicate and 390 grams 50% NaOH solution in 422 grams of water. This mixture was heated to 65° C., with stirring, and reacted for 3 hours. The resultant product was hot washed to remove residual traces of entrained silica. Particle size distribution indicated retention of approximately 40 micron average size. SEM indicated individual crystal size well below 0.5 micron, much smaller than typical commercial Zeolite A.
A test was conducted to assess the relative performance of the microspheres for multivalent cation sequestration versus a commercial organic ion-exchange resin employed in contact water softening by Brita. The test was carried out in the following manner:
1) Calcium/Magnesium solution was made following Brita's procedure for test water preparation (Temporary Hardness Reduction Protocol).