Settling clay-containing slimes
AssigneeInternational Minerals & Chemical Corp.
InventorsOthmer F. Batzer, John A. Stewart
Life of this patent
Estimating the term…
Loading patent…
AssigneeInternational Minerals & Chemical Corp.
InventorsOthmer F. Batzer, John A. Stewart
Estimating the term…
The settling of finely-divided solids that are in suspension in an aqueous medium due to the presence of a colloidal argillaceous mineral is enhanced by adding a small but effective amount of hydrogen peroxide to the suspension. This invention is especially useful for treating aqueous suspensions of ultrafine clay and other materials resulting from the hydraulic concentration of an ore material, such as phosphate slimes.
A process for settling waste slime solids, from a phosphate are processing operation, including suspended attapulgite, montmorillonite, and fine sand from an aqueous suspension thereof, wherein said suspension contains from about 0.01% to about 35% by weight of solids, which comprises the steps of adding hydrogen peroxide to said suspension in an amount to enhance the settling of said solids, said amount being at least about 2 pounds per ton of suspended solids, and settling said solids from said suspension.
Dependencies are inferred from the claim text.
Drawings are temporarily unavailable. Open the PDF at USPTO
Treatment of water, waste water, or sewage: by flocculation or precipitation of suspended impurities
Separation of suspended solid particles from liquids by sedimentation: using flocculating agents
By oxidation: oxidation by peroxides
Phosphorus containing: phosphate slimes
Term ended 27 Sep 1994 (estimated)
USPTO file history isn’t available for this patent, so only indexed dates are shown.
This invention relates to a process for separating finely-divided solids that are suspended in an aqueous medium and, more particularly, to a process for treating a colloidal suspension of clay, alone or in combination with other solid materials, to enhance the settling of the solids.
Clays having a micaceous or platey structure such as bentonite (a montmorillonite clay) acquire the properties of self-suspension, swelling and gelatinizing when they are mixed with water. The clays are advantageously used for these unique properties in many industries. An example of such a beneficial use is in the well drilling industry where bentonite is a component of drilling fluids to suspend the cuttings and carry them out of the well bore.
These same properties of some clays present considerable problems in other industries when it is desired to remove the clays and other materials from suspension in an aqueous medium. For example, many foundries use a sand washing operation that produces as an undesirable by-product a wash water containing on the order of about 0.2 to about 1.2% by weight of suspended bentonite, carbonaceous material and fine sand. The disposal of this waste product has become a problem in view of recent stringent pollution regulations. The use of standard filtering methods and apparatus for separating the finely-divided material from the waste water before discharging or recycling the water is not entirely satisfactory since the fine suspended particles rapidly blind the filter media.
The following non-limiting examples are illustrative of the present invention.
This example illustrates the effect of the process of this invention for flocculating and settling finely-divided material from an aqueous suspension as hereinabove described. The suspension which was utilized in this experiment was a sample of phosphate slimes containing about 4% by weight of suspended solids. Samples of 100 milliliters each of the slime were added to 5 granduated cylinders. A 30% solution of hydrogen peroxide was added to four of the samples in the amounts of 0.025, 0.05, 0.1, and 0.2 milliliter, respectively. No hydrogen peroxide was added to the fifth sample since it was used as a control. The graduated cylinders were each inverted several times to allow thorough mixing and the volume of clear water at the upper portion of each sample was observed and recorded over a 24-hour period. The results of this experiment are given in Table 1.
Table 1 ______________________________________ TIME 0 0.025 0.05 0.1 0.2 (hours) (mls.) (mls.) (mls.) (mls.) (mls.) ______________________________________ 1.0 6 4 4 20 21 1.5 8 4 26 26 28 2.0 10 10 30 30 31 2.5 11 24 30 31 31 3.0 12 24 30 34 34 4.0 14 24 30 34 36 5.0 16 24 30 36 42 6.0 18 26 30 36 42 7.0 20 28 30 38 42 24.0 25 32 40 43 45 ______________________________________