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US4218315A Expired / Lapsed US ⏱️ 0.0 years remaining

Oxidation and adsorption method for removing contaminating substances from liquids

Assignee: Individual
•
Filing: 1978-09-11
•
Granted: 1980-08-19
•
Expires: 1998-09-11
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Abstract

Abstract The specification describes an oxidation and adsorption method for removing contaminating materials (pollutants) from aqueous liquids. The liquids are first subjected to an electrochemical treatment for the purpose of coagulation or agglomeration and partial oxidation by addition of NaOCl. Following this, using sedimentation and/or flotation, the agglomerated and coalesced sludge is removed from the liquid. In the liquid an excess of OCl - remains and this liquid, enriched in this manner, is supplied to adsorption columns, in which inorganic adsorption compositions are located having a high specific surface area so that a further oxidation is achieved by the excess OCl - , together with a partial adsorption and by addition of O 3 , complete oxidation is achieved. The organic contaminating materials are converted into CO 2 products of adsorbing materials of different grain sizes and specific surface areas made of inorganic materials, following which the CO 2 escapes from the liquid and is stored. The thus cleaned liquid then leaves the oxidation and adsorbing columns.

Inventors

  • 👤 Karl H. Hartkorn

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 21:47
CPC Classifications
B; B01; B01D; B01D15/00; C; C02; C02F; C02F9/00; C02F1/00; C02F1/28; C02F1/281; C02F1/283; C02F1/46; C02F1/461; C02F1/463; C02F1/467; C02F1/4672; C02F1/4674; C02F1/72; C02F1/76; C02F1/78

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 224 words
A process for removing contaminating materials from a polluted aqueous liquid, said contaminating materials including solid contaminants, ranging in size from suspended solids in the macrorange through colloids and dissolved organic contaminants, which comprises the steps of: (a) adding a predetermined amount of NaOCl solution to said liquid, forming a mixture; (b) electrolyzing said mixture to coagulate at least some of said contaminants into a sludge and to form OCl - ions capable of oxidizing said contaminants; (c) separating the sludge from said mixture, said remaining mixture containing dissolved organic contaminants and residual OCl - ions, said predetermined amount of NaOCl solution being at least adequate to yield said residual OCl - ions; (d) adding ozone to said remaining mixture to oxidize said dissolved organic contaminants to form CO 2 and an oxidation residue; (e) contacting said remaining mixture with particles of an inorganic solid adsorbent by percolating said remaining mixture through a column containing a bed of said adsorbent so as to oxidize said contaminants with said residual OCl - ions and said ozone; (f) adsorbing the oxidation residue from said remaining mixture on said inorganic solid adsorbent while venting and collecting the CO 2 ; (g) regenerating said inorganic adsorbent by flushing with the collected CO 2 ; and (h) collecting the decontaminated aqueous liquid after percolation through said inorganic adsorbent bed.
Claim 2
Dependent Claim 224 words
A process for removing contaminating materials from a polluted aqueous liquid, said contaminating materials including solid contaminants, ranging in size from suspended solids in the macrorange through colloids and dissolved organic contaminants, which comprises the steps of: (a) adding a predetermined amount of NaOCl solution to said liquid, forming a mixture; (b) electrolyzing said mixture to coagulate at least some of said contaminants into a sludge and to form OCl - ions capable of oxidizing said contaminants; (c) separating the sludge from said mixture, said remaining mixture containing dissolved organic contaminants and residual OCl - ions, said predetermined amount of NaOCl solution being at least adequate to yield said residual OCl - ions; (d) adding ozone to said remaining mixture to oxidize said dissolved organic contaminants to form CO 2 and an oxidation residue; (e) contacting said remaining mixture with particles of an inorganic solid adsorbent by percolating said remaining mixture through a column containing a bed of said adsorbent so as to oxidize said contaminants with said residual OCl - ions and said ozone; (f) adsorbing the oxidation residue from said remaining mixture on said inorganic solid adsorbent while venting and collecting the CO 2 ; (g) regenerating said inorganic adsorbent by flushing with the collected CO 2 ; and (h) collecting the decontaminated aqueous liquid after percolation through said inorganic adsorbent bed.
Claim 3
Dependent Claim 45 words
The process according to claim 1, wherein the adsorbents are porous adsorbents selected from the group consisting of pressed glauconite, pressed fire clay, silicates, and montmorillonite, and are in substantially spherically form, and have an adsorption surface in excess of 300 meters 2 per gram.
Claim 4
Dependent Claim 11 words
The process according to claim 1, wherein the adsorbents are acid-activated.
Claim 5
Dependent Claim 25 words
The process according to claim 1, wherein the adsorbents, upon loss of adsorption ability after initial regeneration, are thermally regenerated at temperatures above 240° C.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-08-19 1984-02-18 1984-08-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-08-19 1988-02-18 1988-08-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-08-19 1992-02-18 1992-08-19 $7700.00 Window Closed / Lapsed

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