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US3962077A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the purification of waste waters

Assignee: Tecneco SpA
•
Filing: 1974-06-14
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Granted: 1976-06-08
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Expires: 1994-06-14
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Abstract

Abstract The present invention concerns a method for purifying waste waters which come from the regeneration of the anionic and cationic resins used in the treatment of sugar juices. The method includes subjecting the waste waters to one or more zones which include an inverse osmosis section and one or more electrolysis cells.

Inventors

  • 👤 Giorgio Pascarella
  • 👤 Francesco Salvemini

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 13:15
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/46; C02F1/461; B; B01; B01D; B01D61/00; B01D61/02; B01D61/025; B01D61/026; B01D2311/00; B01D2311/06

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 259 words
A process for the purification of waste waters containing organic and inorganic products which may or may not be ionizable, said waste waters characterized as coming from the regeneration of the anionic and cationic demineralizing resins, the decoloring resins, and the decalcifying resins used for the treatment of the sugar juices in the sugar industry, said process comprising the following steps: A. feeding said waste waters coming from the regeneration of the decoloring resins to an inverse osmosis section consisting of two stages; B. feeding waste waters which come from the regeneration of the anionic demineralizing resins to an anodic compartment of one or more electrolytic cells each having two compartments and subjecting said water therein to electrolysis; C. feeding waters which come from the regeneration of the cationic demineralizing resins to a cathodic compartment of one or more electrolytic cells each having two compartments and subjecting said water therein to electrolysis; D. feeding waters coming from the regeneration of decalcifying resins to a precipitation treatment with sodium hydroxide, and carbon dioxide, subsequently neutralizing said waters and subjecting them to a final inverse osmosis treatment; E. mixing and neutralizing the treated waters rich in organic materials from steps B and C hereinabove, where they are not completely demineralized, and then subjecting the waters to an inverse osmosis treatment and thereafter mixing them with treated solution rich in organic substances from step A; and F. feeding treated waters from step E containing organic compounds (organic waters), after having been mixed together, to an evaporator for recovering the dry organic substance.
Claim 2
Dependent Claim 259 words
A process for the purification of waste waters containing organic and inorganic products which may or may not be ionizable, said waste waters characterized as coming from the regeneration of the anionic and cationic demineralizing resins, the decoloring resins, and the decalcifying resins used for the treatment of the sugar juices in the sugar industry, said process comprising the following steps: A. feeding said waste waters coming from the regeneration of the decoloring resins to an inverse osmosis section consisting of two stages; B. feeding waste waters which come from the regeneration of the anionic demineralizing resins to an anodic compartment of one or more electrolytic cells each having two compartments and subjecting said water therein to electrolysis; C. feeding waters which come from the regeneration of the cationic demineralizing resins to a cathodic compartment of one or more electrolytic cells each having two compartments and subjecting said water therein to electrolysis; D. feeding waters coming from the regeneration of decalcifying resins to a precipitation treatment with sodium hydroxide, and carbon dioxide, subsequently neutralizing said waters and subjecting them to a final inverse osmosis treatment; E. mixing and neutralizing the treated waters rich in organic materials from steps B and C hereinabove, where they are not completely demineralized, and then subjecting the waters to an inverse osmosis treatment and thereafter mixing them with treated solution rich in organic substances from step A; and F. feeding treated waters from step E containing organic compounds (organic waters), after having been mixed together, to an evaporator for recovering the dry organic substance.
Claim 3
Dependent Claim 24 words
The process of claim 1 wherein the waters coming from the regeneration of the decoloring resins are rich in sodium chloride and organic substances.
Claim 4
Dependent Claim 57 words
The process of claim 1, step A, wherein the first stage of the inverse osmosis section yields (i) a solution concentrated in organic substances having a low sodium chloride content and (ii) a diluted sodium chloride solution free from organic substances; and the second stage yields practically deionized water by concentration of the sodium chloride solution (ii).
Claim 5
Dependent Claim 41 words
A process for the purification of waste waters from the regeneration of the decoloring resins according to claim 3 characterized in that the organic effluent stream (ii) containing sodium chloride is fed to a roasting furnace for recovering the sodium chloride.
Claim 6
Dependent Claim 23 words
The process of claim 1 wherein the waters coming from the regeneration of the anionic demineralizing resins contain ammonium hydroxide and organic substances.

References Cited (Backward Citations)

US3268441A Cited
US3781174A Cited
US3639231A Cited
US3791866A Cited
US3823086A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-06-08 1979-12-08 1980-06-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-06-08 1983-12-08 1984-06-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-06-08 1987-12-08 1988-06-08 $7700.00 Window Closed / Lapsed

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