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US4057495A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for treating a waste water containing a nonionic surface active agent

Assignee: LION (LION CORPORATION) KK
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Filing: 1976-09-17
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Granted: 1977-11-08
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Expires: 1996-09-17
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Abstract

Abstract A method comprises in combination a step of effecting treatment by a foam separation method and a pressure/heating step for effecting treatment in the presence of an inorganic electrolyte, thereby recovering a nonionic surface active agent from a nonionic surface active agent containing waste water, while at the same time purifying the waste water.

Inventors

  • 👤 Mototaka Kinoshita
  • 👤 Akio Okabe
  • 👤 Susumu Ando

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 22:57
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/24; C02F1/02; C02F1/025

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 254 words
A method for recovering a nonionic surface active agent from a nonionic surface active agent containing waste water to purify the waste water, which consists of separating by a foam separation step a low concentration waste water with less than 500 ppm of a nonionic surface active agent into a concentrated water containing more than 500 ppm of nonionic surface active agent and a treated water containing less than 3 ppm of nonionic surface active agent; adding an inorganic electrolyte selected from the group consisting of Na 2 SO 4 , K 2 SO 4 , Al 2 (SO 4 ) 3 , Fe 2 (SO 4 ) 3 , NaCl, KCl, CaCl 2 , MgCl 2 , FeCl 2 , FeCl 3 and AlCl 3 to the concentrated water to insure a concentration of electrolyte in the concentrated water of more than 50 ppm, heating the resultant concentrated water containing electrolyte to 100° to 200° C under a pressure of 2 to 5 kg/cm 2 to separate it into a high concentration nonionic surface active agent solution and a separated water, and recycling the separated water to the foam separation step, said nonionic surface active agent being selected from the group consisting of polyoxyethylenealkylether represented by a general formula: RO--(CH.sub.2 --CH.sub.2 --O).sub.n H, polyoxyethylenealkylphenylether represented by a general formula: ##STR4## and fatty ester of polyethyleneglycol represented by a general formula: R--COO--(CH.sub.2 --CH.sub.2 --O).sub.n H, where R denotes C 6 to C 24 alkyl radical or alkenyl radical and n denotes 2 to 40.
Claim 2
Independent Claim 254 words
A method for recovering a nonionic surface active agent from a nonionic surface active agent containing waste water to purify the waste water, which consists of separating by a foam separation step a low concentration waste water with less than 500 ppm of a nonionic surface active agent into a concentrated water containing more than 500 ppm of nonionic surface active agent and a treated water containing less than 3 ppm of nonionic surface active agent; adding an inorganic electrolyte selected from the group consisting of Na 2 SO 4 , K 2 SO 4 , Al 2 (SO 4 ) 3 , Fe 2 (SO 4 ) 3 , NaCl, KCl, CaCl 2 , MgCl 2 , FeCl 2 , FeCl 3 and AlCl 3 to the concentrated water to insure a concentration of electrolyte in the concentrated water of more than 50 ppm, heating the resultant concentrated water containing electrolyte to 100° to 200° C under a pressure of 2 to 5 kg/cm 2 to separate it into a high concentration nonionic surface active agent solution and a separated water, and recycling the separated water to the foam separation step, said nonionic surface active agent being selected from the group consisting of polyoxyethylenealkylether represented by a general formula: RO--(CH.sub.2 --CH.sub.2 --O).sub.n H, polyoxyethylenealkylphenylether represented by a general formula: ##STR4## and fatty ester of polyethyleneglycol represented by a general formula: R--COO--(CH.sub.2 --CH.sub.2 --O).sub.n H, where R denotes C 6 to C 24 alkyl radical or alkenyl radical and n denotes 2 to 40.
Claim 3
Dependent Claim 29 words
A method according to claim 1 in which said inorganic electrolyte is selected from the group consisting of Na 2 SO 4 , CaCl 2 and AlCl 3 .
Claim 4
Dependent Claim 23 words
A method according to claim 1 in which the resultant concentrated water containing the inorganic electrolyte is heated at 120° to 150° C.
Claim 5
Dependent Claim 28 words
A method according to claim 1 wherein the separated water is mixed with the low concentration waste water before recycling the separated water to the foam separation step.
Claim 6
Dependent Claim 36 words
A method according to claim 1 in which 50 to 500 ppm of inorganic electrolyte is added to the concentrated water to insure a concentration of electrolyte in the concentrated water of more than 50 ppm.

References Cited (Backward Citations)

US3898159A Cited
DE2361620A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-11-07 1981-05-09 1981-11-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-11-07 1985-05-09 1985-11-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-11-07 1989-05-09 1989-11-08 $7700.00 Window Closed / Lapsed

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