Process for treating waste water containing chlorinated organic compounds from production of epichlorohydrin

• US 5,393,428 A
• Filed: 09/02/1993
• Issued: 02/28/1995
• Est. Priority Date: 09/06/1992
• Status: Expired due to Fees

• Current Assignee: Solvay Deutschland GmbH (Solvac SA)
• Original Assignee: Solvay Deutschland GmbH (Solvac SA)
• Inventors: Ploenissen, Erich, Sell, Michael, Dillenburg, Helmut, Dilla, Wolfgang
• Primary Examiner(s): WYSE, THOMAS G
• Application Number:
  US08/114,635
• Time in Patent Office: 544 Days
• Field of Search: 210/631, 210/757, 210/761-763, 210/766, 210/774, 210/908, 210/909
• US Class Current: 210/631
• CPC Class Codes: C02F 1/025 Thermal hydrolysis
• CPC Class Codes: C02F 1/66 by neutralisation; pH adjustment for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58
• CPC Class Codes: C02F 1/70 by reduction C02F1/4676 takes precedence
• CPC Class Codes: C02F 1/725 by catalytic oxidation
• CPC Class Codes: C02F 2101/36 containing halogen
• CPC Class Codes: C02F 3/02 Aerobic processes
• CPC Class Codes: C02F 3/1231 Treatments of toxic sewage
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage
• CPC Class Codes: C07D 301/32 Separation; Purification
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 210/908 Organic
• CPC Class Codes: Y10S 210/909 Aromatic compound, e.g. pcb, phenol

Abstract

A process for treating waste water containing chlorinated organic substances, particularly waste water from production of epichlorohydrin which contains more than 10 mg of adsorbable organic halogen compounds (AOX) per liter, comprising charging the waste water at a pH of 10 to 14 (measured at room temperature) into a reactor and maintaining a temperature of at least 75°C., a pressure of at least 1 bar (abs.), and a residence time of at least 0.5 hours in said reactor, thereby partially dechlorinating and/or dehydrochlorinating chlorinated organic compounds contained in the waste water, and thereafter subjecting the waste water to further dechlorination and/or dehydrochlorination treatment in the presence of a hydrogen-containing gas, a hydrogen-releasing compound and/or a catalytically active material; and optionally subjecting the waste water to a biological treatment with the use of microorganisms; and apparatus for carrying out the foregoing process.

Claims

1. A process for treating a liquid containing more than 10 mg of adsorbable organic halogen compounds (AOX) per liter comprising the steps of

introducing said liquid at a pH of 10 to 14 (measured at room temperature) into a reactor and in a first treatment step maintaining a temperature of at least 75°

C., a pressure of at least 1 bar (abs.) and a residence time of at least 0.5 hours in said reactor, thereby partially dechlorinating or dehydrochlorinating chlorinated organic compounds contained in the liquid;

subsequently subjecting said liquid in a second treatment step to a further dechlorination or dehydrochlorination treatment in the presence of a hydrogen-containing gas, a compound which releases hydrogen or a catalytically active substance, and

discharging the treated liquid.

2. A process according to claim 1, further comprising subjecting the liquid after said further dechlorination or dehydrochlorination treatment to a biological purification treatment with microorganisms.

3. A process according to claim 1, wherein said liquid is waste water from the production of epichlorohydrin.

4. A process according to claim 1, further comprising adjusting the pH of said fluid to a value of from 10 to 14 prior to said introducing step.

5. A process according to claim 1, wherein said liquid is thermally treated in said first treatment step at a temperature of from 85°

to 185°

C. and a pressure of from 2 to 10.5 bar (abs.), with a residence time of from 1 to 8 hours, and said second treatment step is carried out in the presence of substantially pure hydrogen, a metal, a metal alloy, an inorganic or organic metal compound, or a mixture of at least two of the foregoing substances.

6. A process according to claim 1, wherein said second treatment step is carried out in the presence of a catalytically active palladium-containing compound deposited on a carrier.

7. A process according to claim 6, wherein said carrier is an aluminum-oxide-containing carrier.

8. A process according to claim 1, wherein said liquid is waste water containing at least 0.15 g/liter of dissolved halogen-containing organic compounds.

9. A process according to claim 1, wherein said second treatment step is carried out in a series of at least 3 tubular reactors and wherein said liquid flows through said tubular reactors at a flow velocity of at least 4 meters per second.

10. A process according to claim 9, wherein said second treatment step is carried out in a series of 4 tubular reactors.

11. A process according to claim 9, wherein said liquid flows through said tubular reactors at a flow velocity of at least 8.5 meters per second.

12. A process according claim 1, further comprising the step of at least partially freeing said liquid of suspended solids.

13. A process according to claim 12, wherein said liquid is at least partially freed of suspended solids by chemical treatment.

14. A process according to claim 12, wherein said liquid is at least partially freed of suspended solids by mechanical filtration.