Effluent treatment

• US 3,966,601 A
• Filed: 10/11/1973
• Issued: 06/29/1976
• Est. Priority Date: 11/01/1972
• Status: Expired due to Term

• Current Assignee: Robinson Brothers Limited
• Original Assignee: Robinson Brothers Limited
• Inventors: Stevenson, Arthur, Harkness, Neil
• Primary Examiner(s): Wyse, Thomas G.
• Application Number:
  US05/405,476
• Time in Patent Office: 992 Days
• Field of Search: 210/54, 210/55, 210/53, 210/52, 210/51, 210/42, 260/513.5, 423/366
• US Class Current: 210/710
• CPC Class Codes: C02F 1/5236 using inorganic agents

Abstract

A purification process for industrial effluent containing dissolved dithiocarbamate is described. Before discharging the effluent, it is mixed at pH 6 to 8 with a soluble heavy metal salt and heavy metal dithiocarbamate thereby precipitated and the precipitate is separated from the effluent. By the process poisoning of fish in water courses into which the effluents are discharged can be avoided as can malfunctioning of sewage treatment processes handling the effluents.

Claims

1. A process for purifying industrial effluent from a plant where dithiocarbamates are made or used and which contains at least 200 p.p.m. dissolved dithiocarbamate consisting essentially of, before discharging the effluent, adjusting the pH, if necessary to a pH of 6 to 8, mixing the effluent at a pH of 6 to 8 with an excess of up to 200% of the stoichiometric amount of at least one soluble heavy metal salt selected from the group consisting of iron and copper and thereby precipitating heavy metal dithiocarbamate, separating the precipitated heavy metal dithiocarbamate from the effluent, discharging the effluent and the said of said precipitate by dumping or incineration.

2. A process according to claim 1 in which the precipitation is effected by use of an iron salt followed by use of a copper salt.

3. A process according to claim 1 in which the precipitation is effected by use of an iron salt and a copper salt simultaneously.

4. A process according to claim 1 carried out continuously.

5. A process according to claim 4 in which the pH of the effluent to be treated is continuously or periodically measured and soluble base or acid added, if necessary, so as to maintain the pH within the specified range.

6. A process according to claim 4 in which the dissolved dithiocarbamate content of the effluent to be treated is continuously or periodically measured and the proportion of the soluble heavy metal salt used changed, if necessary, so as to be substantially constant in relation to the dissolved dithiocarbamate content.

7. A process according to claim 4 in which the dissolved dithiocarbamate content of the treated effluent is continuously or periodically measured and the proportion of soluble heavy metal salt used changed, if necessary, so as to yield treated effluent of substantially constant dissolved dithiocarbamate content.

8. A process according to claim 1 in which the effluent to which the soluble heavy metal salt is added has a pH of from 6.7 to 7.3.

9. A process according to claim 1 in which the heavy metal salt and the amount thereof is such that the effluent being discharged contains less than 12 p.p.m. dithiocarbamate.

10. A process according to claim 1 in which a copper salt is used as heavy metal salt at least at the final stage of precipitation.

11. A process according to claim 10 in which the amount of heavy metal salt is such that the effluent being discharged contains less than 2 p.p.m. dithiocarbamate.

12. A process according to claim 1 in which a small amount of high molecular weight polyelectrolyte flocculating agent is mixed into the effluent after the addition of the heavy metal salt and before the separation of the precipitate.

13. A process according to claim 12 in which the amount of the flocculating agent added was from 1 to 2 p.p.m. based on the effluent treated.

14. A process for purifying industrial effluent from a plant where dithiocarbamate is made or used and which contains at least 200 p.p.m. dissolved dithiocarbamate consisting essentially of, before discharging the effluent, adjusting the pH if necessary to a pH of 6 to 8, mixing the effluent at a pH of 6 to 8 with an excess of up to 200% of the stoichiometric amount of soluble iron and copper salts, either simultaneously or first with the iron salt and then with the copper salt, thereafter adding an aqueous solution of a high molecular weight polyacrylamide flocculating agent, and thereby precipitating iron and copper dithiocarbamates, separating the precipitated dithiocarbamates froms the effluent, discharging the effluent having a dithiocarbamate content of not more than 2 p.p.m., and incinerating the separated copper and iron dithiocarbamates.

15. A process according to claim 14 in which the amount of the flocculating agent added was from 1 to 2 p.p.m. based on the effluent treated.