Removal of dissolved hydrogen sulfide and a reduction in BOD is achieved by the addition of nitrate ions to waste systems in an amount sufficient to stimulate growth of bacteria which utilize dissolved hydrogen sulfide in their metabolism. Specifically, about 2.4 lbs. nitrate oxygen per lb. of sulfide is required.
|
28. The process according to 23 wherein, during the process, additional minor odors associated with other sulphur-containing compounds are also
eliminated.29. A process for removing existing dissolved hydrogen sulfide from waste systems wherein removal is achieved by a mechanism consisting essentially of: (a) adding nitrate ions to the waste in accordance with a ratio of 2.4 parts nitrate oxygen for each 1 part existing dissolved hydrogen sulfide in order to provide a source of oxygen for naturally occurring bacteria present in the waste which utilize dissolved hydrogen sulfide in their metabolism; (b) providing sufficient time to culture said bacteria within said waste systems; and (c) providing ongoing time sufficient to enable said bacteria to remove substantially all said existing dissolved hydrogen sulfide. 30. A process for removing from waste systems existing dissolved hydrogen sulfide and other minor odors associated with other sulphur-containing compounds wherein removal is achieved by a mechanism consisting essentially of: providing a source of oxygen in the form of nitrate in the waste in accordance with a ratio of substantially 2.4 parts nitrate oxygen for each 1 part existing dissolved hydrogen sulfide to cause naturally occurring bacteria in the waste which utilize dissolved hydrogen sulfide and sulfur in their metabolism to grow, and providing sufficient time for the bacteria to culture in said waste, to thereby initiate a biochemical reaction which has the following half reactions: 8 NO3- ā4N2 +12O2 12O2 +5H2 Sā5SO42- +4H2 O+2H+ to thereby remove substantially all of said existing dissolved hydrogen sulfide. 1. A process for removing dissolved hydrogen sulfide from waste systems comprising the steps of:
(a) adding nitrate ions to the waste in accordance with a ratio of at least 2.4 parts nitrate oxygen for each 1 part dissolved sulfide in order to provide a source of oxygen for naturally occurring bacteria present in the waste which utilize dissolved hydrogen sulfide in their metabolism; (b) providing sufficient time to culture said bacteria within said waste systems; and (c) providing ongoing time sufficient to enable said bacteria to remove the dissolved hydrogen sulfide.
2. A process according to
3. A process according to
4. A process according to
5. A process according to
6. A process according to
7. A process according to
8. A process according to
9. A process according to
10. A process according to
11. A process according to
12. A process according to
13. A process according to
14. A process according to
15. A process according to
16. A process according to
about 70%. 17. A process according to
18. A process for removing from waste systems dissolved hydrogen sulfide and other minor odors associated with other sulphur-containing compounds comprising the steps of: providing a source of oxygen in the form of nitrate in the form of nitrate in the waste in sufficient amount to cause naturally occurring bacteria in the waste which utilize dissolved hydrogen sulfide and sulfur in their metabolism to grow, and providing sufficient time for the bacteria to culture in said waste, to thereby initiate a biochemical reaction which has the following half reactions:
8 NO3 -ā4N2 +1202 1202 +5H2 Sā5SO42- +4H2 O+2H+ 19. The process according to
20. The process according to
21. The process according to
provided for the bacteria to culture. 22. The process according to
23. A process for removing dissolved H2 S and reducing sewage BOD in sewer systems comprising the steps of:
(a) adding a source of oxygen in the form of nitrate to the sewer system in an amount equal to about 2.4 lb. oxygen per lb. sulfide; and (b) providing about 8 to about 96 hours to allow naturally occurring bacteria already present in the system to culture as a result of the addition of said source of oxygen; and providing about 1.5 to about 20 hours to effect ongoing H2 S removal and sewage BOD reduction.
24. The process according to
25. The process according to
26. The process according to
27. The process according to
|
NO3 -existing dissolved hydrogen sulfide and a corresponding reduction in sewage BOD. By properly feeding sodium nitrate into the sewage or waste, odor and corrosion problems can also be substantially eliminated.
While the invention has been described in connection with what is presently known to be the most practical and preferred embodiment, it is to be understood that the invention is not to be limited to the disclosed embodiment, but on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims.
Hunniford, David J., Davis, H. Forbes
Patent | Priority | Assignee | Title |
7087172, | Mar 05 2003 | Evoqua Water Technologies LLC | Methods for reducing nitrate demands in the reduction of dissolved and/or atmospheric sulfides in wastewater |
7138049, | Mar 05 2003 | Evoqua Water Technologies LLC | Apparatus for reducing nitrate demands in the reduction of dissolved and/or atmospheric sulfides in wastewater |
7186341, | Mar 05 2003 | Evoqua Water Technologies LLC | Methods and apparatus for reducing nitrate demands in the reduction of dissolved and/or atmospheric sulfides in wastewater |
7285207, | Mar 05 2003 | Evoqua Water Technologies LLC | Methods and apparatus for reducing nitrate demands in the reduction of dissolved and/or atmospheric sulfides in wastewater |
7326340, | Mar 05 2003 | Evoqua Water Technologies LLC | System for controlling sulfide generation |
7553420, | Dec 02 2003 | Evoqua Water Technologies LLC | Systems and methods for wastewater odor control |
7799215, | Jan 30 2008 | Evoqua Water Technologies LLC | Wastewater treatment systems |
7799224, | Jan 30 2008 | Evoqua Water Technologies LLC | Wastewater treatment methods |
7972532, | Dec 02 2003 | Evoqua Water Technologies LLC | Composition for odor control |
8430112, | Jul 13 2010 | Evoqua Water Technologies LLC | Slurry feed system and method |
8968646, | Feb 18 2011 | Evoqua Water Technologies LLC | Synergistic methods for odor control |
Patent | Priority | Assignee | Title |
1701825, | |||
1997252, | |||
221232, | |||
3219576, | |||
3300404, | |||
3401113, | |||
3502566, | |||
3607736, | |||
3639263, | |||
3867284, | |||
3930998, | Sep 18 1974 | ZIMPRO PASSAVANT ENVIRONMENTAL SYSTEMS, INC , A CORP OF WI | Wastewater treatment |
3959127, | Dec 05 1973 | The United States of America as represented by the Secretary of the Navy | Biodegradation of oil on water surfaces |
3959130, | Aug 16 1973 | Heinrich Koppers Gesellschaft mit beschrankter Haftung | Process for decontaminating sewage containing cyanide |
3966450, | Aug 12 1974 | FMC Corporation | Animal waste odor treatment |
4098690, | Mar 29 1976 | The University of Illinois Foundation | Water purification process |
4108771, | Feb 06 1974 | Weiss & Co.; Kemiska Konsultbyran A.G.; Chemical Consults Corp., Ltd. | Elimination of odors from organic wastes |
4115258, | Jan 08 1973 | Treatment of sewage | |
4148726, | Jan 08 1973 | Process for treatment of sewage in a gravity sewer | |
4153547, | Feb 06 1978 | Use of acidified copper sulfate in hydrogen sulfide removal | |
4297216, | Jan 22 1975 | Hitachi, Ltd. | Method for treatment of biochemical waste |
4446031, | Jun 30 1981 | Tioxide Group Limited | Sewage treatment composition its manufacture and use |
4501668, | Dec 07 1982 | Degussa Aktiengesellschaft | Process for the elimination of hydrogen sulfide or iron sulfide from an aqueous system |
4505819, | Aug 18 1980 | AUSTGEN BIOJET INTERNATIONAL PTY LTD ; AUSTGEN BIOJET HOLDINGS PTY LTD | Method for the anaerobic degradation of organic material |
4680127, | Dec 13 1985 | Betz Laboratories, Inc. | Method of scavenging hydrogen sulfide |
4681687, | Oct 20 1986 | Nalco Chemical Company | Use of alkali metal nitrites to inhibit H2 S formation in flue gas desulfurization system sludges |
4725405, | Mar 31 1982 | Prestone Products Corporation | Organosiloxane-silicate copolymer antifreeze composition with nitrate corrosion inhibitor |
4760027, | Apr 09 1986 | ABB ENVIRONMENTAL SERVICES INC | Microbiological desulfurization of gases |
DE3414556, | |||
JP57187079, |
Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
May 09 1995 | U.S. Filter Distribution Group, Inc. | (assignment on the face of the patent) | / | |||
May 31 2000 | U S FILTER DISTRIBUTION GROUP, INC | United States Filter Corporation | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 010859 | /0573 | |
Jul 31 2004 | United States Filter Corporation | USFilter Corporation | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 015093 | /0586 |
Date | Maintenance Fee Events |
Sep 27 2001 | M185: Payment of Maintenance Fee, 12th Year, Large Entity. |
Date | Maintenance Schedule |
Apr 11 2003 | 4 years fee payment window open |
Oct 11 2003 | 6 months grace period start (w surcharge) |
Apr 11 2004 | patent expiry (for year 4) |
Apr 11 2006 | 2 years to revive unintentionally abandoned end. (for year 4) |
Apr 11 2007 | 8 years fee payment window open |
Oct 11 2007 | 6 months grace period start (w surcharge) |
Apr 11 2008 | patent expiry (for year 8) |
Apr 11 2010 | 2 years to revive unintentionally abandoned end. (for year 8) |
Apr 11 2011 | 12 years fee payment window open |
Oct 11 2011 | 6 months grace period start (w surcharge) |
Apr 11 2012 | patent expiry (for year 12) |
Apr 11 2014 | 2 years to revive unintentionally abandoned end. (for year 12) |