Waste treatment process

• US 4,009,098 A
• Filed: 02/16/1973
• Issued: 02/22/1977
• Est. Priority Date: 02/16/1973
• Status: Expired due to Term

• Current Assignee: Ecolotrol, Inc.
• Original Assignee: Ecolotrol, Inc.
• Inventors: Jeris, John S.
• Primary Examiner(s): Wyse, Thomas G.
• Application Number:
  US05/333,394
• Time in Patent Office: 1,467 Days
• Field of Search: 210/11, 210/17, 210/15, 210/20, 210/2-8, 210/14, 210/16
• US Class Current: 210/618
• CPC Class Codes: C02F 3/06 using submerged filters
• CPC Class Codes: C02F 3/085 Fluidized beds
• CPC Class Codes: C02F 3/26 using pure oxygen or oxygen-rich gas
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

Process for removing organic carbon from waste water to reduce biochemical oxygen demand by generating a fluidized bed formed from biota attached to a solid particulate carrier and waste water, providing enough oxygen to allow the biota to reduce the biochemical oxygen demand of the waste water passing therethrough and then mechanically removing excess bacterial growth formed on the carrier during the process.

Claims

1. Process for removing biochemical oxygen demand from waste water by passing the waste water through a bed of microorganisms adapted to oxidize biochemical oxygen demand under aerobic conditions, said bed adapted to pass suspended solids present in said waste water therethrough, comprising:

a. generating an upflow fluidized bed of solid particulate carrier having a cultured layer of said microorganisms seeded thereon by passing waste water upwardly through said bed at a flow rate of at least about 6 gallons per minute per square foot of bed to impart to said microorganism attached particles movement within said bed;

b. providing about 0.1 to 1.5 milligrams of oxygen per milligram of biochemical oxygen demand removed from said waste water in the waste water to allow said microorganisms to reduce the biochemical oxygen demand of the waste water passing therethrough; and

c. removing excess microorganism growth from said bed particles in order to increase the specific gravity of said particles such that significant amounts of biochemical oxygen demand are reduced from a volume of waste water passing through said bed in 30 minutes or less and floc produced by removal of excess growth is carried from the process without interferring with the efficient operation thereof.

2. The process in accordance with claim 1 wherein said excess microorganism growth is removed at the down-stream portion of said fluidized bed by a rotating flexible stirrer.

3. The process in accordance with claim 1 in which the carrier has a particle size from about 0.2 to 3 millimeters and a specific gravity of at least about 1.1.

4. The process in accordance with claim 1 in which the oxygen source is selected from the group consisting of an oxygen containing gas or oxygen.

5. The process in accordance with claim 1 in which the fluidized bed is formed by passing waste water through a vertical column containing said microorganism on said carrier particle substrate at a flow rate between about 6 and 40 gallons per minute per square foot of bed.

6. The process of claim 1 in which the carrier substrate is a porous particulate material of substantially uniform size having a particle diameter of 0.4 to 1.5 millimeters of the specific gravity of at least about 1.3.

7. The process of claim 1 including the steps of generating at least one additional fluidized bed employing waste water treated by said fluidized bed according to steps (a), (b) and (c) to further reduce biochemical oxygen demand of said waste water.

8. The process of claim 1 including the steps of recovering the waste water passing through the bed and recycling the treated waste water through the bed in accord with steps (a), (b) and (c) to further reduce biochemical oxygen demand of said waste water.