Intermittent aeration type biological treatment process and system therefor

• US 4,818,408 A
• Filed: 09/03/1987
• Issued: 04/04/1989
• Est. Priority Date: 09/09/1986
• Status: Expired due to Term

• Current Assignee: Nishihara Environmental Sanitation Research Corporation Limited, Nishihara Om-Tech Company Limited
• Original Assignee: Nishihara Environmental Sanitation Research Corporation Limited, Nishihara Om-Tech Company Limited
• Inventors: Hamamoto, Youichi
• Primary Examiner(s): Castel, Benoit
• Application Number:
  US07/092,489
• Time in Patent Office: 579 Days
• Field of Search: 210/641, 210/96.1, 210/626
• US Class Current: 210/614
• CPC Class Codes: C02F 2209/22 O2
• CPC Class Codes: C02F 2209/44 Time
• CPC Class Codes: C02F 3/006 Regulation methods for biological treatment
• CPC Class Codes: C02F 3/301 Aerobic and anaerobic treatment in the same reactor
• CPC Class Codes: G05D 21/02 characterised by the use of electric means
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

The present invention is concerned with an intermittent aeration type biological treatment process and system, wherein waste water is caused to flow into an aeration tank, and aeration is repeatedly stopped and started in the aeration tank to treat the waste water. Concentration values of dissolved oxygen during aeration of the waste water in the aeration tank are continuously measured by a dissolved oxygen concentration measuring device provided in the aeration tank. Deficient values of dissolved oxygen and dissolved oxygen variation values at predetermined time intervals are calculated from the values thus measured. The deficient values and variation values are integrated and processed by an oxygen requirement value calculating-integrating operation unit to calculate an oxygen requirement value for the activated sludge in the current aeration step. The necessary aeration time duration for the succeeding step is obtained from the value of this oxygen requirement value, to thereby control the operating time duration of the aeration device. By use of the process and the system, wasteful operating energy can be eliminated and satisfactory treated water can be constantly obtained.

Claims

1. An intermittent aeration process for the biological treatment of waste water, comprising:

(a) contacting influent waste water and activated sludge in an aeration tank wherein the mixture of waste water and activated sludge forms a mixed liquor that undergoes intermittent aeration, wherein the aeration step and the cessation of aeration are alternately repeated; and

wherein the duration of the aeration step is determined by

(b) continuously measuring the concentration of the dissolved oxygen value of the liquor during the aeration step and calculating the values of deficient dissolved oxygen and the dissolved oxygen variation at predetermined time intervals;

(c) integrating and processing the values of deficient dissolved oxygen and the dissolved oxygen variation by an oxygen requirement value calculating-integrating operational unit to calculate an oxygen requirement value for the activated sludge in the current aeration step, and the necessary aeration time duration for the next succeeding step to thereby control the aeration for the next succeeding step.

2. The process of claim 1, wherein the aeration time duration is determined from the oxygen requirement value calculated from the rate of respiration of the activated sludge.

3. The process of claim 2, wherein the rate of respiration of the activated sludge is calculated from the difference between the concentration of dissolved oxygen and the concentration of saturated oxygen of the mixed liquor and a variation value of the concentration of dissolved oxygen.

4. The process of claim 3, wherein the variable rate of respiration of the activated sludge fluctuating in accordance with the flow rate of influent waste water is calculated to provide the minimum necessary aeration.

5. The process of claim 3, wherein the oxygen requirement value-integrating operational unit comprises a microcomputer, with a device to control aeration.

6. The process of claim 3, wherein the mixed liquor, upon completion of the intermittent aeration activated sludge treatment, is introduced into a settling tank, wherein a portion of the settled sludge is recycled to the aeration treatment and the supernatant liquid is discharged as treated water.

7. The process of claim 3, wherein the predetermined time intervals vary from about 1 to 10 minutes.

8. An intermittent aeration type biological treatment system comprising:

(a) an aeration tank with an inlet into which influent waste water flows and an outlet for effluent treated waste water;

(b) said aeration tank housing an aeration device for aerating the waste water in the aeration tank;

(c) a control unit for controlling the operative starting and stopping of said aeration device;

(d) a dissolved oxygen measuring device disposed in said aeration tank;

(e) an oxygen requirement value calculating-integrating operational unit mounted upon said dissolved oxygen measuring device; and

(f) a driving circuit connected to said oxygen requirement value calculating-integrating operational unit and said aeration device.

9. The system of claim 8, wherein the aeration device includes a blower and a diffuser.

10. The system of claim 8, wherein the integrating-operational unit comprises a microcomputer.

11. The system of claim 10, wherein the microcomputer includes an on-off control device to operate the blower.