Pathogen reduction system used in treating wastewater

• US 6,117,203 A
• Filed: 11/10/1997
• Issued: 09/12/2000
• Est. Priority Date: 11/10/1997
• Status: Expired due to Fees

• Current Assignee: Kruger (Veolia Environnement SA)
• Original Assignee: Kruger Incorporated
• Inventors: Andersen, Edvin, Buchhave, Karsten
• Primary Examiner(s): Langel, Wayne
• Assistant Examiner(s): Wong, Melanie C.
• Application Number:
  US08/966,728
• Time in Patent Office: 1,037 Days
• Field of Search: 71/9, 71/12, 71/14, 210/609, 210/175, 210/253, 210/768, 210/774, 210/742
• US Class Current: 71/12
• CPC Class Codes: C02F 11/185 by pasteurisation
• CPC Class Codes: F28D 7/024 the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
• CPC Class Codes: F28F 2280/02 Removable elements

Abstract

A pathogen reduction system for a sludge treatment process that employees multiple reactors operating in a batch mode to reduce pathogen levels in the sludge while providing a continuous flow of pathogen reduced sludge to a digester. In addition, the present invention entails an efficient heat exchanger for heating and cooling the sludge being treated in the above process. In particular, the heat exchanger is of the counterflow type and includes a helical coil confined in an annular chamber for transmitting one media and wherein the helical coil is spaced so as to form another helical flow channel that is defined by the annular chamber and the helical coil itself. Consequentially, one media is directed through the helical coil while another media is directed through the flow channel that is defined in part by the helical coil.

Claims

1. A pre-digestion pathogen reduction system for treating sludge prior to the sludge being directed into a digester in a wastewater treatment system, comprising:

a) an inlet for directing the incoming sludge into the system;

b) a series of reactors for receiving the incoming sludge as a series of batches, holding the batches of incoming sludge for a predetermined time to produce a pathogen-reduced sludge, and discharging the batches of treated sludge in a manner so as to form a continuous outflow of treated sludge to the digester, each reactor being operative to assume the feeding, holding, and discharge modes in sequence;

c) a sludge-to-sludge heat exchanger disposed on an inlet side of the reactors for receiving both the incoming sludge and the treated pathogen reduced sludge and transferring the heat associated with the treated sludge to the incoming sludge;

d) an outlet for directing the treated sludge from the reactors to the sludge-to-sludge heat exchanger prior to the sludge being directed to the digester such that as the treated sludge passes through the sludge-to-sludge heat exchanger, the heat associated therewith is transferred to the incoming sludge so as to heat the incoming sludge while at the same time cooling the treated sludge; and

e) at least one additional heat exchanger for cooling the treated sludge leaving the reactors, the additional heat exchanger being a wastewater effluent heat exchanger that is coupled to a source of wastewater effluent wherein the wastewater effluent effectively cools the treated sludge.

2. The system of claim 1 wherein each reactor at any one time is operative to assume a feeding, holding, or discharge mode with respect to the sludge being treated.

3. The system of claim 1 wherein a heating heat exchanger is communicatively connected to an external source of heat and to the incoming sludge such that the external source of heat is utilized to heat the sludge prior to the sludge entering the reactors.

4. The system of claim 1 wherein the reactors are disposed in parallel relationship and operate to treat the sludge in batch form but yet continuously direct sludge from the reactors to the digester.

5. The system of claim 1 wherein there is provided a control valve on both the inlet and outlet sides of each reactor for controlling the flow of sludge into and from the reactor.

6. The system of claim 5 including a programmable controller for controlling the control valves and controlling the flow of sludge to and from the respective reactors.

7. The system of claim 6 including at least three reactors disposed in parallel relationship, and wherein the programmable controller in conjunction with the control valves direct sludge into one reactor while directing sludge from a second reactor while sludge is being held in the third reactor.

8. The system of claim 7 wherein the programmable controller in conjunction with the control valves is operative to sequentially change the mode of operation of each reactor such that during the course of treating the sludge for pathogens each reactor cycles between three separate modes of operation, a filling mode, a holding mode, and a discharge mode.

9. The system of claim 8 wherein the controller is a programmable controller and wherein the programmable controller in conjunction with the control valves controls the mode of each reactor such that in general each reactor cycles through a series of different modes of operation during the pathogen reduction process.

10. A system for reducing the pathogens in sludge comprising:

a sludge inlet line;

a series of batch reactors connected to the sludge inlet line for receiving incoming sludge therefrom, the series of batch reactors disposed in parallel relationship and wherein during a selected treatment interval one reactor assumes a holding and treating mode and produces treated sludge while the other reactor assumes a discharge mode;

a series of heat exchangers for heating incoming sludge and cooling the treated sludge including at least one sludge-to-sludge heat exchanger operatively connected between the sludge inlet line and the series of reactors for heating incoming sludge passing in the inlet line and for cooling treated sludge leaving the reactors and wherein the sludge-to-sludge heat exchanger is connected to the inlet line such that incoming sludge passing through the inlet line is directed through the sludge-to-sludge heat exchanger before reaching the reactors; and

wherein the system includes an outlet line for directing treated sludge from the reactors back to and through the sludge-to-sludge heat exchanger such that the treated sludge passing from the outlet line back through the sludge-to-sludge heat exchanger acts to heat the incoming sludge while at the same time the treated sludge is cooled; and

a series of control valves disposed on inlet and outlet sides of the reactors and a programmable controller operatively connected to the control valves for controlling the same such that the individual reactors can be controlled to operate in a batch mode while the series of reactors as a group can be controlled to provide a continuous flow of sludge through the reactors.

11. The system of claim 10 wherein the pathogen reduction system is coupled to a digester that reduces the volatile solids within the sludge while the pathogen reduction system reduces the pathogen concentration within the sludge.

12. The system of claim 10 wherein the series of reactors include three reactors disposed in parallel relationship with each reactor sequentially assuming a filling, holding and discharging mode and wherein the operating modes of the three reactors are staggered such that generally the individual reactors assume different operating modes.

13. The system of claim 10 including a series of additional heat exchangers that form a part of the system and which function to further heat and cool the treated sludge and the incoming sludge.

14. The system of claim 13 wherein the series of heat exchangers includes a heat exchanger operatively connected to a wastewater effluent supply and to the treated sludge exiting the reactors for effectively cooling the treated sludge, and wherein the series of heat exchangers includes another heat exchanger connected to an external source of heat and operatively associated with the incoming sludge being directed to the reactors for providing additional heat to the incoming sludge.

15. A method of treating sludge to reduce the pathogen concentration of the sludge comprising:

a) heating incoming sludge by directing the incoming sludge into and through a sludge-to-sludge heat exchanger;

b) directing the heated incoming sludge to a series of reactors;

c) during one phase, holding the heated sludge within one reactor for a selected time period while discharging heated sludge from another reactor;

d) during another phase, discharging the heated sludge from the one reactor while holding the sludge in the other reactor, thereby processing the heated sludge in batch form while providing a continuous outflow of treated sludge from the reactors;

e) directing the treated sludge from the reactors back to the sludge-to-sludge heat exchanger and routing the treated sludge back through the sludge-to-sludge heat exchanger such that heat associated with the treated sludge heats the incoming sludge and in the process the heated sludge is cooled;

f) further cooling the treated sludge by directing the treated sludge to a separate cooling heat exchanger; and

g) directing treated wastewater effluent to the cooling heat exchanger and utilizing the treated effluent to cool the treated sludge after the treated sludge has exited the reactors.

16. The method of claim 15 including directing the incoming sludge through a second heat exchanger that is operatively coupled to an external source of heat.

17. The method of claim 15 including directing the continuous outflow of treated sludge from the reactors to a digester for further treatment.

18. The method of claim 15 including heating the incoming sludge to a temperature of approximately 60 to 70°

C.

19. The method of claim 15 wherein the reactors include three reactors disposed in parallel relationship with each reactor assuming a sludge filling, holding and discharging mode during certain times of the pathogen reduction process, and wherein the operation mode the three reactors are staggered such that generally the three reactors are operating in different modes at any one time such that the sludge is processed in batch form but continuously fed to and from the reactors.

20. The method of claim 19 including holding the sludge within the reactors for approximately one hour.

21. The method of claim 15 including locating the cooling heat exchanger downstream from the sludge-to-sludge heat exchanger such that the treated sludge is cooled by the effluent after it has been first cooled by the sludge-to-sludge heat exchanger.

22. The method of claim 21 including direct the incoming sludge through a second heating heat exchanger prior to the incoming sludge reaching the reactors, and heating a system of water and directing the heated water to the second heating heat exchanger so as to provide additional heat to the incoming sludge prior to reaching the reactors.

23. The method of claim 15 wherein there is provided a control valve on both the inlet and outlet sides of each reactor and wherein the control valves and the flow of sludge through the reactors are controlled by a programmable controller.