System and method for reducing the pathogen concentration of sludge

• US 6,325,935 B1
• Filed: 08/02/1999
• Issued: 12/04/2001
• Est. Priority Date: 08/02/1999
• Status: Expired due to Fees

• Current Assignee: Kruger (Veolia Environnement SA)
• Original Assignee: Kruger (Veolia Environnement SA)
• Inventors: Hojsgaard, Soren J.
• Primary Examiner(s): Upton, Christopher
• Application Number:
  US09/364,994
• Time in Patent Office: 855 Days
• Field of Search: 210/609, 210/613, 210/742, 210/764, 210/766, 210/175, 210/259, 165/299, 165/300
• US Class Current: 210/609
• CPC Class Codes: C02F 11/04 Anaerobic treatment; Production of methane by such processes
• CPC Class Codes: C02F 11/18 by thermal conditioning by pyrolysis C02F11/10

Abstract

A waste treatment system comprises a first heat exchanger positioned before one or more reactors. The reactors discharge treated sludge to a second heat exchanger. The first and second heat exchangers share a heat transfer medium wherein the heat from the treated sludge is transferred to the incoming sludge. The treated sludge is cooled to reach an optimal temperature range before entry into a digester. The system also is adapted to allow a pipe cleaning device or “pig” to clean the heat exchangers by being forced through the heat exchangers by pressurized and pasteurized wastewater.

Claims

1. A method of treating sludge to reduce pathogens within the sludge, comprising:

a. directing incoming sludge through a first heat exchanger;

b. directing the incoming sludge from the first heat exchanger to one or more reactors for holding and treating the sludge;

c. directing the treated sludge from the one or more reactors through a second heat exchanger;

d. directing a heat transfer medium through the first and second heat exchangers for efficiently heating the incoming sludge and cooling the treated sludge;

e. directing the treated sludge from the second heat exchanger and ultimately to a digester; and

f. varying the flow of the heat transfer medium through the first and second heat exchangers so as to cool the treated sludge to a target temperature range before reaching the digester.

2. The method of claim 1 wherein varying the flow of the heat transfer medium through the first and second heat exchangers so as to cool the treated sludge to the target temperature range comprises the step of varying the flow of the heat transfer medium through the first and second heat exchangers such that the temperature of the treated sludge reaching the digester approximates the target temperature range of approximately 34-38°

C.

3. The method of claim 1 further comprising the step of directing the treated sludge through a third heat exchanger for further cooling after directing the treated sludge through the second heat exchanger.

4. The method of claim 3 further comprising the step of using water as the heat transfer medium for the third heat exchanger.

5. The method of claim 1 further comprising the step of measuring the temperature of the treated sludge after passage through said second heat exchanger and prior to reaching the digester to determine if the temperature approaches the target temperature range.

6. The method of claim 5 further comprising the step of increasing the flow rate of the heat transfer medium to increase the cooling of the treated sludge.

7. The method of claim 5 further comprising the step of decreasing the flow rate of the heat transfer medium to decrease the cooling of the treated sludge.

8. The method of claim 1 further comprising the step of interposing a heating heat exchanger between the first heat exchanger and the one or more reactors, wherein the heating heat exchanger transfers heat from an external source to the incoming sludge.

9. The method of claim 1 including continuing to monitor the temperature of the treated sludge before it enters the digester and controlling the flow rate of the heat transfer medium in accordance with the temperature of the treated sludge before it reaches the digester such that the flow rate of the heat transfer medium is selectively increased to cool the treated sludge and selectively decreased in order to retain more heat within the treated sludge.

10. The method of claim 9 wherein the heat transfer medium is pumped through the first and second heat exchangers by variable speed pump and wherein the variable speed pump is controlled by a CPU.

11. The method of claim 1 wherein the first and second heat exchangers include an inner conduit through which the incoming and treated sludge move and an outer conduit, that at least partially surrounds the inner conduit, through which the heat transfer medium passes.

12. A predigestion pathogen reduction system for removing pathogens from sludge, comprising:

a. a first heat exchanger for receiving incoming sludge and heating the same;

b. one or more reactors in fluid communication with the first heat exchanger for receiving sludge therefrom, the one or more reactors adapted to hold and treat the heated sludge;

c. a second heat exchanger disposed in fluid communication with the one or more reactors for receiving treated sludge therefrom and cooling the treated sludge as it passes through the second heat exchanger;

d. a digester located down stream from the second heat exchanger for receiving treated sludge after the same has been cooled by the second heat exchanger;

e. a heat transfer medium contained within a closed loop that extends in a heat exchange relationship with both the first and second heat exchangers and wherein the heat transfer medium functions to remove heat from the treated sludge and add heat to the incoming sludge; and

f. a variable speed pump connected within the closed loop for pumping the heat transfer medium through the first and second heat exchangers and for varying the flow rate of the heat transfer medium in the closed loop so as to cool the treated sludge to a target temperature range prior to the treated sludge reaching the digester.

13. The system of claim 12 wherein the second heat exchanger that functions to cool the treated sludge includes first and second heat exchanger sections connected in series.

14. The system of claim 12 including a controller for sensing the temperature of the treated sludge prior to introduction into the digester and controlling the speed of a variable speed pump such that the temperature of the treated sludge approaches the target temperature range prior to introduction into the digester.

15. The system of claim 12 further comprising a third heat exchanger for cooling the treated sludge, said third heat exchanger fluidly connected to said digester and positioned serially between said second heat exchanger and said digester wherein said third heat exchanger contains an external heat transfer medium.

16. The system of claim 12 further comprising a heating heat exchanger positioned between said first heat exchanger and the one or more reactors, wherein said heating heat exchanger heats the incoming sludge to a desired temperature range prior to introducing the incoming sludge to the one or more reactors.

17. A method of transferring heat in a pathogen reduction system for sludge, comprising:

a. directing incoming, pathogen bearing sludge through a first heat exchanger and heating the incoming sludge;

b. introducing the heated incoming sludge to one or more reactors to reduce the pathogens therein to create treated sludge;

c. directing the treated sludge from the one or more reactors to a second heat exchanger and cooling the treated sludge;

d. transferring the treated sludge to a digester; and

e. transferring heat from the treated sludge to the incoming sludge by directing a closed loop through the first and second heat exchangers and channeling a heat exchange medium through the closed loop in a direction counter to the flow of both the incoming sludge and the treated sludge and relying solely on the heat transfer characteristics of the heat transfer medium to transfer heat from the treated sludge to the incoming sludge.

18. The method of claim 17 further including varying the flow rate of the heat transfer medium so as to control the temperature of the treated sludge prior to entry into the digester.

19. The method of claim 18 wherein there is a target temperature range for the treated sludge entering the digester and wherein the flow rate of the heat transfer medium is varied such that the target temperature range is met.

20. The method of claim 17 further comprising the step of directing the treated sludge through a third heat exchanger for further cooling after directing the treated sludge through the second heat exchanger.

21. The method of claim 20 further comprising the step of using water as the heat transfer medium for the third heat exchanger.

22. The method of claim 17 including a variable speed pump for pumping the heat transfer medium between the first and second heat exchangers and a controller operatively connected to the variable speed pump for varying the speed of the pump and consequently varying the flow rate of the heat transfer medium.

23. The method of claim 22 including sensing the temperature of the treated sludge before introduction into the digester and wherein the control exercised by the controller over the variable speed pump is a function of the temperature of the treated sludge measured prior to introduction into the digester.