Treatment of a suspension in a bioreactor with integrated hydraulic bottom layer removal

• US 7,300,584 B2
• Filed: 07/06/2004
• Issued: 11/27/2007
• Est. Priority Date: 12/11/2003
• Status: Active Grant

• Current Assignee: Linde-KCA-Dresden GmbH
• Original Assignee: Linde-KCA-Dresden GmbH
• Inventors: Langhans, Gerhard, Buechner, Thomas, Herms, Matthias
• Primary Examiner(s): Barry; Chester T.
• Application Number:
  US10/883,977
• Publication Number:
  US 20050126997A1
• Time in Patent Office: 1,239 Days
• Field of Search: 210/601, 210/629
• US Class Current: 210/629
• CPC Class Codes: C02F 2303/12 Prevention of foaming
• CPC Class Codes: C02F 3/2873 with internal draft tube circulation
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

A process and a device for biological treatment of a suspension in a bioreactor (2) are described. To circulate the suspension, at least some of the suspension is routed through a vertically aligned guide zone (5) so that a vertical flow of the suspension is produced. To control sediment problems, it is suggested that by feeding a fluid, especially a free liquid jet, via at least one nozzle (11), a horizontal flow is superimposed on the vertical flow in the vicinity of the bottom of the bioreactor (2), by which a spiral flow to the central outlet area of the bioreactor (2) is produced (FIG. 1).

Claims

1. A process for biological treatment of a suspension in a bioreactor comprising a central outlet area near the bottom and a vertically aligned guide zone, said process comprising:

circulating a suspension within said bioreactor, wherein at least some of the suspension is routed upward through said vertically aligned guide zone by the injection of gas into the vertically aligned guide zone, whereby a vertical flow of at least a portion of the suspension is produced downward outside of the vertically aligned guide zone; and

feeding at least one jet of fluid at an angle of 0 to 10°

downward from horizontal in the bottom part of the bioreactor, the jet superimposing on the downward vertical flow at the bottom part of the bioreactor, so as to establish a spiral flow to the central outlet area of the bioreactor.

2. A process according to claim 1, wherein the jet of fluid is fed into the bioreactor at a flow velocity of 10 to 15 m/s.

3. A process according to claim 1, wherein the jet of fluid is fed into the bioreactor at a volumetric flow rate of 300 to 600 m³/h.

4. A process according to claim 1, wherein in the bottom part of the bioreactor at the bioreactor wall, the spiral flow has a flow velocity of about 0.5 m/s.

5. A process according to claim 1, wherein the jet of fluid is fed into the bioreactor at an offset angle to radial flow of 40 to 50°

.

6. A process according to claim 1 wherein the fluid is fed into the bioreactor at an angle of >

0 to 10°

downward from horizontal.

7. A process according to claim 1, comprising withdrawing suspension from the bioreactor and recycling said suspension into the bioreactor via a nozzle as said at least one horizontal jet of fluid.

8. A process according to claim 1, wherein the jet of fluid is fed into the bioreactor via several nozzles distributed on the periphery of the bioreactor in the vicinity of the bottom.

9. A process according to claim 8, wherein the nozzles are supplied with a jet of fluid, at different times.

10. A process according to claim 8, wherein the nozzles are operated with a common pump and are successively supplied from said common pump by means of cyclic switching.

11. A process according to claim 7, wherein the suspension is suctioned off from the center of the bottom of the bioreactor.

12. A process according to claim 7, wherein fluid that is suctioned off from the bioreactor is fed into the bioreactor in part or in a time sequence via at least one upper nozzle to form a jet of fluid, the nozzle is provided in the area of the suspension fill level such that the surface of the suspension and/or the top scum floating on the surface of the suspension is forced into rotary flow.

13. A process according to claim 12, wherein the jet of fluid from the at least one upper nozzle is fed into the fermentation reactor via nozzles that are located tangentially on the periphery of the tank.

14. A process according to claim 13, wherein the upper nozzles are supplied from the same pump as the nozzles located in the vicinity of the bottom.

15. A process for biological treatment of a suspension in a bioreactor comprising a central outlet area near the bottom and a vertically aligned guide zone, said process comprising:

circulating a suspension within said bioreactor, wherein at least some of the suspension is routed upward through said vertically aligned guide zone by the injection of gas into the vertically aligned guide zone, whereby a vertical flow of at least a portion of the suspension is produced downward outside of the vertically aligned guide zone; and

feeding at least one jet of fluid at an angle of 0 to 10°

downward from horizontal in the bottom part of the bioreactor, the jet superimposing on the downward vertical flow at the bottom part of the bioreactor, so as to establish a spiral flow to the central outlet area of the bioreactor,

wherein no moving parts are present in the bioreactor.

17. A process according to claim 15, wherein the jet of fluid is fed into the bioreactor via several nozzles distributed on the periphery of the bioreactor in the vicinity of the bottom.

19. A process according to claim 15, comprising withdrawing suspension from the bioreactor and recycling said suspension into the bioreactor via a nozzle as said at least one horizontal jet of fluid.

21. A process according to claim 15, wherein the jet of fluid is fed into the bioreactor at an offset angle to radial flow of 40 to 50°

.

23. A process according to claim 15, wherein the fluid is fed into the bioreactor at an angle of >

0 to 10°

downward from horizontal.

16. A process for biological treatment of a suspension in a bioreactor comprising a central outlet area near the bottom and a vertically aligned guide zone, said process comprising:

circulating a suspension within said bioreactor, wherein at least some of the suspension is routed upward through said vertically aligned guide zone by the injection of gas into the vertically aligned guide zone, whereby a vertical flow of at least a portion of the suspension is produced downward outside of the vertically aligned guide zone; and

feeding at least one jet of fluid at an angle of 0 to 10°

downward from horizontal in the bottom part of the bioreactor, the jet superimposing on the downward vertical flow at the bottom part of the bioreactor, so as to establish a spiral flow to the central outlet area of the bioreactor,

wherein the means within said bioreactor for circulating the suspension, for providing the vertical flow, and for establishing said spiral flow to the central outlet area of the bioreactor consists essentially of the vertically aligned guide zone into which gas is introduced and the at least one jet of fluid at an angle of 0 to 10°

downward from horizontal.

18. A process according to claim 16, wherein the jet of fluid is fed into the bioreactor via several nozzles distributed on the periphery of the bioreactor in the vicinity of the bottom.

20. A process according to claim 16, comprising withdrawing suspension from the bioreactor and recycling said suspension into the bioreactor via a nozzle as said at least one horizontal jet of fluid.

22. A process according to claim 16, wherein the jet of fluid is fed into the bioreactor at an offset angle to radial flow of 40 to 50°

.

24. A process according to claim 16, wherein the fluid is fed into the bioreactor at an angle of >

0 to 10°

downward from horizontal.