WO1998009919B1

WO1998009919B1 - Microbial remediation reactor and process

Info

Publication number: WO1998009919B1
Application number: PCT/US1997/015558
Authority: WO
Filing date: 1997-09-03
Publication date: 1998-05-22

Abstract

Embodiments of a remediation reactor and mixer/contactor blade for the reactor are shown and described, the reactor (11) being for containing a liquid slurry, suspension or settled bed of solid particles containing microorganisms. Inside the vessel is a supply conduit and at least one generally horizontal stirrer blade (27) in fluid connection with the supply conduit. The stirrer blade is a mixer/contactor which has a leading side having openings through which fluid may pass. The stirrer blade rotates in the vessel, and this rotation is made easier by the hydraulic forces of fluid flowing out from the stirrer blade. The flowing fluid creates a fluidization zone in the slurry, suspension or settled bed at or near the leading edge of the stirrer blade. The fluidization zone is less dense than the rest of the sediment bed, and the stirrer blade tends to rotate into the fluidization zone. This way, controlled rotation of the stirrer blade may be created near the bottom of the vessel, enhancing mixing of the microorganisms with the slurry, suspension or settled bed in the vessel, without unnecessarily damaging the microorganisms, especially when the flowing fluid contains contaminants which are nutrients for the microorganisms. Also, shown and described is a vessel which incorporates a mixing blade through which a gas and/or a liquid is recirculated. The mixing blade is rotated through a sand layer or other settled bed of solid particles, which acts as a medium supporting microbial growth and/or as a filter to remove particulate matter from the vessel effluent which is drawn off from below the settled bed layer. Fluid recirculation aids in the fluidization of the filter medium and allows for intermittent operation with a significant reduction in energy and operating costs. The vessel may be operated as an aerobic bioreactor by recirculating air or as an anaerobic bioreactor by recirculating an inert gas. Rotation of the mixing blade through the filter medium with recirculation of fluids through the mixing blade allows the filter medium to be efficiently backwashed in order to prevent filter plugging.

Claims

22

AMENDED CLAIMS

[received by the International Bureau on 25 March 1998 (25.03.98); original claims 1-3, 8, 11 and 12 amended; new claims 31-35 added; remaining claims unchanged (3 pages)]

1. A process for remediating a liquid waste stream or a contaminated sludge or soil which comprises: maintaining a slurry or suspension, and a substantially settled bed of solid particles, in a reactor, said solid particles colonized by micro-organisms; providing at least one generally horizontal stirrer blade within said reactor, said stirrer blade being adapted to rotate within said reactor and having a certain direction of rotation and a leading side and a trailing side, there being openings at or near the leading side through which fluid may pass; and withdrawing liquid from said settled bed of said reactor.

2. The process of Claim 1, wherein no motorized force is provided to the stirrer blade.

3. The process of Claim 1 , which further comprises passing fluid through said openings at or near the leading side ofthe blade.

4. The process of Claim 3, which further comprises passing liquid withdrawn from said settled bed as fluid through said openings at or near the leading side of the blade.

5. The process of Claim 4 wherein the liquid withdrawn from said settled bed has less suspended solids than the liquid in said reactor.

6. The process of Claim 4 wherein an inlet stream to the vessel is provided, and the liquid above said settled bed has a higher concentration of waste or contaminants than the inlet stream.

1 7. The process of Claim 4 wherein the liquid withdrawn from said settled bed is

2 withdrawn from below said settled bed.

8. The process of Claim 1 wherein a plurality of said stirrer blades are provided.

1 9. The process of Claim 8 wherein the fluid passing through said openings of one of said

2 stirrer blades is different from the fluid passing through said openings of another of said

3 stirrer blades.

1 10. The process of Claim 8 which also comprises providing at least one of said stirrer

2 blades within said settled bed.

l 1 1. The process of Claim 1 wherein said stirrer blade operates intermittently.

l 12. The process of Claim 1 wherein said stirrer blade operates continuously.

1 13. The process of Claim 8 which also comprises:

2 providing at least one of said stirrer blades within said settled bed; and

3 providing at least one of said stirrer blades above said settled bed.

1 14. The process of Claim 13 wherein the said stirrer blades both within and above said

₂ settled bed operate intermittently. 24

29. The process of Claim 27 wherein the stirrer blade within said settled bed operates intermittently, and the stirrer blade above said settled bed operates continuously.

30. The process of Claim 27 wherein the stirrer blades in both the settled bed and above said settled bed operate continuously.

31. The process of Claim 17, wherein no motorized force is provided to the stirrer blade.

32. The process of Claim 17, wherein the settled bed substantially comprises a filtration medium.

33. The process of Claim 17, wherein one of said stirrer blades is provided in said settled bed and is rotated to fluidize the settled bed, to renew the filtration capacity ofthe settled bed.

34. The process of Claim 1, wherein the settled bed substantially comprises a filtration medium.

35. The process of Claim 1, wherein one of said stirrer blades is provided in said settled bed and is rotated to fluidize the settled bed, to renew the filtration capacity ofthe settled bed.