IP Library Granted Patent US 8,557,111
Granted Patent B2
US 8,557,111 · App. 12/832,718 · Granted Oct 15, 2013

Low concentration wastewater treatment system

Inventors: William G. Conner (Dhahran, SA); Thomas E. Schultz (Waukesha, WI)
Assignees: Saudi Arabian Oil Company; Siemens Energy, Inc.
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Quick Facts
Patent No.
US 8,557,111
App. No.
12/832,718
Granted
Oct 15, 2013
Kind
B2
Abstract

A low concentration wastewater treatment system is provided that includes a high flux adsorbent material treatment system integrated with a low flux adsorbent material biological regeneration reactor. The high flux adsorbent material treatment system includes one or more unit operations for mixing low concentration wastewater with adsorbent material that is fresh, recycled, or a combination of both, and for decanting a liquid effluent having a reduced level of contaminants. The adsorbent material with adsorbed contaminants is regenerated in a low flux adsorbent material biological regeneration reactor in which a biological reaction occurs, such as biological oxidation, wherein organic contaminants in the wastewater are metabolized generally into carbon dioxide and water. Excess biomass is removed from the adsorbent material, and the thus-regenerated adsorbent material is recycled to the high flux adsorbent material treatment system.

Claims (33)

1. A wastewater treatment system comprising:

a high flux adsorption system including

an inlet for receiving wastewater,

a source of adsorbent material for contacting the wastewater and adsorbing contaminants from the wastewater,

a liquid outlet for discharging a major portion of the received wastewater that has been contacted by the adsorbent material, and

an adsorbent material outlet for discharging adsorbent material having adsorbed contaminants and a minor portion of the received wastewater; and

a low flux adsorbent material biological regeneration reactor system for maintaining the adsorbent material having adsorbed contaminants in suspension for a period of time that is sufficient to allow microorganisms to digest adsorbed organic contaminants, the low flux adsorbent material biological regeneration reactor system including

a biological regeneration reactor having

an inlet for receiving adsorbent material with adsorbed contaminants from the adsorbent material outlet of the high flux adsorption system,

a mixed liquor outlet, and

an adsorbent material outlet in communication with the source of adsorbent material of the high flux adsorption system.

2. The system of claim 1 in which the low flux adsorbent material biological regeneration reactor system further comprises:

a shearing apparatus for shearing excess accumulated biomass from adsorbent material, the shearing apparatus being positioned within the biological regeneration reactor and/or separate from the biological regeneration reactor and connected to the adsorbent material outlet for receiving adsorbent material from the biological regeneration reactor;

an adsorbent material/biomass separation zone for separating free biomass from a mixture of adsorbent material and free biomass;

an adsorbent material conduit for passing separated adsorbent material from the adsorbent material/biomass separation zone to the high flux adsorption system; and

a biomass conduit for passing separated biomass from the adsorbent material/biomass separation zone to the biological regeneration reactor or a location downstream of the biological regeneration reactor.

3. The system of claim 1 in which the low flux adsorbent material biological regeneration reactor system further comprises:

a combined apparatus for shearing and separating accumulated biomass from adsorbent material being positioned within the biological regeneration reactor and/or separate from the biological regeneration reactor and connected to the adsorbent material outlet for receiving adsorbent material from the biological regeneration reactor, and having an outlet for discharging separated adsorbent material and an outlet for discharging free biomass;

an adsorbent material conduit in communication with the adsorbent material outlet of the combined apparatus for returning adsorbent material to the high flux adsorption system; and

a biomass conduit in communication with the biomass outlet of the combined apparatus for passing separated biomass to the biological regeneration reactor or a location downstream of the biological regeneration reactor.

4. The system of claim 1 , wherein the low flux adsorbent material biological regeneration reactor system further comprises a membrane operating system in fluid communication with the mixed liquor outlet of the biological regeneration reactor.

5. The system of claim 1 , wherein the low flux adsorbent material biological regeneration reactor system further comprises a clarifier and/or a settler in fluid communication with the mixed liquor outlet of the biological regeneration reactor.

6. The system of claim 1 , wherein the high flux adsorption system includes a mixing zone and a settling zone.

7. The system of claim 1 , wherein the high flux adsorption system includes an adsorbent material filtration apparatus.

8. The system of claim 1 , wherein the high flux adsorption system includes a continuous backwash filter.

9. The system of claim 1 , wherein the high flux adsorption system includes a continuous regenerating filtration system or a continuous regenerating walnut shell filter.

10. The system of claim 1 , further comprising an upstream wastewater treatment system that discharges a low concentration wastewater, and wherein the wastewater inlet of the mixing zone is a low concentration wastewater inlet.

11. The system of claim 1 , further comprising

a sensor constructed and arranged to measure a parameter of the system; and

a controller in electronic communication with the sensor programmed to instruct performance of an act based on the measured parameter of the system.

12. The wastewater treatment system of claim 11 , wherein the measured parameter is the concentration of one or more predetermined compounds.

13. The wastewater treatment system of claim 11 , wherein the act comprises removing at least a portion of the adsorbent material from the biological regeneration reactor.

14. The wastewater treatment system of claim 11 , wherein the act comprise adding adsorbent material to the biological regeneration reactor.

Assignments (7)
CORRECTIVE ASSIGNMENT TO CORRECT THE INCORRECT APPICATION NUMBER 12/832,178 PREVIOUSLY RECORDED AT REEL: 028574 FRAME: 0913. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Aug 8, 2014
From: SIEMENS INDUSTRY, INC.
To: SIEMENS ENERGY, INC.
Reel/Frame 033595/0321 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 13, 2013
From: SIEMENS INDUSTRY, INC.
To: SIEMENS ENERGY, INC.
Reel/Frame 030995/0601 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 18, 2012
From: SIEMENS INDUSTRY, INC.
To: SIEMENS ENERGY, INC.
Reel/Frame 028574/0913 →
MERGER Recorded Jun 8, 2012
From: SIEMENS WATER TECHNOLOGIES HOLDING CORP.
To: SIEMENS INDUSTRY, INC.
Reel/Frame 028346/0683 →
MERGER Recorded Jun 4, 2012
From: SIEMENS WATER TECHNOLOGIES CORP.
To: SIEMENS WATER TECHNOLOGIES HOLDING CORP.
Reel/Frame 028310/0218 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 18, 2010
From: CONNER, WILLIAM G.
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 024852/0994 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 27, 2010
From: SCHULTZ, THOMAS E.
To: SIEMENS WATER TECHNOLOGIES CORP.
Reel/Frame 024746/0966 →
Continuity (2)
Provisional Application 61224011 · Jul 8, 2009
Related Publication 20110006002A1 · Jan 13, 2011