Wastewater treatment system and method
Disclosed is a system and method for treating municipal and sanitary wastewater that uses only mechanical devices and processes, which eliminates biological processes and settling tanks. The system includes a three-output axial-flow type separator that separates wastewater into three fluid streams according to the specific gravity of the solids within the fluid streams. The lighter-than-water and heavier-than-water solids streams are combined and the resultant sludge is mechanically dewatered without intermediary biological-process systems or sedimentation. The partially clarified water component can be directly filtered by a membrane filter and optionally optically or chemically disinfected for reuse or disposal. The system advantageously simplifies municipal and sanitary wastewater treatment eliminating traditional primary and secondary treatment stages, and significantly reducing the system's operational footprint. The system and method can be scaled to very large municipal systems.
1. A system for treating sanitary wastewater, comprising:
a three-output axial-flow type separator includes a first outlet port discharging a lighter-than-water solids stream, a second outlet port discharging a heavier-than-water solids stream, and a third outlet port discharging a partially clarified water stream;
a mechanical sludge-dewatering device; and
the lighter-than-water solids stream and the heavier-than-water solids stream, in combination, feed the mechanical sludge-dewatering device without any intermediary biological-process systems and without sedimentation devices.
2. The system of claim 1 , wherein:
the three-output axial-flow type separator including an inlet that receives the sanitary wastewater without a biological pre-treatment stage and without a sedimentation pre-treatment stage.
3. The system of claim 2 , further comprising:
a membrane filter; and
the partially clarified water stream feeds the membrane filter without any intermediary biological processes systems and without sedimentation devices.
4. The system of claim 3 , wherein:
the membrane filter discharges a filtration wastewater; and
the filtration wastewater feeds the inlet.
5. The system of claim 2 , wherein:
the mechanical sludge-dewatering device includes a discharge of a mechanical sludge-dewatering wastewater; and
the mechanical sludge-dewatering wastewater feeds into the inlet.
6. The system of claim 1 , further comprising:
a membrane filter; and
the partially clarified water stream feeds the membrane filter without any intermediary biological processes systems and without sedimentation devices.
7. The system of claim 6 , wherein:
the three-output axial-flow type separator includes an inlet;
the membrane filter discharges a filtration wastewater; and
the filtration wastewater feeds the inlet.
8. The system of claim 1 , further comprising:
the three-output axial-flow type separator is a first three-output axial-flow type separator and a second three-output axial-flow type separator;
the first outlet port is a second three-output axial-flow type separator first outlet;
the second outlet port is a second three-output axial-flow type separator second outlet; and
a first three-output axial-flow type separator lighter-than-water solids stream and a first three-output axial-flow type separator heavier-than-water solids stream, in combination, feed a second three-output axial-flow type separator inlet.
9. The system of claim 1 , wherein:
the three-output axial-flow type separator includes an inlet;
the mechanical sludge-dewatering device includes a discharge of a mechanical sludge-dewatering wastewater; and
the mechanical sludge-dewatering wastewater feeds into the inlet.
10. The system of claim 1 , further including:
the three-output axial-flow type separator includes an inlet to receive inlet wastewater; and
a gas bubble injection device positioned to inject gas bubbles into the inlet wastewater.
11. A system for treating sanitary wastewater, comprising:
a three-output axial-flow type separator including a first outlet port discharging a lighter-than-water solids stream, a second outlet port discharging a heavier-than-water solids stream, and a third outlet port discharging a partially clarified water stream;
a mechanical sludge-dewatering device;
the lighter-than-water solids stream and the heavier-than-water solids stream in combination creates a combined stream that feeds the mechanical sludge-dewatering device; and
the combined stream having solids concentration capable of directly feeding the mechanical sludge-dewatering device.
12. The system of claim 11 , further including a membrane filter receiving the partially clarified water stream.
13. The system of claim 12 , wherein:
the three-output axial-flow type separator includes an inlet;
the membrane filter discharges a filtration wastewater; and
the filtration wastewater feeds into the inlet.
14. The system of claim 11 , wherein:
the three-output axial-flow type separator includes an inlet;
the mechanical sludge-dewatering device includes a discharge of a mechanical sludge-dewatering wastewater; and
the mechanical sludge-dewatering wastewater feeds into the inlet.
15. A method for treating sanitary wastewater, comprising:
combining a lighter-than-water solids stream and a heavier-than-water solids stream from corresponding first and second outlets of a three-output axial-flow type separator, creating a combined stream; and
sludge-dewatering the combined stream using a mechanical sludge-dewatering device without intermediary biological processes and without sedimentation.
16. The method of claim 15 , further comprising:
receiving a sanitary wastewater stream into the three-output axial-flow type separator without pretreating the sanitary wastewater by biological processes and without pretreating the sanitary wastewater by sedimentation.
17. The method of claim 15 , further comprising:
processing a partially clarified water stream discharged from the three-output axial-flow type separator through a membrane filter without any intermediary biological processes and without sedimentation.
18. The method of claim 17 , further comprising:
adding surfactants to the partially clarified water stream before the membrane filter.
19. The method of claim 15 , further comprising:
determining a solids concentration of the combined stream;
retrieve a solids concentration predetermined range; and
dynamically change an input flow rate to the three-output axial-flow type separator based on comparing the solids concentration of the combined stream and the solids concentration predetermined range.
20. The method of claim 15 , further comprising:
determining a solids concentration of the combined stream;
retrieve a solids concentration predetermined range; and
dynamically change a flow rate of a partially clarified water stream discharged from the three-output axial-flow type separator, based on comparing the solids concentration of the combined stream and the solids concentration predetermined range.
21. The method of claim 15 , further comprising:
adding polymers to an inlet of the three-output axial-flow type separator to facilitate discharge of suspended solids.
22. The method of claim 15 , further comprising:
receiving a sanitary wastewater stream into the three-output axial-flow type separator; and
injecting gas bubbles into the sanitary wastewater stream before the sanitary wastewater stream enters the three-output axial-flow type separator.
23. A method for treating sanitary wastewater, comprising:
creating a combined stream by combining a lighter-than-water solids stream and a heavier-than-water solids stream from corresponding first and second outlets of a three-output axial-flow type separator; and
sludge-dewatering the combined stream using a mechanical sludge-dewatering device, the combined stream having solids concentration capable of directly feeding the mechanical sludge-dewatering device.
24. The method of claim 23 , further comprising:
processing a partially clarified water stream discharged from the three-output axial-flow type separator through a membrane filter.
25. The method of claim 24 , further comprising:
adding surfactants to the partially clarified water stream before the membrane filter.
26. The method of claim 23 , further comprising:
determining the solids concentration of the combined stream;
retrieve a solids concentration predetermined range; and
dynamically change an input flow rate to the three-output axial-flow type separator based on comparing the solids concentration of the combined stream and the solids concentration predetermined range.
27. The method of claim 23 , further comprising:
determining the solids concentration of the combined stream;
retrieve a solids concentration predetermined range; and
dynamically change a flow rate of a partially clarified water stream discharged from the three-output axial-flow type separator, based on comparing the solids concentration of the combined stream and the solids concentration predetermined range.
28. The method of claim 23 , further comprising:
adding polymers to an inlet of the three-output axial-flow type separator to facilitate discharge of suspended solids.
29. The method of claim 23 , further comprising:
receiving a sanitary wastewater stream into the three-output axial-flow type separator; and
injecting gas bubbles into the sanitary wastewater stream before the sanitary wastewater stream enters the three-output axial-flow type separator.