US2010213123A1PendingUtilityA1
Ballasted sequencing batch reactor system and method for treating wastewater
Individually held — no corporate assignee on recordPriority: Jan 9, 2007Filed: Apr 27, 2010Published: Aug 26, 2010
Est. expiryJan 9, 2027(~0.5 yrs left)· nominal 20-yr term from priority
C02F 3/1263C02F 1/5236C02F 1/38C02F 1/36C02F 2305/12Y02W10/10C02F 1/488C02F 3/1284C02F 1/56
54
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Claims
Abstract
A ballasted sequencing batch reactor system for treating wastewater including one or more sequencing batch reactors. A weighting agent impregnation subsystem is configured to mix biological flocs and weighting agent to form weighted biological flocs. A weighting agent recovery subsystem is configured to recover weighting agent from the weighted biological flocs and reintroduce the recovered weighting agent to the weighting agent impregnation subsystem.
Claims
exact text as granted — not AI-modified1 . A ballasted sequencing batch reactor system for treating wastewater comprising:
one or more sequencing batch reactors; a weighting agent impregnation subsystem configured to mix biological flocs and weighting agent to form weighted biological flocs; a weighting agent recovery subsystem configured to recover weighting agent from the weighted biological flocs and reintroduce the recovered weighting agent to the weighting agent impregnation subsystem.
2 . The system of claim 1 further including a sludge storage tank configured to receive settled sludge from the one or more sequencing batch reactors, store the settled sludge therein, and regulate the flow of settled sludge to weighting agent recovery subsystem.
3 . The system of claim 1 in which the weighting agent recovery subsystem includes a separator subsystem for separating the weighting agent from the weighted biological flocs.
4 . The system of claim 3 in which the separator subsystem includes a shear mill.
5 . The system of claim 3 in which the separator subsystem includes a centrifugal separator.
6 . The system of claim 3 in which the separator subsystem includes an ultrasonic separator.
7 . The system of claim 3 in which the separator subsystem includes a shear mill and a wet drum magnetic separator.
8 . The system of claim 3 in which the separator subsystem includes a shear mill and a centrifugal separator.
9 . The system of claim 3 in which the separator subsystem includes an ultrasonic separator and a wet drum magnetic separator.
10 . The system of claim 3 in which the separator subsystem includes an ultrasonic separator and a centrifugal separator.
11 . The system of claim 4 in which the shear mill includes a rotor and a stator, wherein the rotor and/or the stator include slots sized as to optimize separation of weighting agent from the weighted biological flocs.
12 . The system of claim 1 in which the weighting agent impregnation subsystem includes an impregnation tank and at least one mixer.
13 . The system of claim 1 in which the capacity of the system is increased by reducing the duration of a settle phase.
14 . The system of claim 1 in which the one or more sequencing batch reactors are configured to decant clear effluent from settled sludge to provide a treated effluent.
15 . The system of claim 14 in which the weighted biological flocs enhance the quality of the treated effluent by reducing the concentration of suspended solids and related contaminants therein.
16 . The system of claim 1 further including a wasting subsystem for wasting settled sludge from the weighting agent recovery subsystem to control a population of microorganisms in a mixed liquor in the one or more sequencing batch reactors.
17 . The system of claim 16 in which the capacity of the system is increased by increasing the concentration of the mixed liquor in the one or more sequencing batch reactors by reducing the amount of settled sludge wasted by a wasting subsystem.
18 . The system of claim 17 in which the capacity of the system is increased by reducing the duration of a react phase.
19 . The system of claim 17 in which the amount of settled sludge wasted by the wasting subsystem is reduced to increase the concentration of mixed liquor suspended solids for enhancing nitrification and/or de-nitrification of ammonia in the mixed liquid.
20 . The system of claim 19 in which nitrification is enhanced by increasing the amount of dissolved oxygen introduced into the one or more sequencing batch reactors.
21 . The system of claim 1 in which a coagulant is added to the one or more sequencing batch reactors for removing phosphorus by precipitation and/or coagulation.
22 . The system of claim 1 in which a flocculant is added to the one or more sequencing batch reactors for enhancing settling and thickening of the weighted biological flocs and for providing agglomeration of non-impregnated biological flocs and/or partially impregnated biological flocs with weighted biological flocs.
23 . The system of claim 1 in which the weighting agent impregnation subsystem includes a venturi mixer/eductor.
24 . The system of claim 1 in which a majority of the weighting agent has a particle size less than about 100 μm.
25 . The system of claim 1 in which a majority of the weighting agent has a particle size less than about 40 μm.
26 . The system of claim 1 in which a majority of the weighting agent has a particle size less than about 20 μm.
27 . The system of claim 1 in which the weighting agent includes magnetite.
28 . The system of claim 1 further including a mixer disposed in each of the one or more sequencing batch reactors for maintaining the suspended solids or the mixed liquor in suspension.
29 . A method for treating wastewater using one or more sequencing batch reactors, the method comprising:
a) receiving influent wastewater in the one or more sequencing batch reactors; b) forming biological flocs in the one or more sequencing batch reactors; c) impregnating weighting agent into the biological flocs to form weighted biological flocs; and d) recovering weighting agent from the weighted biological flocs to reintroduce the weighting agent to step c).
30 . The method of claim 29 further including the step of separating the weighting agent from the weighted biological flocs.
31 . The method of claim 29 further including the step of collecting the weighting agent and recycling the weighting agent to step c).
32 . The method of claim 29 further including the step of providing weighting agent in which the majority of the weighting agent has a particle size less than about 100 μm.
33 . The method of claim 29 further including the step of providing weighting agent in which the majority of the weighting agent has a particle size less than about 40 μm.
34 . The method of claim 29 further including the step of providing weighting agent in which the majority of the weighting agent has a particle size less than about 20 μm.
35 . The method of claim 29 further including the step of introducing dissolved oxygen to a population of microorganisms to promote growth of biological flocs in a mixed liquor defined by a concentration of mixed liquor suspended solids.
36 . The method of claim 35 further including the step of introducing a flocculant to the mixed liquor to enhance settling and thickening of the weighted biological flocs and to establish agglomeration of non-impregnated biological flocs and/or partially impregnated biological flocs with the weighted biological flocs.
37 . The method of claim 35 further including the step of separating and collecting the weighted biological flocs from the mixed liquor in the one or more sequencing batch reactors to provide a secondary effluent and a settled sludge.
38 . The method of claim 37 further including the step of recycling the majority of the settled sludge to step b).
39 . The method of claim 37 further including the step of decanting the clean effluent from the settled sludge in the one or more sequencing batch reactors to provide a treated effluent.
40 . The method of claim 37 further including the step of wasting the remaining settled sludge using a wasting subsystem to control the population of the microorganisms in the mixed liquor.
41 . The method of claim 29 further including the step of increasing the capacity of the system by reducing the duration of a settle phase.
42 . The method of claim 39 further including the step of enhancing the quality of the treated effluent by reducing the concentration of suspended solids and related contaminants therein.
43 . The method of claim 27 further including the step of wasting settled sludge from the weighting agent recovery subsystem to control a population of microorganisms in a mixed liquor in the one or more sequencing batch reactors.
44 . The method of claim 43 further including the step of increasing the capacity of the system by increasing the concentration of the mixed liquor in the one or more sequencing batch reactors by reducing the amount of settled sludge wasted by a wasting subsystem.
45 . The method of claim 44 further including the step of increasing the capacity of the system by reducing the duration of a react phase.
46 . The method of claim 43 further including the step of reducing the amount of settled sludge wasted by the wasting subsystem to increase the concentration of mixed liquor suspended solids which enhances nitrification and/or de-nitrification of ammonia in the mixed liquid.
47 . The method of claim 35 further including the step of enhancing nitrification by increasing the amount of dissolved oxygen introduced into the one or more sequencing batch reactors.
48 . The method of claim 29 in which the weighting agent is impregnated into the biological flocs in step b) by mixing the mixed liquor and the biological flocs at a predetermined energy level.Join the waitlist — get patent alerts
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