Membrane bioreactor system using reciprocating membrane
The present invention relates to membrane bioreactor (“MBR”) system that includes a mechanical membrane reciprocation system to reduce or eliminate membrane fouling. The disclosed MBR system can be operated with higher flux and lower fouling than MBR systems using air scouring. Furthermore the system can remove nitrogen and phosphorous with one RAS and one or no internal recirculation line. The membrane can be reciprocated by a low RPM motor connected to a pulley via belt to rotate rotor to convert rotational motion into reciprocating motion of membrane. Various mechanical means can also be employed to create the reciprocating motion.
1. A reciprocating membrane bioreactor system comprising:
a biological treatment train ( 50 ) for receiving influent ( 10 ) to be treated, the biological treatment train ( 50 ) producing treated wastewater;
a membrane tank ( 60 ) housing a membrane ( 70 ), the treated wastewater from the biological treatment train ( 50 ) being filtered through the membrane ( 70 ) to produce effluent ( 40 );
a reciprocation apparatus ( 80 ) for reciprocating the membrane ( 70 ), the reciprocation reducing fouling on the membrane ( 70 ),
wherein the reciprocation apparatus ( 80 ) comprises a motor ( 103 ) connected to a pulley ( 101 ) via a belt ( 102 ) to rotate a rotor ( 100 ) so as to convert rotational motion into reciprocating motion of a sliding frame ( 90 ) through a shaft ( 110 ), wherein the sliding frame is interconnected to the membrane so as to move the membrane submerged in the membrane tank in a horizontal reciprocating motion determined by a speed at which the rotor rotates.
2. The reciprocating membrane bioreactor system as described in claim 1 wherein shock load due to reciprocating motion is reduced by a dampener ( 94 ) in between the sliding frame ( 90 ) and the shaft ( 110 ), and wherein the sliding frame ( 90 ) is configured to move along sliding rails with linear bearings and pillow block ( 91 ) supports.
3. The reciprocating membrane bioreactor system as described in claim 1 wherein shock load due to reciprocating motion is reduced by a dampener ( 94 ) in between the sliding frame ( 90 ) and the shaft ( 110 ), and wherein the sliding frame ( 90 ) is configured to move along sliding rails with linear bearings and pillow block ( 91 ) supports.
4. The reciprocating membrane bioreactor system as described in claim 1 wherein the biological treatment train comprises:
an anaerobic treatment tank ( 51 ) for biologically treating the influent in the absence of dissolved oxygen;
an anoxic treatment tank ( 52 ) for denitrifying the treated wastewater under oxygen-depleted conditions;
an aerobic treatment tank ( 53 ) for biologically treating the wastewater in the presence of dissolved oxygen; and
wherein the membrane tank ( 60 ) for produces effluent through the membranes ( 70 ) being reciprocated repetitively via the reciprocation apparatus ( 80 ).
5. The reciprocating membrane bioreactor system as described in claim 4 further comprising an activated sludge return line ( 31 ) for delivering the activated sludge from the membrane tank ( 60 ) to the anoxic treatment tank ( 52 ) and an internal recirculation line ( 32 ) from the anoxic tank ( 52 ) to the anaerobic tank ( 51 ).
6. The reciprocating membrane bioreactor system as described in claim 4 further comprising an activated sludge return line ( 33 ) for delivering the activated sludge from the membrane tank ( 60 ) to the anaerobic treatment tank ( 51 ) and an internal recirculation line ( 34 ) from the aerobic tank ( 53 ) to the anoxic tank ( 52 ).
7. The reciprocating membrane bioreactor system as described in claim 4 further comprising an activated sludge return line ( 31 ) for delivering the activated sludge from the membrane tank ( 60 ) to the anoxic treatment tank ( 52 ).
8. The reciprocating membrane bioreactor system as described in claim 1 wherein the biological treatment train comprises:
an anoxic treatment tank ( 52 ) for denitrifying the treated wastewater under oxygen-depleted conditions;
an aerobic treatment tank ( 53 ) for biologically treating the wastewater in the presence of dissolved oxygen; and
the membrane tank ( 60 ) produces effluent through the membranes ( 70 ) being reciprocated repetitively via the reciprocation apparatus ( 80 ).
9. The reciprocating membrane bioreactor system as described in claim 8 further comprising an activated sludge return line ( 31 ) that delivers the activated sludge from the membrane tank ( 60 ) to the anoxic treatment tank ( 52 ).
10. The reciprocating membrane bioreactor system as described in claim 1 further comprising a recirculation line from the membrane tank ( 60 ) to the biological treatment train ( 50 ) providing an oxygen-depleted condition.
11. A reciprocating membrane bioreactor system comprising:
a biological treatment train ( 50 ) for receiving influent ( 10 ) to be treated, the biological treatment train ( 50 ) producing treated wastewater;
a membrane ( 70 ), the treated wastewater from the biological treatment train ( 50 ) being filtered through the membrane ( 70 ) to produce effluent ( 40 );
a reciprocation apparatus ( 80 ) for reciprocating the membrane ( 70 ), the reciprocation reducing fouling on the membrane ( 70 ) and providing oxygen depleted conditions in the biological treatment train ( 50 ),
wherein the reciprocation apparatus ( 80 ) comprises a motor ( 103 ) connected to a pulley ( 101 ) via a belt ( 102 ) to rotate a rotor ( 100 ) so as to convert rotational motion into reciprocating motion of a sliding frame ( 90 ) through a shaft ( 110 ), wherein the sliding frame is interconnected to the membrane so as to move the membrane submerged in a membrane tank in a horizontal reciprocating motion determined by a speed at which the rotor rotates.
12. The reciprocating membrane bioreactor system as described in claim 11 , wherein the biological treatment train ( 50 ) comprises an aerobic treatment tank ( 53 ) for biologically treating the wastewater in the presence of dissolved oxygen.
13. The reciprocating membrane bioreactor system as described in claim 11 , wherein the biological treatment train ( 50 ) comprises:
an anoxic treatment tank ( 52 ) for denitrifying the treated wastewater under oxygen-depleted conditions;
an aerobic treatment tank ( 53 ) for biologically treating the wastewater in the presence of dissolved oxygen; and
an activated sludge return line ( 31 ) delivers the activated sludge from the aerobic treatment tank ( 53 ) to the anoxic treatment tank ( 52 ).
14. The reciprocating membrane bioreactor system as described in claim 11 , the biological treatment train ( 50 ) comprises;
an anaerobic treatment tank ( 51 ) for biologically treating the influent in the absence of dissolved oxygen;
an anoxic treatment tank ( 52 ) for denitrifying the treated wastewater under oxygen-depleted conditions;
an aerobic treatment tank ( 53 ) for biologically treating the wastewater in the presence of dissolved oxygen;
an activated sludge return line ( 31 ) delivers the activated sludge from the aerobic treatment tank ( 53 ) to the anoxic treatment tank ( 52 ); and
an internal recirculation line ( 32 ) from the anoxic tank ( 52 ) to the anaerobic tank ( 51 ).
15. The reciprocating membrane bioreactor system as described in claim 11 , wherein the biological treatment train ( 50 ) comprises:
an anaerobic treatment tank ( 51 ) for biologically treating the influent in the absence of dissolved oxygen;
an anoxic treatment tank ( 52 ) for denitrifying the treated wastewater under oxygen-depleted conditions;
an aerobic treatment tank ( 53 ) for biologically treating the wastewater in the presence of dissolved oxygen;
an activated sludge return line ( 33 ) for delivering the activated sludge from the aerobic treatment tank ( 53 ) to the anaerobic treatment tank ( 51 ); and
an internal recirculation line ( 34 ) from the aerobic tank ( 53 ) to the anoxic tank ( 52 ).
16. The reciprocating membrane bioreactor system as described in claim 11 , wherein the biological treatment train ( 50 ) comprises:
an anoxic treatment tank ( 52 ) for denitrifying the treated wastewater under oxygen-depleted conditions;
an anaerobic treatment tank ( 51 ) for biologically treating the influent in the absence of dissolved oxygen;
an aerobic treatment tank ( 53 ) for biologically treating the wastewater in the presence of dissolved oxygen; and
an activated sludge return line ( 31 ) delivers the activated sludge from the aerobic treatment tank ( 53 ) to the anoxic treatment tank ( 52 ).