Combined microfiltration or ultrafiltration and reverse osmosis processes
View Patent ↗A water treatment system combines a microfiltration or ultrafiltration membrane system with a downstream reverse osmosis membrane system. The MF or UF system has multiple trains of immersed membrane modules. The trains are connected to a common permeate pump. The permeate pump discharges directly into the inlet of an RO feed pump. The membrane trains are each subjected to the same suction. The permeate pumps are operated to provide the required flow to the RO feed pump at or above the minimum inlet pressure of the RO feed pump.
1. A water treatment system comprising,
a microfiltration or ultrafiltration membrane system comprising multiple trains of immersed membranes;
a reverse osmosis membrane system;
one set of one or more permeate pumps connected to all of the trains;
a set of one or more feed pumps for the reverse osmosis system,
wherein an outlet from the set of one or more permeate pumps is connected by a closed passage to an inlet of the set of one or more feed pumps,
a flowmeter configured to read a rate of flow of permeate from the reverse osmosis system;
one or more variable speed drive units connected to the set of one or more permeate pumps; and
a controller adapted to receive signals from the flow meter and adjust the speed of the variable speed drive units in correspondence with the received signals to modulate the speed of the permeate pump to produce a desired rate of flow of permeate from the reverse osmosis system.
2. The water treatment system of claim 1 comprising a feed water manifold connected to a feed water inlet of each of a plurality of tanks housing the trains, wherein the feed water inlets are below the water level in the tanks.
3. The water treatment system of claim 1 having 5 or more trains.
4. A water treatment process comprising the steps of,
providing a flow of feed water to multiple trains of immersed microfiltration or ultrafiltration membranes;
applying a suction pressure generated at the inlet of one or more permeate pumps to a header connected to all of the trains, to withdraw a permeate from the trains;
flowing the permeate under pressure from an outlet of the one or more permeate pumps to an inlet of one or more feed pumps of a reverse osmosis membrane system; and
varying the speed of the one or more permeate pumps as required to produce a desired flow rate of the permeate from the reverse osmosis membrane system.
5. The process of claim 4 wherein the desired flow rate of the permeate from the reverse osmosis membrane system is a generally constant flow rate.
6. The process of claim 4 wherein the pressure is 125 kPa or more.
7. The process of claim 4 further comprising steps of determining whether the flux of a train is exceeding a predetermined maximum flux and, if so, partially closing a flow control valve between the train and the one or more permeate pumps.
8. The process of claim 7 wherein determining the flux of a train comprises shutting an inlet to a tank containing the train, measuring the rate of reduction in water level in the tank, and calculating the flux of the train based on the measured rate or reduction.
9. The process of claim 7 wherein determining the flux of a train comprises measuring the water level in a tank containing the train and calculating or determining the flux of the train based on the measured water level.
10. The process of claim 7 wherein determining the flux of a train comprises determining a difference between the static pressure in an inlet to a tank containing the train and a water level in that tank and calculating or determining the flux of the train based on the difference.