Water treatment assembly including hyperfiltration module and cation exchange resin
View Patent ↗A water treatment assembly ( 10 ) and method for its operation, comprising a spiral wound hyperfiltration membrane module ( 12 ) connected to: i) a feed line ( 14 ) adapted for connection to a source of pressurized feed water, ii) a permeate line ( 16 ) adapted for connection to a dispenser of treated water and iii) a concentrate line ( 18 ) adapted for connection with a drain; wherein the assembly includes a pressurizable reservoir ( 22 ) containing weak acid cation exchange resin ( 25 ) and further includes at least one valve for selectively diverting flow of pressurized feed water along the feed line ( 14 ), through the reservoir ( 22 ) and returning to the feed line ( 14 ) prior to passing through the hyperfiltration membrane module ( 12 ).
1. A process of operating a water treatment assembly, wherein the assembly comprises:
a spiral wound hyperfiltration membrane module comprising at least one membrane envelope and feed channel spacer sheet wound about a permeate collection tube, wherein the module is connected to:
i) a feed line adapted for connection to a source of pressurized feed water,
ii) a permeate line adapted for connection to a dispenser of treated water and
iii) a concentrate line adapted for connection with a drain;
wherein the assembly further comprises a pressurizable reservoir containing weak acid cation resin and at least one valve for selectively diverting flow of pressurized feed water along the feed line, through the reservoir and returning to the feed line prior to passing through the module; and wherein the assembly includes at least one of:
a valve located along the permeate line adapted to increase resistance to flow, and
a valve located along the concentrate line adapted to decrease resistance to flow;
wherein the process comprises introducing pressurized feed water into the feed line and operating the assembly in three distinct modes comprising a standard mode, a flushing mode, and a dormant mode, wherein the majority of pressurized feed water bypasses the reservoir during the standard operating mode, the majority of pressurized feed water passes through the reservoir during the flushing mode, and no pressurized feed water passes through the module during the dormant mode, and wherein the flushing mode precedes the dormant mode such that feed water flows from the reservoir to the module and is retained within the module during the dormant mode, and during the flushing mode, at least one of the following occurs:
a) the valve located along the permeate line is positioned to selectively increase resistance to flow and
b) the valve located along the concentrate line is positioned to selectively decrease resistance to flow.
2. The process of claim 1 , wherein the average time spent in the flushing mode is between 1% and 20% of time spent in the standard mode.
3. The process of claim 1 , wherein the duration of the flushing mode is less than 1 minute.
4. The process of claim 1 , wherein the hyperfiltration membrane module has a feed spacer free volume that is less than 0.2 liter per square meter of membrane.