Biofilm reduction in pressure driven membrane-based water treatment systems
A process for reducing and/or eliminating biofilm growth and removal thereof formed during operation of pressure-induced filtration systems such as reverse osmosis systems. The systems and methods are particularly suitable for use with pressure-driven membrane filtration, including microfiltration, ultrafiltration, nanofiltration and reverse osmosis.
1 . A process for reducing biofilm and/or preventing the formation of the biofilm in the vicinity of a membrane used in a pressurized membrane based water treatment system, the process comprising:
contacting the biofilm with a chlorine dioxide solution, wherein the chlorine dioxide is at a concentration of at least 0.1 milligrams per liter; and
maintaining the chlorine dioxide solution within the water treatment system in an amount effective to prevent formation of the biofilm.
2 . The process of claim 1 , wherein the chlorine dioxide solution recirculates through the membrane and into a permeate.
3 . The process of claim 1 , wherein the chlorine dioxide solution is introduced intermittently based on a predetermined volume of water processed in the water treatment system.
4 . The process of claim 1 , wherein the chlorine dioxide solution is at a concentration effective to provide a residual chlorine dioxide concentration in a permeate downstream from the membrane of at least 1 part per million.
5 . The process of claim 1 , wherein the water treatment system is a selected one of a reverse osmosis system, a microfiltration system, a nanofiltration system, and an ultrafiltration system.
6 . The process of claim 1 , wherein the membrane is selected from a group consisting of ceramic, cellulose acetate, polyamide, polyester, fiberglass, sulfonated polysulfone, acrylonitrile, polyvinylidene fluoride, polycarbonate, polypropylene, polyethylene, and polytetrafluoroethylene.
7 . A process for detecting and preventing biofouling in a reverse osmosis system, the process comprising:
monitoring a normalized permeate flow of the reverse osmosis system by measuring water temperature, average applied temperature, average feed osmotic pressure, permeate pressure, and actual permeate flow;
comparing the normalized permeate flow to a start up normalized permeate flow; and
introducing a chlorine dioxide solution into the reverse osmosis system when a percentage difference between the normalized permeate flow and the start up permeate flow is a predetermined percentage, wherein the chlorine dioxide is introduced at a concentration of at least 1 part per million.
8 . The process of claim 7 , wherein the percentage difference between the normalized permeate flow and the start up permeate flow is greater than 15%.
9 . The process of claim 7 , wherein the membrane is selected from a group consisting of ceramic, cellulose acetate, polyamide, polyester, fiberglass, sulfonated polysulfone, acrylonitrile, polyvinylidene fluoride, polycarbonate, polypropylene, polyethylene, and polytetrafluoroethylene.
10 . The process of claim 7 , wherein the chlorine dioxide solution is at a concentration effective to provide a residual chlorine dioxide concentration in a permeate downstream from the membrane of less than 1 part per million.
11 . The process of claim 7 , further comprising applying a normal flux decline to the normal permeate flow to account for compaction of the membrane.
12 . The process of claim 7 , wherein the chlorine dioxide solution is at a concentration effective to provide a residual chlorine dioxide concentration in a permeate downstream from the membrane of at least 1 part per million.
13 . The process of claim 7 , wherein the start up normalized permeate flow rate is determined at time zero to about 100 hours of operation.
14 . The process of claim 7 , wherein the percentage difference between the normalized permeate flow and the startup permeate flow decreases after introducing the chlorine dioxide solution.