Techniques for managing scale formation in water filtration systems and a reverse osmosis (RO) and nanofiltration (NF) system implementing same
The present disclosure is directed to filtering technologies that combine elements of continuous and batch NF/RO based on the constraints of the end-user facility to achieve a target balance between, for instance, recovery and power consumption, and to reduce long term operating cost of a plant. A method for extending batch operation into a second induction period with antiscalant injection is also disclosed herein, with the second induction period allowing for yet higher water recovery.
1. A filter system comprising:
at least one inlet fluidly coupled to at least one feed stream;
at least one filter membrane fluidly coupled to the at least one inlet to receive feed water from the at least one feed stream;
at least one pump configured to generate a pressure to displace the feed water from the at least one feed stream into the at least one filter membrane and produce an output permeate stream; and
a controller configured to:
cause a first driving signal to be provided to the at least one pump to cause the generated pressure at the at least one filter membrane that exceeds an osmotic pressure associated with the at least one filter membrane and substantially maintain a first target recovery rate, the first target recovery rate being greater than a maximum non-scaling recovery rate for the at least one filter membrane and having an associated duration of time prior to when a pre-antiscalant maximum non-scaling recovery state is reached for the at least one filter membrane;
determine when the pre-antiscalant maximum non-scaling recovery state is reached for the filter membrane; and
in response to determining the pre-antiscalant maximum non-scaling recovery state is reached, cause one or a plurality of antiscalant doses to be provided to the filter membrane to increase an amount of time between when a post-antiscalant maximum non-scaling recovery state is reached and when subsequent scaling and/or fouling of the filter membrane occurs.
2. The filter system of claim 1 , wherein causing the first driving signal to be provided to the at least one pump further comprises causing the at least one pump to monotonically increase pressure beyond osmotic pressure associated with the at least one filter membrane after the antiscalant is introduced to maintain the first target recovery rate during at least a portion of a second induction period.
3. The filter system of claim 1 , wherein the at least one filter membrane comprises at least one high-pressure filter membrane with a pressure casing capable of withstanding at least 90 bar of pressure.
4. The filter system of claim 1 , wherein the at least one filter membrane comprises at least first and second filter membranes, each of the first and second filter membranes providing at least a portion of first and second filter stages, respectively.
5. The filter system of claim 4 , further comprising a filter valve arrangement to switchably fluidly couple the first and/or second filter membranes to the at least one feed stream.
6. The filter system of claim 1 , wherein the at least one inlet fluidly couples to a bleed of a second filter system such that the at least one feed stream comprises concentrate from the second filter system.
7. The filter system of claim 1 , wherein the wherein the at least one inlet fluidly couples to an outlet of a second filter system such that the at least one feed stream comprises permeate output by the second filter system.
8. The filtration system of claim 1 , wherein the controller is further configured to detect that the pre-antiscalant maximum non-scaling recovery state has been reached based on a quality measurement of the output permeate stream.
9. The filtration system of claim 1 , wherein the controller is further configured to detect the pre-antiscalant maximum non-scaling recovery state prior to reaching the maximum non-scaling recovery state.
10. The filtration system of claim 9 , wherein the controller is further configured to detect the pre-antiscalant maximum non-scaling recovery state based on a constant duration of time.
11. The filtration system of claim 9 , wherein the controller is further configured to detect the pre-antiscalant maximum non-scaling recovery state based on a concentration of antiscalant within the at least one feed stream.
12. The filtration system of claim 9 , wherein the controller further comprises a first induction period and a second induction period, the second induction period occurring after the first induction period, the first induction period ending when the pre-antiscalant maximum non-scaling recovery state is reached and the second induction period extending from when the one or plurality of antiscalant doses are provided to the filter membrane to when the post-antiscalant maximum non-scaling recovery state is reached.
13. The filtration system of claim 12 , wherein the second induction period is equal to or longer than the first induction period.
14. The filtration system of claim 12 , wherein the second induction period has an overall duration that is at least half an overall duration of the first induction period.
15. The filtration system of claim 1 , wherein the controller is further configured to cause the at least one pump to exert a pressure of 90-120 bar on the filter membrane.
16. The filtration system of claim 1 , wherein the target recovery rate is 100% or the target recovery rate is less than 100% and greater than the maximum non-scaling recovery rate of the filter membrane.