Oxidizing compositions for removing sulfur compounds from hydrocarbon fuels and wastewater
US-2024400426-A1 · Dec 5, 2024 · US
US11939234B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11939234-B2 |
| Application number | US-201916960699-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 16, 2019 |
| Priority date | Jan 19, 2018 |
| Publication date | Mar 26, 2024 |
| Grant date | Mar 26, 2024 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A water purification apparatus and method for optimizing efficiency of the water purification apparatus comprising a fluid circuit including a Reverse Osmosis, RO, unit ( 3 ), providing a permeate flow, and an electrically controlled deionization unit ( 4 ) downstream the RO unit ( 3 ) receiving at least part of the permeate flow. The method comprises obtaining (S 1 ) a value indicative of power consumption by the electrically controlled deionization unit and determining (S 2 ) whether the obtained value indicative of the power consumption meets at least one criterion. The method further comprises controlling recirculation of reject water produced by the water purification apparatus, based on a result of the determining (S 2 ), in order to optimize efficiency of the water purification apparatus.
Opening claim text (preview).
The invention claimed is: 1. A method for optimizing efficiency of a water purification apparatus comprising a fluid circuit including a reverse osmosis (RO) unit that provides a permeate flow, and an electrically controlled deionization unit downstream from the RO unit that receives at least part of the permeate flow, the method comprising: obtaining, using a sensor, a current or voltage value indicative of power consumption by the electrically controlled deionization unit; determining whether the obtained current or voltage value meets at least one power consumption criterion; and controlling, using one or more valve units, recirculation of reject water produced by the water purification apparatus based on whether the obtained current or voltage value meets the at least one power consumption criterion, wherein the controlling comprises at least one of: increasing the recirculation of reject water in response to determining that the obtained current or voltage value indicative of power consumption is below a first threshold, or decreasing the recirculation of reject water in response to determining that the obtained current or voltage value indicative of power consumption is above a second threshold. 2. The method according to claim 1 , wherein the reject water comprises a reject flow from the RO unit, and the controlling comprises controlling a recirculation of the reject flow from the RO unit to an incoming flow of the RO unit. 3. The method according to claim 1 , wherein the reject water comprises a reject flow from the electrically controlled deionization unit, and the controlling comprises controlling a recirculation of the reject flow from the electrically controlled deionization unit to an incoming flow of the RO unit. 4. The method according to claim 1 , further comprising determining whether a recovery rate of the water purification apparatus meets at least one recovery rate criterion, wherein the recovery rate is a ratio of a product flow rate from the deionization unit to an incoming flow rate of incoming water to the RO unit. 5. The method according to claim 4 , further comprising determining a quality of the incoming water, indicative of a number of ions in the incoming water, based on at least one of whether (i) the obtained current or voltage value meets the at least one power consumption criterion, or (ii) the recovery rate of the water purification apparatus meets the at least one recovery rate criterion. 6. The method according to claim 5 , further comprising determining a high quality of the incoming water in response to: determining that the obtained current or voltage value indicative of power consumption is below or equal to the first threshold, wherein the first threshold is equal to or lower than the second threshold, and determining the recovery rate of the water purification apparatus is above or equal to a first recovery rate threshold, wherein a second recovery rate threshold is equal to or lower than the first recovery rate threshold, and wherein the high quality indicates a low number of ions in the incoming water. 7. The method according to claim 6 , further comprising determining a low quality of the incoming water in response to: determining that the obtained current or voltage value indicative of power consumption is above the second threshold, and determining the recovery rate of the water purification apparatus is below the second recovery rate threshold, and wherein the low quality indicates a high number of ions in the incoming water. 8. The method according to claim 7 , further comprising issuing a notification in response to determining that the obtained current or voltage value indicative of power consumption is above the second threshold and the recovery rate of the water purification apparatus is below the second recovery rate threshold. 9. The method according to claim 7 , further comprising stopping water purification in response to determining that the obtained current or voltage value indicative of power consumption is above the second threshold and the recovery rate of the water purification apparatus is below a third recovery rate threshold. 10. The method according to claim 1 , further comprising: monitoring a conductivity of a product flow rate from the electrically controlled deionization unit; and determining an efficiency of the electrically controlled deionization unit based on whether the conductivity meets at least one conductivity criterion and the obtained current or voltage value indicative of power consumption meets the at least one power consumption criterion. 11. The method according to claim 10 , further comprising determining that the electrically controlled deionization unit has insufficient efficiency in response to determining that the conductivity is increasing while the power consumption is stable during a same period of time. 12. The method according to claim 1 , wherein the electrically controlled deionization unit is any of: an electrodeionization (EDI) unit, a capacitive deionization (CDI) unit, or an electrodialysis reversal (EDR) unit. 13. A water purification apparatus comprising: a fluid circuit comprising: a reverse osmosis (RO) unit arranged to provide a permeate flow, and an electrically controlled deionization unit arranged downstream from the RO unit to receive at least part of the permeate flow; and a control arrangement comprising a control unit configured to perform the following operations: obtain, using a sensor, a current or voltage value indicative of power consumption by the electrically controlled deionization unit, determine whether the obtained current or voltage value meets at least one power consumption criterion, and control, using one or more valve units, recirculation of reject water produced by the water purification apparatus based on whether the obtained current or voltage value meets the at least one power consumption criterion, including at least one of (i) increasing the recirculation of reject water in response to a determination that the obtained current or voltage value indicative of power consumption is below a first threshold, or (ii) decreasing the recirculation of reject water in response to a determination that the obtained current or voltage value indicative of power consumption is above a second threshold. 14. The water purification apparatus according to claim 13 , wherein the reject water comprises a reject flow from the RO unit and the control unit is configured to control the control arrangement to control recirculation of the reject flow from the RO unit to an incoming flow of the RO unit by means of a valve unit. 15. The water purification apparatus according to claim 13 , wherein the reject water comprises a reject flow from the electrically controlled deionization unit and the control unit is configured to control the control arrangement to control recirculation of the reject flow from the electrically controlled deionization unit to an incoming flow of the RO unit by means of a valve unit. 16. The water purification apparatus according to claim 13 , wherein the control unit is configured to determine whether a recovery rate of the water purification apparatus meets at least one recovery rate criterion, wherein the recovery rate is a ratio of a product flow rate from the deionization unit to an incoming flow rate of incoming water to the RO unit. 17. The water purification apparatus according to claim 16 , wherein the control unit is configured to determine a quality of the incoming water, indicative of a number of ions in the incoming water
Related publications grouped by family.
Answers are generated from the same data shown on this page.