Oxidizing compositions for removing sulfur compounds from hydrocarbon fuels and wastewater
US-2024400426-A1 · Dec 5, 2024 · US
US10155672B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10155672-B2 |
| Application number | US-201414758274-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 8, 2014 |
| Priority date | Jan 11, 2013 |
| Publication date | Dec 18, 2018 |
| Grant date | Dec 18, 2018 |
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A method and apparatus for operating an electro-deionization (EDI) module produces purified water using a power supply controller to provide more efficient and accurate operation.
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What is claimed is: 1. A method of operating an electro-deionization (EDI) module to produce highly purified water from feed water comprising: receiving a range and a target within the range for a water quality value of the highly purified water; receiving values for the water quality (WQ) of the highly purified water from a water quality sensor; applying power to the EDI module to bring the WQ within the received range; and continuously adjusting the power to maintain the WQ near the received target within the range for water quality; saving a system state including a baseline current; restarting the EDI module initially using the baseline current; and wherein applying power to bring the WQ within the received range comprises applying one of a predetermined maximum initial power and a predetermined minimum initial power to the EDI module until the WQ is within the received range. 2. The method of claim 1 , wherein applying power to bring the WQ within the received range comprises: determining an ionic load of feed water; predetermining for the EDI module a relationship between power requirements and the ionic load of the feed water; and applying power to the EDI module to supply a current as a function of the feed water ionic load and the power requirements of the EDI module. 3. The method of claim 2 , wherein determining the ionic load of the feed water comprises: providing an EDI module with an approximately known excess capacity; applying a minimum power; measuring a time interval for a change in WQ; and determining the feed water ionic load as a function of the time interval, the approximately known excess capacity of the EDI module and the applied minimum power. 4. The method of claim 1 , wherein continuously adjusting the power to maintain the WQ near the received target for water quality comprises: predetermining a transfer function to apply changes in power to the EDI module based on differences in the WQ and the received target water quality; and operating the EDI module in closed loop operation using the predetermined transfer function. 5. The method of claim 4 further comprising: adjusting the transfer function while operating the EDI module by probing the EDI module to determine the change in measured WQ as a function of a probing change in the power applied to the EDI module. 6. The method of claim 5 , wherein the received range and target within the range for a water quality value of the highly purified water are combined into a target; and the method further comprises first applying power to the EDI module to bring the WQ within the received target and then continuously adjusting the power and probing to maintain the WQ near the received target for water quality. 7. The method of claim 4 , wherein the transfer function is a Proportional, Integral, Derivative (PID) function or a derivative function. 8. The method of claim 4 , wherein predetermining a transfer function comprises: calculating the transfer function using at least one purification factor. 9. The method of claim 8 , wherein the at least one purification factor comprises at least one of: feed water ionic load; performance of reverse osmosis (RO) pretreatment of the feed water; and EDI module performance. 10. The method of claim 4 further comprising: determining a lag time between changes in power application to the EDI module and changes in measured WQ value; and adjusting the transfer function to compensate for the lag time when adjusting the power to maintain the WQ near the received target for water quality. 11. The method of claim 4 , wherein the received range, the received target and a baseline current are parameters of the transfer function. 12. The method of claim 11 , wherein the baseline current parameter is adjusted using a transfer function. 13. The method of claim 1 , further comprising: determining a maintenance power; and applying the maintenance power when operation of the EDI module is stopped to counteract effects of back-diffusion. 14. The method of claim 1 , wherein applying power to the EDI module to bring the WQ within the received range comprises applying at least one of: a voltage; and a current; and wherein adjusting the power to maintain the WQ near the received target within the range comprises adjusting at least one of: a voltage; and a current. 15. The method of claim 1 , further comprising controlling the water quality within a controllable range having a width less than or equal to about 5 MΩ·cm. 16. The method of claim 1 , further comprising controlling the water quality within a controllable range having a width less than or equal to about 2 MΩ·cm.
Apparatus for electrochemical processes · CPC title
electrodeionisation · CPC title
by reverse osmosis · CPC title
Voltage · CPC title
for obtaining ultra-pure water · CPC title
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