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| 국가/구분 | United States(US) Patent 등록 |
|---|---|
| 국제특허분류(IPC7판) |
|
| 출원번호 | US-0539596 (2006-10-06) |
| 등록번호 | US-8562803 (2013-10-22) |
| 발명자 / 주소 |
|
| 출원인 / 주소 |
|
| 대리인 / 주소 |
|
| 인용정보 | 피인용 횟수 : 3 인용 특허 : 370 |
A fluid treatment apparatus for treating a fluid comprises an electrochemical cell having fluid orifices to receive and release fluid, and a fluid passageway connecting the orifices with a water-splitting ion exchange membrane is exposed to the fluid in the passageway. First and second electrodes ar
A fluid treatment apparatus for treating a fluid comprises an electrochemical cell having fluid orifices to receive and release fluid, and a fluid passageway connecting the orifices with a water-splitting ion exchange membrane is exposed to the fluid in the passageway. First and second electrodes are positioned about the membrane. The apparatus also comprises a controller to control and operate a power supply and valve system. The power supply supplies a current to the first and second electrodes at sufficiently high current density to result in bacteriostasis, deactivation, or a reduction in the microorganisms in the fluid. The controller can also operate a set of cells to deionize fluid and regenerate the cells.
1. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising (i) a plurality of fluid orifices to receive an input fluid and release an output fluid, the input fluid comprising a first level of active microorganisms;(ii) first and second electrodes; and(iii) an ion exchange memb
1. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising (i) a plurality of fluid orifices to receive an input fluid and release an output fluid, the input fluid comprising a first level of active microorganisms;(ii) first and second electrodes; and(iii) an ion exchange membrane between the first and second electrodes to treat the input fluid to form the output fluid;(b) a power supply having an output to apply a current to, and an output voltage across, the first and second electrodes; and(c) a control module comprising program code to: (i) receive a signal from the power supply to detect the current through the first and second electrodes; and(ii) send a signal to the power supply to apply an output voltage across the first and second electrodes to maintain a current having a current density which is sufficiently high to deactivate the microorganisms in the fluid such that the output fluid comprises a second level of active microorganisms which is less than the first level of active microorganisms in the input fluid. 2. An apparatus according to claim 1 wherein the control module comprises program code to send a signal to the power supply to apply an output voltage across the first and second electrodes to maintain a current having a current density from about 0.01 to about 20 mA/cm2. 3. An apparatus according to claim 1 wherein the first and second levels comprise colony forming units per 100 mL of fluid, and wherein the second level comprises fewer colony forming units per 100 mL of the output fluid than the first level of colony forming units per 100 mL of the input fluid. 4. An apparatus according to claim 3 wherein the control module comprises program code to send a signal to the power supply to maintain a current density that is sufficiently high to substantially prevent an increase in the colony forming units per 100 mL in the output fluid. 5. An apparatus according to claim 4 wherein the control module controls the power supply to apply an output voltage across the first and second electrodes to maintain a current having a current density that is sufficiently high to provide an output fluid having a second level of colony forming units per 100 mL that is at least about 90% lower than the first level of colony forming units per 100 mL of the input fluid. 6. An apparatus according to claim 4 wherein the input fluid comprises a first level of a microorganism comprising a heterotrophe bacteria plate count of at least about 500 Cfu/mL, and wherein the control module comprises program code to send a signal to the power supply to set a current density sufficiently high to provide an output fluid having a second level of heterotrophe bacteria plate count that is less than about 450 Cfu/mL. 7. An apparatus according to claim 1 wherein the first and second levels of active microorganisms comprise heterotrophe bacteria plate counts. 8. An apparatus according to claim 7 wherein the input fluid comprises a first level of a microorganism comprising a heterotrophe bacteria plate count of at least about 500 Cfu/mL, and wherein the control module comprises program code to send a signal to the power supply to maintain a current density sufficiently high to provide an output fluid having a second level of heterotrophe bacteria plate count that is less than about 450 Cfu/mL. 9. An apparatus according to claim 1 wherein the control module controls the power supply to maintain a current density sufficiently high to provide an output fluid having at least one log reduction of bacteria plate count for a fluid residence time of at least 0.05 minute. 10. An apparatus according to claim 1 wherein the control module comprises program code to send a signal to the power supply to maintain a current density sufficiently high to provide an output fluid having at least two log reduction of bacteria plate count. 11. An apparatus according to claim 1, wherein the control module comprises program code to send a signal to the power supply to maintain the current in response to a measured voltage across a resistor placed in series with the output of the power supply. 12. An apparatus according to claim 1 wherein the control module comprises program code to send a signal to a voltage level selector to produce a timing signal to control the output voltage applied by the power supply. 13. An apparatus according to claim 12, wherein the voltage level selector comprises: (a) a zero-crossing detector;(b) a capacitor and switched resistor network; and(c) a timer. 14. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising (i) a plurality of fluid orifices to receive an input fluid and release an output fluid, the input fluid comprising a first heterotrophe bacteria plate count, and the output fluid comprising a second heterotrophe bacteria plate count;(ii) first and second electrodes; and(iii) an ion exchange membrane between the first and second electrodes to treat the input fluid to form the output fluid, the ion exchange membrane comprising both anion and cation exchange surfaces;(b) a power supply to apply a current to the first and second electrodes; and(c) a control module to receive a signal from the power supply and to send a signal to the power supply, the control module comprising program code to: (i) receive a signal from the power supply to detect a voltage drop per membrane layer; and(i) send a signal to the power supply to supply a current to the first and second electrodes to maintain an electric potential drop of at least about 0.05 volts/membrane and that is sufficiently high to substantially prevent an increase in the plate count of the heterotrophe bacteria in the output fluid, so that a second plate count of heterotrophe bacteria in the output fluid is lower than the first plate count of heterotrophe bacteria in the input fluid. 15. An apparatus according to claim 14 wherein the control module comprises program code to send a signal to the power supply to maintain a current to obtain an electric potential drop of less than about 20 volts/membrane. 16. An apparatus according to claim 14 wherein the ion exchange membrane comprises multiple membrane layers between the first and second electrodes. 17. An apparatus according to claim 16 wherein the control module comprises program code to send a signal to the power supply to maintain a current sufficiently high to obtain an average electric potential drop of at least about 0.05 volts/membrane layer. 18. An apparatus according to claim 16 wherein the control module comprises program code to send a signal to the power supply to maintain a current sufficiently high to obtain an average electric potential drop of at least about 0.5 volts/membrane layer. 19. An apparatus according to claim 16 wherein the control module comprises program code to send a signal to the power supply to maintain a current to obtain an average electric potential drop of less than about 20 volts/membrane layer. 20. An apparatus according to claim 14 wherein the second plate count of heterotrophe bacteria is reduced by at least by a factor of 10 from the first plate count. 21. An apparatus according to claim 14 wherein the second plate count of heterotrophe bacteria is reduced by at least by a factor of 100 from the first plate count. 22. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising a housing having a plurality of orifices, and an ion exchange membrane between a pair of electrodes;(b) a power supply to supply a current to the electrodes;(c) a valve to control the flow of fluid through the orifices of the cell; and(d) a control module comprising program code to: (1) in a deionization cycle, send a signal to the valve to open the valve to flow fluid into an orifice of the cell while sending a signal to the power supply to supply a current having a current density to the pair of electrodes to form deionized fluid which is released at another orifice; and(2) in a post deionization cycle, send a signal to the valve to close the valve to substantially stop the flow of fluid into the cell, while continuing to send a signal to control the power supply to supply a deionization current to the electrodes for a time period. 23. An apparatus according to claim 22 wherein the control module comprises program code to, in a post-deionization cycle, send a signal to the power supply to apply a deionization current that is maintained at a current density of at least about 0.5 mA/cm2, and for a time period of less than about 10 minutes. 24. An apparatus according to claim 22 wherein the time period is less than about 5 minutes. 25. An apparatus according to claim 22 wherein the control module comprises program code to, in a deionization cycle, send a signal to the power supply to maintain a current density that is at least about 0.05 mA/cm2. 26. An apparatus according to claim 22 wherein the control module comprises program code to, in a post-deionization cycle, send a signal to the power supply to maintain a current density that is less than about 5 mA/cm2. 27. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising a housing having a plurality of orifices, and an ion exchange membrane between a pair of electrodes;(b) a power supply to supply a current to the electrodes of the cell;(c) a valve to control the flow of fluid through the orifices of the cell; and(d) a control module comprising program code to: (1) in a fluid deionization cycle, send a signal to the valve to operate the valve to pass fluid into an orifice of the cell while sending a signal to the power supply to supply a current to the electrodes to form deionized fluid that is released at another orifice; and(2) in a regeneration cycle, send a signal to the valve to operate the valve to provide a timed burst of fluid into an orifice of the cell, the timed burst comprising opening the valve for a time period shorter than the regeneration cycle time, while sending a signal to the power supply to supply a current to the electrodes to regenerate the ion exchange membrane to form regenerate fluid which is released at another orifice, and then send a signal to close the valve. 28. An apparatus according to claim 27 wherein the control module comprises program code to, during a regeneration cycle, operate the valve to provide a plurality of timed bursts of fluid in the regeneration cycle time. 29. An apparatus according to claim 27 wherein the control module comprises program code to, during a regeneration cycle, operate the valve to provide timed bursts of fluid for time periods of from about 0.1% to about 80% of the regeneration cycle time. 30. An apparatus according to claim 27 wherein the control module comprises program code to, during a regeneration cycle, operate the valve to provide timed bursts of fluid for time periods of from about 0.1 to about 40 seconds. 31. An apparatus according to claim 27 wherein the control module comprises program code to, during a regeneration cycle, operate the valve to provide timed bursts of fluid for different time periods during the regeneration cycle time. 32. An apparatus according to claim 31 wherein the control module comprises program code to, during a regeneration cycle, operate the valve to provide timed bursts of fluid (i) during a first regeneration stage for time periods of from about 0.1% to about 30% of the regeneration cycle time; (ii) during a second regeneration stage for time period of from about 0.3% to about 80% of the regeneration cycle time; and (iii) during a third regeneration stage for time periods of from about 0.1% to about 30% of the regeneration cycle time. 33. An apparatus according to claim 31 wherein the control module comprises program code to, during a regeneration cycle, operate the valve to provide timed bursts of fluid (i) during a first regeneration stage for time periods of from about 0.1 to about 10 seconds; (ii) during a second regeneration stage for time periods of from about 3 to about 40 seconds; and (iii) during a third regeneration stage for time periods of from about 0.1 to about 10 seconds. 34. An apparatus according to claim 27 wherein the control module comprises program code to operate the valve to provide timed bursts of fluid during one regeneration stage that is a least about 2 times longer than the time period during another regeneration stage. 35. An apparatus according to claim 27 wherein the control module comprises program code to operate the valve to provide timed bursts of fluid during a last regeneration stage having a time period that is less than about ½ the time period of a preceding or following regeneration stage. 36. An apparatus according to claim 27 wherein the control module comprises program code to, during a regeneration cycle, operate the valve to provide timed bursts of fluid during (i) a first regeneration stage which is performed from the commencement of the regeneration cycle until a time of less than about 2 minutes later, (ii) a second regeneration stage, which is performed for a time of at least about 3 minutes further, and (iii) a third regeneration stage, which is performed for at least about 3 minutes further. 37. An apparatus according to claim 27 further comprising a flow sensor that measures a flow rate through the first cell and sends a flow signal to the control module to operate the valve to set the duration of the timed bursts of fluid. 38. An apparatus according to claim 27 wherein in (a) the electrochemical cell is a first cell, and further comprising a second electrochemical cell comprising a housing having a plurality of orifices, a pair of electrodes, and an ion exchange membrane between the electrodes, and wherein the control module comprises program code to send a signal to the power supply and to the valve to deionize fluid in the second cell in a deionization cycle and pass the deionized fluid to the orifice of the first cell which is in a regeneration cycle. 39. A method of operating an electrochemical cell comprising a pair of electrodes about an ion exchange membrane, the method comprising: (a) in a fluid deionization cycle, passing fluid into the cell while powering the electrodes to deionize the fluid to form deionized fluid; and(b) in a regeneration cycle, providing a timed burst of fluid into the cell while powering the electrodes to regenerate the ion exchange membrane, the timed burst lasting from about 0.1% to about 80% of the regeneration cycle time, where the regeneration cycle time is the total time during which the ion exchange membrane is regenerated before it is used again for a deionization cycle. 40. A method according to claim 39 wherein the timed burst lasts from about 0.3% to about 30% of the regeneration cycle time. 41. A method according to claim 39 comprising, in a regeneration cycle, providing a plurality of timed bursts of fluid into the cell while powering the electrodes to regenerate the ion exchange membrane. 42. A method according to claim 41 wherein the number of timed bursts is at least about 10. 43. A method according to claim 41 wherein the timed bursts of fluid are performed in two or more stages and wherein the duration of the timed bursts are different for different stages. 44. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising a housing having a plurality of orifices, and an ion exchange membrane between a pair of electrodes;(b) a power supply to supply a current to the electrodes of the cell;(c) a valve to control the flow of fluid through the orifices of the cell; and(d) a control module comprising program code to: (1) in a deionization cycle, send a signal to the valve to open the valve to flow fluid into an orifice of the cell while sending a signal to the power supply to supply a current to the electrodes to deionize the fluid to form deionized fluid which is released at another orifice;(2) in a regeneration cycle, send a signal to the valve to open the valve to flow fluid into an orifice of the cell and send a signal to the power supply to: (i) in a main regeneration step, supply a current having a polarity to the electrodes to regenerate the ion exchange membrane to form regenerate fluid which is released at another orifice; and(ii) in a post regeneration step, reverse the polarity of the current. 45. An apparatus according to claim 44 wherein the control module comprises program code to, during the post regeneration step, send a signal to the power supply to supply the current for a time period of at least about 0.5 minutes. 46. An apparatus according to claim 44 wherein the control module comprises program code to, at the end of the post regeneration step, send a signal to the power supply to terminate the reverse polarity current supplied to the electrodes while sending a signal to the valve to maintain the valve open to allow a volume of fluid to continue to flow into the orifice of the cell, the volume being at least 20% of the cell void volume. 47. A fluid treatment method conducted in an electrochemical cell, the method comprising: (a) in a deionization cycle, flowing fluid into the cell while passing a current through the fluid to form deionized fluid which is released from the cell;(b) in a regeneration cycle, flowing fluid into the cell and (i) in a main regeneration step, passing a current having a polarity through the fluid to regenerate the ion exchange membrane to form regenerate fluid which is released from the cell; and(ii) in a post regeneration step, reversing the polarity of the current. 48. A method according to claim 47 wherein, in the post regeneration step, the current is supplied for at least about 0.5 minutes. 49. A method according to claim 47 comprising, after (b)(ii), terminating the reverse polarity current while continuing to flow fluid into the cell. 50. A method according to claim 49 comprising, after terminating the reverse polarity current, continuing to flow fluid into the cell for at least about 1 minute. 51. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising a housing having inlet and deionized fluid orifices, and an ion exchange membrane between first and second electrodes, the first electrode being adjacent to the inlet fluid orifice and the second electrode adjacent to the deionized fluid orifice;(b) a power supply to supply a current to the electrodes of the cell;(c) a valve to control the flow of fluid through the inlet and deionized fluid orifices of the cell; and(d) a control module comprising program code to: (1) in a deionization cycle, send a signal to the valve to open the valve to flow fluid into the inlet fluid orifice of the cell while sending a signal to the power supply to supply a current to the first electrode to deionize the fluid to form deionized fluid which is released at the deionized fluid orifice; and(2) in a regeneration cycle, send a signal to the valve to open the valve to flow fluid into the deionized fluid orifice of the cell while sending a signal to the power supply to supply a current having a first positive polarity to the second electrode to regenerate the ion exchange membrane to form regenerate fluid which is released from the inlet fluid orifice. 52. An apparatus according to claim 51 wherein in (d)(2), the control module comprises program code to send a signal to the power supply to supply a current which generates a current density of from about 0.02 mA/cm2 to about 20 mA/cm2. 53. An apparatus according to claim 51 wherein the power supply comprises a voltage supply. 54. An apparatus according to claim 53 wherein the voltage supply supplies a time modulated voltage to the first and second electrodes. 55. An apparatus according to claim 51 wherein the deionized fluid has a conductivity of less than 50% that of the fluid treated during the deionization cycle. 56. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising a housing having inlet and deionized fluid orifices, and an ion exchange membrane between first and second electrodes, the first electrode being adjacent to the inlet fluid orifice and the second electrode adjacent to the deionized fluid orifice;(b) a power supply to supply a current to the electrodes of the cell;(c) a valve to control the flow of fluid through the inlet and deionized fluid orifices of the cell; and(d) a control module comprising program code to: (1) in a deionization cycle, send a signal to the valve to open the valve to flow fluid into the inlet fluid orifice of the cell while sending a signal to the power supply to supply a current having a first positive polarity to the first electrode to deionize the fluid to form deionized fluid which is released at the deionized fluid orifice; and(2) in a regeneration cycle, send a signal to the valve to open the valve to flow deionized fluid into the deionized fluid orifice of the cell while sending a signal to the power supply to supply a current having a first positive polarity to the second electrode to regenerate the ion exchange membrane to form regenerate fluid which is released from the inlet fluid orifice. 57. An apparatus according to claim 56 wherein the deionized fluid has a conductivity of less than 50% that of the fluid treated during the deionization cycle. 58. An apparatus according to claim 56 wherein in(d)(2), the control module comprises program code to send a signal to the power supply to supply a current which generates a current density of from about 0.02 mA/cm2 to about 20 mA/cm2. 59. An apparatus according to claim 56 wherein the power supply comprises a voltage supply. 60. An apparatus according to claim 59 wherein the voltage supply supplies a time modulated voltage to the first and second electrodes. 61. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising a housing having inlet and deionized fluid orifices, and an ion exchange membrane between first and second electrodes, the first electrode being adjacent to the inlet orifice and the second electrode adjacent to the deionized fluid orifice;(b) a variable voltage supply that provides a time modulated direct current voltage to the electrodes of the cell, the time modulated direct current voltage having a single polarity that remains either positive or negative;(c) a valve to control the flow of fluid through the inlet and deionized fluid orifices of the cell; and(d) a control module comprising program code to, in a regeneration cycle, send a signal to the valve to open the valve to flow fluid into the deionized fluid orifice of the cell while sending a signal to the variable voltage supply to supply a time modulated direct current voltage to the electrodes of the cell. 62. An apparatus according to claim 61 wherein the control module comprises program code to send a signal to the valve to open the valve to flow deionized fluid into the deionized fluid orifice. 63. An apparatus according to claim 61 wherein the second electrode is maintained at a positive polarity. 64. An apparatus according to claim 61 wherein the time modulated current comprises a first current and a second current, and wherein the first current is greater than the second current. 65. An apparatus according to claim 64 wherein the duty cycle for the first current is larger than that of the second current. 66. A fluid treatment apparatus comprising: (a) an electrochemical cell comprising a housing having a plurality of orifices, and an ion exchange membrane between a pair of electrodes;(b) a power supply to supply a current to the electrodes;(c) a valve to control the flow of fluid through the orifices of the cell; and(d) a control module comprising program code to: (1) in a deionization cycle, send a signal to the valve to open the valve to flow fluid into an orifice of the cell while sending a signal to the power supply to supply a current having a current density to the pair of electrodes to form deionized fluid which is released at another orifice; and(2) in a regeneration cycle, send a signal to the valve to open the valve to supply deionized fluid to an orifice while sending a signal to the power supply to supply a modulated regeneration current to the electrodes. 67. An apparatus according to claim 66 wherein the control module comprises program code to, in a regeneration cycle, send a signal to the power supply to maintain first and second currents across the electrodes. 68. An apparatus according to claim 67 wherein the first current is larger than the second current. 69. An apparatus according to claim 68 wherein the duty cycle of the first current is larger than the duty cycle of the second current. 70. An apparatus according to claim 69 wherein the first current provides a current density of from about 0.5 mA/cm2 to about 5 mA/cm2. 71. An apparatus according to claim 70 wherein the second current provides a current density of from about 0.05 mA/cm2 to about 3 mA/cm2. 72. An apparatus according to claim 69 wherein the duty cycle for the first current is about 100% and the duty cycle for the second current is less than about 70%.
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