US20130081949A1 - Apparatus for removal of ions, and a method of manufacturing an apparatus for removal of ions from water - Google Patents

Apparatus for removal of ions, and a method of manufacturing an apparatus for removal of ions from water Download PDF

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Publication number
US20130081949A1
US20130081949A1 US13/698,265 US201113698265A US2013081949A1 US 20130081949 A1 US20130081949 A1 US 20130081949A1 US 201113698265 A US201113698265 A US 201113698265A US 2013081949 A1 US2013081949 A1 US 2013081949A1
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Prior art keywords
water
electrodes
electrode
spacer
flow
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US13/698,265
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English (en)
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Hank Robert Reinhoudt
Albert van der Wal
Piotr Edward Dlugolecki
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Voltea BV
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Voltea BV
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Publication of US20130081949A1 publication Critical patent/US20130081949A1/en
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
    • C02F1/4691—Capacitive deionisation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/46—Apparatus for electrochemical processes
    • C02F2201/461—Electrolysis apparatus
    • C02F2201/46105—Details relating to the electrolytic devices
    • C02F2201/46115—Electrolytic cell with membranes or diaphragms
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/16—Regeneration of sorbents, filters
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/49002—Electrical device making
    • Y10T29/49117—Conductor or circuit manufacturing

Definitions

  • the invention relates to an apparatus to remove ions.
  • a method for water purification is by capacitive deionization, using an apparatus having a flow through capacitor (FTC) to remove ions in water.
  • the FTC functions as an electrically regenerable cell for capacitive deionization.
  • ions are removed from an electrolyte and are held in an electric double layer at the electrodes.
  • the electrodes can be (partially) electrically regenerated to desorb such previously removed ions without adding chemicals.
  • the apparatus to remove ions comprises one or more pairs of spaced apart electrodes (a cathode and an anode) and may comprise a spacer, the spacer separating the electrodes and allowing water to flow between the electrodes.
  • the apparatus comprises a housing comprising a water inlet to let water in the housing and a water outlet to let water out of the housing.
  • the layers of electrodes (and spacers) are stacked in a “sandwich” fashion by compressive force, normally by mechanical fastening.
  • the efficiency of the apparatus during purification is significant because it is indicative of the amount of water that may be purified by the apparatus over a period of time.
  • an apparatus to remove ions from water comprising:
  • a first and second electrode connected to a power controller configured to apply an electrical potential difference between the first and the second electrodes
  • the spacer between the first and second electrodes to allow water to flow in between the first and second electrodes, the spacer comprising a pillar structure.
  • a method of manufacturing an apparatus to remove ions from water comprising:
  • an apparatus to remove ions from water comprising:
  • a first and second electrode connected to a power controller configured to apply an electrical potential difference between the first and the second electrodes
  • the spacer between the first and second electrodes to allow water to flow in between the first and second electrodes, the spacer comprising a helical structure.
  • FIG. 1 shows a schematic representation of an embodiment of an electrode for use in an embodiment of the invention
  • FIG. 2 shows a schematic representation of a stack of electrodes for use in an embodiment of the invention
  • FIG. 3 shows a schematic representation of an apparatus to remove ions for use in an embodiment of the invention
  • FIG. 4 shows schematically the ion concentration between two electrodes
  • FIGS. 5 a - c show schematic cross-sections of a part of an apparatus to remove ions according to an embodiment of the invention
  • FIG. 7 shows a schematic arrangement of an apparatus to remove ions for use in an embodiment of the invention
  • FIGS. 9 a to 9 e show apparatus to remove ions according to an embodiment of the invention.
  • An advantage of a rectangular or a hexagonal shape of the electrode may be that this type of electrode may be efficiently produced with respect to use of material.
  • An advantage of a round shaped electrode with a round hole in the center may be that distance between the outer edge and the inner edge (i.e. the distance the water will flow along the electrode) is substantially constant for all flow directions.
  • FIG. 2 shows a stack of electrodes.
  • the first electrodes 21 and the second electrodes 22 each comprises a current collector, indicated by 34 in FIG. 3 , and an ion storage material, indicated by 35 in FIG. 3 .
  • the current collector is connected to a power controller PC configured to apply an electrical potential difference between two adjacent electrodes.
  • the ion storage material may store ions that have been removed from the water.
  • the ion storage material may be a so-called high surface area material with more than 500 m 2 /gr, more than 1000 m 2 /gr, or more than 2000 m 2 /gr.
  • the material may comprise activated carbon, carbon aerogel, graphene, carbon nanofiber and/or carbon nanotube on both sides of the electrode which are in contact with the water.
  • the spacer 36 may have a shape as is depicted in FIG. 1 .
  • a main function of a spacer is to separate the first electrode from the second electrode, for example by maintaining a substantially constant or fixed distance between the two electrodes.
  • the electrodes may have a charge barrier, for example an ion exchange membrane or an ion selective membrane.
  • a charge barrier for example an ion exchange membrane or an ion selective membrane.
  • the membrane provided on or to the cathode may be permeable for cations and only substantially allow the transport of cations and substantially block the transport of anions and the membrane provided on or to the anode may be permeable for anions and substantially block the transport of cations.
  • FIG. 4 shows two adjacent electrodes in an apparatus to remove ions.
  • the dotted line 41 indicates the concentration of ions in the water flowing between the two electrodes.
  • the ion concentration is lower than in the center.
  • the ion concentration in the water in region 42 may be lower than the ion concentration in region 43 .
  • FIG. 4 only two regions are depicted, it should be understood that the ion concentration may decrease gradually or even linearly with the distance from one of the electrodes and that therefore the choice of regions is arbitrary.
  • ion exchange membranes or ion selective membranes are used, which are placed between the electrode and the spacer, a similar situation may occur, where the ion concentration in the water in region 42 may be lower than the ion concentration in region 43 .
  • a low ion concentration close to the electrode (or membrane) may result in a low ion flux to the electrode (or through the membrane) to the electrode.
  • the ion flux may be increased, hence improving ion removal efficiency.
  • the ion concentration near the electrodes may be increased for example by mixing the water, by the displacement of the water in a substantially direction perpendicular to electrodes or by increasing the mobility of the ions in the water.
  • the ion improvement device comprises a mixing device.
  • the mixing device may be a spacer with a special structure that causes mixing of the water and which may even cause turbulence in the water.
  • the spacer may have a spiral or a helical structure.
  • a helical spacer may influence the water flow by forcing the fluid to twist along the spacer.
  • the effect may be a faster local velocity of the water or it may result in that water with higher ion concentration further away from the electrode (or membrane) is brought closer to the electrode (or membrane), which may increase the ion flux towards the electrode.
  • a helical spacer may improve the ion flux by a factor up to two times compared to a non-helical spacer.
  • a helical spacer may increase the mixing of the water where the flow is still laminar.
  • a helical spacer may promote turbulence in the flow channel, which may further improve the mixing of the water.
  • the ion flux improvement device may comprise a turbulence creator to create a turbulent flow in the water in the spacer or a recirculation circuit with a pump and a storage facility.
  • a turbulence creator to create a turbulent flow in the water in the spacer or a recirculation circuit with a pump and a storage facility.
  • water from the FTC with low ion concentration may be mixed with water in the storage facility with a higher ion concentration.
  • the storage water may be used for other purposes, for example as a swimming pool, or for irrigation.
  • FIG. 5 a shows a schematic cross section of a first and a second electrode, between which water is flowing.
  • the elements in FIG. 5 such as electrodes 21 and 22 and their sizes and mutual distances are depicted schematically. It may be that the flow of water through the spacer is more or less laminar, e.g. the water flows in more or less constant layers (parallel to the electrodes) without mixing of the water or without water flowing with a direction component perpendicular to the electrodes.
  • region 61 the flow velocity of a laminar flow parallel to the electrodes is depicted, wherein the length of the straight arrows indicates the velocity of the flow: a longer arrow indicates a higher velocity.
  • the ion improvement device may comprise a velocity adjuster 64 configured to adjust a flow velocity of a first portion of the water with respect to a second portion of the water, wherein, in use i.e. during ion removal from the water, in the first portion an ion concentration is higher than in the second portion. If a portion of water experiences the electrical potential difference for a longer period of time (i.e. its flow velocity is lower) than another portion of water, then at the same ion concentration in the water the number of ions removed from this portion will be higher than from another portion of water that experiences the electrical potential difference for a shorter period of time.
  • a velocity adjuster 64 configured to adjust a flow velocity of a first portion of the water with respect to a second portion of the water, wherein, in use i.e. during ion removal from the water, in the first portion an ion concentration is higher than in the second portion.
  • Region 65 depicts a possible effect on the flow velocity of the water, wherein the length of the straight arrows indicates the absolute velocity of the flow: a longer arrow indicates a higher velocity and the orientation of the arrow indicates the direction of the flow.
  • the velocity adjuster 64 has reduced the velocity of the water so much that the velocity in the center of the flow channel has become lower than closer to the electrodes.
  • a lower reduction of the flow velocity in the center may be achieved, where the flow will only gradually decrease from the center to close to the electrodes.
  • the velocity adjuster may cause the velocity to be more uniform inside the spacer, where the flow velocity will be substantially independent from the distance from the electrode.
  • the velocity adjuster 64 may comprise a porous material, wherein the flow resistance in the center of the velocity adjuster is larger than in one or more edges, causing the velocity of the water passing through the center of the velocity adjuster 64 (for example in region 63 ) to be reduced compared to the water passing through the edge of the velocity adjuster 64 (for example in region 62 ).
  • the flow resistance of this velocity adjuster may be continuously increasing from an edge, near one of the electrodes, towards the center of the velocity adjuster, i.e. the central axis of the spacer.
  • the porosity of the velocity adjuster 64 may be varied from a value larger than 70%, larger than 80%, or larger than 90% close to an electrode (e.g. region 62 ) to a value of smaller than 70%, smaller than 60% or smaller than 50% towards the center of the velocity adjuster (e.g. region 63 ). Porosity may be measured as a percentage of the volume of voids over the total volume.
  • the velocity adjuster 64 for use in the apparatus to remove ions may comprise a spacer with multiple layers between the electrodes and the layer(s) close to the electrode(s) may have a low flow resistance and the layer(s) further away from the electrode(s) a relatively higher flow resistance.
  • the low flow resistance may cause a higher velocity of the water close to an electrode and the higher flow resistance may cause a lower velocity of the water further away from the electrode.
  • Without the velocity adjuster 64 less ions will be removed from the water in the center of the flow channel or spacer, because these ions will have to migrate over a larger distance whereas the residence time of the ion in the center of the flow channel or spacer is lower than that closer to an electrode.
  • FIG. 5 b is an example of such a velocity adjuster 64 for use in an apparatus to remove ions according to an embodiment of the invention.
  • the velocity adjuster 64 has channel walls creating small channels 67 , 68 in the spacer 64 .
  • the channel walls are permeable for water and/or ions flowing through them but they create a resistivity for the water flow. As depicted the channel walls are substantially parallel to the electrodes but they may be more randomly oriented.
  • a small channel 68 in the middle of the spacer creates a higher flow resistivity than a larger small channel 67 closer to an electrode.
  • the flow velocity of the water flowing in the flow direction substantially parallel to the channel walls is thereby adjusted so that the flow velocity is lower in the middle of the spacer than the flow velocity closer to the electrodes 21 , 22 .
  • the flow resistance of the small channels may be continuously increasing from a larger small channel 67 near the edge, near one of the electrodes 21 , 22 , towards the middle, i.e. the central small channel 68 of the spacer.
  • the water further away of an electrode may get a lower velocity so that it stays longer between the electrodes and there is more time by the electrodes 21 , 22 to attract the ions.
  • Water close to an electrode may be relatively quickly de-ionized because of the close proximity of the electrode and may therefore be for a relatively short time between the electrodes.
  • the water further away from the electrode may because of the higher flow resistance further away from the electrode also be moved towards an electrode so that the ions are more easily attracted to an electrode.
  • FIG. 6 Another example of a velocity adjuster may be a shifted spacer, as is depicted in FIG. 6 .
  • the spacer may comprise a grid structure 71 .
  • the grid structure will influence the velocity of the water flowing through the spacer. It may also cause mixing of the water or cause a displacement of the water in a direction perpendicular to electrodes. By shifting or rotating the orientation of the grid with respect to the electrode, these effects may be further optimized.
  • FIG. 6 shows a shifted grid structure 72 .
  • the shift or rotation of the orientation may be around 45 degrees, where the threads of the spacer are at an angle of around 45 degrees with respect to the side of one of the electrodes, as can be seen from FIG. 6 . Or in other words, the threads of the spacer are substantially parallel to the diagonal of the electrode.
  • the dimensions of the spacer are about the same as the dimension of the electrode shown in FIG. 1 or may be a bit larger, for example 17 ⁇ 17 cm.
  • FIG. 7 shows another embodiment of an ion flux improvement device, comprising an electrical current measurement device A and a flow controller FC.
  • the current measurement device A measures the current flowing to the first electrode 21 or to the second electrode 22 .
  • the ion flux is a function of the electrical current and the electrical current may thus be used as a measure for the ion flux.
  • the current measurement device A provides a current signal to the flow controller FC, which may adjust the water flow depending on the measured electrical current.
  • the flow controller FC may be configured to adjust the flow velocity of the water, for example by controlling the pump P, via a control signal. In this way, the ion flux may be controlled via the flow controller.
  • An optimum ion flux to the electrode (or membrane) may be obtained when the percentage of ions removed from the water per cycle is relatively low, for example below 80%, below 60%, below 40% or below 20%. In one cycle the water flows once between two FTC electrodes.
  • a high ion flux may thus be obtained for example at a flow velocity higher than 1 liter/m 2 projected electrode area/min, or higher than 2 liters/m 2 projected electrode area/min or even higher than 3 liters/m 2 projected electrode area/min or even higher than 4 liters/m 2 projected electrode area/min.
  • the ion flux which is defined per unit time per projected electrode area, may increase because the number of cycles per unit time may also increase with higher flow velocity.
  • the ion flux improvement devices may comprise a deionization rate measurement device to measure the deionization rate (i.e. the percentage of ions removed from the water) per cycle.
  • the deionization rate measurement device may comprise two ion concentration measurement devices, one measuring the ion concentration of the water before the water flows between the electrodes and one measuring the ion concentration of the water after flowing between the electrodes.
  • the deionization rate measurement device may comprise only one of these two ion concentration measurement devices and an electrical current measurement device as described above.
  • the deionization rate measurement device may calculate the deionization rate on the basis of one measurement of the ion concentration and the measurement of the current flowing to one of the electrodes.
  • the deionization rate measurement device may provide a deionization rate signal indicating the measured or calculated deionization rate.
  • the ion flux improvement device may further comprise a flow controller to control the water flow in response to the deionization rate signal.
  • a flow controller to control the water flow in response to the deionization rate signal.
  • the ion flux may be higher than 0.5 grams salt per m 2 projected electrode area per min, higher than 1.0 gram salt per m 2 projected electrode area per min, higher than 1.5 grams salt per m 2 projected electrode area per min or higher than 2.0 grams salt per m 2 projected electrode area per min.
  • Increasing the flow velocity may cause the flow regime to change from a laminar flow to an unsteady or turbulent flow.
  • the pressure drop shows a linear relationship with the flow velocity.
  • the pressure drop over the spacer or flow channel is no longer linear with the flow velocity, but increases more rapidly with the flow. This involves more pumping energy.
  • the pressure drop should be limited, for example in the range of 0-20 bar per m 2 projected electrode area, in the range of 15-18 bar per m 2 projected electrode area or in the range of 2-10 bar per m 2 projected electrode area.
  • the pressure drop may be limited to 0.1-20 bar per m 2 projected electrode area or 1-15 bar per m 2 projected electrode area.
  • FIG. 8 a discloses a cross-section of an apparatus to remove ions according to a further embodiment of the invention comprising a first and second electrode 21 , 22 and a spacer between the first and second electrodes 21 , 22 .
  • the spacer may have a helical structure 81 .
  • the thickness of the spacer with the helical structure 81 may be 20-300 micrometers, 40-200 micrometers, 60-150 micrometers or 70-120 micrometers.
  • the helical structure 81 may influence the principal water flow 83 by forcing the fluid to twist along the helical structure in a direction 85 .
  • the effect may be a faster local velocity of the water or it may result in that water with a higher ion concentration further away from the electrode (or membrane) may be brought closer to the electrode (or membrane), which may increase the ion flux towards the electrode.
  • a helical structure in the spacer may improve the ion flux by a factor up to two times compared to a spacer without a helical structure.
  • a helical structure may increase the mixing of the water where the flow is still laminar.
  • a helical structure may promote turbulence in the flow channel, which may further improve the mixing of the water.
  • the electrodes may comprise a flat surface and multiple helical structures may be sandwiched between the flat surface of the first electrode and the flat surface of the second electrode.
  • the spacer is to keep the surfaces of the two electrodes at a substantial constant distance of, for example, between 0.02 and 0.5 mm. This is significant because if the distance between the electrodes is irregular then this may affect the flux of ions towards the electrode, with lower fluxes where the spacer is thicker.
  • the helical structure 81 may provide seven twists over the length of the helical structure. Seven twists would assure that the water is flowing along each electrode at least seven times.
  • the porosity of the spacer with the helical structure may be larger than 50%, larger than 60%, larger than 70% or larger than 80%.
  • FIG. 8 b discloses a cross-section of an apparatus to remove ions according to a further embodiment of the invention comprising a first and second electrode 21 , 22 and a spacer between the first and second electrodes 21 , 22 .
  • the spacer has a helical structure 81 having a less steep torsion and only half a twist in total.
  • An advantage may be that the flow resistance in such a case is lower and that the water will rotate along an electrode.
  • An optimum between low flow resistance and sufficient interaction with the electrodes may be with a number of twists between 0.5 and 7, between 1 and 5 or between 2 and 4.
  • FIG. 8 c discloses a cross-section of an apparatus to remove ions according to a further embodiment of the invention.
  • FIG. 8 c gives a top view of a spacer with one of the electrodes removed so that multiple adjacent helical structures 81 on top of the flat surface of the electrode 22 can be seen.
  • the helical structures have four and half twists and the twists of two adjacent helical structures 81 are opposite.
  • the helical structures 81 cause the water to twist 85 around the principal flow direction 83 of the water and since two adjacent helical structures 81 have an opposite twist the water in between the helical structures 81 move in the same direction substantially perpendicular to the principal flow direction 83 . This may improve the flow of the water towards an electrode at a position 89 in between the helical structures 81 . Since two adjacent helical structures are co-operating there may be a relatively low increase of the flow resistance.
  • the twist direction of two adjacent helical structures 81 may also be the same which causes turbulence in between the helical structures and improved mixing.
  • the helical structures in FIG. 8 c have a support 87 in the center. This forces the water out of the center of the helical structure towards the electrodes where the water is de-ionized.
  • Any embodiment of the above described apparatus to remove ions may be used for the removal of ions from water in a swimming pool, from water in a storage tank or from water in a factory plant or from ground water.
  • FIG. 9 a discloses a cross-section of an apparatus to remove ions according to a further embodiment of the invention comprising a first and second electrode 21 , 22 and a spacer between the first and second electrodes 21 , 22 .
  • the spacer may have a structure as a pillar 91 to keep the electrodes at a substantially fixed distance.
  • the thickness of the spacer with the pillar structure may be 20-300 micrometers, 40-200 micrometers, 60-150 micrometers or 70-120 micrometers.
  • the pillar structure 91 may be produced in a netting structure or framework 93 to form a layer which may form the spacer.
  • the spacer is electrically insulating and at the same time open enough for water and ions to move through.
  • the term pillar is to be interpreted as a structural element that keeps the first and second electrodes at a distance.
  • the netting 93 keeps the pillar 91 substantially perpendicular compared to the main direction of the spacer.
  • the netting framework causes a higher flow resistivity in the middle of the flow channel between the electrodes 21 , 22 thereby forcing the water in the flow channel to move closer to the first or second electrode resulting in increased de-ionization of water.
  • the netting framework and the pillars may cause better mixing of the water in the flow channel, which may increase the ion flux towards an electrode.
  • the spacer comprising pillars and a netting is that it creates a very open spacer (particularly in the flow direction) with a low flow resistivity, which may result in a lower pressure drop over the channel, or increased flow in the flow channel and it may also result in a reduced risk of fouling of the spacer.
  • the porosity of the spacer with the pillar structure may be larger than 50%, larger than 60%, larger than 70% or larger than 90%.
  • the electrodes may have a flat surface and multiple pillars held by the netting may be sandwiched between the flat surface of the first electrode and the flat surface of the second electrode.
  • One of the functions of the spacer is to keep the surfaces of the two electrodes at a substantially constant or fixed distance of, for example, between 0.02 and 0.5 mm. This is significant because if the distance between the electrodes is irregular, then the ion flux towards the electrodes may be affected.
  • FIG. 9 b gives a top view of a part of a spacer with one of the electrodes removed so that the multiple adjacent pillars 91 on top of the flat surface of the electrode 22 which are held in the netting 93 can be seen.
  • the netting 93 provides support over the full surface of the electrode so that it keeps the pillars 91 substantially perpendicular to the surface of the electrode as well as at a substantially fixed distance with respect to each other.
  • FIG. 9 c discloses a cross-section of an apparatus to remove ions according to a further embodiment of the invention.
  • the pillar 95 in this embodiment may comprise a spherical, elliptical or egg shape so that the pillar structure may have a thicker middle portion so as to provide for a higher flow resistivity in the middle of the flow channel in order to force the water flowing in the center part of the flow channel between the electrodes 21 , 22 in the direction of an electrode. At the same time the flow velocity in the center of the flow channel may be reduced compared to that of the water flowing closer to the first and/or second electrode.
  • the pillar may have a conical or rhombus structure, which is thicker in the middle than at an edge.
  • the spacer may comprise a netting 97 to keep the pillars 95 in position.
  • the netting of FIG. 9 c may be constructed similarly as the netting in FIG. 9 b.
  • FIG. 9 d discloses a cross-section of an apparatus to remove ions according to a further embodiment of the invention.
  • This embodiment is the same as the embodiment of FIG. 9 c except that the netting is omitted.
  • the pillars 97 may be spherical, elliptical, conical, rhombus or ball shaped so as to provide a higher flow resistivity further away from the electrode 21 , 22 and hence increasing the residence time of the water in the center of the channel compared to that of an edge of the spacer.
  • the pillars 97 may be attached to the electrodes so that the electrodes keep the pillars substantially perpendicular to the electrode surface by, for example, a glue or a specific coating.
  • the pillars may also be produced by printing the pillars on an electrode with, for example, a 3D printer and subsequently providing another electrode on top of the already printed electrode.
  • the pillars may be printed on top of an additional layer, for example an ion exchange membrane, which may be placed on top of the electrode as a separate layer or as a coating or laminate.
  • FIG. 9 e discloses a cross-section of an apparatus to remove ions according to a further embodiment of the invention. This embodiment is the same as the embodiment of FIGS. 9 a and 9 b except that the netting is omitted.
  • the pillars 99 may be connected to the electrodes so that the electrodes keep the pillars substantially perpendicular to the electrodes.
  • the pillars may be produced by printing the pillars on an electrode with, for example, a 3D printer.
  • An advantage of the pillars without a netting is that a very open spacer may be created in which the flow resistivity is reduced as well as the risk of fouling is reduced.
  • ions may be removed by providing a method comprising: providing an electrical potential difference between a first and a second electrode in a housing; allowing water to flow between the first and second electrodes from an inlet in the housing to an outlet in the housing; and improving the ion flux from the water to the first and/or second electrode.
  • the apparatus may comprise a housing, an inlet to let water in the housing, an outlet to let water out of the housing, a first and a second electrode connected to a power controller configured to apply an electrical potential difference between the first and the second electrodes, and an ion flux improvement device configured to improve the ion flux from the water flowing between the first and second electrodes to one of the first and the second electrode.
  • the ion flux improvement device may comprise a mixing device constructed and arranged to mix the water, or an unsteady flow creator configured to create an unsteady flow in the water, or a turbulence creator configured to create turbulence in the water, or a spacer between the first and second electrodes configured to allow water to flow in between the first and second electrodes, the spacer having a spiral structure to change a flow profile of the water.
  • the mixing device may comprise a recirculation circuit constructed and arranged to recirculate water flowing between the first and second electrodes, the recirculation circuit may comprise a pump and a storage facility.
  • the ion flux improvement device may comprise a spacer between the first and second electrodes to allow water to flow in between the first and second electrodes, the spacer may comprise ion-conductive material to increase a mobility of ions towards the first electrode or the second electrode.
  • the ion flux improvement device may comprise a spacer between the first and second electrodes to allow water to flow in between the first and second electrodes, the first and second electrodes and the spacer may have a substantially rectangular sheet-like shape, in which a hole may be provided; and the spacer may comprise a grid structure and an orientation of the grid structure may be rotated with respect to a straight side of the first and second electrodes by at least 30 degrees, in the range of 30-50 degrees or about 45 degrees.
  • the ion flux improvement device may comprise a velocity adjuster constructed and arranged to adjust a flow velocity of a first portion of the water with respect to a second portion of the water, wherein, in use, i.e. when removing ions from water, in the first portion an ion concentration is higher than in the second portion.
  • the ion flux improvement device may comprise an electrical current measurement device arranged and constructed to measure an electrical current between the first and the second electrodes and to provide a current signal indicating the electrical current; and a flow controller arranged and constructed to receive the current signal and adjust a flow velocity at which the water is flowing between the first and second electrodes in response to the current signal.
  • the flux improvement device may comprise a deionization rate measurement device arranged and constructed to measure a deionization rate per cycle of the water flowing between the first and the second electrodes and provide a deionization rate signal indicating the deionization rate; and a flow controller arranged and constructed to receive the deionization rate signal and adjust a flow velocity at which the water is flowing between the first and second electrodes in response to the deionization rate signal.
  • the flow controller may be arranged and constructed to maintain the deionization rate below 60%, below 40% or below 20% of ions removed per cycle.
  • the percentage of ion removal per cycle may be increased for example from 20% in the first cycle to 40% in the second cycle to 60% in the third cycle and to 80% in the fourth cycle and effectively almost complete removal in the fifth cycle.
  • the flow controller may be arranged and constructed to maintain the flow velocity higher than 2 liters/m 2 projected electrode area/min, higher than 3 liters/m 2 projected electrode area/min, or higher than 4 liters/m 2 projected electrode area/min.
  • the flow controller may be constructed and arranged to provide a control signal to a pump, the pump being constructed and arranged to receive the control signal and pump the water between the first and second electrodes with a flow velocity in response to the control signal.
  • An apparatus to remove ions from water comprising:
  • a housing comprising:
  • a velocity adjuster constructed and arranged to adjust a flow velocity of a first portion of the water flowing between the first and second electrodes with respect to a second portion of the water flowing between the first and second electrodes.
  • the velocity adjuster is constructed and arranged to adjust the flow velocity of the first portion of the water to be reduced compared to the flow velocity of the second portion of the water. 3. The apparatus according to clause 1 or clause 2, wherein the first portion of the water is flowing further away from the first electrode and/or the second electrode than the second portion of the water. 4. The apparatus according to any of clauses 1-3, wherein the first portion of the water is flowing through the center of the velocity adjuster. 5. The apparatus according to any of clauses 1-4, wherein the second portion of the water is flowing through an edge of the velocity adjuster. 6. The apparatus according to any of clauses 1-5, wherein the second portion of the water is flowing closer to the first electrode and/or the second electrode in the velocity adjuster. 7.
  • the velocity adjuster comprises a material with a flow resistance which may be adjusted to adjust the flow velocity of the water.
  • the velocity adjuster comprises a porous material, wherein a flow resistance in the center of the velocity adjuster is larger than closer to an edge, causing the velocity of the water passing through the center of the velocity adjuster to be reduced compared to the water passing through the edge of the velocity adjuster.
  • the velocity adjuster comprises a porous material, where the porosity increases from the center of the velocity adjuster to the first electrode and/or the second electrode. 10.
  • the velocity adjuster comprises a spacer with multiple layers between the first and second electrodes and a layer close to the first electrode and/or the second electrode has a low flow resistance and a layer further away from the first electrode and/or the second electrode has a relatively high flow resistance.
  • the layers comprise a porous material with a low flow resistance in a first direction and a higher flow resistance in a second direction, where a layer close to the first electrode and/or the second electrode is oriented such that the first direction is substantially equal to the water flow direction.
  • a layer further away from the first electrode and/or the second electrode is oriented such that the second direction is substantially equal to the water flow direction.
  • a housing comprising:
  • the spacer between the first and second electrodes to allow water to flow in between the first and second electrodes, the spacer comprising a helical structure.
  • first and second electrodes each comprise a substantially flat surface at a substantially constant distance from each other.
  • the helical structure is sandwiched in between the flat surface of the first and second electrodes.
  • the helical structure forces the water to twist along the helical structure.
  • the helical structure forces the water further away from the first electrode and/or the second electrode to a position closer to the first electrode and/or the second electrode.
  • the helical structure creates turbulence in between the first and second electrodes to improve mixing of water.
  • the spacer comprises multiple helical structures.
  • the spacer comprises multiple helical structures and the rotational direction of adjacent helical structures is opposite.
  • the water flow through the spacer has a principal direction substantially parallel to the first electrode and/or the second electrode and the helical structure is oriented substantially parallel to the principal direction.
  • 29. The apparatus according to clause 28, wherein the helical structure forces the water to rotate in direction substantially perpendicular to the principal direction.
  • 30 The apparatus according to clause 29, wherein two adjacent helical structures rotate the water in opposite direction. 31.
  • a housing comprising:
  • the spacer between the first and second electrodes to allow water to flow in between the first and second electrodes, the spacer comprising a pillar structure.
  • the pillar structure is, between the electrodes, substantially perpendicular to the flow direction.
  • the spacer comprises a netting framework to keep pillars of the pillar structure at a substantially fixed distance from each other.
  • the netting framework is constructed and arranged to keep the longitudinal axis of the pillar structure substantially perpendicular with respect to the flow direction of the water flowing between the first and second electrodes.
  • the center part of the pillar structure is attached to a netting framework. 42.
  • the netting framework and/or pillar structure creates movement of water substantially perpendicular to the flow direction of the water flowing between the first and second electrodes.
  • the pillar structure comprises a thicker middle portion in order to provide for an increased flow resistivity in the center of a flow channel in between the first and second electrodes.
  • the thickness of the pillar structure decreases from the center of the pillar structure to an edge of the pillar structure.
  • the pillar structure is spherical, elliptical, rhombus, egg or ball shaped.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Electrochemistry (AREA)
  • Analytical Chemistry (AREA)
  • Molecular Biology (AREA)
  • Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
US13/698,265 2010-05-17 2011-05-17 Apparatus for removal of ions, and a method of manufacturing an apparatus for removal of ions from water Abandoned US20130081949A1 (en)

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EP10163021.8 2010-05-17
EP10163021 2010-05-17
PCT/EP2011/058000 WO2011144635A1 (en) 2010-05-17 2011-05-17 Apparatus for removal of ions, and a method of manufacturing an apparatus for removal of ions from water

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CN102906028A (zh) 2013-01-30
WO2011144635A1 (en) 2011-11-24
EP2571817A1 (en) 2013-03-27
EP2571606A1 (en) 2013-03-27
WO2011144638A1 (en) 2011-11-24
WO2011144636A1 (en) 2011-11-24
JP5783475B2 (ja) 2015-09-24
US9540260B2 (en) 2017-01-10
US20130075260A1 (en) 2013-03-28
CN102906028B (zh) 2014-11-12
EP2571817B1 (en) 2015-01-14
EP2571606B1 (en) 2016-10-19
JP2013529131A (ja) 2013-07-18

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