Ion exchange particle regeneration device
By designing an ion exchange particle regeneration device, the support plate and vibration components are used to prevent particles from stacking and aggregation, the problem of poor regeneration effect is solved, and more efficient regeneration effect and lower cost is achieved.
Patent Information
- Application Number
- CN202510285452.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-03-11
- Publication Date
- 2025-06-10
AI Technical Summary
During the regeneration process of ion exchange particles, there is a problem of poor regeneration effect, which leads to an increase in purification cost and a reduction in purification capacity.
An ion exchange particle regeneration device is designed, including a cation exchange chamber and anion exchange chamber, and the support plate and vibration components are used to prevent particles from stacking and aggregation, thereby improving regeneration efficiency.
By preventing particle stacking and aggregation, the regeneration effect of ion exchange particles is improved, the regeneration cost is reduced, and the service life of particles is extended.
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Figure CN120115201A_ABST
Abstract
Description
Technical Field
[0001] The invention relates to the field of liquid purification, and in particular to an ion exchange particle regeneration device. Background Art
[0002] In various industrial and scientific fields, many liquids need to be purified, and ion exchange particles are used to remove impurity cations and impurity anions in the liquid to meet specific application requirements. For example, in the ultrapure water manufacturing process: in order to obtain water with the required purity, it is necessary to purify and remove impurity cations and impurity anions in the water. For example, in the semiconductor industry: etching liquid is often used in the production process of semiconductor devices. In order to obtain better etching effects, it is necessary to purify and remove impurity cations and impurity anions mixed in the etching liquid. For example, in the beverage industry: in the production and packaging process of beverages, it is necessary to purify and remove impurity cations and impurity anions mixed in the liquid, which helps prevent the oxidation and deterioration of bottled beverages and prolong the shelf life. For example, in the pharmaceutical industry: in drug production, it is necessary to purify and remove impurity cations and impurity anions mixed in the solvent or reaction medium, which is crucial to ensure the quality and stability of the drug; considering the purification cost, it is usually necessary to regenerate the ion exchange particles with weakened purification capacity, and continue to use the regenerated ion exchange particles for liquid purification.
[0003] However, in the actual regeneration process of ion exchange particles, there is a problem of poor regeneration effect. Therefore, how to provide a technical solution to improve the regeneration effect has become a technical problem that technical personnel in this field urgently need to solve. Summary of the invention
[0004] The technical problem solved by the present invention is to regenerate ion exchange particles by providing an ion exchange particle regeneration device to improve the regeneration effect.
[0005] In order to solve the above problems, an embodiment of the present invention provides an ion exchange particle regeneration device, comprising: a cation exchange chamber, comprising a first area for accommodating first cation exchange particles, and a second area for accommodating second cation exchange particles; a first support plate, located in the second area, for supporting the second cation exchange particles, the second cation exchange particles are located above the first cation exchange particles; a vibration component, coupled to the cation exchange chamber, for driving the first cation exchange particles and the second cation exchange particles to vibrate when the ion exchange particles are regenerated.
[0006] Optionally, the ion exchange particle regeneration device further includes: an anion exchange chamber, including a third area for accommodating first anion exchange particles, and a fourth area for accommodating second anion exchange particles; a second support plate, located in the fourth area, for supporting the second anion exchange particles, the second anion exchange particles being located above the first anion exchange particles; the vibration component is also coupled to the anion exchange chamber, and is used to drive the first anion exchange particles and the second anion exchange particles to vibrate when the ion exchange particles are regenerated.
[0007] Optionally, the vibration component includes: a connecting rod coupled to the cation exchange chamber and the anion exchange chamber; and a vibration motor coupled to the connecting rod.
[0008] Optionally, the first cation exchange particles contained in the first zone are adsorbed with first impurity cations of the purified liquid; the second cation exchange particles contained in the second zone are adsorbed with second impurity cations of the purified liquid; the first anion exchange particles contained in the third zone are adsorbed with first impurity anions of the purified liquid; and the second anion exchange particles contained in the fourth zone are adsorbed with second impurity anions of the purified liquid.
[0009] Optionally, the ion exchange particle regeneration device further comprises: a first connecting area located between the first area and the second area, and a second connecting area located between the third area and the fourth area;
[0010] a cation valve, located in the first connecting area, for isolating the mutual flow between the first cation regeneration liquid flowing through the first area and the second cation regeneration liquid flowing through the second area, the first cation regeneration liquid being used for regeneration of the first cation exchange particles, and the second cation regeneration liquid being used for regeneration of the second cation exchange particles;
[0011] The anion valve is located in the second connecting area and is used to isolate the mutual flow between the first anion regeneration liquid flowing through the third area and the second anion regeneration liquid flowing through the fourth area. The first anion regeneration liquid is used for regenerating the first anion exchange particles, and the second anion regeneration liquid is used for regenerating the second anion exchange particles.
[0012] Optionally, the second area is located above the first area, and the fourth area is located above the third area, and further includes: the first support plate has a plurality of first support plate protrusions, and the protrusions are oriented in a direction away from the cation valve, the sidewall of the first support plate protrusion has a plurality of first support plate side wall protrusions, and a first interval is provided between adjacent first support plate side wall protrusions, the first interval is also provided on the first support plate between adjacent first support plate protrusions, and the first interval connects the second area and the first connecting area;
[0013] The second support plate has a plurality of second support plate protrusions, and the protrusions are oriented in a direction away from the anion valve, the sidewalls of the second support plate protrusions have a plurality of second support plate sidewall protrusions, and a second interval is provided between adjacent second support plate sidewall protrusions, the second interval is also provided on the second support plate between adjacent second support plate protrusions, and the second interval communicates with the fourth area and the second connection area;
[0014] A first partition layer, located in the first area, for isolating the first cation exchange particles from the cation valve, the first partition layer having a plurality of first partition layer protrusions, and the protrusions are oriented in a direction away from the cation valve, the sidewall of the first partition layer protrusions having a plurality of first partition layer sidewall protrusions, a third partition is provided between adjacent first partition layer sidewall protrusions, the third partition is also provided on the first partition layer between adjacent first partition layer protrusions, and the third partition connects the first area and the first connecting area;
[0015] The second partition is located in the third area and is used to isolate the first anion exchange particles from the anion valve. The second partition has a plurality of second partition protrusions, and the protrusions are oriented away from the anion valve. The side walls of the second partition protrusions have a plurality of second partition side wall protrusions. A fourth partition is provided between adjacent second partition side wall protrusions. The fourth partition is also provided on the second partition between adjacent second partition protrusions. The fourth partition connects the third area and the second connecting area. The ion exchange particle regeneration device also includes: a filtering unit, including: a filtering tank for containing the liquid to be purified; a filter net for filtering the liquid to be purified in the filtering tank.
[0016] Optionally, the ion exchange particle regeneration device further includes: a detection unit for detecting the ion concentration and / or organic matter concentration in the liquid to be purified after being purified by the cation exchange chamber and the anion exchange chamber; the detection unit includes: an ion concentration detector for detecting the ion concentration in the liquid to be purified after being purified by the cation exchange chamber and the anion exchange chamber; an organic matter concentration detector for detecting the organic matter concentration in the liquid to be purified after being purified by the cation exchange chamber and the anion exchange chamber; the detection unit is selected from the following: the filtration unit is connected to the input end of the cation exchange chamber, the output end of the cation exchange chamber is connected to the input end of the anion exchange chamber, and the output end of the anion exchange chamber is connected to the input end of the detection unit; the filtration unit is connected to the input end of the anion exchange chamber, the output end of the anion exchange chamber is connected to the input end of the cation exchange chamber, and the output end of the cation exchange chamber is connected to the input end of the detection unit.
[0017] Optionally, the ion exchange particle regeneration device includes: a reverse osmosis water tank coupled to the output end of the detection unit, and used to contain purified liquid whose ion concentration and / or organic matter concentration exceeds a preset range.
[0018] Optionally, the cation exchange chamber further includes: a first cation regeneration liquid input port located in the first connection zone, and a second cation regeneration liquid input port located in the second zone; the anion exchange chamber further includes: a first anion regeneration liquid input port located in the second connection zone, and a second anion regeneration liquid input port located in the fourth zone; the ion exchange particle regeneration device further includes: a first cation regeneration liquid tank coupled to the first cation regeneration liquid input port for accommodating the first cation regeneration liquid; a second cation regeneration liquid tank coupled to the second cation regeneration liquid input port for accommodating the second cation regeneration liquid; a first anion regeneration liquid tank coupled to the first anion regeneration liquid input port for accommodating the first anion regeneration liquid; a second anion regeneration liquid tank coupled to the second anion regeneration liquid input port for accommodating the second anion regeneration liquid; the reverse osmosis water tank further includes at least one of the following: the reverse osmosis water tank is coupled to the first cation regeneration liquid input port; the reverse osmosis water tank is coupled to the second cation regeneration liquid input port; the reverse osmosis water tank is coupled to the first anion regeneration liquid input port; the reverse osmosis water tank is coupled to the second anion regeneration liquid input port.
[0019] Optionally, the ion exchange particle regeneration device further includes: a deionized water tank coupled to the output end of the detection unit, and used to contain purified liquid whose ion concentration and / or organic matter concentration is within a preset range.
[0020] Compared with the prior art, the technical solution of the embodiment of the present application has the following advantages:
[0021] The present application provides an ion exchange particle regeneration device, comprising: a cation exchange chamber, a second zone, and a first support plate; the first support plate is used to support the second cation exchange particles and also to isolate the first cation exchange particles and the second cation exchange particles, preventing the second cation exchange particles from stacking on the first cation exchange particles, reducing the probability of aggregation and / or accumulation of lumps between the first cation exchange particles, thereby improving the regeneration effect of the first cation exchange particles and the second cation exchange particles; a vibration component is coupled to the cation exchange chamber, driving the first cation exchange particles and the second cation exchange particles to vibrate when the ion exchange particles are regenerated, reducing the probability of aggregation and / or accumulation of lumps between the particles of the first cation exchange particles and between the particles of the second cation exchange particles, and also improving the regeneration effect of the first cation exchange particles and the second cation exchange particles. BRIEF DESCRIPTION OF THE DRAWINGS
[0022] In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings required for use in the embodiments or the description of the prior art will be briefly introduced below. Obviously, the drawings described below are only embodiments of the present application. For ordinary technicians in this field, other drawings can be obtained based on the provided drawings without paying any creative work.
[0023] Figure 1 It is a schematic diagram of the cross-sectional structure corresponding to an ion exchange particle regeneration device;
[0024] Figure 2 is a schematic structural diagram corresponding to an ion exchange particle regeneration device in an embodiment of the present invention;
[0025] Figure 3 is Figure 2 A schematic cross-sectional structure diagram of a first support plate placed on the area 400a;
[0026] Figure 4 is Figure 2 A schematic cross-sectional structure diagram of a second support plate placed on the area 500a;
[0027] Figure 5 is Figure 2 A schematic cross-sectional structure diagram of a first interlayer placed on the region 600a;
[0028] Figure 6 is Figure 2 A schematic cross-sectional structure diagram of a second spacer placed on the area 700a;
[0029] Figure 7 It is an expanded view of the side wall of a first support plate protrusion in an embodiment of the present invention. DETAILED DESCRIPTION
[0030] The following will be combined with the drawings in the embodiments of the present application to clearly and completely describe the technical solutions in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, not all of the embodiments. Based on the embodiments in the present application, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of this application.
[0031] As known from the background technology, in the actual ion exchange particle regeneration process, there is a problem of poor regeneration effect. The reasons for the poor regeneration effect are analyzed below.
[0032] like Figure 1 FIG. 1 is a schematic cross-sectional structure diagram of an ion exchange particle regeneration device, comprising:
[0033] The regeneration chamber 100 is used to accommodate the first ion exchange particles 101 and the second ion exchange particles 102 .
[0034] The regeneration chamber 100 includes a liquid inlet 103 and a liquid outlet 104 .
[0035] A first filter screen 105 is located at the liquid inlet 103 , and a second filter screen 106 is located at the liquid outlet 104 .
[0036] During the regeneration process, the first ion exchange particles 101 and the second ion exchange particles 102 are randomly mixed in the regeneration chamber 100, and the same regeneration liquid is introduced into the regeneration chamber 100. The regeneration liquid flows into the regeneration chamber 100 from the liquid inlet 103 and flows out of the regeneration chamber 100 from the liquid outlet 104. The first ion exchange particles 101 and the second ion exchange particles 102 are regenerated to restore their purification functions. There are the following problems:
[0037] For the sake of brevity and convenience of description, the first ion exchange particles 101 and the second ion exchange particles 102 are collectively referred to as particles.
[0038] First, the stack of first ion exchange particles 101 and second ion exchange particles 102 aggregates and / or agglomerates into a mass.
[0039] Since the first ion exchange particles 101 and the second ion exchange particles 102 are mixed together in a disorderly manner, the pressure on the particles at the bottom of the regeneration chamber 100 increases, and the probability of the particles in the bottom area 107 of the regeneration chamber 100 stacking, agglomerating and / or condensing into a mass increases, so that the regeneration liquid cannot fully contact with the particles at the bottom of the regeneration chamber 100, thereby reducing the regeneration effect of the particles. In addition:
[0040] (1) The particles that are stacked, aggregated and / or agglomerated increase the flow resistance of the regeneration liquid in the regeneration chamber 100, thereby reducing the regeneration effect and efficiency of the particles.
[0041] (2) The particles that are stacked, aggregated and / or agglomerated into agglomerates may clog the second filter screen 106, increase the flow resistance of the regeneration liquid in the regeneration chamber 100, and reduce the regeneration effect and efficiency of the particles.
[0042] Second, the first ion exchange particles 101 and the second ion exchange particles 102 cannot be regenerated independently.
[0043] Since the first ion exchange particles 101 and the second ion exchange particles 102 are randomly mixed together, the first ion exchange particles 101 and the second ion exchange particles 102 can only be regenerated using the same regeneration liquid. It is impossible to independently regenerate the first ion exchange particles 101 and the second ion exchange particles 102 corresponding to the impurity ions to be removed according to different impurity ions to be removed, thereby reducing the regeneration effect.
[0044] In view of the above technical problems, an embodiment of the present invention provides an ion exchange particle regeneration device, which can improve the regeneration effect and thus improve the purification effect.
[0045] An ion exchange particle regeneration device provided in an embodiment of the present invention includes: a cation exchange chamber, including a first area for accommodating first cation exchange particles, and a second area for accommodating second cation exchange particles; a first support plate, located in the second area, for supporting the second cation exchange particles, the second cation exchange particles are located above the first cation exchange particles; a vibration component, coupled to the cation exchange chamber, for driving the first cation exchange particles and the second cation exchange particles to vibrate when the ion exchange particles are regenerated.
[0046] In the ion exchange particle regeneration device shown in the present application, the first support plate is used to support the second cation exchange particles, and is also used to isolate the first cation exchange particles and the second cation exchange particles, preventing the second cation exchange particles from stacking on the first cation exchange particles, reducing the probability of aggregation and / or accumulation of lumps between the first cation exchange particles, thereby improving the regeneration effect of the first cation exchange particles and the second cation exchange particles; the vibration component is coupled to the cation exchange chamber, and drives the first cation exchange particles and the second cation exchange particles to vibrate when the ion exchange particles are regenerated, reducing the probability of aggregation and / or accumulation of lumps between the particles of the first cation exchange particles and between the particles of the second cation exchange particles, and also improving the regeneration effect of the first cation exchange particles and the second cation exchange particles.
[0047] refer to Figure 2 , is a structural schematic diagram corresponding to an ion exchange particle regeneration device in an embodiment of the present invention, and the ion exchange particle regeneration device may include: a cation exchange chamber 200.
[0048] The cation exchange chamber 200 includes a first zone 202 for accommodating the first cation exchange particles 201 and a second zone 204 for accommodating the second cation exchange particles 203 , and also includes a first connecting zone 205 located between the first zone 202 and the second zone 204 , and the second zone 204 is located above the first zone 202 .
[0049] It should be noted that the first area 202 may also be referred to as a first chamber, the second area 204 may also be referred to as a second chamber, and the first connecting area 205 may also be referred to as a first connecting chamber.
[0050] The material of the cation exchange chamber 200 includes: metal material (such as nickel alloy, titanium alloy, etc.) or plastic material (such as polytetrafluoroethylene, vinyl ester resin, chlorinated polyvinyl chloride, etc.).
[0051] The cation exchange chamber 200 is a column structure, and the column structure includes any of the following: a cylindrical structure, an elliptical cylindrical structure, a square cylindrical structure, etc. The present application embodiment does not limit the material and specific column structure of the cation exchange chamber 200, and those skilled in the art can adjust the settings according to actual conditions. In the present embodiment, the material of the cation exchange chamber 200 is a metal material, and the cation exchange chamber 200 is a cylindrical structure.
[0052] The cation exchange chamber 200 further includes: a first cation regeneration liquid input port 206 located in the first connection zone 205 , and a second cation regeneration liquid input port 207 located in the second zone 204 .
[0053] In this embodiment, the first cation regeneration liquid input port 206 is located between the cation valve 208 and the first zone 202 , and is close to the cation valve 208 .
[0054] It should be noted that the cation exchange chamber 200 includes a first zone 202, a second zone 204 and a first connecting zone 205, but this does not limit the present application. Those skilled in the art can set the number of partitions and the number of connecting zones of the cation exchange chamber 200 according to actual needs. For example, if the cation exchange chamber 200 needs to accommodate three types of cation exchange particles, the cation exchange chamber 200 is provided with three partitions and connecting zones between the partitions.
[0055] Continue to refer Figure 2 The ion exchange particle regeneration device may include: an anion exchange chamber 300.
[0056] The anion exchange chamber 300 includes a third zone 302 for accommodating the first anion exchange particles 301 and a fourth zone 304 for accommodating the second anion exchange particles 303 , and also includes a second connecting zone 305 located between the third zone 302 and the fourth zone 304 , and the fourth zone 304 is located above the third zone 302 .
[0057] It should be noted that the third area 302 may also be referred to as a third chamber, the fourth area 304 may also be referred to as a fourth chamber, and the second connecting area 305 may also be referred to as a second connecting chamber.
[0058] The material of the anion exchange chamber 300 includes: metal material (such as nickel alloy, titanium alloy, etc.) or plastic material (such as polytetrafluoroethylene, vinyl ester resin, chlorinated polyvinyl chloride, etc.);
[0059] The anion exchange chamber 300 is a column structure, and the column structure includes any of the following: a cylindrical structure, an elliptical cylindrical structure, a square cylindrical structure, etc. The present application embodiment does not limit the material and specific column structure of the anion exchange chamber 300, and those skilled in the art can adjust the settings according to actual conditions. In this embodiment, the material of the anion exchange chamber 300 is a metal material, and the anion exchange chamber 300 is a cylindrical structure.
[0060] The anion exchange chamber 300 further includes: a first anion regeneration liquid input port 306 located in the second connection zone 305 , and a second anion regeneration liquid input port 307 located in the fourth zone 304 .
[0061] In this embodiment, the first anion regeneration liquid input port 306 is located between the anion valve 308 and the third zone 302 , and is close to the anion valve 308 .
[0062] It should be noted that the anion exchange chamber 300 includes a third zone 302, a fourth zone 304 and a second connecting zone 305, but this does not limit the present application. Those skilled in the art can set the number of partitions and the number of connecting zones of the anion exchange chamber 300 according to actual needs. For example, if the anion exchange chamber 300 needs to accommodate three types of anion exchange particles, the anion exchange chamber 300 is provided with three partitions and connecting zones between the partitions.
[0063] The first cation exchange particles 201 contained in the first zone 202 are adsorbed with first impurity cations of the purified liquid; the second cation exchange particles 203 contained in the second zone 204 are adsorbed with second impurity cations of the purified liquid; the first anion exchange particles 301 contained in the third zone 302 are adsorbed with first impurity anions of the purified liquid; and the second anion exchange particles 303 contained in the fourth zone 304 are adsorbed with second impurity anions of the purified liquid.
[0064] The first cation exchange particles 201 include one or more of weakly acidic first cation exchange resin particles, weakly acidic first cation exchange montmorillonite particles and weakly acidic first cation exchange fiber particles; the second cation exchange particles 203 include one or more of strongly acidic second cation exchange resin particles, strongly acidic second cation exchange montmorillonite particles and strongly acidic second cation exchange fiber particles; the first anion exchange particles 301 include one or more of weakly basic first anion exchange resin particles, weakly basic first anion exchange montmorillonite particles and weakly basic first anion exchange fiber particles; the second anion exchange particles 303 include one or more of strongly basic second anion exchange resin particles, strongly basic second anion exchange montmorillonite particles and strongly basic second cation exchange fiber particles.
[0065] The types of the first impurity cations include at least calcium ions and / or magnesium ions; the types of the second impurity cations include at least sodium ions and / or potassium ions; the types of the first impurity anions include at least hydroxide ions and / or citrate ions; the types of the second impurity anions include at least sulfate ions and / or nitrate ions.
[0066] In this embodiment, the first cation exchange particles 201 are weakly acidic first cation exchange resin particles, and the first impurity cations are calcium ions and magnesium ions; the second cation exchange particles 203 are strongly acidic first cation exchange resin particles, and the second impurity cations are sodium ions and potassium ions; the first anion exchange particles 301 are weakly basic first anion exchange resin particles, and the first impurity anions are hydroxide ions and citrate ions; the second anion exchange particles 303 are strongly basic second anion exchange resin particles, and the second impurity anions are sulfate ions and nitrate ions.
[0067] In this embodiment, the regeneration process of the first cation exchange particles 201 adsorbed with the first impurity cations of the purified liquid includes: using a weak acid such as acetic acid or malic acid to soak the first cation exchange particles 201 adsorbed with the first impurity cations of the purified liquid, and using hydrogen ions in the weak acid to replace the first impurity cations and separate them from the first cation exchange particles 201, so as to obtain weakly acidic first cation exchange resin particles adsorbed with hydrogen ions; the regeneration process of the second cation exchange particles 203 adsorbed with the second impurity cations of the purified liquid includes: using a strong acid such as hydrochloric acid or sulfuric acid to soak the second cation exchange particles 203 adsorbed with the second impurity cations of the purified liquid, and using hydrogen ions in the strong acid to replace the second impurity cations and separate them from the second cation exchange particles 203, so as to obtain strongly acidic second cation exchange resin particles adsorbed with hydrogen ions.
[0068] In this embodiment, the regeneration process of the first anion exchange particles 301 adsorbing the first impurity anions of the purified liquid includes: soaking the first anion exchange particles 301 adsorbing the first impurity anions of the purified liquid with a weak base such as ammonia water or sodium bicarbonate, and replacing the first impurity anions from the first anion exchange particles 301 with hydroxide ions in the weak base to obtain weakly basic first anion exchange resin particles adsorbing hydroxide ions; the regeneration process of the second anion exchange particles 303 adsorbing the second impurity anions of the purified liquid includes: soaking the second anion exchange particles 303 adsorbing the second impurity anions of the purified liquid with a strong base such as sodium hydroxide or potassium hydroxide, and replacing the second impurity anions from the second anion exchange particles 303 with hydroxide ions in the strong base to obtain strongly basic second anion exchange resin particles adsorbing hydroxide ions.
[0069] In this embodiment, the pH value of the strong acid is greater than or equal to 2 and less than or equal to 4, the pH value of the weak acid is greater than 4 and less than or equal to 6, the pH value of the strong base is greater than 11, and the pH value of the weak base is greater than or equal to 8 and less than or equal to 11.
[0070] The particle characteristics (size, quantity, material, shape, etc.) of the first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301, and the second anion exchange particles 303 are selected according to actual needs and are not intended to limit the present application. In this embodiment, the materials of the first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301, and the second anion exchange particles 303 are all resin particles, and the shape of the resin particles is spherical, and the diameter of the sphere ranges from 0.4 mm to 1 mm.
[0071] Continue to refer Figure 2 The ion exchange particle regeneration device may include: a cation valve 208.
[0072] The cation valve 208 is located in the first connecting area 205, and is used to isolate the mutual flow between the first cation regeneration liquid flowing through the first area 202 and the second cation regeneration liquid flowing through the second area 204. In this embodiment, when the cation valve 208 is closed, the first cation regeneration liquid flowing through the first area 202 cannot flow to the second area 204, and the second cation regeneration liquid flowing through the second area 204 cannot flow to the first area 202, so that the first cation regeneration liquid can independently regenerate the first cation exchange particles 201, and the second cation regeneration liquid can independently regenerate the second cation exchange particles 203.
[0073] The types of the cationic valve 208 include: one or more of a butterfly valve, a ball valve, and a plug valve. In this embodiment, the cationic valve 208 is a butterfly valve.
[0074] The structure of the butterfly valve comprises:
[0075] Valve body: Usually round or oval in shape, with a flow channel inside.
[0076] Butterfly disc: Usually circular, the flow of fluid is controlled by rotating the butterfly disc.
[0077] Valve shaft: The valve shaft connects the butterfly plate and the operating device, allowing the butterfly plate to rotate.
[0078] Sealing ring: The sealing ring is located between the butterfly plate and the valve body to ensure that the valve can be sealed when closed.
[0079] Operating device: The operating device is used to drive the rotation of the butterfly plate and can be manual, electric, pneumatic or hydraulic.
[0080] In this embodiment, the first connection area 205 is used to provide a position space for opening and closing the cation valve 208 .
[0081] In this embodiment, the first cation regeneration liquid is used for regenerating the first cation exchange particles 201 , and the second cation regeneration liquid is used for regenerating the second cation exchange particles 203 .
[0082] The first connection area 205 includes:
[0083] The first cationic regeneration liquid outlet 209 is located in the first zone 202 .
[0084] The second cation regeneration liquid outlet 210 is located between the second zone 204 and the cation valve 208 .
[0085] The cation valve 208 is detachably connected to the cation exchange chamber 200 .
[0086] Continue to refer Figure 2 The ion exchange particle regeneration device may include: an anion valve 308.
[0087] The anion valve 308 is located in the second connecting area 305, and is used to isolate the mutual flow between the first anion regeneration liquid flowing through the third area 302 and the second anion regeneration liquid flowing through the fourth area 304. In this embodiment, when the anion valve 308 is closed, the first anion regeneration liquid flowing through the third area 302 cannot flow to the fourth area 304, and the second anion regeneration liquid flowing through the fourth area 304 cannot flow to the third area 302, so that the first anion regeneration liquid can independently regenerate the first anion exchange particles 301, and the second anion regeneration liquid can independently regenerate the second anion exchange particles 303.
[0088] The types of the anion valve 308 include: one or more of a butterfly valve, a ball valve, and a plug valve. In this embodiment, the anion valve 308 is a butterfly valve.
[0089] The structure of the butterfly valve is described with reference to the description of the butterfly valve of the aforementioned cationic valve 208 and will not be described here.
[0090] In this embodiment, the second connection area 305 is used to provide a position space for opening and closing the anion valve 308 .
[0091] In this embodiment, the first anion regeneration liquid is used to regenerate the first anion exchange particles 301 , and the second anion regeneration liquid is used to regenerate the second anion exchange particles 303 .
[0092] The second connection area 305 includes:
[0093] The first anion regeneration liquid outlet 309 is located in the third zone 302 .
[0094] The second anion regeneration liquid output port 310 is located between the fourth zone 304 and the anion valve 308 .
[0095] The anion valve 308 is detachably connected to the anion exchange chamber 300 .
[0096] Continue to refer Figure 2 The ion exchange particle regeneration device may include: a filtering unit 200a.
[0097] The filtering unit 200a includes: a filtering tank (not shown)
[0098] The filtering pool is used to contain the liquid to be purified.
[0099] The material of the filter pool includes: metal material (such as nickel alloy, titanium alloy, etc.) or plastic material (such as polytetrafluoroethylene, vinyl ester resin, chlorinated polyvinyl chloride, etc.); the filter pool is a column structure, and the column structure includes any of the following: cylindrical structure, elliptical cylindrical structure, square cylindrical structure, etc. The embodiment of the present application does not limit the material and specific column structure of the filter pool, and those skilled in the art can adjust the settings according to actual conditions. In this embodiment, the filter pool material is metal material, and the filter pool is a cylindrical structure.
[0100] The filtering unit 200a further includes a filtering net (not shown).
[0101] The filter screen is used to filter the liquid to be purified in the filter pool.
[0102] In this embodiment, the material of the filter mesh includes stainless steel, nylon and other materials. The filter mesh includes, for example, activated carbon with a filtering function, which is used to filter the liquid to be purified to filter out impurities such as solid particles and plastic particles in the water.
[0103] The regeneration process of the first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301 and the second anion exchange particles 303 also includes: opening the cation valve 208 and the anion valve 308, using the liquid to be purified to rinse the regenerated first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301 and the second anion exchange particles 303, and cooperating with the detection unit 200d to detect whether the regeneration of the first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301 and the second anion exchange particles 303 meets the process requirements.
[0104] Continue to refer Figure 2 The ion exchange particle regeneration device may include: a vibration component.
[0105] The vibration component can be used to drive the first cation exchange particles 201 and the second cation exchange particles 203 to vibrate when the ion exchange particles are regenerated, and can also be used to drive the first anion exchange particles 301 and the second anion exchange particles 303 to vibrate when the ion exchange particles are regenerated, which has the following beneficial effects:
[0106] First, the stacking aggregation and / or agglomeration of the first cation exchange particles 201 in the first zone 202 is reduced, so that the first cation regeneration liquid is in full contact with the first cation exchange particles 201, thereby improving the regeneration effect of the first cation exchange particles 201; at the same time, the stacking aggregation and / or agglomeration of the second cation exchange particles 203 in the second zone 204 is reduced, so that the second cation regeneration liquid is in full contact with the second cation exchange particles 203, thereby improving the regeneration effect of the second cation exchange particles 203.
[0107] In addition, reducing the stacking aggregation and / or agglomeration of the first cation exchange particles 201 in the first zone 202 can reduce the flow resistance of the first cation regeneration liquid in the first zone 202, thereby improving the regeneration effect and regeneration efficiency; reducing the stacking aggregation and / or agglomeration of the second cation exchange particles 203 in the second zone 204 can reduce the flow resistance of the second cation regeneration liquid in the second zone 204, thereby improving the regeneration effect and regeneration efficiency.
[0108] Second, the stacking aggregation and / or agglomeration of the first anion exchange particles 301 in the third zone 302 is reduced, so that the first anion regeneration liquid is in full contact with the first anion exchange particles 301, thereby improving the regeneration effect of the first anion exchange particles 301; at the same time, the stacking aggregation and / or agglomeration of the second anion exchange particles 303 in the fourth zone 304 is reduced, so that the second anion regeneration liquid is in full contact with the second anion exchange particles 303, thereby improving the regeneration effect of the second anion exchange particles 303.
[0109] In addition, reducing the stacking aggregation and / or agglomeration of the first anion exchange particles 301 in the third zone 302 can reduce the flow resistance of the first anion regeneration liquid in the third zone 302, thereby improving the regeneration effect and regeneration efficiency; reducing the stacking aggregation and / or agglomeration of the second anion exchange particles 303 in the fourth zone 304 can reduce the flow resistance of the second anion regeneration liquid in the fourth zone 304, thereby improving the regeneration effect and regeneration efficiency.
[0110] Third, the vibration component drives the first cation exchange particles 201 to vibrate, which can reduce the first cation exchange particles from blocking the first barrier layer 600 (see Figure 5 ) probability, reducing the flow resistance of the first cation regeneration liquid and improving the regeneration effect; the vibration component drives the second cation exchange particles 203 to vibrate, which can reduce the second cation exchange particles blocking the first support plate 400 (see Figure 3 ) probability, reducing the flow resistance of the second cation regeneration liquid and improving the regeneration effect.
[0111] Fourth, the vibration component drives the first anion exchange particles 301 to vibrate, which can reduce the first anion exchange particles from blocking the second barrier layer 700 (see Figure 6 ) probability, reducing the flow resistance of the first anion regeneration liquid and improving the regeneration effect; the vibration component drives the second anion exchange particles 303 to vibrate, which can reduce the second anion exchange particles blocking the second support plate 500 (see Figure 4 ) probability, reducing the flow resistance of the second anion regeneration liquid and improving the regeneration effect.
[0112] It should be noted that, in this embodiment, the ion exchange particles include: first cation exchange particles 201, second cation exchange particles 203, first anion exchange particles 301, and second anion exchange particles 303, but this is not intended to limit the present application.
[0113] The vibration component comprises:
[0114] The connecting rod 200 b is coupled to the cation exchange chamber 200 and the anion exchange chamber 300 .
[0115] The vibration motor 200c is coupled to the connecting rod 200b.
[0116] A vibration component is coupled to the cation exchange chamber 200 .
[0117] In this embodiment, the vibration motor 200c is connected to the connecting rod 200b, and the connecting rod 200b is connected to the cation exchange chamber 200 and the anion exchange chamber 300. The vibration generated by the vibration motor 200c drives the cation exchange chamber 200 and the anion exchange chamber 300 to vibrate through the connecting rod 200b, thereby driving the first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301 and the second anion exchange particles 303 to vibrate.
[0118] In this embodiment, the vibration motor 200c drives the cation exchange chamber 200 and the anion exchange chamber 300 to vibrate along the X direction and / or the Y direction.
[0119] The structure of the vibration motor 200c mainly includes: a rotor (eccentric wheel): usually composed of a semicircular or irregularly shaped metal block, which is installed away from the center axis. When the motor rotates, the rotation of the eccentric wheel will generate an unbalanced torque, thereby causing vibration. The rotor is connected to the connecting rod 200b; a stator (coil and magnet), a group of wire coils wound on the stator frame, which will generate a magnetic field when current passes through; the magnet interacts with the magnetic field generated by the coil to drive the rotor to rotate; bearings (or support structures): used to support the rotor and allow it to rotate freely while maintaining the stability of the rotor; a casing: protects all internal components and is usually made of plastic or metal materials.
[0120] Continue to refer Figure 2 The ion exchange particle regeneration device may include: a detection unit 200d.
[0121] The detection unit 200d is used to detect the ion concentration and / or organic matter concentration in the liquid to be purified after being purified by the cation exchange chamber 200 and the anion exchange chamber 300. In this embodiment, the detection unit 200d is used to detect whether the ion concentration and / or organic matter concentration in the liquid to be purified is within a preset range after purification by the regenerated first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301 and the second anion exchange particles 303. If it exceeds the preset range, the first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301 and the second anion exchange particles 303 need to be regenerated.
[0122] It should be noted that when the liquid to be purified is purified by the regenerated first cation exchange particles 201, second cation exchange particles 203, first anion exchange particles 301 and second anion exchange particles 303, the cation valve 208 and the anion valve 308 are in an open state.
[0123] The detection unit is selected from the following:
[0124] The filtration unit is connected to the input end of the cation exchange chamber, the output end of the cation exchange chamber is connected to the input end of the anion exchange chamber, and the output end of the anion exchange chamber is connected to the input end of the detection unit;
[0125] The filtration unit is connected to the input end of the anion exchange chamber, the output end of the anion exchange chamber is connected to the input end of the cation exchange chamber, and the output end of the cation exchange chamber is connected to the input end of the detection unit.
[0126] In this embodiment, the filtration unit 200a is connected to the input end SR1 of the cation exchange chamber through a valve F1, the output end SC1 of the cation exchange chamber is connected to the input end SR2 of the anion exchange chamber through a valve F2, and the output end SC2 of the anion exchange chamber is connected to the input end SR3 of the detection unit through a valve F3.
[0127] The detection unit 200d includes: an ion concentration detector (not shown).
[0128] The ion concentration detector is used to detect the ion concentration in the liquid to be purified after the liquid is purified by the cation exchange chamber 200 and the anion exchange chamber 300.
[0129] The working principle of the ion concentration detector may include: detecting the electrical conductivity of the purified liquid, the ions in the purified liquid being able to conduct electricity, and determining the ion concentration in the purified liquid by testing the electrical conductivity of the purified liquid.
[0130] The working principle of the ion concentration detector may also include: detecting the color change of the purified liquid, allowing the ions in the purified liquid to change the color of certain reagents, and determining the ion concentration in the purified liquid by the intensity of the color.
[0131] The detection unit 200d includes an organic matter concentration detector (not shown).
[0132] The organic matter concentration detector is used to detect the organic matter concentration in the liquid to be purified after the liquid is purified by the cation exchange chamber 200 and the anion exchange chamber 300.
[0133] The working principle of the organic matter concentration detector may include: infrared spectroscopy, which is based on the principle that organic molecules will vibrate and absorb under infrared light of a specific wavelength. Different organic molecules have different absorption characteristics. By detecting these characteristic absorption peaks, the type and concentration of the organic matter can be determined.
[0134] Continue to refer Figure 2 , the ion exchange particle regeneration device may include:
[0135] The first cation regeneration liquid pool 211 is coupled to the first cation regeneration liquid input port 206 and is used to accommodate the first cation regeneration liquid. In this embodiment, the first cation regeneration liquid pool 211 is connected to the first cation regeneration liquid input port 206 via a valve F4.
[0136] The materials of the first cation regeneration liquid pool 211 include: metal materials (such as nickel alloy, titanium alloy, etc.) or plastic materials (such as polytetrafluoroethylene, vinyl ester resin, chlorinated polyvinyl chloride, etc.); the first cation regeneration liquid pool 211 is a columnar structure, and the columnar structure includes any of the following: a cylindrical structure, an elliptical cylindrical structure, a square cylindrical structure, etc. The embodiment of the present application does not limit the material and specific columnar structure of the first cation regeneration liquid pool 211, and those skilled in the art can adjust the settings according to actual conditions. In this embodiment, the material of the first cation regeneration liquid pool 211 is metal, and the first cation regeneration liquid pool 211 is a cylindrical structure.
[0137] The second cation regeneration liquid pool 212 is coupled to the second cation regeneration liquid input port 207 and is used to accommodate the second cation regeneration liquid. In this embodiment, the second cation regeneration liquid pool 212 is connected to the second cation regeneration liquid input port 207 via a valve F5.
[0138] The materials of the second cation regeneration liquid pool 212 include: metal materials (such as nickel alloys, titanium alloys, etc.) or plastic materials (such as polytetrafluoroethylene, vinyl ester resins, chlorinated polyvinyl chloride, etc.); the second cation regeneration liquid pool 212 is a columnar structure, and the columnar structure includes any of the following: a cylindrical structure, an elliptical cylindrical structure, a square cylindrical structure, etc. The embodiment of the present application does not limit the material and specific columnar structure of the second cation regeneration liquid pool 212, and those skilled in the art can adjust the settings according to actual conditions. In this embodiment, the material of the second cation regeneration liquid pool 212 is metal, and the second cation regeneration liquid pool 212 is a cylindrical structure.
[0139] The first anion regeneration liquid pool 311 is coupled to the first anion regeneration liquid input port 306 and is used to contain the first anion regeneration liquid. In this embodiment, the first anion regeneration liquid pool 311 is connected to the first anion regeneration liquid input port 306 via a valve F6.
[0140] The materials of the first anion regeneration liquid pool 311 include: metal materials (such as nickel alloys, titanium alloys, etc.) or plastic materials (such as polytetrafluoroethylene, vinyl ester resins, chlorinated polyvinyl chloride, etc.); the first anion regeneration liquid pool 311 is a columnar structure, and the columnar structure includes any of the following: a cylindrical structure, an elliptical cylindrical structure, a square cylindrical structure, etc. The embodiment of the present application does not limit the material and specific columnar structure of the first anion regeneration liquid pool 311, and those skilled in the art can adjust the settings according to actual conditions. In this embodiment, the material of the first anion regeneration liquid pool 311 is metal, and the first anion regeneration liquid pool 311 is a cylindrical structure.
[0141] The second anion regeneration liquid pool 312 is coupled to the second anion regeneration liquid input port 307 and is used to accommodate the second anion regeneration liquid. In this embodiment, the second anion regeneration liquid pool 312 is connected to the second anion regeneration liquid input port 307 via a valve F7.
[0142] The materials of the second anion regeneration liquid pool 312 include: metal materials (such as nickel alloys, titanium alloys, etc.) or plastic materials (such as polytetrafluoroethylene, vinyl ester resins, chlorinated polyvinyl chloride, etc.); the second anion regeneration liquid pool 312 is a columnar structure, and the columnar structure includes any of the following: a cylindrical structure, an elliptical cylindrical structure, a square cylindrical structure, etc. The embodiment of the present application does not limit the material and specific columnar structure of the second anion regeneration liquid pool 312, and those skilled in the art can adjust the settings according to actual conditions. In this embodiment, the material of the second anion regeneration liquid pool 312 is metal, and the second anion regeneration liquid pool 312 is a cylindrical structure.
[0143] Continue to refer Figure 2 , the ion exchange particle regeneration device may include:
[0144] The first cation regeneration liquid waste liquid pool 213 is coupled to the first cation regeneration liquid outlet 209, and is used to accommodate the waste liquid generated by the first cation regeneration liquid after regenerating the first cation exchange particles 201. In this embodiment, the first cation regeneration liquid waste liquid pool 213 is connected to the first cation regeneration liquid outlet 209 through a valve F8.
[0145] The second cation regeneration liquid waste liquid pool 214 is coupled to the second cation regeneration liquid outlet 210, and is used to accommodate the waste liquid generated by the second cation regeneration liquid after regenerating the second cation exchange particles 203. In this embodiment, the second cation regeneration liquid waste liquid pool 214 is connected to the second cation regeneration liquid outlet 210 via a valve F9.
[0146] The first anion regeneration liquid waste pool 313 is coupled to the first anion regeneration liquid outlet 309, and is used to accommodate the waste liquid generated by the first anion regeneration liquid after regenerating the first anion exchange particles 301. In this embodiment, the first anion regeneration liquid waste pool 313 is connected to the first anion regeneration liquid outlet 309 through a valve F10.
[0147] The second anion regeneration liquid waste pool 314 is coupled to the second anion regeneration liquid outlet 310, and is used to accommodate the waste liquid generated by the second anion regeneration liquid after regenerating the second anion exchange particles 303. In this embodiment, the second anion regeneration liquid waste pool 314 is connected to the second anion regeneration liquid outlet 310 via a valve F11.
[0148] In other embodiments, the waste liquid generated by regenerating the first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301, and the second anion exchange particles 303 can share a waste liquid pool.
[0149] Continue to refer Figure 2 The ion exchange particle regeneration device may include: a reverse osmosis water tank 200n.
[0150] The reverse osmosis water tank 200n is coupled to the output terminal SC3 of the detection unit and is used to contain purified liquid whose ion concentration and / or organic matter concentration exceeds a preset range.
[0151] In this embodiment, the reverse osmosis pool 200n is connected to the output end SC3 of the detection unit through the reverse osmosis pool valve F12. The detection unit 200d detects the liquid to be purified, and when the ion concentration and / or organic matter concentration in the purified liquid exceeds a preset range after purification by the regenerated first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301 and the second anion exchange particles 303, the reverse osmosis pool valve F12 is opened, so that the purified liquid flows to the reverse osmosis pool 200n.
[0152] The material of the reverse osmosis pool 200n includes: metal material (such as nickel alloy, titanium alloy, etc.) or plastic material (such as polytetrafluoroethylene, vinyl ester resin, chlorinated polyvinyl chloride, etc.); the reverse osmosis pool 200n is a columnar structure, and the columnar structure includes any of the following: a cylindrical structure, an elliptical cylindrical structure, a square cylindrical structure, etc. The embodiment of the present application does not limit the material and specific columnar structure of the reverse osmosis pool 200n, and those skilled in the art can adjust the settings according to actual conditions. In this embodiment, the reverse osmosis pool 200n is made of metal, and the reverse osmosis pool 200n is a cylindrical structure.
[0153] The reverse osmosis water pool also includes at least one of the following:
[0154] The reverse osmosis water tank is coupled to the first cation regeneration liquid input port, and the purified liquid in the reverse osmosis water tank that exceeds a preset range is used to clean the regenerated first cation exchange particles and the first zone.
[0155] The reverse osmosis water tank is coupled to the second cation regeneration liquid input port, and the purified liquid in the reverse osmosis water tank that exceeds a preset range is used to clean the regenerated second cation exchange particles and the second zone.
[0156] The reverse osmosis water tank is coupled to the first anion regeneration liquid input port, and the purified liquid in the reverse osmosis water tank that exceeds a preset range is used to clean the regenerated first anion exchange particles and the third zone.
[0157] The reverse osmosis water tank is coupled to the second anion regeneration liquid input port, and the purified liquid in the reverse osmosis water tank that exceeds a preset range is used to clean the regenerated second anion exchange particles and the fourth zone.
[0158] It should be noted that when the first cation exchange particles 201 and the first zone 202, the second cation exchange particles 203 and the second zone 204 are cleaned and regenerated, the cation valve 208 is in a closed state, and when the first anion exchange particles 301 and the third zone 302, the second anion exchange particles 303 and the fourth zone 304 are cleaned and regenerated, the anion valve 308 is in a closed state, that is, the first cation exchange particles 201 and the first zone 202, the second cation exchange particles 203 and the second zone 204, the first anion exchange particles 301 and the third zone 302, the second anion exchange particles 303 and the fourth zone 304 after cleaning and regeneration are independently cleaned to improve the cleaning effect.
[0159] In this embodiment, the reverse osmosis water pool 200n is connected to the first cation regeneration liquid input port 206 through the reverse osmosis water pool first valve F13, the reverse osmosis water pool 200n is connected to the second cation regeneration liquid input port 207 through the reverse osmosis water pool second valve F14, the reverse osmosis water pool 200n is connected to the first anion regeneration liquid input port 306 through the reverse osmosis water pool third valve F15, and the reverse osmosis water pool 200n is connected to the second anion regeneration liquid input port 307 through the reverse osmosis water pool fourth valve F16.
[0160] Continue to refer Figure 2 The ion exchange particle regeneration device may include: a deionized water tank 200k.
[0161] The deionized water pool 200k is used to hold the purified liquid whose ion concentration and / or organic matter concentration meets the preset range after the first cation exchange particles 201, the second cation exchange particles 203, the first anion exchange particles 301 and the second anion exchange particles 303 are regenerated.
[0162] The deionized water pool 200k is coupled to the output end SC3 of the detection unit. In this embodiment, the deionized water pool 200k is connected to the output end SC3 of the detection unit through the deionized water pool valve F17.
[0163] The material of the deionized water pool 200k includes: metal material (such as nickel alloy, titanium alloy, etc.) or plastic material (such as polytetrafluoroethylene, vinyl ester resin, chlorinated polyvinyl chloride, etc.); the deionized water pool 200k is a columnar structure, and the columnar structure includes any of the following: a cylindrical structure, an elliptical cylindrical structure, a square cylindrical structure, etc. The embodiment of the present application does not limit the material and specific columnar structure of the deionized water pool 200k, and those skilled in the art can adjust the settings according to actual conditions. In this embodiment, the material of the deionized water pool 200k is metal, and the deionized water pool 200k is a cylindrical structure.
[0164] Continue to refer Figure 2 and Figure 3 ,in, Figure 3 is Figure 2 A schematic cross-sectional structure diagram of a first support plate placed on the area 400a; the ion exchange particle regeneration device may include: a first support plate 400.
[0165] The first support plate 400 is used to support the second cation exchange particles 203, which are located above the first cation exchange particles 201, and is also used to isolate the first cation exchange particles 201 and the second cation exchange particles 203, preventing the second cation exchange particles from stacking on the first cation exchange particles 201, thereby reducing the probability of aggregation and / or accumulation of agglomerations between the first cation exchange particles 201, thereby improving the regeneration effect of the first cation exchange particles 201 and the second cation exchange particles 203.
[0166] The first support plate 400 is also used to isolate the second cation exchange particles 203 from the cation valve 208. When the cation valve 208 is opened, the second cation exchange particles 203 are prevented from moving between the first zone 202 and the cation valve 208, thereby reducing the probability of a decrease in the number of the second cation exchange particles 203 in the second zone 204, thereby improving the regeneration effect.
[0167] In this embodiment, the first support plate 400 is located in the second area 204 . In other embodiments, the first support plate 400 may be located in the first connection area 205 .
[0168] In order to make the drawings concise and clear, and to more clearly show the structure of the first support plate 400, the cation exchange chamber 200 and the first support plate 400 are drawn separately, corresponding to Figure 2 and Figure 3 The area 400a within the second zone 204 is used to place the first support plate 400.
[0169] The first support plate 400 includes a base plate 400b, which is used to provide a location space for setting the first support plate protrusions, and is also used to provide support for the first support plate protrusions and connections between the first support plate protrusions.
[0170] The first support plate has a plurality of first support plate protrusions, and the protrusions are oriented in a direction away from the cationic valve. The side wall of the first support plate protrusion has a plurality of first support plate side wall protrusions. A first interval is provided between adjacent first support plate side wall protrusions, and the first interval is also provided on the first support plate between adjacent first support plate protrusions.
[0171] In this embodiment, the first support plate protrusions are evenly distributed on the first support plate. In other embodiments, they may be unevenly distributed, but this does not limit the present application.
[0172] The plurality of first support plate protrusions have the following beneficial effects: providing space for setting the first interval, reducing the flow resistance of the second cation regeneration liquid flowing through the second zone, thereby improving the regeneration effect.
[0173] The plurality of first support plate sidewall protrusions have the following beneficial effects: preventing the second cationic regeneration particles from moving to the first interval, thereby reducing the probability of the second cationic regeneration particles blocking the first interval.
[0174] The first partition has the following beneficial effect: it provides a flow channel for the second cation regeneration liquid to flow through the second zone 204.
[0175] In this embodiment, the first support plate 400 has two first support plate protrusions, namely a first support plate protrusion 401 and a first support plate protrusion 402. The first support plate protrusion 401 is oriented away from the cationic valve 208, and the first support plate protrusion 402 is oriented away from the cationic valve 208.
[0176] In this embodiment, the side wall of the first support plate protrusion 401 has four first support plate side wall protrusions, namely, the first support plate side wall protrusion 401a, the first support plate side wall protrusion 401b, the first support plate side wall protrusion 401c and the first support plate side wall protrusion 401d; the side wall of the first support plate protrusion 402 has four first support plate side wall protrusions, namely, the first support plate side wall protrusion 402a, the first support plate side wall protrusion 402b, the first support plate side wall protrusion 402c and the first support plate side wall protrusion 402d.
[0177] A first spacer is provided between adjacent protrusions on the side walls of the first support plate, and the first spacer is also provided on the first support plate between adjacent protrusions on the first support plate. For the convenience of description, the first spacer provided between adjacent protrusions on the side walls of the first support plate is a first spacer 403a, and the first spacer provided on the first support plate 400 between adjacent protrusions on the first support plate is a first spacer 403b.
[0178] The shape of the first interval includes: a square, a triangle, a polygon, a circle, and an ellipse. In this embodiment, the shape of the first interval is a square.
[0179] In this embodiment, a first spacer 403a is provided between the first support plate side wall protrusion 401a and the first support plate side wall protrusion 401b, a first spacer 403a is provided between the first support plate side wall protrusion 401c and the first support plate side wall protrusion 401d, a first spacer 403a is provided between the first support plate side wall protrusion 402a and the first support plate side wall protrusion 402b, and a first spacer 403a is provided between the first support plate side wall protrusion 402c and the first support plate side wall protrusion 402d; the first spacer 403b is provided on the first support plate 400 between the adjacent first support plate protrusions 401 and 402.
[0180] In this embodiment, the first support plate protrusion has a first support plate cavity 401e, and the first interval connects the second area 204 and the first connecting area 205, that is, the second area 204 is connected to the first interval 403a, the first interval 403a is connected to the first support plate cavity 401e, the first support plate cavity 401e is connected to the first connecting area 205, and the second area 204 is connected to the first interval 403b, and the first interval 403b is connected to the first connecting area 205.
[0181] In this embodiment, the first support plate 400 is detachably connected to the cation exchange chamber 200. The shape of the protrusion of the first support plate includes: one or more of a cylinder, a square cylinder and a truncated cone; in this embodiment, the shape of the protrusion of the first support plate is a truncated cone, and the bottom (large bottom) of the truncated cone with a larger bottom area is connected to the first support plate 400, which has the following beneficial effects:
[0182] First, it is convenient to take out the second cation exchange particles 203 between the adjacent protrusions of the first support plate. In the direction away from the cation valve 208 toward the second area 204, the space between the adjacent protrusions of the first support plate increases.
[0183] Second, the truncated cone provides more space for the first intervals, so that more first intervals can be designed on the raised side wall of the first support plate.
[0184] For example, the cylinder and the truncated cone share the same base with the largest bottom area, and the side area provided by the truncated cone is larger than the side area provided by the cylinder.
[0185] The shape of the protrusion on the side wall of the first support plate includes: an outwardly convex sphere, or a part of a sphere. In this embodiment, the shape of the protrusion on the side wall of the first support plate is a part of a sphere, that is, an outwardly convex curved surface.
[0186] In some embodiments, the side wall of the first support plate may include multiple layers of first support plate side wall protrusions, and the number of first support plate side wall protrusions of each layer increases layer by layer from the top (small bottom of the cone) to the bottom (large bottom of the cone), thereby providing more position space for the setting of the first interval, reducing the flow resistance of the second cation regeneration liquid flowing through the second zone, and further improving the regeneration effect.
[0187] refer to Figure 7 , Figure 7 It is a side wall expansion diagram of a first support plate protrusion in an embodiment of the present invention. In this embodiment, the first support plate protrusion 800 is in the shape of a truncated cone, and the side wall expansion diagram of the truncated cone is an annular sector SX. On the annular sector SX, the first support plate protrusion 800 may include 18 first support plate side wall protrusions 801, and first intervals 801a are provided between adjacent first support plate side wall protrusions 801. Adjacent first support plate side wall protrusions 801 are connected by side wall blocks CBK on the first support plate side wall.
[0188] Although in Figure 7 In the example, a support plate protrusion 800 includes four layers of first support plate side wall protrusions 801, and the number of first support plate side wall protrusions 801 in each layer is increased by one. However, in the specific implementation, the specific number and distribution of the first support plate side wall protrusions 801 are not limited. Figure 3 The illustrated case is that the protrusions of the first support plate include two layers of protrusions on the side walls of the first support plate.
[0189] In a specific implementation, for the first support plate, its base, the first support plate protrusion, and the first support plate side wall protrusion can be integrally formed.
[0190] like Figure 3 In the illustrated embodiment, the base 400b, the first support plate protrusion and the first support plate side wall protrusion are integrally formed.
[0191] It should be noted that, regarding the characteristic parameters such as the height, number, spacing of the first support plate protrusions, and the characteristic parameters such as the height, number, spacing of the first support plate side wall protrusions, those skilled in the art can design them according to actual needs, and this does not limit the present application.
[0192] Continue to refer Figure 2 and Figure 4 ,in, Figure 4 is Figure 2 A schematic cross-sectional structure diagram of a second support plate placed on the area 500a; the ion exchange particle regeneration device may include: a second support plate 500.
[0193] The second support plate 500 is used to support the second anion exchange particles 303, which are located above the first anion exchange particles 301, and is also used to isolate the first anion exchange particles 301 and the second anion exchange particles 303, so as to prevent the second anion particles from stacking on the first anion exchange particles 301, thereby reducing the probability of aggregation and / or accumulation of agglomerations between the first anion exchange particles 301, thereby improving the regeneration effect of the first anion exchange particles 301 and the second anion exchange particles 303.
[0194] The second support plate 500 is also used to isolate the second anion exchange particles 303 from the anion valve 308. When the anion valve 308 is opened, the second anion exchange particles 303 are prevented from moving between the third zone 302 and the anion valve 308, thereby reducing the probability of a decrease in the number of the second anion exchange particles 303 in the fourth zone 304, thereby improving the regeneration effect.
[0195] In this embodiment, the second support plate 500 is located in the fourth area 304 . In other embodiments, the second support plate 500 may be located in the second connection area 305 .
[0196] In order to make the drawings concise and clear, and to more clearly show the structure of the second support plate 500, the anion exchange chamber 300 and the second support plate 500 are drawn separately, corresponding to Figure 2 and Figure 4 ; The area 500a within the fourth zone 304 is used to place the second support plate 500.
[0197] The second support plate 500 includes a base plate 500b, which is used to provide a location space for setting the second support plate protrusions, and is also used to provide support for the second support plate protrusions and connections between the second support plate protrusions.
[0198] The second support plate has a plurality of second support plate protrusions, and the protrusions are oriented in a direction away from the anion valve, the side walls of the second support plate protrusions have a plurality of second support plate side wall protrusions, and a second interval is provided between adjacent second support plate side wall protrusions, and the second interval is also provided on the second support plate between adjacent second support plate protrusions.
[0199] In this embodiment, the second support plate protrusions are evenly distributed on the second support plate. In other embodiments, they may be unevenly distributed, but this does not limit the present application.
[0200] The plurality of second support plate protrusions have the following beneficial effects: providing a location space for setting the second interval, and reducing the flow resistance of the second anion regeneration liquid flowing through the fourth zone.
[0201] The plurality of protrusions on the side walls of the second support plates have the following beneficial effect: preventing the second anion regeneration particles from moving to the second interval, thereby reducing the probability of the second anion regeneration particles blocking the second interval.
[0202] The second interval has the following beneficial effect: it provides a flow channel for the second anion regeneration liquid to flow through the fourth zone 304.
[0203] In this embodiment, the second support plate 500 has two second support plate protrusions, namely a second support plate protrusion 501 and a second support plate protrusion 502. The second support plate protrusion 501 is oriented away from the anion valve 308, and the second support plate protrusion 502 is oriented away from the anion valve 308.
[0204] In this embodiment, the side wall of the second support plate protrusion 501 has four second support plate side wall protrusions, namely, the second support plate side wall protrusion 501a, the second support plate side wall protrusion 501b, the second support plate side wall protrusion 501c and the second support plate side wall protrusion 501d; the side wall of the second support plate protrusion 502 has four second support plate side wall protrusions, namely, the second support plate side wall protrusion 502a, the second support plate side wall protrusion 502b, the second support plate side wall protrusion 502c and the second support plate side wall protrusion 502d.
[0205] A second interval is provided between adjacent protrusions on the side walls of the second support plate, and the second interval is also provided on the second support plate 500 between adjacent protrusions on the second support plate. For the convenience of description, the second interval provided between adjacent protrusions on the side walls of the second support plate is a second interval 503a, and the second interval provided on the second support plate 500 between adjacent protrusions on the second support plate is a second interval 503b.
[0206] The shape of the second interval includes: one of a square, a triangle, a polygon, a circle, and an ellipse. In this embodiment, the shape of the second interval is a square.
[0207] In this embodiment, a second spacer 503a is provided between the second support plate side wall protrusion 501a and the second support plate side wall protrusion 501b, a second spacer 503a is provided between the second support plate side wall protrusion 501c and the second support plate side wall protrusion 501d, a second spacer 503a is provided between the second support plate side wall protrusion 502a and the second support plate side wall protrusion 502b, and a second spacer 503a is provided between the second support plate side wall protrusion 502c and the second support plate side wall protrusion 502d; the second spacer 503b is provided on the second support plate 500 between the adjacent second support plate protrusions 501 and the second support plate protrusions 502.
[0208] In this embodiment, the second support plate protrusion has a second support plate cavity 501e, and the second interval connects the fourth area 304 and the second connection area 305, that is, the fourth area 304 connects the second interval 503a, the second interval 503a connects the second support plate cavity 501e, the second support plate cavity 501e connects the second connection area 305, and the fourth area 304 connects the second interval 503b, and the second interval 503b connects the second connection area 305.
[0209] In this embodiment, the second support plate 500 and the anion exchange chamber 300 are detachably connected.
[0210] The shape of the protrusion of the second support plate includes: one or more of a cylinder, a square cylinder and a truncated cone; in this embodiment, the shape of the protrusion of the second support plate is a truncated cone, and the bottom of the truncated cone with a larger bottom surface area is connected to the second support plate 500, which has the following beneficial effects:
[0211] First, it is convenient to take out the second anion exchange particles 303 between the adjacent second support plate protrusions. In the direction away from the anion valve 308 toward the fourth area 304, the space between the adjacent second support plate protrusions increases.
[0212] Second, the truncated cone provides more space for the second intervals, so that more second intervals can be designed on the raised side wall of the second support plate.
[0213] For example, the base of the cylinder shares the base with the largest bottom area of the truncated cone, and the side area provided by the truncated cone is greater than the side area provided by the cylinder.
[0214] The shape of the protrusion on the side wall of the second support plate includes: an outwardly convex sphere, or a part of a sphere. In this embodiment, the shape of the protrusion on the side wall of the second support plate is a part of a sphere, that is, a convex curved surface.
[0215] In this embodiment, the shape of the protrusion of the second support plate is a truncated cone. The side wall expansion diagram of the truncated cone can refer to the description of the side wall expansion diagram of the protrusion of the first support plate being a truncated cone, which will not be repeated here.
[0216] In this embodiment, the base 500b, the second support plate protrusion, and the second support plate side wall protrusion are integrally formed.
[0217] It should be noted that, regarding the characteristic parameters such as the height, number, spacing of the protrusions on the second support plate, and the characteristic parameters such as the height, number, spacing of the protrusions on the side wall of the second support plate, those skilled in the art can design them according to actual needs, and this does not limit the present application.
[0218] Continue to refer Figure 2 and Figure 5 ,in, Figure 5 is Figure 2 A schematic cross-sectional structure diagram of a first partition placed on the area 600a; the ion exchange particle regeneration device may include: a first partition 600.
[0219] The first partition layer 600 is used to isolate the first cation exchange particles 201 and the second cation exchange particles 203, preventing the second cation exchange particles 203 from stacking on the first cation exchange particles 201, reducing the probability of aggregation and / or accumulation of agglomeration between the first cation exchange particles 201, thereby improving the regeneration effect of the first cation exchange particles 201 and the second cation exchange particles 203.
[0220] The first partition layer 600 is used to isolate the first cation exchange particles 201 from the cation valve 208. When the cation valve 208 is opened, the first cation exchange particles 201 are prevented from moving to the second area 204 through the first connecting area 205, thereby reducing the probability of a decrease in the number of the first cation exchange particles 201 in the first area 202, thereby improving the regeneration effect.
[0221] In this embodiment, the first spacer 600 is located in the first area 202 . In other embodiments, the first spacer 600 may be located in the first connection area 205 .
[0222] In order to make the drawings concise and clear, and to more clearly show the structure of the first barrier layer 600, the cation exchange chamber 200 and the first barrier layer 600 are drawn separately, corresponding to Figure 2 and Figure 5 ; The area 600a within the first zone 202 is used to place the first partition layer 600.
[0223] The first partition layer 600 includes a base plate 600b, which is used to provide a location space for setting the first partition layer protrusions, and is also used to provide support for the first partition layer protrusions and connections between the first partition layer protrusions.
[0224] The first partition layer has a plurality of first partition layer protrusions, and the protrusions are oriented in a direction away from the cationic valve. The sidewall of the first partition layer protrusion has a plurality of first partition layer sidewall protrusions. A third spacer is provided between adjacent first partition layer sidewall protrusions, and the third spacer is also provided on the first partition layer between adjacent first partition layer protrusions.
[0225] In this embodiment, the first spacer protrusions are evenly distributed on the first spacer. In other embodiments, they may be unevenly distributed, but this does not limit the present application.
[0226] The multiple first spacer protrusions have the following beneficial effects: providing space for setting the third spacer and reducing the flow resistance of the first cation regeneration liquid flowing through the first zone.
[0227] The plurality of first spacer sidewall protrusions have the following beneficial effects: preventing the first cationic regeneration particles from moving to the third space, thereby reducing the probability of the first cationic regeneration particles blocking the third space.
[0228] The third partition has the following beneficial effect: providing a flow channel for the first cation regeneration liquid to flow through the first zone.
[0229] In this embodiment, the first partition layer 600 has two first partition layer protrusions, namely a first partition layer protrusion 601 and a first partition layer protrusion 602. The first partition layer protrusion 601 is oriented away from the cationic valve 208, and the first partition layer protrusion 602 is oriented away from the cationic valve 208.
[0230] In this embodiment, the side wall of the first partition protrusion 601 has four first partition side wall protrusions, namely, the first partition side wall protrusion 601a, the first partition side wall protrusion 601b, the first partition side wall protrusion 601c and the first partition side wall protrusion 601d; the side wall of the first partition protrusion 602 has four first partition side wall protrusions, namely, the first partition side wall protrusion 602a, the first partition side wall protrusion 602b, the first partition side wall protrusion 602c and the first partition side wall protrusion 602d.
[0231] A third spacer is provided between adjacent protrusions on the side walls of the first spacer layer, and the third spacer is also provided on the first spacer layer between adjacent protrusions on the first spacer layer. For the convenience of description, the third spacer provided between adjacent protrusions on the side walls of the first spacer layer is a third spacer 603a, and the third spacer provided on the first spacer layer 600 between adjacent protrusions on the first spacer layer is a third spacer 603b.
[0232] The shape of the third interval includes: one of a square, a triangle, a polygon, a circle, and an ellipse. In this embodiment, the shape of the third interval is a square.
[0233] In this embodiment, a third spacer 603a is provided between the first spacer side wall protrusion 601a and the first spacer side wall protrusion 601b, a third spacer 603a is provided between the first spacer side wall protrusion 601c and the first spacer side wall protrusion 601d, a third spacer 603a is provided between the first spacer side wall protrusion 602a and the first spacer side wall protrusion 602b, and a third spacer 603a is provided between the first spacer side wall protrusion 602c and the first spacer side wall protrusion 602d; the third spacer 603b is provided on the first spacer 600 between the adjacent first spacer protrusion 601 and first spacer protrusion 602.
[0234] In this embodiment, the first partition protrusion has a first partition cavity 601e, and the third interval connects the first area 202 and the first connecting area 205, that is, the first area 202 is connected to the third interval 603a, the third interval 603a is connected to the first partition cavity 601e, the first partition cavity 601e is connected to the first connecting area 205, and the first area 202 is connected to the third interval 603b, and the third interval 603b is connected to the first connecting area 205.
[0235] In this embodiment, the first partition 600 and the cation exchange chamber 200 are detachably connected.
[0236] The shape of the protrusion of the first interlayer includes: one or more of a cylinder, a square cylinder and a truncated cone; in this embodiment, the shape of the protrusion of the first interlayer is a truncated cone, and the bottom of the truncated cone with a larger bottom area is connected to the first interlayer 600, which has the following beneficial effects:
[0237] First, it is convenient to take out the first cation exchange particles 201 between adjacent protrusions of the first barrier layer. In the direction away from the cation valve 208 toward the first area 202, the space between adjacent protrusions of the first barrier layer increases.
[0238] Second, the truncated cone provides more space for the third spacers, so that more third spacers can be designed on the raised side wall of the first spacer layer.
[0239] For example, the base of the cylinder shares the base with the largest bottom area of the truncated cone, and the side area provided by the truncated cone is greater than the side area provided by the cylinder.
[0240] The shape of the protrusion on the side wall of the first spacer layer includes: an outwardly convex sphere, or a part of a sphere. In this embodiment, the shape of the protrusion on the side wall of the first spacer layer is a part of a sphere, that is, a convex curved surface.
[0241] In the present embodiment, the shape of the protrusion of the first partition layer is an inverted cone (the large bottom of the cone is on top, and the small bottom is on the bottom). The side wall expansion diagram of the cone can refer to the description of the side wall expansion diagram of the protrusion of the first support plate as a cone, which will not be repeated here.
[0242] In this embodiment, the base 600b, the first barrier layer protrusion, and the first barrier layer side wall protrusion are integrally formed.
[0243] It should be noted that, regarding the characteristic parameters such as the height, number, spacing of the first spacer protrusions, and the characteristic parameters such as the height, number, spacing of the first spacer sidewall protrusions, those skilled in the art can design them according to actual needs, and this does not limit the present application.
[0244] Continue to refer Figure 2 and Figure 6 ,in, Figure 6 is Figure 2 A schematic cross-sectional structure diagram of a second partition placed on the area 700a; the ion exchange particle regeneration device may include: a second partition 700.
[0245] The second partition layer 700 is used to isolate the first anion exchange particles 301 and the second anion exchange particles 303, prevent the second anion exchange particles 303 from stacking on the first anion exchange particles 301, reduce the probability of aggregation and / or accumulation of the first anion exchange particles 301, and thus improve the regeneration effect of the first anion exchange particles 301 and the first anion exchange particles 301.
[0246] The second partition layer 700 is used to isolate the first anion exchange particles 301 from the anion valve 308. When the anion valve 308 is opened, the first anion exchange particles 301 are prevented from moving to the fourth area 304 through the second connecting area 305, thereby reducing the probability of a decrease in the number of the first anion exchange particles 301 in the third area 302, thereby improving the regeneration effect.
[0247] In this embodiment, the second spacer 700 is located in the third area 302 . In other embodiments, the second spacer 700 may be located in the second connection area 305 .
[0248] In order to make the drawings concise and clear, and to more clearly show the structure of the second partition 700, the cation exchange chamber 200 and the second partition 700 are drawn separately, corresponding to Figure 2 and Figure 6 The area 700a within the third zone 302 is used to place the second partition layer 700.
[0249] The second partition layer 700 includes a base plate 700b, which is used to provide a location space for setting the second partition layer protrusions, and is also used to provide support for the second partition layer protrusions and connection between the second partition layer protrusions.
[0250] The second partition layer has a plurality of second partition layer protrusions, and the protrusions are oriented in a direction away from the anion valve. The sidewalls of the second partition layer protrusions have a plurality of second partition layer sidewall protrusions. A fourth spacer is provided between adjacent second partition layer sidewall protrusions, and the fourth spacer is also provided on the second partition layer between adjacent second partition layer protrusions.
[0251] In this embodiment, the second spacer protrusions are evenly distributed on the second spacer. In other embodiments, they may be unevenly distributed, but this is not intended to limit the present application.
[0252] The plurality of second spacer protrusions have the following beneficial effects: providing space for setting the fourth spacer and reducing the flow resistance of the first anion regeneration liquid flowing through the third zone.
[0253] The plurality of second spacer sidewall protrusions have the following beneficial effects: preventing the first anion regeneration particles from moving to the fourth space, thereby reducing the probability of the first anion regeneration particles blocking the fourth space.
[0254] The fourth interval has the following beneficial effect: providing a flow channel for the first anion regeneration liquid to flow through the third zone.
[0255] In this embodiment, the second partition layer 700 has two second partition layer protrusions, namely a second partition layer protrusion 701 and a second partition layer protrusion 702. The second partition layer protrusion 701 is oriented away from the anion valve 308, and the second partition layer protrusion 702 is oriented away from the anion valve 308.
[0256] In this embodiment, the side wall of the second partition layer protrusion 701 has four second partition layer side wall protrusions, namely, the second partition layer side wall protrusion 701a, the second partition layer side wall protrusion 701b, the second partition layer side wall protrusion 701c and the second partition layer side wall protrusion 701d; the side wall of the second partition layer protrusion 702 has four second partition layer side wall protrusions, namely, the second partition layer side wall protrusion 702a, the second partition layer side wall protrusion 702b, the second partition layer side wall protrusion 702c and the second partition layer side wall protrusion 702d.
[0257] A fourth spacer is provided between adjacent protrusions on the side walls of the second spacer layer, and the fourth spacer is also provided on the second spacer layer between adjacent protrusions on the second spacer layer. For the convenience of description, the fourth spacer provided between adjacent protrusions on the side walls of the second spacer layer is a fourth spacer 703a, and the fourth spacer provided on the second spacer layer 700 between adjacent protrusions on the second spacer layer is a fourth spacer 703b.
[0258] The shape of the fourth interval includes: one of a square, a triangle, a polygon, a circle, and an ellipse. In this embodiment, the shape of the fourth interval is a square.
[0259] In this embodiment, a fourth spacer 703a is provided between the second spacer side wall protrusion 701a and the second spacer side wall protrusion 701b, a fourth spacer 703a is provided between the second spacer side wall protrusion 701c and the second spacer side wall protrusion 701d, a fourth spacer 703a is provided between the second spacer side wall protrusion 702a and the second spacer side wall protrusion 702b, and a fourth spacer 703a is provided between the second spacer side wall protrusion 702c and the second spacer side wall protrusion 702d; the fourth spacer 703b is provided on the second spacer 700 between the adjacent second spacer protrusions 701 and second spacer protrusions 702.
[0260] In this embodiment, the second spacer protrusion has a second spacer cavity 701e, and the fourth spacer connects the third area 302 and the second connection area 305, that is, the third area 302 is connected to the fourth spacer 703a, the fourth spacer 703a is connected to the second spacer cavity 701e, the second spacer cavity 701e is connected to the second connection area 305, and the third area 302 is connected to the fourth spacer 703b, and the fourth spacer 703b is connected to the second connection area 305.
[0261] In this embodiment, the second partition layer 700 and the anion exchange chamber 300 are detachably connected.
[0262] The shape of the second interlayer protrusion includes: one or more of a cylinder, a square cylinder and a truncated cone; in this embodiment, the shape of the second interlayer protrusion is a truncated cone, and the bottom of the truncated cone with a larger bottom area is connected to the second interlayer 700, which has the following beneficial effects:
[0263] First, it is convenient to take out the first anion exchange particles 301 between adjacent protrusions of the second barrier layer. In the direction away from the anion valve 308 toward the third area 302, the space between adjacent protrusions of the second barrier layer increases.
[0264] Second, the truncated cone provides more space for the fourth spacers, so that more fourth spacers can be designed on the raised side wall of the second spacer layer.
[0265] For example, the base of the cylinder shares the base with the largest bottom area of the truncated cone, and the side area provided by the truncated cone is greater than the side area provided by the cylinder.
[0266] The shape of the protrusion on the side wall of the second spacer layer includes: an outwardly convex sphere, or a part of a sphere. In this embodiment, the shape of the protrusion on the side wall of the second spacer layer is a part of a sphere, that is, an outwardly convex curved surface.
[0267] In the present embodiment, the shape of the protrusion of the second partition layer is an inverted cone (the large bottom of the cone is on top, and the small bottom is on the bottom). The side wall expansion diagram of the cone can refer to the description of the side wall expansion diagram of the protrusion of the first support plate as a cone, which will not be repeated here.
[0268] In this embodiment, the base 700b, the second spacer protrusion, and the second spacer sidewall protrusion are integrally formed.
[0269] It should be noted that, regarding the characteristic parameters such as the height, number, spacing of the second spacer protrusions, and the characteristic parameters such as the height, number, spacing of the second spacer sidewall protrusions, those skilled in the art can design them according to actual needs, and this does not limit the present application.
[0270] Although the present invention has been disclosed as above in the form of a preferred embodiment, it is not intended to limit the present invention. Any person skilled in the art may make possible changes and modifications to the technical solution of the present invention by using the methods and technical contents disclosed above without departing from the spirit and scope of the present invention. Therefore, any simple modifications, equivalent changes and modifications made to the above embodiments based on the technical essence of the present invention without departing from the content of the technical solution of the present invention shall fall within the protection scope of the technical solution of the present invention.
Claims
1. An ion exchange particle regeneration device, characterized in that: include: a cation exchange chamber comprising a first region for accommodating first cation exchange particles, and a second region for accommodating second cation exchange particles; A first support plate, located in the second area, for supporting the second cation exchange particles, wherein the second cation exchange particles are located above the first cation exchange particles; The vibration component is coupled to the cation exchange chamber and is used to drive the first cation exchange particles and the second cation exchange particles to vibrate when the ion exchange particles are regenerated.
2. The ion exchange particle regeneration device according to claim 1, characterized in that: Also includes: an anion exchange chamber comprising a third region for accommodating first anion exchange particles and a fourth region for accommodating second anion exchange particles; a second support plate, located in the fourth area, and used to support the second anion exchange particles, wherein the second anion exchange particles are located above the first anion exchange particles; The vibration component is also coupled to the anion exchange chamber, and is used to drive the first anion exchange particles and the second anion exchange particles to vibrate when the ion exchange particles are regenerated.
3. The ion exchange particle regeneration device according to claim 2, characterized in that: The vibration component comprises: A connecting rod coupled to the cation exchange chamber and the anion exchange chamber; A vibration motor is coupled to the connecting rod.
4. The ion exchange particle regeneration device according to claim 2, characterized in that: The first cation exchange particles contained in the first zone adsorb first impurity cations of the liquid to be purified; The second cation exchange particles contained in the second zone adsorb second impurity cations of the liquid to be purified; The first anion exchange particles contained in the third zone adsorb first impurity anions of the liquid to be purified; The second anion exchange particles contained in the fourth region adsorb second impurity anions of the liquid to be purified.
5. The ion exchange particle regeneration device according to claim 2, characterized in that: Also included: a first connecting region located between the first region and the second region, and a second connecting region located between the third region and the fourth region; a cation valve, located in the first connecting area, for isolating the mutual flow between the first cation regeneration liquid flowing through the first area and the second cation regeneration liquid flowing through the second area, wherein the first cation regeneration liquid is used for regeneration of the first cation exchange particles, and the second cation regeneration liquid is used for regeneration of the second cation exchange particles; The anion valve is located in the second connecting area and is used to isolate the mutual flow between the first anion regeneration liquid flowing through the third area and the second anion regeneration liquid flowing through the fourth area. The first anion regeneration liquid is used for regenerating the first anion exchange particles, and the second anion regeneration liquid is used for regenerating the second anion exchange particles.
6. The ion exchange particle regeneration device according to claim 5, characterized in that: The second area is located above the first area, the fourth area is located above the third area, and further includes: The first support plate has a plurality of first support plate protrusions, and the protrusions are oriented in a direction away from the cationic valve, the sidewalls of the first support plate protrusions have a plurality of first support plate sidewall protrusions, and a first interval is provided between adjacent first support plate sidewall protrusions, the first interval is also provided on the first support plate between adjacent first support plate protrusions, and the first interval communicates the second area and the first connection area; The second support plate has a plurality of second support plate protrusions, and the protrusions are oriented in a direction away from the anion valve, the sidewalls of the second support plate protrusions have a plurality of second support plate sidewall protrusions, and a second interval is provided between adjacent second support plate sidewall protrusions, the second interval is also provided on the second support plate between adjacent second support plate protrusions, and the second interval communicates with the fourth area and the second connection area; A first partition layer, located in the first area, for isolating the first cation exchange particles from the cation valve, the first partition layer having a plurality of first partition layer protrusions, and the protrusions are oriented in a direction away from the cation valve, the sidewall of the first partition layer protrusions having a plurality of first partition layer sidewall protrusions, a third partition is provided between adjacent first partition layer sidewall protrusions, the third partition is also provided on the first partition layer between adjacent first partition layer protrusions, and the third partition connects the first area and the first connecting area; A second partition layer is located in the third area and is used to isolate the first anion exchange particles from the anion valve. The second partition layer has a plurality of second partition layer protrusions, and the protrusions are oriented in a direction away from the anion valve. The sidewalls of the second partition layer protrusions have a plurality of second partition layer sidewall protrusions. A fourth partition is provided between adjacent second partition layer sidewall protrusions. The fourth partition is also provided on the second partition layer between adjacent second partition layer protrusions. The fourth partition connects the third area and the second connection area. The ion exchange particle regeneration device also includes: Filter unit, comprising: A filter tank for holding the liquid to be purified; The filter screen is used to filter the liquid to be purified in the filter pool.
7. The ion exchange particle regeneration device according to claim 6, characterized in that: Also includes: A detection unit, used for detecting the ion concentration and / or organic matter concentration in the liquid to be purified after being purified by the cation exchange chamber and the anion exchange chamber; The detection unit comprises: An ion concentration detector, used to detect the ion concentration in the liquid to be purified after being purified by the cation exchange chamber and the anion exchange chamber; An organic matter concentration detector, used for detecting the organic matter concentration in the liquid to be purified after being purified by the cation exchange chamber and the anion exchange chamber; The detection unit is selected from the following: The filtration unit is connected to the input end of the cation exchange chamber, the output end of the cation exchange chamber is connected to the input end of the anion exchange chamber, and the output end of the anion exchange chamber is connected to the input end of the detection unit; The filtration unit is connected to the input end of the anion exchange chamber, the output end of the anion exchange chamber is connected to the input end of the cation exchange chamber, and the output end of the cation exchange chamber is connected to the input end of the detection unit.
8. The ion exchange particle regeneration device according to claim 7, characterized in that: include: The reverse osmosis water tank is coupled to the output end of the detection unit and is used to contain purified liquid whose ion concentration and / or organic matter concentration exceeds a preset range.
9. The ion exchange particle regeneration device according to claim 8, characterized in that: The cation exchange chamber further comprises: a first cation regeneration liquid input port located in the first connection zone, and a second cation regeneration liquid input port located in the second zone; The anion exchange chamber further comprises: a first anion regeneration liquid input port located in the second connection zone, and a second anion regeneration liquid input port located in the fourth zone; The ion exchange particle regeneration device further comprises: a first cation regeneration liquid tank, coupled to the first cation regeneration liquid input port, for containing a first cation regeneration liquid; a second cationic regeneration liquid tank, coupled to the second cationic regeneration liquid input port, for containing a second cationic regeneration liquid; a first anion regeneration liquid tank, coupled to the first anion regeneration liquid input port, for containing the first anion regeneration liquid; a second anion regeneration liquid tank, coupled to the second anion regeneration liquid input port, for containing the second anion regeneration liquid; The reverse osmosis water pool also includes at least one of the following: The reverse osmosis water tank is coupled to the first cationic regeneration liquid input port; The reverse osmosis water tank is coupled to the second cationic regeneration liquid input port; The reverse osmosis water tank is coupled to the first anion regeneration liquid input port; The reverse osmosis water tank is coupled to the second anion regeneration liquid input port.
10. The ion exchange particle regeneration device according to claim 7, characterized in that: Also includes: The deionized water tank is coupled to the output end of the detection unit and is used to contain purified liquid whose ion concentration and / or organic matter concentration meets a preset range.