Plasma gas-liquid discharge device and device control method
By designing a plasma gas-liquid discharge device with a micron-level trough channel, the problem of plasma interaction area being concentrated on the surface layer in liquid dielectric discharge was solved, and effective treatment of the liquid interior was achieved.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2023-10-20
- Publication Date
- 2026-03-24
AI Technical Summary
In existing technologies, the discharge process in liquid media is mainly concentrated on the surface of the liquid and cannot effectively cover the interior of the liquid, resulting in poor treatment performance.
Design a plasma gas-liquid discharge device, including a high-voltage electrode, a low-voltage electrode, an insulating substrate, and multiple slotted channels. The depth of the slotted channels is on the micrometer level, and a plasma interaction region is formed by an electric field to cover the interior of the liquid.
Through a grooved channel with a depth of micrometers, the plasma interaction area can cover the interior of the liquid, improving the liquid treatment effect, especially the removal efficiency of contaminants inside the liquid.
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Figure CN119865958B_ABST
Abstract
Description
Technical Field
[0001] This invention relates to the field of plasma technology, and more specifically to a plasma gas-liquid discharge device and a device control method. Background Technology
[0002] Low-temperature plasma technology has been widely studied in areas such as material modification, pollution control, and medical disinfection due to its advantages of high reaction rate, high reactivity, and convenient control.
[0003] In a gaseous dielectric discharge environment with good insulation properties, when the external driving energy reaches the energy threshold for the excitation ionization of gas molecules, a series of excitation ionization processes can be induced to generate plasma. However, in a liquid dielectric discharge environment, since the liquid medium is usually non-insulating, under the influence of an applied electric field, ions inside the liquid often undergo charge rearrangement rather than plasma generation. Therefore, the gas-liquid discharge process usually occurs in the gas phase and the gas-liquid interface, causing the plasma's effective area to be mainly concentrated on the liquid surface and not effectively covering the interior of the liquid, resulting in poor liquid treatment performance. Currently, the main method to increase the plasma's effective area inside the liquid is to increase the gas-liquid two-phase area by bubbling into the liquid, thereby establishing a plasma reaction zone within the liquid. However, the random distribution and large degree of freedom of movement of bubbles inside the liquid make controlling the plasma reaction zone inside the liquid still a challenge. Summary of the Invention
[0004] The purpose of this invention is to overcome the problem that the effective area of plasma in the prior art is mainly concentrated on the surface of the liquid and cannot effectively cover the interior of the liquid, resulting in poor liquid treatment effect, and to provide a plasma gas-liquid discharge device and device control method.
[0005] To achieve the above objectives, the first aspect of the present invention provides a plasma gas-liquid discharge device, the discharge device comprising a high-voltage electrode, a low-voltage electrode, an insulating substrate, and a plurality of liquid supply pipes;
[0006] The first surface of the insulating substrate is provided with a plurality of groove channels, and the depth of each groove channel is on the micrometer level.
[0007] The high-voltage electrode and the low-voltage electrode are used to form an electric field, and each of the slotted channels is located in the electric field;
[0008] The outlet of each of the liquid addition pipes is connected to each of the trough-type channels.
[0009] In this embodiment, the high-voltage electrode is a linear high-voltage electrode, the low-voltage electrode is a linear low-voltage electrode, and the linear high-voltage electrode and the linear low-voltage electrode are located on the same target plane; the target plane is parallel to the first surface.
[0010] In this embodiment, the high-voltage electrode is a linear high-voltage electrode, and the low-voltage electrode is a plate-shaped low-voltage electrode. The linear high-voltage electrode is located on one side of the first surface, and the plate-shaped low-voltage electrode is located on one side of the second surface of the insulating substrate; the second surface is opposite to the first surface.
[0011] In this embodiment, the high-voltage electrode is a plate-shaped high-voltage electrode, and the low-voltage electrode is a plate-shaped low-voltage electrode. The plate-shaped high-voltage electrode is located on one side of the first surface, and the plate-shaped low-voltage electrode is located on one side of the second surface of the insulating substrate; the second surface is opposite to the first surface.
[0012] In this embodiment of the application, the slotted channels are parallel to each other, and the direction of the electric field is perpendicular to the extension direction of each slotted channel.
[0013] In this embodiment of the application, the discharge device further includes a hydrophobic and breathable membrane, which is attached to the first surface to cover each of the grooved channels; the surface of the hydrophobic and breathable membrane facing the grooved channels is hydrophobic, and the hydrophobic and breathable membrane as a whole is breathable.
[0014] In this embodiment, the surface of the hydrophobic and breathable membrane facing away from the grooved channel is hydrophilic.
[0015] In this embodiment of the application, the discharge device further includes a plurality of first valves, each of which is respectively disposed on each of the groove-shaped channels.
[0016] In this embodiment of the application, the discharge device further includes a plurality of second valves, each of which is respectively disposed on each of the liquid addition pipes.
[0017] In this embodiment, the spacing between any two adjacent slot channels is on the order of micrometers.
[0018] In this embodiment of the application, the discharge device further includes an airflow control device located on one side of the first surface. The airflow control device is used to control the airflow direction in the gas phase discharge space, which is parallel to the extension direction of the slotted channel.
[0019] A second aspect of the present invention provides a device control method for controlling a plasma gas-liquid discharge device provided in the first aspect of the present invention, the control method comprising:
[0020] Determine the plasma distribution in each of the aforementioned slot channels;
[0021] Based on the distribution, determine the target flow rate corresponding to each of the trough channels;
[0022] Based on the target flow rate, the liquid flow rate in each of the trough channels is controlled.
[0023] In this embodiment of the application, the plasma distribution in each of the slot channels includes the plasma reaction energy ratio between each of the slot channels; determining the plasma distribution in each of the slot channels includes:
[0024] Color-developing liquid is introduced into each of the aforementioned tank channels, and color-developing liquid is taken at the outlet of each of the aforementioned tank channels. Color development and reduction calibration is performed using a calibration solution.
[0025] The plasma reaction energy ratio between each of the aforementioned tank channels is determined based on the amount of calibration liquid consumed.
[0026] In this embodiment of the application, determining the target flow rate corresponding to each of the slotted channels based on the distribution includes:
[0027] A target trough channel is determined from all the trough channels, wherein the target trough channel is the trough channel with the highest plasma reaction energy among all the trough channels;
[0028] When the target solution is introduced into the target tank channel, and the treatment effect of the target solution reaches a preset index, the first flow rate corresponding to the target tank channel is determined.
[0029] The target flow rate corresponding to each of the trough channels is determined based on the first flow rate and the plasma reaction energy ratio between each of the trough channels.
[0030] In this embodiment of the application, each of the grooved channels includes a first grooved channel, and the first grooved channel is any one of the grooved channels;
[0031] When the target flow rate corresponding to the first trough channel is less than the target flow rate corresponding to the target trough channel, controlling the liquid flow rate in each of the trough channels based on the target flow rate includes:
[0032] A first liquid is introduced into the first trough channel so that the flow rate in the first trough channel is equal to the target flow rate corresponding to the target trough channel.
[0033] The aforementioned plasma-liquid discharge device includes a high-voltage electrode, a low-voltage electrode, an insulating substrate, and multiple liquid supply pipes. The first surface of the insulating substrate has multiple grooved channels, each with a depth on the micrometer scale. The high-voltage electrode and the low-voltage electrode form an electric field, and each grooved channel is located within this electric field. The outlet of each liquid supply pipe is connected to each grooved channel. Therefore, the micrometer-deep grooved channels can provide liquid of a depth on the micrometer scale, corresponding to the depth of the liquid surface layer that the plasma's action area can cover. This allows the plasma's action area to encompass the liquid within the grooved channels, resulting in better treatment of the liquid flowing within the channels and thus comprehensively improving the plasma's treatment effect on gas-liquid two-phase media.
[0034] Other features and advantages of the embodiments of this application will be described in detail in the following detailed description section. Attached Figure Description
[0035] The accompanying drawings are provided to further illustrate the embodiments of this application and form part of the specification. They are used together with the following detailed description to explain the embodiments of this application, but do not constitute a limitation on the embodiments of this application. In the drawings:
[0036] Figure 1 and Figure 2 The schematic diagram illustrates a structural schematic of a plasma gas-liquid discharge device according to an embodiment of this application;
[0037] Figure 3 This schematic diagram illustrates the structure of another plasma gas-liquid discharge device according to an embodiment of this application;
[0038] Figure 4 A schematic diagram of the structure of another plasma gas-liquid discharge device according to an embodiment of this application is shown.
[0039] Figure 5 A schematic diagram of the structure of another plasma gas-liquid discharge device according to an embodiment of this application is shown.
[0040] Figure 6 A schematic diagram of the structure of another plasma gas-liquid discharge device according to an embodiment of this application is shown.
[0041] Figure 7 The illustration shows a schematic flowchart of a device control method according to an embodiment of this application.
[0042] Explanation of reference numerals in the attached figures
[0043] 100—Plasma gas-liquid discharge device; 101—High-voltage electrode; 102—Low-voltage electrode; 103—Insulating substrate; 1031—Trench-type channel; 104—Liquid addition pipe; 105—Hydrophobic and breathable membrane; 106—First valve; 107—Second valve. Detailed Implementation
[0044] To make the objectives, technical solutions, and advantages of the embodiments of this application clearer, the technical solutions of the embodiments of this application will be clearly and completely described below with reference to the accompanying drawings. It should be understood that the specific embodiments described herein are only for illustration and explanation of the embodiments of this application and are not intended to limit the embodiments of this application. All other embodiments obtained by those skilled in the art based on the embodiments of this application without creative effort are within the scope of protection of this application.
[0045] It should be noted that if the embodiments of this application involve directional indicators (such as up, down, left, right, front, back, etc.), the directional indicators are only used to explain the relative positional relationship and movement of the components in a certain specific posture (as shown in the figure). If the specific posture changes, the directional indicators will also change accordingly.
[0046] Furthermore, if the embodiments of this application involve descriptions such as "first" or "second," these descriptions are for descriptive purposes only and should not be construed as indicating or implying their relative importance or implicitly specifying the number of technical features indicated. Therefore, features defined with "first" or "second" may explicitly or implicitly include at least one of those features. Additionally, the technical solutions of various embodiments can be combined with each other, but this must be based on the ability of those skilled in the art to implement them. If the combination of technical solutions is contradictory or impossible to implement, it should be considered that such a combination of technical solutions does not exist and is not within the scope of protection claimed in this application.
[0047] As described in the background art, for liquid media in gas-liquid two-phase discharge, the discharge process usually occurs at the gas-liquid interface, i.e., the liquid surface. The non-insulating nature of liquids means that ion charge rearrangement often occurs inside the liquid rather than the generation of plasma. Therefore, for liquid media, the effective area of plasma is mainly concentrated on the liquid surface and cannot effectively cover the interior of the liquid, resulting in poor treatment effect on liquids (such as contaminants in the liquid).
[0048] To address this, one embodiment of this application provides a plasma gas-liquid discharge device 100, which may include a high-voltage electrode 101, a low-voltage electrode 102, an insulating substrate 103, and a plurality of liquid supply channels 104; the first surface of the insulating substrate 103 is provided with a plurality of grooved channels 1031, each grooved channel 1031 having a depth of micrometers; the high-voltage electrode 101 and the low-voltage electrode 102 are used to form an electric field, and each grooved channel 1031 is located in the electric field; the outlet of each liquid supply channel 104 is respectively connected to each grooved channel 1031.
[0049] The high-voltage electrode 101 and the low-voltage electrode 102 can form a discharge space to generate an electric field under the drive of an external power source. Specifically, the high-voltage electrode 101 can be connected to a high-voltage terminal A, and the low-voltage electrode 102 can be connected to a ground terminal B, thereby forming a discharge circuit for discharge. The high-voltage electrode 101 and the low-voltage electrode 102 can be made of metal, such as copper or stainless steel.
[0050] In practical applications, in order to improve the treatment effect of the liquid in the trough channel 1031 by the subsequent plasma gas-liquid discharge device 100, the trough channels 1031 can be parallel to each other, and the electric field direction is perpendicular to the extension direction of each trough channel 1031.
[0051] In this embodiment, to improve the discharge effect of the gas-liquid two-phase system, the high-voltage electrode 101 can be disposed on one side of the first surface of the insulating substrate 103, thereby getting closer to the liquid in the channel 103. The low-voltage electrode 102 can be disposed on one side of the first surface of the insulating substrate 103 or on one side of the second surface of the insulating substrate 103, depending on the electrode configuration, with the second surface opposite to the first surface.
[0052] For example, in one implementation, such as Figure 1 and Figure 2 As shown ( Figure 2 for Figure 1 (Right view), the high-voltage electrode 101 is a linear high-voltage electrode, and the low-voltage electrode 102 is a linear low-voltage electrode. The linear high-voltage electrode and the linear low-voltage electrode are located on the same target plane; the target plane is parallel to the first surface. More specifically, the extension direction of the linear high-voltage electrode is the same as the extension direction of the slotted channel 1031, and the extension direction of the linear low-voltage electrode is the same as the extension direction of the slotted channel 1031.
[0053] In practice, the linear high-voltage electrode and the linear low-voltage electrode are spaced apart by a first preset distance to form a discharge space. The first preset distance can be set according to actual needs, for example, it can be 10mm, 20mm, 30mm, etc.
[0054] In the above embodiments, a linear high-voltage electrode and a linear low-voltage electrode can constitute a set of electrodes. In practical applications, the plasma gas-liquid discharge device 100 may be provided with only one set of electrodes or multiple sets of electrodes, so that when there are a large number of slot channels 1031, each slot channel 1031 can be covered by the electric field.
[0055] In the case where multiple sets of electrodes are provided in the plasma gas-liquid discharge device 100, the order of the electrodes is as follows: high-voltage electrode 101, low-voltage electrode 102, high-voltage electrode 101, low-voltage electrode 102... Not only can an electric field be formed between the high-voltage electrode 101 and the low-voltage electrode 102 in the same set of electrodes, but an electric field can also be formed between the low-voltage electrode 102 in the previous set of electrodes and the high-voltage electrode 101 in the next set of electrodes. Therefore, each slotted channel 1031 can be covered by an electric field.
[0056] Or, for example, in another implementation, such as Figure 3 As shown, the high-voltage electrode 101 is a linear high-voltage electrode, and the low-voltage electrode 102 is a plate-shaped low-voltage electrode. The linear high-voltage electrode is located on one side of the first surface, and the plate-shaped low-voltage electrode is located on one side of the second surface of the insulating substrate 103.
[0057] In practice, the linear high-voltage electrode and the plate-shaped low-voltage electrode are spaced apart by a second preset distance to form a discharge space. The second preset distance can be set according to actual needs, for example, it can be 5mm, 10mm, etc.
[0058] Or, for example, in yet another implementation, such as Figure 4 As shown, the high-voltage electrode 101 is a plate-shaped high-voltage electrode, and the low-voltage electrode 102 is a plate-shaped low-voltage electrode. The plate-shaped high-voltage electrode is located on one side of the first surface, and the plate-shaped low-voltage electrode is located on one side of the second surface of the insulating substrate 103.
[0059] In practical implementation, a third preset distance is spaced between the plate-shaped high-voltage electrode and the plate-shaped low-voltage electrode to form a discharge space. The third preset distance can be set according to actual needs, for example, it can be 5mm, 10mm, etc.
[0060] The insulating substrate 103 can be used to form various slotted channels 1031. The cross-section of the slotted channel 1031 can be, but is not limited to, square, circular, etc. For example, the cross-section of the slotted channel 1031 can be a square of 100μm × 100μm. The insulating substrate 103 can be made of a material with good insulating properties, such as quartz, ceramic, polydimethylsiloxane, etc.
[0061] The grooved channels 1031 formed on the insulating substrate 103 can be used to carry and circulate liquid. Each grooved channel 1031 has an upward-facing opening, so that the liquid flowing through it can be exposed to the gas phase, thereby forming a gas-liquid two-phase discharge environment.
[0062] In this embodiment, by setting the depth of each channel 1031 to the micrometer level, the depth of the liquid flowing within the channel 1031 is also at the micrometer level; that is, the depth of the liquid to be processed is at the micrometer level. In other words, the channel 1031 with a depth at the micrometer level can be used to provide liquid to be processed with a depth at the micrometer level. The depth of the channel 1031 can, for example, be 10 μm to 500 μm.
[0063] As described in the background section of this application, for liquid media in gas-liquid two-phase discharge, the discharge process typically occurs at the liquid surface, and the plasma interaction region can only cover the liquid surface layer. However, this embodiment of the application, by setting a grooved channel 1031 with a depth on the micrometer scale, makes the depth of the liquid to be processed also on the micrometer scale, which is close to the aforementioned liquid surface depth. Therefore, the plasma interaction region can cover the liquid within the grooved channel 1031.
[0064] In other words, in existing technologies, the interior of a liquid (or the deeper layers of water) is too far from the liquid surface, preventing the plasma's effective area from covering the interior and resulting in poor treatment of the liquid's interior. For example, if the object to be treated is wastewater, only surface pollutants can be effectively treated, not those inside the water, leading to poor treatment results. However, in the trough channel 1031 of this embodiment, the liquid is only at a depth of micrometers, ensuring that the liquid within the channel is close to or within the surface layer, with no liquid too far from the surface. Therefore, the plasma's effective area can cover the liquid within the trough channel 1031, resulting in better treatment of the liquid flowing within it.
[0065] In practical implementation, liquid can be introduced into each trough channel 1031 through the first main pipeline C, and the liquid flowing out of each trough channel 1031 converges into the second main pipeline D. Each trough channel 1031, the first main pipeline C, the second main pipeline D, and other pipelines E used for distributing liquid to each trough channel 1031 can be configured as follows: Figure 5 As shown (top view).
[0066] In each of the trough channels 1031, the spacing between any two adjacent trough channels 1031 can also be on the micrometer scale, for example, the spacing is 0μm to 30μm. This can increase the density of the trough channels 1031, improve the utilization rate of plasma, and thus improve the liquid processing efficiency.
[0067] In practical application of the plasma gas-liquid discharge device 100, each tank-type channel 1031 can be used to circulate the liquid to be treated, such as sewage. The liquid to be treated contains substances that can consume plasma, such as pollutants in sewage. The liquid addition pipe 104 can be used to input a replenishing liquid into the tank-type channels 1031. This replenishing liquid does not contain substances that can consume plasma. The replenishing liquid can be, for example, deionized water or purified water. By adding the replenishing liquid, the treatment effect of the plasma gas-liquid discharge device 100 can be optimized. For details, please refer to the device control method section below; it will not be elaborated here.
[0068] To prevent the liquid to be treated in the trough channel 1031 from flowing back into the liquid filling pipe 104, the liquid filling pipe 104 can be located above the trough channel 1031. Furthermore, the number of liquid filling pipes 104 can be the same as the number of trough channels 1031, ensuring a one-to-one correspondence between the liquid filling pipes 104 and the trough channels 1031, such as... Figure 1 As shown. Reference Figure 2 It should be understood that, in order to highlight the structure, Figure 1 In the diagram, the high-pressure electrode 101 and the low-pressure electrode 102 have been schematically moved upwards. The actual positions of the high-pressure electrode 101 and the low-pressure electrode 102 should be the positions of the dashed circles that are blocked by the liquid addition pipe 104.
[0069] In practical implementation, the outlet of the liquid addition pipe 104 can be located upstream of the trough channel 1031, close to its inlet. When adding replenishing liquid to the trough channel 1031, replenishing liquid can be introduced into each liquid addition pipe 104 via the third main pipe F, and then each liquid addition pipe 104 can introduce replenishing liquid into each trough channel 1031. Each liquid addition pipe 104, the third main pipe F, and other pipes G used to distribute replenishing liquid to each liquid addition pipe 104 can be configured as follows: Figure 6 As shown (top view).
[0070] In addition, the diameter of the liquid addition pipe 104 can be matched with the depth of the trough channel 1031, which is also at the micrometer level, thus facilitating the addition of replenishing liquid into the trough channel 1031.
[0071] It is understood that the plasma gas-liquid discharge device 100 provided in this application includes a high-voltage electrode 101, a low-voltage electrode 102, an insulating substrate 103, and multiple liquid supply pipes 104. The first surface of the insulating substrate 103 has multiple grooved channels 1031, each with a depth on the micrometer scale. The high-voltage electrode 101 and the low-voltage electrode 102 form an electric field, and each grooved channel 1031 is located within this electric field. The outlet of each liquid supply pipe 104 is connected to each grooved channel 1031. Therefore, the micrometer-deep grooved channels 1031 can provide liquid of a depth on the micrometer scale, corresponding to the depth of the liquid surface layer that the plasma action area can cover. This allows the plasma action area to encompass the liquid within the grooved channels 1031, resulting in better treatment of the liquid flowing within the grooved channels 1031, thereby improving the liquid treatment effect.
[0072] In practical applications, to prevent liquid overflow in the trough channel 1031, which would increase the liquid load in other trough channels 1031 and consequently lead to poor liquid treatment in those channels, in one embodiment, the plasma gas-liquid discharge device 100 provided in this application further includes a hydrophobic and breathable membrane 105, such as... Figure 1 and Figure 2 As shown, the hydrophobic and breathable membrane 105 is attached to the first surface to cover each of the grooved channels 1031; the surface of the hydrophobic and breathable membrane 105 facing the grooved channels 1031 is hydrophobic, and the hydrophobic and breathable membrane 105 as a whole is breathable.
[0073] The hydrophobic and breathable membrane 105 has a hydrophobic surface facing the grooved channel 1031, which can prevent liquid from passing through to a certain extent, thereby preventing overflow in the grooved channel 1031.
[0074] The hydrophobic and breathable membrane 105 is breathable, allowing gas to come into contact smoothly with the liquid in the trough channel 1031, thus enabling smooth gas-liquid two-phase discharge.
[0075] The opening portion of the trough channel 1031 corresponding to the liquid filling pipe 104 (which can also be understood as the portion covered by the projection of the liquid filling pipe 104) can be sealed by the outer wall of the liquid filling pipe 104 without the need for the hydrophobic and breathable membrane 105.
[0076] Furthermore, in order to prevent liquid overflow in the channel 1031 from increasing the liquid load in other channels 1031, the surface of the hydrophobic and breathable membrane 105 facing away from the channel 1031 is hydrophilic.
[0077] Therefore, when liquid escapes from the grooved channel 1031 through the hydrophobic and breathable membrane 105, the surface of the hydrophobic and breathable membrane 105 in contact with the escaping liquid is hydrophilic, allowing the escaping liquid to return to the grooved channel 1031. This, to a certain extent, prevents the escaping liquid from flowing into other grooved channels 1031.
[0078] To facilitate control of the liquid flow rate in each channel 1031, in one embodiment, the plasma gas-liquid discharge device 100 provided in this application further includes a plurality of first valves 106, such as... Figure 5 As shown, each of the first valves 106 is respectively disposed on each of the grooved channels 1031.
[0079] The size of each first valve 106 can be at the micrometer level, so that the first valve 106 can be set on the trough channel 1031 to control the liquid flow rate in the trough channel 1031.
[0080] In a practical implementation, the portion of the trough channel 1031 near the inlet can be a closed pipe, allowing the first valve 106 to be installed on the closed pipe. For example, the first valve 106 can be installed on the portion closed by the outer wall of the liquid addition pipe 104. Correspondingly, the first main pipe C for distributing liquid to each trough channel 1031 and other distribution pipes can also be closed pipes.
[0081] Similarly, to facilitate control of the replenishment liquid added to each tank channel 1031, in one embodiment, the plasma gas-liquid discharge device 100 provided in this application also includes a plurality of second valves 107, such as... Figure 6 As shown, each of the second valves 107 is respectively installed on each of the liquid filling pipes 104.
[0082] The size of each second valve 107 can be at the micrometer level, so that the second valve 107 can be installed on the liquid filling pipe 104 to control the liquid flow rate in the liquid filling pipe 104.
[0083] In order to avoid the airflow affecting the plasma concentration in the corresponding area above each slotted channel 1031, in one embodiment, the plasma gas-liquid discharge device 100 provided in this application embodiment further includes an airflow control device (not shown in the figure). The airflow control device is located on one side of the first surface and is used to control the airflow direction in the gas phase discharge space, which is parallel to the extension direction of the slotted channel 1031.
[0084] The airflow control device can be used to control the direction of airflow in the gas phase discharge space, and it can also be used to supply gas.
[0085] In this embodiment, by using an airflow control device to control the airflow direction in the gas phase discharge space to be parallel to the extension direction of the grooved channel 1031, plasma generated in the region above the grooved channel 1031 can be prevented from moving to the region above other grooved channels 1031. This ensures that the plasma reaction energy in the region above each grooved channel 1031 is in a relatively stable state, and consequently, the plasma reaction energy in the liquid within each grooved channel 1031 is also in a relatively stable state. Therefore, when the plasma gas-liquid discharge device 100 is subsequently controlled using the device control method described later, the liquid processing effect can be improved.
[0086] Based on the plasma gas-liquid discharge device provided in the above embodiments of this application, this application also provides a device control method, which can be used to control the plasma gas-liquid discharge device in the above embodiments. For example... Figure 7 As shown, the control method may include the following steps:
[0087] Step 201: Determine the distribution of plasma in each trough channel.
[0088] In practice, the distribution of plasma in each channel can be determined after the electric field between the high-voltage electrode and the low-voltage electrode is adjusted to a certain strength so that the electric field can excite the gas molecules in the discharge space to undergo an excited ionization process (the excitation ionization intensity of the discharge process can be monitored by parameters such as voltage and current).
[0089] Specifically, determining the distribution of plasma in each channel can involve determining the distribution of plasma reaction energy in the liquid within each channel.
[0090] In this embodiment, the distribution of plasma can include the ratio of plasma reaction energy between each channel; that is, the ratio of plasma reaction energy dissolved in the liquid of each channel can be denoted as n1:n2:n3:n4:n5...
[0091] Furthermore, in specific implementation, determining the plasma distribution in each of the aforementioned trough channels may include: introducing a colorimetric solution into each of the aforementioned trough channels, taking a sample of the colorimetric solution at the outlet of each of the aforementioned trough channels, and performing colorimetric reduction calibration using a calibration solution; and determining the plasma reaction energy ratio between the aforementioned trough channels based on the amount of calibration solution consumed.
[0092] In the above embodiments, the color developing solution contains a substance that can react with plasma, and the color changes after the color developing solution reacts with the plasma. The color developing solution generates reaction products after reacting with the plasma, and the standardizing substance in the standardizing solution can react with these reaction products. Therefore, the reaction energy ratio of the plasma between each of the tank channels can be determined based on the amount of standardizing substance consumed in the standardizing solution.
[0093] The colorimetric solution can be, for example, a potassium iodide solution, and the standardization solution can be, for example, a sodium thiosulfate solution. Potassium iodide solution is a colorless and transparent solution. When potassium iodide reacts with plasma, elemental iodine is generated, and the colorimetric solution develops color. When using sodium thiosulfate solution for standardization, sodium thiosulfate can react with elemental iodine. Therefore, the amount of sodium thiosulfate consumed corresponds to the amount of plasma consumed by potassium iodide in the colorimetric solution, thereby allowing the determination of the plasma reaction energy ratio between each of the tank channels.
[0094] Generally, the plasma concentration is higher closer to the electrode, resulting in greater plasma reaction energy in the liquid within the channel closer to the electrode. Consequently, the color development of the developing solution is more pronounced in the channel closer to the electrode. If, in practical applications, the color development of the developing solution is not pronounced in any of the channels, especially in the channels near the electrode, it indicates that the electrode may be too far from the insulating substrate, preventing most of the plasma from entering the liquid within the channels and resulting in low plasma utilization. In this case, the distance between the electrode and the insulating substrate can be reduced until a more pronounced color development is achieved in each channel, especially in the channels near the electrode.
[0095] Step 202: Determine the target flow rate corresponding to each of the trough channels based on the distribution.
[0096] Specifically, for any given trough channel, the target flow rate is matched with the plasma reaction energy within that channel. In other words, by setting the liquid flow rate in the trough channel to its target flow rate, the plasma reaction energy within the channel is precisely matched with the amount of substance to be treated in the liquid. This prevents situations where excessive plasma reaction energy leads to plasma waste or insufficient plasma reaction energy results in poor liquid treatment.
[0097] In this embodiment of the application, determining the target flow rate corresponding to each of the trough channels based on the distribution may include: determining a target trough channel from among the trough channels, wherein the target trough channel is the trough channel with the highest plasma reaction energy among the trough channels; introducing a target solution into the target trough channel, and determining the first flow rate corresponding to the target trough channel when the treatment effect of the target solution reaches a preset index; and determining the target flow rate corresponding to each trough channel based on the first flow rate and the plasma reaction energy ratio among the trough channels.
[0098] The target solution can be the liquid to be processed by the plasma gas-liquid discharge device, such as ammonium sulfite solution, calcium sulfite solution, azo dye (AO7) solution or other contaminant solution.
[0099] In the above embodiments, the target channel can be determined by the plasma reaction energy ratio n1:n2:n3:n4:n5... among the various channels.
[0100] In practice, a full load of target solution with a constant concentration can be continuously input into the target channel, and the solution at the outlet of the target channel can be monitored to detect the remaining concentration of the substance to be treated (such as pollutants) in the solution. Simultaneously, the applied voltage and the flow rate of the target solution are controlled until the treatment effect of the target solution reaches a preset target. The applied voltage at this point is recorded, referred to as the target applied voltage; and the flow rate of the target solution at this point is recorded, referred to as the first flow rate. The treatment effect of the target solution reaching the preset target can be defined as the remaining concentration of the substance to be treated in the solution at the outlet of the target channel being less than a preset concentration.
[0101] The first flow rate is the target flow rate corresponding to the target trough channel. This target flow rate can also be understood as the flow rate that matches the plasma reaction energy within the target trough channel. Specifically, when the target solution flowing through the target trough channel reaches the target flow rate, the amount of the substance to be treated in the target solution exactly matches the plasma reaction energy within the channel.
[0102] It is understandable that the greater the plasma reaction energy within the trough channel, the greater the processing capacity, and consequently, the greater the amount of material to be processed and the higher the flow rate of the target solution. Therefore, the ratio between the target flow rates of each trough channel (denoted as Q1, Q2, Q3, Q4, Q5...) satisfies Q1:Q2:Q3:Q4:Q5... = n1:n2:n3:n4:n5... Thus, based on this ratio and the target flow rate corresponding to the target trough channel, the target flow rate for each trough channel can be obtained.
[0103] Step 203: Based on the target flow rate, control the liquid flow rate in each of the trough channels.
[0104] In one embodiment, controlling the liquid flow rate in each of the trough channels based on the target flow rate may include controlling the liquid flow rate in each trough channel to its corresponding target flow rate. Furthermore, the applied voltage may also be controlled to the target applied voltage.
[0105] In a more preferred embodiment, each of the trough channels includes a first trough channel, wherein the first trough channel is any one of the trough channels; when the target flow rate corresponding to the first trough channel is less than the target flow rate corresponding to the target trough channel, the step of controlling the liquid flow rate in each of the trough channels based on the target flow rate includes: introducing a first liquid into the first trough channel to make the flow rate in the first trough channel equal to the target flow rate corresponding to the target trough channel.
[0106] The first liquid is the replenishing liquid mentioned earlier. Generally, the target flow rate corresponding to the target channel is often the highest, while the target flow rates corresponding to other channels are equal to or less than the target flow rate corresponding to the target channel. When the target flow rates corresponding to other channels are equal to the target flow rate corresponding to the target channel, replenishing liquid is not necessary.
[0107] Considering that when the target flow rate of other trough channels is less than that of the target trough channel, if the liquid flow rate in the other trough channels is controlled to their respective target flow rates, based on Q = V / t (where Q is the flow rate, V is the volume of the trough channel, and t is the residence time of the liquid in the trough channel, i.e., the time spent in the channel), the residence time of the liquid in the other trough channels will be too long. For example, for a certain first trough channel, a residence time of 5 minutes is sufficient to process the liquid and achieve the preset treatment effect. However, due to the small target flow rate, a residence time of 10 minutes may result in more plasma dissolving in the liquid, and this plasma will lack a target for treatment, thus wasting plasma.
[0108] The embodiments described above in this application control the flow rate in other tank channels to be equal to the target flow rate corresponding to the target tank channel by adding supplementary liquid, thus ensuring that the liquid in each tank channel has a suitable residence time. Specifically, taking a first tank channel as an example, the flow rate of the supplementary liquid added to the first tank channel is equal to the target flow rate corresponding to the target tank channel minus the target flow rate corresponding to the first tank channel. This avoids wasting plasma and improves the liquid processing efficiency, achieving a balance between processing effect and efficiency.
[0109] To facilitate the explanation of the effects of the plasma gas-liquid discharge device and device control method provided in the embodiments of this application, the following will be described in conjunction with specific embodiments and comparative examples.
[0110] In the following embodiments and comparative examples, linear high-voltage electrodes and linear low-voltage electrodes are used, with a spacing of 5 mm between them. The placement of the linear high-voltage and low-voltage electrodes can be referred to the foregoing description and will not be repeated here. Forty parallel slotted channels are formed on the insulating substrate, numbered sequentially as 1, 2, 3, 4, 5...40. Each slotted channel has a 100 μm × 100 μm square cross-section, and the spacing between any two adjacent slotted channels is 20 μm.
[0111] Under an applied voltage of 18kV, potassium iodide colorimetric solution was introduced into each channel, and the residence time of the potassium iodide colorimetric solution in the channel was controlled to be 4 minutes. Colorimetric solution was collected at the outlet of each channel and calibrated using sodium thiosulfate standard solution. Calculations show that, in order of arrangement, the proportion of calibration solution consumed in calibrating the colorimetric solution sampled from the outlet of each tank channel is 0.97:0.99:1:0.99:0.99:0.97:0.93:0.88:0.86:0.85:0.81:0.72:0.68:0.65:0.63:0.57:0.5:0.46:0.4:0.3:0.32:0.4:0.47:0.53:0.59:0.63:0.68:0.71:0.75:0.79:0.83:0.85:0.88:0.93:0.97:0.98:0.99:1.1:0.98:0.95. Based on the calibration fluid consumption ratio, the tank channel with the highest calibration fluid consumption is selected as the target tank channel.
[0112] Example 1
[0113] Ammonium sulfite solution was introduced into the target tank channel. The applied voltage and the flow rate of the ammonium sulfite solution were adjusted until the treatment effect of the ammonium sulfite solution reached the preset effect. At this point, the applied voltage was recorded as 18kV and the flow rate as 0.36uL / min. Based on the proportion of calibration solution consumed by each tank channel, the target flow rate of the ammonium sulfite solution for the other tank channels was determined. When the target flow rate of the ammonium sulfite solution for the other tank channels was less than 0.36uL / min, it was supplemented with deionized water.
[0114] Samples were taken from the second main pipeline where the liquid from each of the various channel outlets converged to test the concentration of ammonium sulfite in the treated liquid. The calculated removal rate of ammonium sulfite was 98%.
[0115] Example 2
[0116] Calcium sulfite solution was introduced into the target tank channel. The applied voltage and the flow rate of the calcium sulfite solution were adjusted until the treatment effect of the calcium sulfite solution reached the preset effect. At this point, the applied voltage was recorded as 20kV and the flow rate as 0.4uL / min. Based on the proportion of calibration solution consumed by each tank channel, the target flow rate of the calcium sulfite solution for the other tank channels was determined. When the target flow rate of the calcium sulfite solution for the other tank channels was less than 0.4uL / min, it was supplemented with deionized water.
[0117] Samples were taken from the second main pipeline where the liquid from each of the various channel outlets converged to determine the concentration of calcium sulfite in the treated liquid. The calculated removal rate of calcium sulfite was 87%.
[0118] Example 3
[0119] AO7 solution was introduced into the target tank channel, and the applied voltage and AO7 solution flow rate were adjusted until the treatment effect of the AO7 solution reached the preset effect. At this point, the applied voltage was recorded as 20kV and the flow rate as 0.51uL / min. Based on the proportion of calibration solution consumed by each tank channel, the target flow rate of AO7 solution for the other tank channels was determined. When the target flow rate of AO7 solution for the other tank channels was less than 0.51uL / min, it was supplemented with deionized water.
[0120] Samples were taken from the second main pipeline where the liquid from each of the various channel outlets converged to determine the concentration of AO7 in the treated liquid. The calculated AO7 removal rate was 76%.
[0121] Comparative Example 1
[0122] With an applied voltage of 18 kV, ammonium sulfite solution was introduced into each channel at the same concentration as in Example 1. The flow rate of the ammonium sulfite solution in each channel was 0.36 μL / min.
[0123] Samples were taken from the second main pipeline where the liquid from each of the various channel outlets converged to test the concentration of ammonium sulfite in the treated liquid. The calculated removal rate of ammonium sulfite was 84%.
[0124] Comparative Example 2
[0125] With an applied voltage of 20 kV, calcium sulfite solution was introduced into each channel at the same concentration as in Example 2. The flow rate of the calcium sulfite solution in each channel was 0.4 μL / min.
[0126] Samples were taken from the second main pipeline where the liquid from each of the various channel outlets converged to determine the concentration of calcium sulfite in the treated liquid. The calculated removal rate of calcium sulfite was 69%.
[0127] Comparative Example 3
[0128] With an applied voltage of 20 kV, AO7 solution was introduced into each tank channel at the same concentration as in Example 3. The flow rate of AO7 solution in each tank channel was 0.51 μL / min.
[0129] Samples were taken from the second main pipeline where the liquid from each of the various channel outlets converged to determine the concentration of AO7 in the treated liquid. The calculated AO7 removal rate was 58%.
[0130] Based on the comparison results of Example 1 and Comparative Example 2, Example 2 and Comparative Example 2, and Example 3 and Comparative Example 3, it can be seen that the device control method provided in the embodiments of this application can effectively improve the liquid processing effect.
[0131] It should also be noted that the terms "comprising," "including," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent to such process, method, article, or apparatus. Unless otherwise specified, an element defined by the phrase "comprising one..." does not exclude the presence of other identical elements in the process, method, article, or apparatus that includes that element.
[0132] The above are merely embodiments of this application and are not intended to limit the scope of this application. Various modifications and variations can be made to this application by those skilled in the art. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of this application should be included within the scope of the claims of this application.
Claims
1. A device control method, characterized in that, The control method is used to control a plasma gas-liquid discharge device; the discharge device includes a high-voltage electrode, a low-voltage electrode, an insulating substrate, multiple liquid supply pipes, and a hydrophobic and breathable membrane; wherein, the first surface of the insulating substrate has multiple grooved channels, each grooved channel having a depth of micrometers; the high-voltage electrode and the low-voltage electrode are used to form an electric field, and each grooved channel is located in the electric field; the outlet of each liquid supply pipe is connected to each grooved channel; liquid is introduced into each grooved channel through a first main pipeline, and the liquid in each grooved channel flows out and converges into a second main pipeline; the hydrophobic and breathable membrane is attached to the first surface to cover each grooved channel; the surface of the hydrophobic and breathable membrane facing the grooved channel is hydrophobic, and the hydrophobic and breathable membrane as a whole is breathable, so that the gas in the gas phase and the liquid in each grooved channel can contact each other; the surface of the hydrophobic and breathable membrane facing away from the grooved channel is hydrophilic; the control method includes: determining the plasma reaction energy ratio between each grooved channel; from each A target channel is identified among the various tank channels, and the target channel is the one with the highest plasma reaction energy. A target solution is introduced into the target channel, and a first flow rate is determined when the treatment effect of the target solution reaches a preset target. Based on the first flow rate and the plasma reaction energy ratio among the various tank channels, a target flow rate is determined for each tank channel. The target solution contains a substance that can consume plasma. Based on the target flow rate, the liquid flow rate in each tank channel is controlled. If the target flow rate of the first tank channel is less than the target flow rate of the target channel, a first liquid is introduced into the first tank channel through the liquid supply pipe corresponding to the first tank channel, so that the flow rate in the first tank channel is equal to the target flow rate of the target channel. The first tank channel is any one of the various tank channels, and the first liquid does not contain a substance that can consume plasma.
2. The device control method according to claim 1, characterized in that, The high-voltage electrode is a linear high-voltage electrode, and the low-voltage electrode is a linear low-voltage electrode. The linear high-voltage electrode and the linear low-voltage electrode are located on the same target plane; the target plane is parallel to the first surface.
3. The device control method according to claim 1, characterized in that, The high-voltage electrode is a linear high-voltage electrode, and the low-voltage electrode is a plate-shaped low-voltage electrode. The linear high-voltage electrode is located on one side of the first surface, and the plate-shaped low-voltage electrode is located on one side of the second surface of the insulating substrate; the second surface is opposite to the first surface.
4. The device control method according to claim 1, characterized in that, The high-voltage electrode is a plate-shaped high-voltage electrode, and the low-voltage electrode is a plate-shaped low-voltage electrode. The plate-shaped high-voltage electrode is located on one side of the first surface, and the plate-shaped low-voltage electrode is located on one side of the second surface of the insulating substrate; the second surface is opposite to the first surface.
5. The device control method according to any one of claims 1-4, characterized in that, The slotted channels are parallel to each other, and the direction of the electric field is perpendicular to the extension direction of each slotted channel.
6. The device control method according to claim 1, characterized in that, The discharge device also includes a plurality of first valves, each of which is respectively disposed on each of the groove-shaped channels.
7. The device control method according to claim 6, characterized in that, The discharge device also includes a plurality of second valves, each of which is respectively installed on each of the liquid addition pipelines.
8. The device control method according to claim 1, characterized in that, The spacing between any two adjacent slot channels is on the order of micrometers.
9. The device control method according to claim 1, characterized in that, The discharge device further includes an airflow control device located on one side of the first surface. The airflow control device is used to control the airflow direction in the gas phase discharge space, which is parallel to the extension direction of the slotted channel.
10. The device control method according to claim 1, characterized in that, Determining the plasma distribution in each of the aforementioned slotted channels includes: Color-developing liquid is introduced into each of the aforementioned tank channels, and color-developing liquid is taken at the outlet of each of the aforementioned tank channels. Color development and reduction calibration is performed using a calibration solution. The plasma reaction energy ratio between each of the aforementioned tank channels is determined based on the amount of calibration liquid consumed.
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