A low-cost, fast-activation liquid wet cleaning method and device

By reserving medium-term liquid in the secondary tank of the medicine liquid and replenishing it, the problem of insufficient activation of the early batch life of the medicine liquid tank is solved, rapid activation and recycling of the medicine liquid is achieved, and wet cleaning of single crystal solar cells is improved The effect reduces cost and waste discharge, and is suitable for a variety of tank wet processes.

CN117123556BActive Publication Date: 2024-12-17JIANGSU RUNERGY YUEDA PHOTOVOLTAIC TECHNOLOGY CO LTD
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Patent Information

Application Number
CN202311190379.2
Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
Filing Date
2023-09-15
Publication Date
2024-12-17
Estimated Expiration
2043-09-15

AI Technical Summary

Technical Problem

During the wet cleaning process of single crystal solar cell tank, the batch life of the liquid tank is inactive in the early stage, and the reaction product concentration is low, resulting in poor wet treatment effect, especially initial casting, velvet making, alkali casting, etc. The functional tank has a great impact, affecting the photoelectric conversion efficiency of solar cells.

Method used

By reserveing ​​medium-term medicine liquid in the secondary tank of the medicine liquid and replenishing it when the life of the medicine liquid tank reaches, ensuring that the medicine liquid reaches the working liquid level, achieving rapid activation and recycling of the medicine liquid, a new tank body structure is designed. The liquid tank and the liquid secondary tank are connected through pipelines, and are equipped with liquid outlet, liquid inlet, liquid discharge and heater to realize self-replenishment and self-distribution of liquid.

Benefits of technology

Improves the cleaning effect of the early life of the medicine tank, reduces the amount of the medicine tank, reduces the cost of the medicine tank and waste discharge, enhances the stability and photoelectric conversion efficiency of the wool making tank, and is suitable for crystalline silicon solar cell process flow All groove wet processes in

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Abstract

The present invention discloses a low-cost, fast-activation wet cleaning method for liquid medicine, comprising the following steps: obtaining the number of batch lifespans of liquid medicine in a liquid medicine tank; obtaining the position of the liquid level in a liquid medicine sub-tank when the batch lifespan of the liquid medicine in the liquid medicine tank reaches the middle stage; judging whether the position of the liquid level in the liquid medicine sub-tank is above the empty liquid level; if so, opening the liquid discharge valve of the liquid medicine sub-tank to empty the excess liquid medicine; if not, opening the liquid inlet valve of the liquid medicine sub-tank to replenish the liquid medicine in the liquid medicine sub-tank; obtaining the position of the liquid level in the liquid medicine sub-tank in real time during liquid replenishment, and closing the liquid inlet valve of the liquid medicine sub-tank to stop liquid replenishment when the liquid level reaches within the standard range. The present invention can automatically identify the renewal of liquid medicine in the liquid medicine sub-tank, realize self-replenishment and recycling of liquid medicine, and ensure the activity and functionality of liquid medicine. On the basis of existing large-scale production, the cleaning effect of the liquid medicine tank in the early stage of its lifespan is improved; the amount of initially prepared liquid medicine is reduced, so that the liquid medicine can be recycled, and the liquid medicine cost and waste discharge cost are reduced.
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Description

Technical Field

[0001] The invention relates to the technical field of single-crystal solar cell trough-type wet cleaning, in particular to a low-cost, fast-activation liquid wet cleaning method and device. Background Art

[0002] In this technical field, including common functional tanks such as pre-cleaning tanks, pickling tanks, alkali washing tanks, initial polishing tanks, texturing tanks, alkali polishing tanks, etc., the currently widely used mode is "liquid preparation → cleaning → batch / time fixed discharge and replenishment → liquid drainage → re-liquid preparation". The batch life of the liquid medicine tank generally ranges from 50 to 600 batches. When the batch life of the liquid medicine tank reaches the end, the concentration of reaction products and impurity pollutants in the liquid medicine gradually increases to a peak value. At this time, the liquid medicine tank can no longer work normally, and it is necessary to drain all the liquid medicine and then prepare the liquid again to ensure the normal function of the liquid medicine tank.

[0003] However, there are problems with the current model, which mainly occur in the early stage of the batch life of the liquid medicine tank. At this time, the liquid medicine has not yet been activated and the concentration of the reaction product is low, which results in the early liquid medicine tank often failing to play its 100% role, ultimately leading to poor early wet treatment effects, especially for functional tanks such as initial polishing, texturing, and alkali polishing.

[0004] For example, the liquid composition of the texturing tank is water, KOH / NaOH, and texturing additives. In the early stage of the life of the liquid tank, the concentration of silicate in the liquid is low, the solution viscosity is insufficient, and the transport process of OH- ions from the liquid to the reaction interface lacks buffering effect, resulting in poor stability of the texturing process. In the early stage of the batch life of the texturing tank, the surface uniformity of the silicon wafer is poor, and the weight loss and surface reflectivity also fluctuate greatly, which ultimately leads to a decrease in the photoelectric conversion efficiency of solar cells. Summary of the invention

[0005] In view of the deficiencies in the prior art, the present invention provides a low-cost wet cleaning method and device for quickly activating liquid medicine, which solves the problem that in the current cleaning mode, the liquid medicine tank is not activated yet in the early stage of the batch life, and the concentration of the reaction product is low, resulting in the early stage of the liquid medicine tank often failing to play its 100% role, ultimately leading to poor wet processing effects in the early stage, especially the functional tanks such as initial polishing, silk making, and alkali polishing are greatly affected.

[0006] To achieve the above objectives, the present invention is implemented through the following technical solutions:

[0007] A low-cost wet cleaning method with fast activation of liquid medicine. When the batch life of the liquid medicine tank is reached, the liquid medicine is emptied. When re-preparing the liquid, the liquid outlet valve of the liquid medicine sub-tank is opened, and the mid-term liquid medicine reserved in the liquid medicine sub-tank is added. After the liquid medicine reaches the working liquid level, the texturing begins.

[0008] The working steps include:

[0009] S1: Get the number of times the batch life of the medicine solution in the medicine solution tank is reached;

[0010] S2: when the batch life of the medicine solution in the medicine solution tank reaches the middle stage, obtaining the position of the liquid level in the medicine solution auxiliary tank;

[0011] S3: Determine whether the liquid level in the liquid auxiliary tank is above the empty liquid level;

[0012] S4: If yes, open the drain valve of the liquid auxiliary tank to drain the excess liquid;

[0013] If not, opening the liquid inlet valve of the liquid medicine auxiliary tank to replenish the liquid medicine into the liquid medicine auxiliary tank;

[0014] S5: During the liquid replenishment, the liquid level in the liquid auxiliary tank is obtained in real time. When the liquid level reaches within the standard range, the liquid inlet valve of the liquid auxiliary tank is closed to stop the liquid replenishment.

[0015] Furthermore, S4 includes:

[0016] When the liquid inlet valve of the liquid medicine sub-tank is opened, the discharge valve of the liquid medicine tank is closed synchronously, and the liquid medicine sub-tank directly replenishes the liquid medicine of the liquid medicine tank process discharge.

[0017] Furthermore, S4 includes:

[0018] The liquid medicine auxiliary tank is replenished in batches, with the replenishment volume of each batch being 1-10L, and the interval of replenishment is consistent with the interval time of the liquid medicine tank process.

[0019] Furthermore, the S1 comprises the following steps:

[0020] S11: Obtaining target feature data dimensions associated with the attenuation of the life of the drug solution batch;

[0021] S12: obtaining target cleaning condition information in the medicine tank, and establishing a data model for the attenuation of the batch life of the medicine in the medicine tank according to the target cleaning condition information in the medicine tank and the target characteristic data dimension;

[0022] S13: using the data model to predict the batch life of the medicine in the medicine tank.

[0023] Furthermore, the S11 comprises the following steps:

[0024] S111: Acquiring cleaning condition information in the sample solution tank;

[0025] S112: determining a plurality of characteristic data dimensions according to the cleaning condition information in the sample liquid tank;

[0026] S113: Determine a target feature data dimension related to the life decay of a batch of drug solution from the multiple feature data dimensions.

[0027] Furthermore, the S112 includes the following steps:

[0028] S1121: Determine the liquid condition information related to the liquid batch life from the cleaning condition information in the sample liquid tank;

[0029] S1122: Determine multiple characteristic data dimensions based on the liquid medicine working condition information.

[0030] Furthermore, the S113 includes the following steps:

[0031] S1131: Determine, according to the cleaning condition information in the sample liquid tank, feature data corresponding to each feature data dimension in the plurality of feature data dimensions;

[0032] S1132: performing correlation analysis on the life decay of the drug solution batch for the feature data corresponding to each feature data dimension respectively, and obtaining the target feature data dimension related to the life decay of the drug solution batch.

[0033] Further, the S12 comprises the following steps:

[0034] S121: Target cleaning condition information in the liquid medicine tank, determining a target dimension weight for the target feature data dimension;

[0035] S122: Using the target dimension weight, a data model for the attenuation of the batch life of the medicine solution in the medicine solution tank is established.

[0036] A low-cost, fast-activation liquid wet cleaning device, used to implement the low-cost, fast-activation liquid wet cleaning method;

[0037] The invention comprises a medicine liquid tank and a medicine liquid sub-tank, wherein the medicine liquid tank and the medicine liquid sub-tank are connected by a pipeline, and a medicine liquid sub-tank outlet valve is arranged in the pipeline connecting the medicine liquid tank and the medicine liquid sub-tank, a medicine liquid tank fixed discharge valve is arranged in the pipeline leading from the medicine liquid sub-tank to the outside, a medicine liquid tank drain valve is arranged in the pipeline leading from the medicine liquid tank to the outside, a heater is arranged between the medicine liquid tank and the medicine liquid sub-tank, an output end of the heater leads to the medicine liquid tank, an input end of the medicine liquid tank is connected to the medicine liquid sub-tank, the medicine liquid tank fixed discharge valve and one end of a circulation pump, the other end of the circulation pump is connected to the medicine liquid tank, and the other end of the medicine liquid tank fixed discharge valve leads to the outside.

[0038] Furthermore, the liquid medicine tank structure is a new type of tank structure, including a liquid medicine auxiliary tank, which is connected to the liquid medicine tank and the liquid medicine circulation pipeline through a pipeline, and is equipped with an independent discharge pipeline and a control valve;

[0039] Furthermore, the volume of the liquid medicine auxiliary tank is 10-50L;

[0040] Furthermore, the secondary tank for the liquid medicine has reserved therein a medium-term liquid medicine accounting for 1% to 20% of the total volume of the liquid medicine tank;

[0041] Furthermore, the mid-term medicine solution is discharged into the auxiliary tank by controlling the liquid inlet valve of the auxiliary tank at the middle of the batch life of the medicine solution tank to supply the next preparation;

[0042] Furthermore, the mid-term medicine solution refers to 20%-80% of the overall life of the medicine solution;

[0043] Furthermore, the wet cleaning method is applicable to all tank wet processes in the process flow of crystalline silicon solar cells, including but not limited to pre-cleaning tanks, acid washing tanks, alkaline washing tanks, initial polishing tanks, texturing tanks, alkaline polishing tanks and other commonly used functional tanks.

[0044] Compared with the prior art, the present invention has at least the following beneficial effects:

[0045] The present invention provides a low-cost wet cleaning method for quickly activating a chemical solution, and designs a new type of tank structure, thereby improving the cleaning effect of the chemical solution tank in the early stage of its service life (or improving other functional effects, with different effects depending on the function of the adapted tank) on the basis of existing large-scale production; the tank structure is simple and easy to operate, and there is no need to frequently adjust the process; and the amount of initially prepared chemical solution is reduced, so that the chemical solution can be recycled, reducing the cost of the chemical solution and the cost of waste discharge; it can be widely applicable to all tank-type wet processes in the process flow of crystalline silicon solar cells, including but not limited to pre-cleaning tanks, acid washing tanks, alkali washing tanks, initial polishing tanks, texturing tanks, alkali polishing tanks and other commonly used functional tanks. BRIEF DESCRIPTION OF THE DRAWINGS

[0046] Figure 1 is a flow chart of the method of the present invention;

[0047] Figure 2 A schematic diagram showing the comparison between the surface reflectivity of the silicon wafer prepared in the present invention and that in normal production;

[0048] Figure 3 A schematic diagram showing the comparison between the weight reduction of a single silicon wafer produced by the present invention and that in normal production;

[0049] Figure 4 It is a schematic diagram of the main structure of the present invention.

[0050] In the figure: 1. medicine liquid tank; 2. liquid outlet valve of medicine liquid auxiliary tank; 3. medicine liquid auxiliary tank; 4. heater; 5. liquid inlet valve of medicine liquid auxiliary tank; 6. liquid drain valve of medicine liquid auxiliary tank; 7. fixed and drain valve of medicine liquid tank; 8. circulation pump; 9. liquid drain valve of medicine liquid tank. DETAILED DESCRIPTION

[0051] The technical solutions in the embodiments of the present invention will be described clearly and completely below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, rather than all the embodiments.

[0052] Example 1

[0053] See also Figure 1-4 The present invention provides a technical solution: a low-cost wet cleaning method for rapidly activating a liquid medicine, characterized in that:

[0054] When the batch life of the liquid in the liquid tank 1 is reached, the liquid is drained. When preparing the liquid again, the liquid outlet valve 2 of the liquid auxiliary tank is opened, and the reserved medium-term liquid in the liquid auxiliary tank 3 is added. When the liquid reaches the working liquid level, the texturing begins.

[0055] The working steps include:

[0056] S1: Get the number of times the batch life of the medicine solution in the medicine solution tank 1 is reached;

[0057] S2: when the batch life of the medicine solution in the medicine solution tank 1 reaches the middle stage, obtaining the position of the liquid level in the medicine solution auxiliary tank 3;

[0058] S3: Determine whether the liquid level in the liquid auxiliary tank 3 is above the empty liquid level;

[0059] S4: If yes, open the liquid drain valve 6 of the liquid auxiliary tank to drain the excess liquid;

[0060] If not, open the liquid inlet valve 5 of the liquid auxiliary tank to add liquid medicine into the liquid auxiliary tank 3;

[0061] S5: During the liquid replenishment, the position of the liquid level in the liquid auxiliary tank 3 is obtained in real time. When the liquid level reaches within the standard range, the liquid inlet valve of the liquid auxiliary tank 3 is closed to stop the liquid replenishment.

[0062] Preferably, S4 includes:

[0063] When the liquid inlet valve 5 of the liquid medicine auxiliary tank is opened, the liquid medicine tank fixed discharge valve 7 is closed synchronously, and the liquid medicine auxiliary tank 3 directly replenishes the liquid medicine of the liquid medicine tank 1 for process fixed discharge.

[0064] Preferably, S4 includes:

[0065] The liquid medicine auxiliary tank 3 is replenished in batches, with the replenishment volume of each batch being 1-10L, and the interval of replenishment is consistent with the process interval of the liquid medicine tank 1.

[0066] Preferably, the auxiliary liquid tank 3 is reserved with 1%-20% of the total volume of the liquid tank 1;

[0067] Preferably, the mid-term medicine liquid is discharged into the medicine liquid auxiliary tank 3 by controlling the medicine liquid auxiliary tank inlet valve 5 at the middle of the batch life of the medicine liquid tank 1 to supply the next liquid preparation;

[0068] Preferably, the mid-term medicine solution refers to 20%-80% of the overall life of the medicine solution.

[0069] The working principle and beneficial effects of the above scheme:

[0070] The present invention solves the problem that in the early stage of the batch life of the liquid medicine tank 1, the liquid medicine has not been activated and the concentration of the reaction product is low, resulting in the early stage of the liquid medicine tank 1 often failing to play its 100% role, and ultimately leading to poor wet processing effect in the early stage, especially the functional tanks such as initial polishing, texturing, and alkali polishing are greatly affected by the mixing of the mid-term liquid medicine reserved in the liquid medicine sub-tank 3 with the new liquid medicine.

[0071] The present invention provides a low-cost wet cleaning method for quickly activating liquid medicine, and designs a new tank structure, which can automatically identify the liquid medicine in the liquid medicine sub-tank 3 for updating, realize the self-replenishment and recycling of the liquid medicine, ensure the activity and functionality of the liquid medicine, and save the cost of the liquid medicine. Thus, on the basis of existing large-scale production, the cleaning effect of the liquid medicine tank 1 in the early period of its life is improved; the tank structure is simple, easy to operate, and there is no need to adjust the process frequently; and the amount of the initial liquid medicine is reduced, so that the liquid medicine can be recycled, and the cost of the liquid medicine and the cost of waste discharge are reduced; it can be widely applied to all tank-type wet processes in the process flow of crystalline silicon solar cells, including but not limited to pre-cleaning tanks, pickling tanks, alkali washing tanks, initial polishing tanks, velvet-making tanks, alkali polishing tanks and other commonly used functional tanks.

[0072] Example 2

[0073] See also Figure 1-4 On the basis of Example 1, a single crystal texturing and cleaning method with rapid activation of liquid is provided. After the batch life of the texturing liquid tank 1 is reached, the liquid is emptied. When the liquid is prepared again, the liquid outlet valve 2 of the liquid auxiliary tank is opened, and the intermediate liquid reserved in the liquid auxiliary tank 3 is added. After the liquid reaches the working liquid level, texturing begins.

[0074] Preferably, the tank volume of the liquid medicine tank 1 is 500L, and the tank volume of the liquid medicine auxiliary tank 3 is 50L;

[0075] Preferably, the life of the drug solution tank 1 is 200 batches;

[0076] Preferably, the auxiliary liquid tank 3 is reserved with mid-term liquid accounting for 10% of the total volume of the liquid tank 1;

[0077] Preferably, the mid-term medicine liquid is discharged into the medicine liquid auxiliary tank 3 by controlling the medicine liquid auxiliary tank inlet valve 5 at the middle of the batch life of the medicine liquid tank 1 to supply the next liquid preparation;

[0078] Preferably, the mid-term medicine solution refers to 30%-40% of the overall life of the medicine solution;

[0079] Compared with the weight loss and surface reflectivity of each batch of single crystal silicon wafers after texturing during normal production, the weight loss and surface reflectivity of batches 1-40 using this method have increased significantly, and compared with batches 41-200, the overall fluctuation is relatively gentle.

[0080] It can be seen that the single crystal texturing and cleaning method of the low-cost fast-activation liquid of the present invention improves the texturing effect in the early stage of the texturing tank's life on the basis of existing large-scale production, makes the texturing tank more stable throughout its entire life cycle, reduces the amount of initially prepared liquid, allows the liquid to be recycled, and reduces the liquid cost and waste discharge cost.

[0081] Example 3

[0082] On the basis of Example 1, S1 comprises the following steps:

[0083] S11: Obtaining target feature data dimensions associated with the attenuation of the life of the drug solution batch;

[0084] The life of a drug batch can be the number of cycles of the drug, that is, the number of times the drug cycle participates in the reaction. The more the drug participates, the lower the life of the drug batch. Therefore, the life of the drug batch can be predicted by calculating the decay of the drug batch life.

[0085] The target feature data dimensions include at least one or more of the following:

[0086] The dimensions of ambient temperature, circulation speed, and the amount of objects to be cleaned;

[0087] The ambient temperature dimension can be the temperature of the working environment of the liquid medicine;

[0088] The circulation speed dimension may be the flow rate of the liquid medicine driven by the circulation pump 8;

[0089] The dimension of the amount of the object to be cleaned may be the amount of solar cells to be cleaned in the liquid tank 1;

[0090] The dimensions of the amount of objects to be cleaned, the ambient temperature, and the circulation speed will all affect the reaction rate of the liquid medicine, that is, how fast the liquid medicine batch life decays;

[0091] Obtaining cleaning condition information in the sample liquid tank 1;

[0092] Determine multiple feature data dimensions according to the cleaning condition information in the sample liquid tank 1;

[0093] Determine the liquid condition information related to the liquid batch life from the cleaning condition information in the sample liquid tank 1;

[0094] According to the working condition information of the liquid medicine, multiple characteristic data dimensions are determined.

[0095] From the multiple feature data dimensions, a target feature data dimension related to the life decay of the drug solution batch is determined.

[0096] Determine, according to the cleaning condition information in the sample liquid tank 1, the feature data corresponding to each feature data dimension in the multiple feature data dimensions;

[0097] The characteristic data corresponding to each characteristic data dimension is respectively subjected to correlation analysis on the attenuation of the batch life of the drug solution to obtain the target characteristic data dimension related to the attenuation of the batch life of the drug solution.

[0098] S12: Obtain target cleaning condition information in the medicine tank 1, and establish a data model for the attenuation of the batch life of the medicine in the medicine tank 1 according to the target cleaning condition information in the medicine tank 1 and the target characteristic data dimension;

[0099] Target cleaning condition information in the liquid medicine tank 1, and determining a target dimension weight for the target feature data dimension;

[0100] The target dimension weight is used to establish a data model for the attenuation of the batch life of the medicine solution in the medicine solution tank 1.

[0101] The target cleaning condition information may be data such as the volume and internal pressure of the liquid tank 1;

[0102] The target cleaning condition information used when establishing the data model for the attenuation of the batch life of the medicine solution in the medicine solution tank 1 may be the historical average data information of the medicine solution tank 1;

[0103] S13: using the data model to predict the batch life of the medicine in the medicine tank 1.

[0104] Example 4

[0105] See also Figure 2 , a low-cost, fast-activation liquid wet cleaning device, used to implement the low-cost, fast-activation liquid wet cleaning method.

[0106] Preferably, it includes a medicine liquid tank 1 and a medicine liquid sub-tank 3, the medicine liquid tank 1 and the medicine liquid sub-tank 3 are connected by a pipeline, and a medicine liquid sub-tank outlet valve 2 is provided in the pipeline connecting the medicine liquid tank 1 and the medicine liquid sub-tank 3, a medicine liquid tank fixed drain valve 7 is provided in the pipeline from the medicine liquid sub-tank 3 to the outside, a medicine liquid tank drain valve 9 is provided in the pipeline from the medicine liquid tank 1 to the outside, a heater 4 is provided between the medicine liquid tank 1 and the medicine liquid sub-tank 3, the output end of the heater 4 leads to the medicine liquid tank 1, the input end of the medicine liquid tank 1 is connected to the medicine liquid sub-tank 3, the medicine liquid tank fixed drain valve 7, and one end of a circulation pump 8, the other end of the circulation pump 8 is connected to the medicine liquid tank 1, and the other end of the medicine liquid tank fixed drain valve 7 leads to the outside.

[0107] The working principle and beneficial effects of the above scheme:

[0108] After the batch life of the liquid tank 1 is reached, the liquid is emptied. When preparing the liquid again, the liquid outlet valve 2 of the liquid auxiliary tank is opened, and the reserved medium-term liquid in the liquid auxiliary tank 3 is added. When the liquid reaches the working liquid level, the texturing begins.

[0109] The circulation pump 8 is used to circulate the liquid medicine in the liquid medicine tank 1 to ensure the uniformity of the liquid medicine in the liquid medicine tank 1.

[0110] After the liquid medicine reaches the batch life, the liquid medicine auxiliary tank drain valve 6, the liquid medicine tank fixed drain valve 7, and the liquid medicine tank drain valve 9 are opened to discharge the waste liquid in the device and wait for the next liquid replenishment;

[0111] The heater 4 is used to heat the circulating liquid medicine to increase the reaction rate of the liquid medicine;

[0112] The present invention solves the problem that in the early stage of the batch life of the liquid medicine tank 1, the liquid medicine has not been activated and the concentration of the reaction product is low, resulting in the early stage of the liquid medicine tank 1 often failing to play its 100% role, and ultimately leading to poor wet processing effect in the early stage, especially the functional tanks such as initial polishing, texturing, and alkali polishing are greatly affected by the mixing of the mid-term liquid medicine reserved in the liquid medicine sub-tank 3 with the new liquid medicine.

[0113] In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inside", "outside" and the like indicate positions or positional relationships based on the positions or positional relationships shown in the drawings, and are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as limiting the present invention; the terms "first", "second", and "third" are only used for descriptive purposes, and cannot be understood as indicating or implying relative importance. In addition, unless otherwise clearly specified and limited, the terms "installed", "connected", and "connected" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection, or it can be an indirect connection through an intermediate medium, or it can be a connection between the two elements. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood according to specific circumstances. Moreover, the terms "comprises," "comprising," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that includes a list of elements includes not only those elements but also other elements not expressly listed, or also includes elements inherent to such process, method, article, or apparatus.

[0114] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A low-cost, fast-activation liquid wet cleaning method, characterized in that: When the batch life of the liquid medicine in the liquid medicine tank (1) is reached, the liquid medicine is drained. When preparing the liquid again, the liquid outlet valve (2) of the liquid medicine auxiliary tank is opened, and the intermediate liquid medicine reserved in the liquid medicine auxiliary tank (3) is added. When the liquid medicine reaches the working liquid level, the texturing process starts. The working steps include: S1: Obtain the number of times the batch life of the medicine solution in the medicine solution tank (1) has passed; S2: when the batch life of the medicine solution in the medicine solution tank (1) reaches the middle stage, obtaining the position of the liquid level in the medicine solution auxiliary tank (3); S3: determining whether the liquid level in the liquid auxiliary tank (3) is above the empty liquid level; S4: If yes, open the liquid drain valve (6) of the liquid medicine auxiliary tank to drain the excess liquid medicine; If not, the liquid inlet valve (5) of the liquid medicine auxiliary tank is opened to replenish the liquid medicine into the liquid medicine auxiliary tank (3); S5: During the liquid replenishment, the position of the liquid level in the liquid auxiliary tank (3) is obtained in real time. When the liquid level reaches within the standard range, the liquid auxiliary tank and the liquid inlet valve (5) are closed to stop the liquid replenishment.

2. A low-cost, fast-activation liquid wet cleaning method according to claim 1, characterized in that: Included in S4: When the liquid inlet valve (5) of the liquid medicine auxiliary tank is opened, the liquid medicine tank fixed discharge valve (7) is closed synchronously, and the liquid medicine auxiliary tank (3) directly replenishes the liquid medicine of the liquid medicine tank (1) for process fixed discharge.

3. The wet cleaning method of a low-cost, fast-activation liquid according to claim 1, characterized in that: Included in S4: The liquid medicine auxiliary tank (3) is replenished in batches, with the replenishment volume of each batch being 1-10L, and the interval of replenishment is consistent with the process-determined interval of the liquid medicine tank (1).

4. The wet cleaning method of a low-cost, fast-activation liquid according to claim 1, characterized in that: The S1 comprises the following steps: S11: Obtaining target feature data dimensions associated with the attenuation of the life of the drug solution batch; S12: obtaining target cleaning condition information in the medicine liquid tank (1), and establishing a data model for the attenuation of the batch life of the medicine liquid in the medicine liquid tank (1) according to the target cleaning condition information in the medicine liquid tank (1) and the target characteristic data dimension; S13: using the data model, predicting the batch life of the medicine solution in the medicine solution tank (1).

5. A low-cost, fast-activation liquid wet cleaning method according to claim 4, characterized in that: The S11 comprises the following steps: S111: Acquiring cleaning condition information in the sample liquid tank (1); S112: determining a plurality of characteristic data dimensions according to the cleaning condition information in the sample liquid tank (1); S113: Determine a target feature data dimension related to the life decay of a batch of drug solution from the multiple feature data dimensions.

6. A low-cost, fast-activation liquid wet cleaning method according to claim 5, characterized in that: The S112 comprises the following steps: S1121: Determine the cleaning condition information of the sample liquid tank (1) related to the life of the liquid batch; S1122: Determine multiple characteristic data dimensions based on the liquid medicine working condition information.

7. The low-cost, fast-activation liquid wet cleaning method according to claim 5, characterized in that: The S113 comprises the following steps: S1131: Determine, based on the cleaning condition information in the sample liquid tank (1), the feature data corresponding to each feature data dimension in the plurality of feature data dimensions; S1132: performing correlation analysis on the life decay of the drug solution batch for the feature data corresponding to each feature data dimension respectively, and obtaining the target feature data dimension related to the life decay of the drug solution batch.

8. The low-cost, fast-activation liquid wet cleaning method according to claim 4, characterized in that: The S12 comprises the following steps: S121: Target cleaning condition information in the liquid medicine tank (1), determining a target dimension weight for the target feature data dimension; S122: Using the target dimension weight, a data model for the attenuation of the batch life of the medicine solution in the medicine solution tank (1) is established.

9. A low-cost, fast-activation liquid wet cleaning device, characterized in that: A wet cleaning method for realizing a low-cost rapid activation liquid as described in any one of claims 1 to 8; The invention comprises a medicine liquid tank (1) and a medicine liquid auxiliary tank (3), wherein the medicine liquid tank (1) and the medicine liquid auxiliary tank (3) are connected via a pipeline, and a medicine liquid auxiliary tank outlet valve (2) is arranged in the pipeline connecting the medicine liquid tank (1) and the medicine liquid auxiliary tank (3), a medicine liquid tank fixed discharge valve (7) is arranged in the pipeline connecting the medicine liquid auxiliary tank (3) to the outside, and a medicine liquid tank discharge valve (9) is arranged in the pipeline connecting the medicine liquid tank (1) to the outside, a heater (4) is arranged between the medicine liquid tank (1) and the medicine liquid auxiliary tank (3), and the output end of the heater (4) is connected to the medicine liquid tank (1), and the input end of the medicine liquid tank (1) is connected to the medicine liquid auxiliary tank (3), the medicine liquid tank fixed discharge valve (7), and one end of a circulation pump (8), the other end of the circulation pump (8) is connected to the medicine liquid tank (1), and the other end of the medicine liquid tank fixed discharge valve (7) is connected to the outside.