Wastewater recycling method and device of glass cleaning machine

Abstract

The invention relates to a waste water recycling method and device for a glass cleaning machine, and the method comprises the steps: carrying out the component analysis of glass waste water of the glass cleaning machine, obtaining the parameters of the glass waste water and the required reaction agent content, and obtaining the ideal reaction agent content value of the glass waste water; obtaining a current reaction agent content value of the recovery reaction tank, adjusting the current reaction agent content value, obtaining a chemical combination change relation between the adjustment reaction agent and the glass wastewater, and according to the chemical combination change relation, when the agent content in the recovery reaction tank and the impurity content of the glass wastewater reach dynamic balance, stopping the recovery of the glass wastewater. And filtering and purifying the glass wastewater in the recovery reaction tank to obtain chemical recovery liquid, mixing the chemical recovery liquid with the new reaction chemical in the recovery reaction tank, and cooperatively recovering the next round of glass wastewater to obtain glass wastewater circulation data of the glass cleaning machine. The waste water recycling device has the effect of improving the waste water recycling rate of the glass cleaning machine.

Description

Technical Field

[0001] The present application relates to the technical field of wastewater recycling, and in particular to a method and device for recycling wastewater of a glass washing machine. Background Art

[0002] At present, glass is widely used in all walks of life. Whether it is windows or electronic screens, glass is needed. In the glass production process, cleaning the glass before leaving the factory is an indispensable process in glass processing.

[0003] Existing glass washing machines often generate a large amount of cleaning wastewater in the process of cleaning various types of glass, especially when cleaning large-size glass. The current treatment of glass washing wastewater is often discharged after simple static treatment, which not only wastes a lot of water resources and increases unnecessary corporate cleaning costs, but also easily discharges substandard cleaning wastewater during the continuous cleaning process of the glass, causing environmental pollution. Therefore, it is necessary to further optimize the treatment method of glass washing wastewater of glass washing machines. Summary of the invention

[0004] In order to improve the wastewater recycling rate of a glass washing machine, the present application provides a wastewater recycling method and device for a glass washing machine.

[0005] In the first aspect, the above-mentioned invention objective of the present application is achieved through the following technical solutions: A method for recycling waste water of a glass washing machine, comprising: Analyze the components of the glass wastewater from the glass washing machine, obtain the glass wastewater parameters and analyze the required reaction reagent content of the glass wastewater to obtain the ideal reaction reagent content value of the glass wastewater; Obtaining the current reaction reagent content value of the recovery reaction tank, and adjusting the current reaction reagent content value according to the ideal reaction reagent content value, and obtaining the chemical change relationship between the adjusted reaction reagent and the glass wastewater; According to the chemical change relationship, when the reagent content in the recovery reaction tank and the impurity content in the glass wastewater reach a dynamic balance, the glass wastewater in the recovery reaction tank is filtered and purified to obtain a reagent recovery liquid; The reagent recovery liquid is mixed with the new reaction reagent in the recovery reaction tank, and the next round of glass waste water is synergistically recovered and treated to obtain the glass waste water circulation data of the glass washing machine.

[0006] In a preferred example, the present application can be further configured as follows: the component analysis of the glass wastewater from the glass washing machine is performed to obtain the glass wastewater parameters and analyze the required reaction agent content of the glass wastewater to obtain the ideal reaction agent content value of the glass wastewater, specifically including: The glass wastewater with different wastewater component contents is subjected to chemical reaction with the corresponding reaction agent content, and the ratio between the glass wastewater component and the reaction agent content is analyzed according to the chemical reaction result to obtain the wastewater chemical reaction relationship; According to the wastewater chemical reaction relationship and the current glass wastewater parameters, the required reaction agent content of the current glass wastewater is analyzed to obtain the ideal reaction agent content value of the current glass wastewater.

[0007] By adopting the above technical scheme, the composition of glass wastewater after cleaning the glass by a glass washing machine is analyzed, and the content of reaction reagents required for the wastewater is analyzed, so as to improve the rationality of the configuration of the reaction reagents, and in combination with the current reaction reagent content value of the current recovery reaction tank, the actual content of the reaction reagent in the recovery reaction tank is adaptively adjusted, and the chemical change relationship between the reaction reagent and the glass wastewater is obtained during the reaction process, and the replacement of organic matter in the glass wastewater is monitored in real time. When the reagent content and the impurity content of the wastewater reach the preset standard, the glass wastewater is filtered and purified, so as to recycle the reusable reagent recovery liquid, and the next round of glass wastewater is synergistically recovered by mixing the reagent recovery liquid with the new reaction reagent in the reaction tank, forming a closed-loop glass wastewater recycling process, thereby improving the wastewater recycling rate of the glass washing machine.

[0008] In a preferred example, the present application can be further configured as follows: the reagent recovery liquid is mixed with the new reaction reagent in the recovery reaction tank, and the next round of glass waste water is cooperatively recovered and processed to obtain glass waste water circulation data of the glass washing machine, specifically including: The reagent recovery liquid is mixed with the new reaction reagent in the recovery reaction tank to obtain a mixed reagent content value of the mixed reaction liquid; Obtaining a new ideal reaction reagent content of the next round of glass wastewater, and adjusting the mixed reagent content according to the new ideal reaction reagent content to obtain a new round of new reagent adjustment data; The reaction reagent corresponding to the new reagent adjustment data is subjected to a new chemical combination reaction with the next round of glass waste water to obtain the glass waste water circulation data of the glass cleaning machine.

[0009] By adopting the above technical scheme, the reagent recovery liquid is mixed with the new reaction reagent in the recovery reaction tank, and the mixed reagent content value is obtained. In combination with the new ideal reaction reagent content of the next round of glass waste water, the content of the mixed reagent for recycling is adjusted to make the new round of new reagent adjustment conditions more compatible with the next round of glass waste water, and the reaction reagent corresponding to the new reagent adjustment data is subjected to a new chemical reaction with the next round of glass waste water, thereby realizing the recycling of glass waste water from the glass washing machine and improving the adaptability between each round of glass waste water and the recycled mixed reagent.

[0010] In a preferred example, the present application can be further configured as follows: according to the chemical change relationship, when the reagent content in the recovery reaction pool and the impurity content in the glass waste water reach a dynamic balance, the glass waste water in the recovery reaction pool is filtered and purified to obtain a reagent recovery liquid, specifically including: According to the chemical change relationship, the precipitation state of wastewater impurities in the reaction tank is obtained, and according to the precipitation state of wastewater impurities, it is judged whether the reagent content in the recovery reaction tank and the impurity content of the glass wastewater have reached a dynamic balance; If yes, the glass wastewater in the recovery reaction tank is filtered, the precipitated flocculent substances are filtered, and the supernatant liquid is retained to obtain the reagent recovery liquid; If not, the reaction liquid in the recovery reaction tank is treated with a reaction reagent supplement according to the ratio of the reagent content to the impurity content of the glass wastewater.

[0011] In a preferred example, the present application can be further configured as follows: according to the chemical change relationship, when the reagent content in the recovery reaction pool and the impurity content in the glass waste water reach a dynamic balance, the glass waste water in the recovery reaction pool is filtered and purified to obtain a reagent recovery liquid, and further includes: The glass wastewater in the recovery reaction tank is filtered and purified by an RO membrane to obtain a pharmaceutical recovery liquid.

[0012] By adopting the above technical scheme, the precipitation state of wastewater impurities in the reaction tank is obtained according to the chemical change relationship, and it is judged whether the reagent content in the recovery reaction tank and the impurity content of the glass wastewater have reached a dynamic balance, which is helpful to improve the accuracy of controlling the precipitation of glass wastewater substances. When the preset precipitation standard is reached, the glass wastewater is filtered and the reagent recovery liquid is recycled. If the preset precipitation standard is not reached, the reaction reagent in the recovery reaction tank is supplemented until the recovery and filtration standard of the glass wastewater is reached, thereby improving the accuracy of glass wastewater discharge control.

[0013] In the second aspect, the above invention objective of the present application is achieved through the following technical solutions: A wastewater recycling device for a glass washing machine, the device is applied to the wastewater recycling method for the glass washing machine, the device comprises: The data analysis module is used to analyze the components of the glass wastewater from the glass washing machine, obtain the parameters of the glass wastewater, analyze the content of the reaction reagent required for the glass wastewater, and obtain the ideal content value of the reaction reagent for the glass wastewater; The reagent adjustment module is used to obtain the current reagent content value of the recovery reaction tank, and adjust the current reagent content value according to the ideal reagent content value, and obtain the chemical change relationship between the adjusted reagent and the glass wastewater; A filtering and processing module is used to filter and purify the glass waste water in the recovery reaction tank according to the chemical change relationship to obtain a reagent recovery liquid when the reagent content in the recovery reaction tank and the impurity content in the glass waste water reach a dynamic balance; The recycling processing module is used to mix the reagent recovery liquid with the new reaction reagent in the recovery reaction tank, perform collaborative recycling processing on the next round of glass waste water, and obtain the glass waste water circulation data of the glass washing machine.

[0014] By adopting the above technical scheme, the composition of glass wastewater after cleaning the glass by a glass washing machine is analyzed, and the content of reaction reagents required for the wastewater is analyzed, so as to improve the rationality of the configuration of the reaction reagents, and in combination with the current reaction reagent content value of the current recovery reaction tank, the actual content of the reaction reagent in the recovery reaction tank is adaptively adjusted, and the chemical change relationship between the reaction reagent and the glass wastewater is obtained during the reaction process, and the replacement of organic matter in the glass wastewater is monitored in real time. When the reagent content and the impurity content of the wastewater reach the preset standard, the glass wastewater is filtered and purified, so as to recycle the reusable reagent recovery liquid, and the next round of glass wastewater is synergistically recovered by mixing the reagent recovery liquid with the new reaction reagent in the reaction tank, forming a closed-loop glass wastewater recycling process, thereby improving the wastewater recycling rate of the glass washing machine.

[0015] On the third aspect, the above-mentioned purpose of the present application is achieved through the following technical solutions: A computer device comprises a memory, a processor and a computer program stored in the memory and executable on the processor. When the processor executes the computer program, the steps of the wastewater recycling method of the glass washing machine are implemented.

[0016] Fourthly, the above-mentioned purpose of the present application is achieved through the following technical solutions: A computer-readable storage medium stores a computer program, and when the computer program is executed by a processor, the steps of the wastewater recycling method of the glass washing machine are implemented.

[0017] In summary, the present application includes at least one of the following beneficial technical effects: 1. Analyze the composition of wastewater after washing glass in a glass washing machine, analyze the content of the required reagents in the wastewater, so as to improve the rationality of the configuration of the reagents, and adjust the actual content of the reagents in the recovery reaction tank adaptively in combination with the current reagent content value of the current recovery reaction tank, and obtain the chemical change relationship between the reagents and the glass wastewater during the reaction process, and monitor the replacement of organic matter in the glass wastewater in real time. When the reagent content and the impurity content of the wastewater reach the preset standard, the glass wastewater is filtered and purified, so as to recycle the reusable reagent recovery liquid, and the next round of glass wastewater is synergistically recovered by mixing the reagent recovery liquid with the new reagent in the reaction tank, forming a closed-loop glass wastewater recycling process, thereby improving the wastewater recycling rate of the glass washing machine; 2. Mix the reagent recovery liquid with the new reaction reagent in the recovery reaction tank, obtain the content value of the mixed reagent, and adjust the content of the recycled mixed reagent in combination with the new ideal reaction reagent content of the next round of glass wastewater, so that the new round of new reagent adjustment is more compatible with the next round of glass wastewater, and the reaction reagent corresponding to the new reagent adjustment data is subjected to a new chemical reaction with the next round of glass wastewater, thereby realizing the recycling of glass wastewater from the glass washing machine and improving the compatibility between each round of glass wastewater and the recycled mixed reagent; 3. Obtain the precipitation state of wastewater impurities in the reaction tank according to the chemical change relationship, and judge whether the reagent content in the recovery reaction tank and the impurity content of the glass wastewater have reached a dynamic balance, which is helpful to improve the accuracy of controlling the precipitation of glass wastewater substances. When the preset precipitation standard is reached, the glass wastewater is filtered and the reagent recovery liquid is recycled. If the preset precipitation standard is not reached, the reaction reagent in the recovery reaction tank is supplemented until the recovery and filtration standard of the glass wastewater is reached, thereby improving the accuracy of glass wastewater discharge control. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] Figure 1 This is a flow chart of a method for recycling waste water of a glass washing machine according to this embodiment.

[0019] Figure 2 This is a flow chart for implementing step S10 of a method for recycling waste water of a glass washing machine in this embodiment.

[0020] Figure 3 This is a flow chart for implementing step S30 of a method for recycling waste water of a glass washing machine in this embodiment.

[0021] Figure 4 This is a flow chart for implementing step S40 of a method for recycling waste water of a glass washing machine in this embodiment.

[0022] Figure 5It is a structural block diagram of a wastewater recycling device of a glass washing machine in this embodiment.

[0023] Figure 6 It is a schematic diagram of the internal structure of the computer device used to implement the wastewater recycling method in this embodiment. DETAILED DESCRIPTION

[0024] The present application is further described in detail below in conjunction with the accompanying drawings.

[0025] In one embodiment, if Figure 1 As shown, the present application discloses a method for recycling wastewater from a glass washing machine, which specifically includes the following steps: S10: Analyze the components of the glass wastewater from the glass washing machine, obtain the glass wastewater parameters and analyze the required reaction reagent content of the glass wastewater, and obtain the ideal reaction reagent content value of the glass wastewater.

[0026] Specifically, Figure 2 As shown, step S10 includes: S101: performing a chemical reaction on glass wastewater with different wastewater component contents and corresponding reaction agent contents, analyzing the ratio between the glass wastewater components and the reaction agent contents according to the chemical reaction results, and obtaining a wastewater chemical reaction relationship.

[0027] Specifically, glass wastewater with different wastewater component contents is collected and chemically reacted with different content of reaction reagents, and the reaction ratio between the glass wastewater components and the reaction reagent content is analyzed according to the chemical reaction results, so as to obtain the wastewater chemical reaction relationship of the glass washing machine.

[0028] S102: Analyze the reaction reagent content required for the current glass wastewater according to the wastewater chemical reaction relationship and the current glass wastewater parameters to obtain an ideal reaction reagent content value for the current glass wastewater.

[0029] Specifically, according to the wastewater chemical reaction relationship and the current glass wastewater parameters, the reaction agent content that matches the current glass wastewater parameters is sought in the wastewater chemical reaction relationship to obtain the reaction agent content required for the current glass wastewater, and the reaction agent content value of the current glass wastewater that meets the wastewater chemical reaction relationship is used as the ideal reaction agent content value.

[0030] S20: obtaining the current reaction reagent content value of the recovery reaction tank, and adjusting the current reaction reagent content value according to the ideal reaction reagent content value, and obtaining the chemical change relationship between the adjusted reaction reagent and the glass wastewater.

[0031] Specifically, the current reactant content value in the recovery reaction pool is obtained, and the reactant content value of the recovery reaction pool is adjusted according to the ideal reactant content value, the adjusted reactant is mixed with glass waste water for reaction, and the chemical change relationship between the adjusted reactant and the glass waste water is obtained during the mixing process, which in this embodiment refers to the relationship between the change in the reactant content and the change in the impurity content in the glass waste water.

[0032] S30: According to the chemical change relationship, when the reagent content in the recovery reaction tank and the impurity content in the glass waste water reach a dynamic balance, the glass waste water in the recovery reaction tank is filtered and purified to obtain a reagent recovery liquid.

[0033] Specifically, Figure 3 As shown, step S30 includes: S301: According to the chemical change relationship, the precipitation state of wastewater impurities in the reaction tank is obtained, and according to the precipitation state of wastewater impurities, it is determined whether the reagent content in the recovery reaction tank and the impurity content in the glass wastewater have reached a dynamic balance.

[0034] Specifically, according to the chemical change relationship, the precipitation state of wastewater in the reaction tank is obtained, and according to the precipitation state of wastewater impurities, it is judged whether the reagent content in the recovery reaction tank and the impurities in the glass wastewater have reached a dynamic balance. For example, when no flocculent matter continues to precipitate in the reaction tank or the mixed liquid in the current reaction tank is collected to analyze the impurity content of the glass wastewater, when the impurity content of the glass wastewater is lower than the preset standard value, it means that dynamic balance has been reached.

[0035] S302: If yes, the glass wastewater in the recovery reaction tank is filtered, the precipitated flocculent substances are filtered, and the supernatant liquid is retained to obtain the reagent recovery liquid.

[0036] Specifically, when the reagent content in the reaction tank and the impurity content of the glass wastewater reach a dynamic balance and no flocculent matter is precipitated, the glass wastewater in the recovery reaction tank is filtered, the precipitated flocculent matter is filtered, the supernatant liquid is retained to obtain the reagent recovery liquid, and the supernatant liquid is circulated to the new reaction tank to wait for the next round of glass wastewater recovery.

[0037] S303: If not, the reaction liquid in the recovery reaction tank is supplemented with reaction reagents according to the ratio of the reagent content to the impurity content of the glass wastewater.

[0038] Specifically, when the reagent content in the reaction tank and the impurity content in the glass waste water have not reached a dynamic balance, that is, the impurity content in the glass waste water of the mixed liquid in the reaction tank is higher than the discharge standard, the reaction liquid in the recovery reaction tank is supplemented with reaction reagent according to the ratio of the reagent content to the impurity content in the glass waste water until the impurity content in the glass waste water reaches the preset discharge standard.

[0039] In this embodiment, the glass wastewater in the recovery reaction tank is filtered and purified by an RO membrane to obtain a reagent recovery liquid.

[0040] S40: Mix the reagent recovery liquid with the new reaction reagent in the recovery reaction tank, perform coordinated recovery treatment on the next round of glass waste water, and obtain glass waste water circulation data of the glass washing machine.

[0041] Specifically, Figure 4 As shown, step S40 includes: S401: Performing a liquid mixing process on the reagent recovery liquid and the new reaction reagent in the recovery reaction tank to obtain a mixed reagent content value of the mixed reaction liquid.

[0042] Specifically, the reagent recovery liquid is mixed with the new reaction reagent in the recovery reaction tank, and the mixed reagent content value of the mixed reaction liquid is obtained.

[0043] S402: Obtain the new ideal reaction reagent content of the next round of glass wastewater, and adjust the mixed reagent content according to the new ideal reaction reagent content to obtain a new round of new reagent adjustment data.

[0044] Specifically, the new ideal reaction reagent content of the next round of glass waste water is obtained, that is, the new ideal reaction reagent content required for the next round of glass waste water is obtained according to the next glass cleaning waste water of the glass cleaning machine, and the mixed reagent content is adjusted according to the new ideal reaction reagent content, including adding water to reduce the reagent concentration, or adding reagents to increase the reagent concentration, etc., so as to obtain a new round of new reagent adjustment data.

[0045] S403: Perform a new chemical reaction with the next round of glass wastewater using the reaction reagent corresponding to the new reagent adjustment data to obtain glass wastewater circulation data of the glass cleaning machine.

[0046] Specifically, the reaction reagent corresponding to the new reagent adjustment data is subjected to a new chemical reaction with the next round of glass wastewater, and the chemical product is filtered and purified, thereby forming a closed loop of recycling of glass wastewater and obtaining glass wastewater circulation data of the glass washing machine.

[0047] It should be understood that the size of the serial numbers of the steps in the above embodiments does not mean the order of execution. The execution order of each process should be determined by its function and internal logic, and should not constitute any limitation on the implementation process of the embodiments of the present application.

[0048] In one embodiment, a wastewater recycling device for a glass washing machine is provided, and the wastewater recycling device for the glass washing machine corresponds one-to-one to the wastewater recycling method for the glass washing machine in the above embodiment. Figure 5As shown, the wastewater recycling device of the glass washing machine includes a data analysis module, a reagent adjustment module, a filtration processing module and a recycling processing module. The detailed description of each functional module is as follows: The data analysis module is used to analyze the components of the glass wastewater from the glass washing machine, obtain the glass wastewater parameters and analyze the reaction agent content required for the glass wastewater, and obtain the ideal reaction agent content value of the glass wastewater.

[0049] The reagent adjustment module is used to obtain the current reagent content value of the recovery reaction tank, and adjust the current reagent content value according to the ideal reagent content value, and obtain the chemical change relationship between the adjusted reagent and the glass wastewater.

[0050] The filtering and processing module is used to filter and purify the glass waste water in the recovery reaction tank according to the chemical change relationship to obtain the reagent recovery liquid when the reagent content in the recovery reaction tank and the impurity content of the glass waste water reach a dynamic balance.

[0051] The recycling and processing module is used to mix the reagent recovery liquid with the new reaction reagent in the recovery reaction tank, and to carry out coordinated recycling and processing of the next round of glass waste water to obtain the glass waste water circulation data of the glass washing machine.

[0052] Preferably, the recycling processing module specifically includes: The liquid mixing submodule is used to perform liquid mixing processing on the reagent recovery liquid and the new reaction reagent in the recovery reaction tank to obtain the mixed reagent content value of the mixed reaction liquid.

[0053] The reagent adjustment submodule is used to obtain the new ideal reaction reagent content of the next round of glass wastewater, and adjust the mixed reagent content according to the new ideal reaction reagent content to obtain a new round of new reagent adjustment data.

[0054] The new chemical combination submodule is used to carry out a new chemical combination reaction treatment on the reaction reagent corresponding to the new reagent adjustment data and the next round of glass waste water to obtain the glass waste water circulation data of the glass washing machine.

[0055] Preferably, the filtering processing module specifically includes: The data judgment submodule is used to obtain the precipitation state of wastewater impurities in the reaction tank according to the chemical change relationship, and judge whether the reagent content in the recovery reaction tank and the impurity content in the glass wastewater have reached a dynamic balance according to the precipitation state of wastewater impurities.

[0056] The filtering submodule is used to filter the glass wastewater in the recovery reaction tank, filter the precipitated flocculent substances, and retain the supernatant liquid to obtain the reagent recovery liquid.

[0057] The reagent replenishment submodule is used to, if not, carry out reagent replenishment treatment on the reaction liquid in the recovery reaction tank according to the ratio of the reagent content to the impurity content of the glass waste water.

[0058] Preferably, the filtration treatment module further comprises: filtering and purifying the glass wastewater in the recovery reaction tank through an RO membrane to obtain a reagent recovery liquid.

[0059] Preferably, the data analysis module specifically includes: The ratio analysis submodule is used to carry out a chemical reaction between glass wastewater with different wastewater component contents and the corresponding reaction agent content, analyze the ratio between the glass wastewater components and the reaction agent content according to the chemical reaction results, and obtain the wastewater chemical reaction relationship.

[0060] The reagent analysis submodule is used to analyze the reaction reagent content required for the current glass wastewater according to the wastewater chemical reaction relationship and the current glass wastewater parameters, and obtain the ideal reaction reagent content value of the current glass wastewater.

[0061] The specific definition of the wastewater recycling device of the glass washing machine can be found in the definition of the wastewater recycling method of the glass washing machine above, which will not be repeated here. Each module in the above-mentioned wastewater recycling device of the glass washing machine can be implemented in whole or in part by software, hardware and a combination thereof. The above-mentioned modules can be embedded in or independent of the processor in the computer device in the form of hardware, or can be stored in the memory of the computer device in the form of software, so that the processor can call and execute the operations corresponding to the above modules.

[0062] In one embodiment, a computer device is provided. The computer device may be a server, and its internal structure diagram may be as follows: Figure 6 As shown. The computer device includes a processor, a memory, a network interface and a database connected through a system bus. Among them, the processor of the computer device is used to provide computing and control capabilities. The memory of the computer device includes a non-volatile storage medium and an internal memory. The non-volatile storage medium stores an operating system, a computer program and a database. The internal memory provides an environment for the operation of the operating system and the computer program in the non-volatile storage medium. The database of the computer device is used to store glass wastewater recycling data of a glass washing machine. The network interface of the computer device is used to communicate with an external terminal through a network connection. When the computer program is executed by the processor, a wastewater recycling method of a glass washing machine is implemented.

[0063] In one embodiment, a computer-readable storage medium is provided, on which a computer program is stored. When the computer program is executed by a processor, the steps of a method for recycling waste water of a glass washing machine are implemented.

[0064] Those of ordinary skill in the art can understand that all or part of the processes in the above-mentioned embodiment methods can be completed by instructing the relevant hardware through a computer program, and the computer program can be stored in a non-volatile computer-readable storage medium. When the computer program is executed, it can include the processes of the embodiments of the above-mentioned methods. Among them, any reference to memory, storage, database or other media used in the embodiments provided in this application may include non-volatile and / or volatile memory. Non-volatile memory may include read-only memory (ROM), programmable ROM (PROM), electrically programmable ROM (EPROM), electrically erasable programmable ROM (EEPROM) or flash memory. Volatile memory may include random access memory (RAM) or external cache memory. By way of illustration and not limitation, RAM is available in many forms, such as static RAM (SRAM), dynamic RAM (DRAM), synchronous DRAM (SDRAM), double data rate SDRAM (DDRSDRAM), enhanced SDRAM (ESDRAM), synchronous link (Synchlink) DRAM (SLDRAM), memory bus (Rambus) direct RAM (RDRAM), direct memory bus dynamic RAM (DRDRAM), and memory bus dynamic RAM (RDRAM), etc.

[0065] Those skilled in the art can clearly understand that for the convenience and simplicity of description, only the division of the above-mentioned functional units and modules is used as an example. In actual applications, the above-mentioned functions can be distributed and completed by different functional units and modules as needed, that is, the internal structure of the device can be divided into different functional units or modules to complete all or part of the functions described above.

[0066] The embodiments described above are only used to illustrate the technical solutions of the present application, rather than to limit them. Although the present application has been described in detail with reference to the aforementioned embodiments, a person skilled in the art should understand that the technical solutions described in the aforementioned embodiments may still be modified, or some of the technical features may be replaced by equivalents. Such modifications or replacements do not deviate the essence of the corresponding technical solutions from the spirit and scope of the technical solutions of the embodiments of the present application, and should all be included in the protection scope of the present application.

Claims

1. A method for recycling waste water from a glass washing machine, characterized in that: include: Analyze the components of the glass wastewater from the glass washing machine, obtain the glass wastewater parameters and analyze the required reaction reagent content of the glass wastewater to obtain the ideal reaction reagent content value of the glass wastewater; Obtaining the current reaction reagent content value of the recovery reaction tank, and adjusting the current reaction reagent content value according to the ideal reaction reagent content value, and obtaining the chemical change relationship between the adjusted reaction reagent and the glass wastewater; According to the chemical change relationship, when the reagent content in the recovery reaction tank and the impurity content in the glass wastewater reach a dynamic balance, the glass wastewater in the recovery reaction tank is filtered and purified to obtain a reagent recovery liquid; The reagent recovery liquid is mixed with the new reaction reagent in the recovery reaction tank, and the next round of glass waste water is synergistically recovered and treated to obtain the glass waste water circulation data of the glass washing machine.

2. The method for recycling waste water of a glass washing machine according to claim 1, characterized in that: The liquid of the reagent recovery is mixed with the new reaction reagent in the recovery reaction tank, and the next round of glass wastewater is processed in a coordinated manner to obtain the glass wastewater circulation data of the glass washing machine, specifically including: The reagent recovery liquid is mixed with the new reaction reagent in the recovery reaction tank to obtain a mixed reagent content value of the mixed reaction liquid; Obtaining a new ideal reaction reagent content of the next round of glass wastewater, and adjusting the mixed reagent content according to the new ideal reaction reagent content to obtain a new round of new reagent adjustment data; The reaction reagent corresponding to the new reagent adjustment data is subjected to a new chemical combination reaction with the next round of glass waste water to obtain the glass waste water circulation data of the glass cleaning machine.

3. The method for recycling waste water of a glass washing machine according to claim 1, characterized in that: According to the chemical change relationship, when the reagent content in the recovery reaction pool and the impurity content in the glass wastewater reach a dynamic balance, the glass wastewater in the recovery reaction pool is filtered and purified to obtain a reagent recovery liquid, which specifically includes: According to the chemical change relationship, the precipitation state of wastewater impurities in the reaction tank is obtained, and according to the precipitation state of wastewater impurities, it is judged whether the reagent content in the recovery reaction tank and the impurity content in the glass wastewater have reached a dynamic balance; If yes, the glass wastewater in the recovery reaction tank is filtered, the precipitated flocculent substances are filtered, and the supernatant liquid is retained to obtain the reagent recovery liquid; If not, the reaction liquid in the recovery reaction tank is supplemented with reaction reagents according to the ratio of the reagent content to the impurity content of the glass wastewater.

4. The method for recycling waste water of a glass washing machine according to claim 3, characterized in that: According to the chemical change relationship, when the reagent content in the recovery reaction pool and the impurity content in the glass waste water reach a dynamic balance, the glass waste water in the recovery reaction pool is filtered and purified to obtain a reagent recovery liquid, and the method further includes: The glass wastewater in the recovery reaction tank is filtered and purified by an RO membrane to obtain a pharmaceutical recovery liquid.

5. The method for recycling waste water of a glass washing machine according to claim 1, characterized in that: The component analysis of the glass wastewater from the glass washing machine is performed to obtain the glass wastewater parameters and analyze the required reaction agent content of the glass wastewater to obtain the ideal reaction agent content value of the glass wastewater, specifically including: The glass wastewater with different wastewater component contents is subjected to chemical reaction with the corresponding reaction agent content, and the ratio between the glass wastewater component and the reaction agent content is analyzed according to the chemical reaction result to obtain the wastewater chemical reaction relationship; According to the wastewater chemical reaction relationship and the current glass wastewater parameters, the required reaction agent content of the current glass wastewater is analyzed to obtain the ideal reaction agent content value of the current glass wastewater.

6. A wastewater recycling device for a glass washing machine, characterized in that: The device is applied to the wastewater recycling method of the glass washing machine according to any one of claims 1 to 5, and the device comprises: The data analysis module is used to analyze the components of the glass wastewater from the glass washing machine, obtain the parameters of the glass wastewater, analyze the content of the reaction reagent required for the glass wastewater, and obtain the ideal content value of the reaction reagent for the glass wastewater; The reagent adjustment module is used to obtain the current reagent content value of the recovery reaction tank, and adjust the current reagent content value according to the ideal reagent content value, and obtain the chemical change relationship between the adjusted reagent and the glass wastewater; A filtering and processing module is used to filter and purify the glass waste water in the recovery reaction tank according to the chemical change relationship to obtain a reagent recovery liquid when the reagent content in the recovery reaction tank and the impurity content in the glass waste water reach a dynamic balance; The recycling processing module is used to mix the reagent recovery liquid with the new reaction reagent in the recovery reaction tank, perform collaborative recycling processing on the next round of glass waste water, and obtain the glass waste water circulation data of the glass washing machine.

7. A computer device comprising a memory, a processor, and a computer program stored in the memory and executable on the processor, characterized in that: When the processor executes the computer program, the steps of the wastewater recycling method of the glass washing machine as claimed in any one of claims 1 to 5 are implemented.

8. A computer-readable storage medium storing a computer program, characterized in that: When the computer program is executed by a processor, the steps of the method for recycling waste water of a glass washing machine as claimed in any one of claims 1 to 5 are implemented.

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