Condensate box for optimization treatment of fluid and condensate water and fluid control method

Abstract

The invention provides a condensate box for fluid and condensate optimization treatment and a fluid control method, and the condensate box comprises a first air inlet parameter obtaining subsystem which is used for obtaining a first air inlet parameter of a steam pipe; the second air inlet parameter acquisition subsystem is used for acquiring a second air inlet parameter of the exhaust pipe; the target air inlet parameter control subsystem is used for controlling a target air inlet parameter of an air inlet in the side plate of the steaming oven according to the first air inlet parameter and the second air inlet parameter; and the condensate water treatment subsystem is used for judging whether a condensate water overflow risk exists or not, and if yes, waste water is automatically discharged. According to the condensate water box for fluid and condensate water optimization treatment and the fluid control method, the target air inlet parameter of the air inlet in the side plate of the steaming oven is controlled in real time according to the fluid dynamic simulation results of the first air inlet parameter and the second air inlet parameter, and the real-time performance of fluid control is higher and more accurate; when the condensate water overflow risk exists, waste water is discharged in time, and equipment work is safer.

Description

Technical Field

[0001] The present invention relates to the field of fluid control technology, and in particular to a condensation box and a fluid control method for optimizing the treatment of fluid and condensed water. Background Art

[0002] Integrated kitchen appliances refer to kitchen equipment that integrates the functions of common kitchen appliances such as range hoods, stoves, steamers, and ovens through an integrated design to make the functions of each module more coordinated, making it more humane in daily use.

[0003] The invention patent with application number: CN201910362195.7 discloses an integrated stove with a cooking device, including a cooking device with a cooking cavity and a stove, the stove includes a stove shell, the cooking cavity is provided with a first air outlet, and the stove shell is provided with a first air inlet and a first exhaust port which are communicated with the interior of the stove shell, the first air inlet is fluidly connected with the first air outlet, and the first exhaust port is provided at least one of the front side, left side, right side or rear side of the stove shell. The present invention can improve the smoke exhaust efficiency, and can dissipate heat for electronic components by providing a heat dissipation channel in the stove shell, and can use the steam discharged from the first exhaust port to soften the grease condensed on the panel, thereby facilitating the cleaning of the panel. At the same time, the smoke discharged from the cooking cavity can be cooled to avoid scalding users by high-temperature gas, and the heat generated when the integrated stove is working can be utilized to avoid energy waste.

[0004] Although the above-mentioned prior art has a condensation box in the stove shell, the third air inlet of the condensation box is fluidly connected with the first air inlet of the above-mentioned stove shell, and the third air outlet of the condensation box is fluidly connected with the exhaust port of the above-mentioned stove shell, but no analysis of the fluid behavior is performed (for example: when the air intake displacement of the first air inlet is too large, the air outlet of the first air outlet is not smooth), and the condensed waste water is not treated, there is a risk of waste water overflow, posing a safety hazard.

[0005] In view of this, there is an urgent need for a condensation box and a fluid control method for optimizing the treatment of fluid and condensed water, so as to at least solve the above-mentioned deficiencies. Summary of the invention

[0006] One of the purposes of the present invention is to provide a condensate box and a fluid control method for optimizing the treatment of fluid and condensed water, obtain a first air intake parameter of a steam pipe connected to the condensate box and a second air intake parameter of an exhaust pipe connected to the condensate box, and control the target air intake parameter of an air inlet on a side panel of a steam oven in real time according to the first air intake parameter and the second air intake parameter, thereby improving the real-time and accuracy of fluid control; judge the overflow risk of condensed water, and if there is an overflow risk, discharge the waste water in time, so that the equipment operates more safely.

[0007] An embodiment of the present invention provides a condensation box for optimizing the treatment of fluid and condensed water, comprising:

[0008] A first air intake parameter acquisition subsystem, used to acquire a first air intake parameter of a steam pipe connected to the condensate box;

[0009] A second air intake parameter acquisition subsystem, used to acquire a second air intake parameter of the exhaust pipe connected to the condensation box;

[0010] A target air intake parameter control subsystem, used to control the target air intake parameter of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter;

[0011] The condensate water treatment subsystem is used to obtain the water storage signal of the condensate box in real time, analyze the water storage signal, and determine whether there is a risk of condensate overflow. If so, the waste water in the condensate box is automatically discharged.

[0012] Preferably, the target air intake parameter control subsystem controls the target air intake parameter of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter, and performs the following operations:

[0013] Obtain fluid space structure information of the stove steam oven;

[0014] Based on the fluid spatial structure information, standard fluid characteristics of the fluid spatial structure are evaluated;

[0015] Constructing a fluid dynamics model according to the first air intake parameter, the second air intake parameter and the fluid space structure information;

[0016] Get real-time fluid characteristics in fluid dynamics models;

[0017] Calculating a first characteristic difference between the real-time fluid characteristic and the standard fluid characteristic;

[0018] According to the first characteristic difference, the air intake parameters of the air intake port on the side panel of the steam oven are controlled.

[0019] Preferably, the target air intake parameter control subsystem controls the target air intake parameter of the air intake port on the side panel of the steam oven according to the first characteristic difference, and performs the following operations:

[0020] Get the first current air intake parameter of the air intake port on the side panel of the steam oven;

[0021] Randomly determine a numerical adjustment direction of the first current air intake parameter to adjust the numerical value of the first current air intake parameter, and obtain a second current air intake parameter;

[0022] acquiring a simulated fluid characteristic according to a second current intake parameter;

[0023] Calculating a second characteristic difference between the simulated fluid characteristic and the standard fluid characteristic;

[0024] When the first characteristic difference is greater than or equal to the second characteristic difference, the randomly determined numerical adjustment direction is used as the target adjustment direction;

[0025] When the first characteristic difference is smaller than the second characteristic difference, the opposite direction of the randomly determined numerical value adjustment direction is used as the target adjustment direction;

[0026] The first current air intake parameter is adjusted according to the target adjustment direction to obtain the target air intake parameter.

[0027] Preferably, the target intake parameter control subsystem adjusts the first current intake parameter according to the target adjustment direction to obtain the target intake parameter and performs the following operations:

[0028] acquiring a third current air intake parameter in real time based on the adjusted first current air intake parameter;

[0029] acquiring, according to a third current intake parameter, an adjustment fluid characteristic;

[0030] Obtaining a first change amount per unit time of a third current intake parameter and a second change amount per unit time of a third characteristic difference of the adjusted fluid characteristic;

[0031] The first change amount increment is determined according to the change in the quotient of the first change amount and the second variable.

[0032] Preferably, the condensate water processing subsystem analyzes the water storage signal, determines whether there is a risk of condensate water overflow, and performs the following operations:

[0033] Obtaining water volume prediction basis information of the condensation box; the water volume prediction basis information includes: user cooking habit information and scheduled cooking information;

[0034] According to the water volume prediction basis information and the current time, the condensate volume of the stove steam oven in the next operation is predicted;

[0035] Analyze the water storage signal to obtain the remaining water capacity of the condensate box;

[0036] If the amount of condensed water is greater than the remaining water capacity, it is determined that there is a risk of condensed water overflow.

[0037] An embodiment of the present invention provides a condensation box fluid control method for optimizing the treatment of fluid and condensed water, comprising:

[0038] Obtaining a first air intake parameter of a steam pipe connected to the condensate box;

[0039] Obtain the second air intake parameter of the exhaust pipe connected to the condensation box;

[0040] Controlling target air intake parameters of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter;

[0041] The water storage signal of the condensate box is obtained in real time, and the water storage signal is analyzed to determine whether there is a risk of condensate overflow. If so, the waste water in the condensate box is automatically discharged.

[0042] Preferably, controlling the target air intake parameter of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter includes:

[0043] Obtain fluid space structure information of the stove steam oven;

[0044] Based on the fluid spatial structure information, standard fluid characteristics of the fluid spatial structure are evaluated;

[0045] Constructing a fluid dynamics model according to the first air intake parameter, the second air intake parameter and the fluid space structure information;

[0046] Get real-time fluid characteristics in fluid dynamics models;

[0047] Calculating a first characteristic difference between the real-time fluid characteristic and the standard fluid characteristic;

[0048] According to the first characteristic difference, the air intake parameters of the air intake port on the side panel of the steam oven are controlled.

[0049] Preferably, according to the first characteristic difference, controlling the target air intake parameters of the air intake port on the side panel of the steam oven includes:

[0050] Get the first current air intake parameter of the air intake port on the side panel of the steam oven;

[0051] Randomly determine a numerical adjustment direction of the first current air intake parameter to adjust the numerical value of the first current air intake parameter, and obtain a second current air intake parameter;

[0052] acquiring a simulated fluid characteristic according to a second current intake parameter;

[0053] Calculating a second characteristic difference between the simulated fluid characteristic and the standard fluid characteristic;

[0054] When the first characteristic difference is greater than or equal to the second characteristic difference, the randomly determined numerical adjustment direction is used as the target adjustment direction;

[0055] When the first characteristic difference is smaller than the second characteristic difference, the opposite direction of the randomly determined numerical value adjustment direction is used as the target adjustment direction;

[0056] The first current air intake parameter is adjusted according to the target adjustment direction to obtain the target air intake parameter.

[0057] Preferably, adjusting the first current air intake parameter according to the target adjustment direction to obtain the target air intake parameter includes:

[0058] acquiring a third current air intake parameter in real time based on the adjusted first current air intake parameter;

[0059] acquiring, according to a third current intake parameter, an adjustment fluid characteristic;

[0060] Obtaining a first change amount per unit time of a third current intake parameter and a second change amount per unit time of a third characteristic difference of the adjusted fluid characteristic;

[0061] The first change amount increment is determined according to the change in the quotient of the first change amount and the second variable.

[0062] Preferably, analyzing the water storage signal to determine whether there is a risk of condensate overflow includes:

[0063] Obtaining water volume prediction basis information of the condensation box; the water volume prediction basis information includes: user cooking habit information and scheduled cooking information;

[0064] According to the water volume prediction basis information and the current time, the condensate volume of the stove steam oven in the next operation is predicted;

[0065] Analyze the water storage signal to obtain the remaining water capacity of the condensate box;

[0066] If the amount of condensed water is greater than the remaining water capacity, it is determined that there is a risk of condensed water overflow.

[0067] The beneficial effects of the present invention are:

[0068] The present invention obtains a first air intake parameter of the steam pipe connected to the condensate box and a second air intake parameter of the exhaust pipe connected to the condensate box, and controls the target air intake parameter of the air inlet on the side panel of the steam oven in real time according to the first air intake parameter and the second air intake parameter, thereby improving the real-time and accuracy of fluid control; judges the overflow risk of condensed water, and if there is an overflow risk, discharges the waste water in time, making the equipment safer to operate.

[0069] Other features and advantages of the present invention will be described in the following description, and partly become apparent from the description, or understood by practicing the present invention. The purpose and other advantages of the present invention can be realized and obtained by the structures specifically pointed out in the present application documents.

[0070] The technical solution of the present invention is further described in detail below through the accompanying drawings and embodiments. BRIEF DESCRIPTION OF THE DRAWINGS

[0071] The accompanying drawings are used to provide a further understanding of the present invention and constitute a part of the specification. Together with the embodiments of the present invention, they are used to explain the present invention and do not constitute a limitation of the present invention. In the accompanying drawings:

[0072] Figure 1A schematic diagram of a condensation box for optimizing the treatment of fluid and condensed water according to an embodiment of the present invention;

[0073] Figure 2 A schematic diagram of a stove steam oven in an embodiment of the present invention;

[0074] Figure 3 Schematic diagram of a condensate box fluid control method for optimizing the treatment of fluid and condensed water in an embodiment of the present invention. DETAILED DESCRIPTION

[0075] The preferred embodiments of the present invention are described below in conjunction with the accompanying drawings. It should be understood that the preferred embodiments described herein are only used to illustrate and explain the present invention, and are not used to limit the present invention.

[0076] The embodiment of the present invention provides a condensation box for optimizing the treatment of fluid and condensed water, such as Figure 1 As shown, including:

[0077] The first air intake parameter acquisition subsystem 1 is used to acquire the first air intake parameter of the steam pipe connected to the condensation box; wherein the first air intake parameter is: the steam air intake parameter of the steam pipe connected to the condensation box, such as: the steam flow rate and water content of the connection interface between the condensation box and the steam pipe;

[0078] The second air intake parameter acquisition subsystem 2 is used to acquire the second air intake parameter of the exhaust pipe connected to the condensation box; wherein the second air intake parameter is: the air intake parameter of the exhaust pipe connected to the condensation box, such as: the air flow rate of the connection interface between the condensation box and the exhaust pipe;

[0079] The target air intake parameter control subsystem 3 is used to control the target air intake parameter of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter; wherein the target air intake parameter is: the air intake parameter set at the air intake port on the side panel of the steam oven, such as: the setting parameter of the fan (direction, speed);

[0080] The condensate processing subsystem 4 is used to obtain the water storage signal of the condensate box in real time, analyze the water storage signal, and determine whether there is a risk of condensate overflow. If so, the waste water in the condensate box is automatically discharged. The water storage signal is obtained based on the detection of the water volume sensor in the condensate box. It is determined whether there is a risk of condensate overflow, and the most recent condensate volume of the stove steam oven in the future is predicted. If the total amount of condensate predicted and the current condensate volume is greater than the capacity of the condensate box, it is determined that there is a risk of condensate overflow, and the waste water in the condensate box is automatically discharged. If the stove steam oven is Figure 2 shown.

[0081] The working principle and beneficial effects of the above technical solution are:

[0082] The present invention obtains a first air intake parameter of the steam pipe connected to the condensate box and a second air intake parameter of the exhaust pipe connected to the condensate box, and controls the target air intake parameter of the air inlet on the side panel of the steam oven in real time according to the first air intake parameter and the second air intake parameter, thereby improving the real-time and accuracy of fluid control; judges the overflow risk of condensed water, and if there is an overflow risk, discharges the waste water in time, making the equipment safer to operate.

[0083] In one embodiment, controlling the target air intake parameter of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter includes:

[0084] Obtaining fluid space structure information of the stove steam oven; wherein the fluid space structure information is: a 1:1 proportional three-dimensional model of the fluid connection space in the steam oven;

[0085] According to the fluid space structure information, the standard fluid characteristics of the fluid space structure are evaluated; wherein the standard fluid characteristics are: a characteristic representation of the fluid space structure corresponding to an ideal fluid flow condition, such as: a steam flow trajectory, an intake air flow trajectory;

[0086] A fluid dynamics model is constructed according to the first intake parameter, the second intake parameter and the fluid spatial structure information; wherein the fluid dynamics model is a mathematical model that simulates the flow behavior of the fluid in the three-dimensional model corresponding to the fluid spatial structure based on the fluid dynamics mechanism and according to the first intake parameter and the second intake parameter;

[0087] Acquire real-time fluid characteristics in the fluid dynamics model; wherein the real-time fluid characteristics are: a characteristic representation of the gas flow behavior in the fluid dynamics model, such as: how much viscosity, how continuous, etc., according to the fluid characteristics reading template preset in the fluid dynamics model and the simulation results in the fluid dynamics model;

[0088] Calculating a first characteristic difference between the real-time fluid characteristic and the standard fluid characteristic; wherein the first characteristic difference represents the degree of difference between the real-time fluid flow condition and the standard fluid flow condition in the condensation box, and the greater the first characteristic difference, the greater the degree of difference;

[0089] According to the first characteristic difference, the air intake parameters of the air intake port on the side panel of the steam oven are controlled.

[0090] The working principle and beneficial effects of the above technical solution are:

[0091] The present invention evaluates the standard fluid characteristics of the fluid space structure according to the acquired fluid space structure information of the stove steam oven, and then constructs a fluid dynamics model according to the first air intake parameter, the second air intake parameter and the fluid space structure information measured in real time. The fluid dynamics model can perform fluid dynamics simulation based on the first air intake parameter, the second air intake parameter and the fluid space structure information, extract the real-time fluid characteristics of the simulated fluid behavior in the simulation result, and then control the air intake parameters of the air inlet on the side panel of the steam oven according to the first characteristic difference between the real-time fluid characteristics and the standard fluid characteristics, thereby improving the suitability of fluid control.

[0092] In one embodiment, based on the fluid spatial structure information, evaluating the standard fluid characteristics of the fluid spatial structure includes:

[0093] Connecting to the design expert video node and sending fluid space structure information; wherein the design expert video node is: the video communication network node of the fluid dynamics expert;

[0094] According to the returned video of the design expert video node, a local discussion area of ​​the fluid space structure is determined; wherein the local discussion area is: a part relative to the fluid space structure obtained by analyzing the returned video;

[0095] Obtaining a preset visualization template of the airflow pattern; wherein the visualization template is: an indication template indicating the designed airflow pattern, such as: an airflow direction arrow indicating a "vortex" and an airflow direction arrow indicating an upward flow;

[0096] Determine discussion record items on the timeline according to the discussion record of the local discussion area, the discussion record items including: airflow pattern determination basis items and airflow pattern description items;

[0097] According to the time axis, the time point interval of the airflow pattern description item is read; wherein the time point interval is: the time difference between the airflow pattern description item and the description time;

[0098] If the time point interval is less than the preset time point interval threshold, the last airflow morphology description item on the time axis is determined to be the target airflow morphology description item, and after obtaining the target airflow morphology description item, the target number of airflow morphology determination basis items are subjected to rationality analysis to determine the reasonable airflow morphology description item; wherein, the preset time point interval threshold is manually preset, such as: 3 seconds; the rationality analysis includes: analyzing whether the description personnel weight of the airflow morphology description item and the airflow morphology determination basis item are reasonable; the target number is: 20; the description personnel weight of the reasonable airflow morphology description item is greater than the description personnel weight of other airflow morphology description items, and the airflow morphology determination basis item retrieved based on the fluid dynamics knowledge graph is reasonable;

[0099] If the time point interval is greater than or equal to a preset time point interval threshold, obtain the discussion record item between the target airflow pattern description item and the airflow pattern description item before the target airflow pattern description item to perform rationality analysis and determine a reasonable airflow pattern description item;

[0100] Determine an associated airflow pattern of the target airflow pattern; wherein the associated airflow pattern is: an airflow pattern that was historically generated together with the target airflow pattern;

[0101] According to the target airflow form and the associated airflow form, a visualization template ranking table is obtained and displayed to the design expert; wherein the visualization template ranking table is: the visualization template of the target airflow form is ranked first, and then the template selection list of the visualization template of the associated airflow form is ranked in descending order according to the association value of the associated airflow form;

[0102] Obtain the fluid space structure diagram with the visualization template annotated by the design expert;

[0103] Determine standard fluid characteristics based on the fluid space structure diagram and the preset interpretation rules of the visualization template.

[0104] The working principle and beneficial effects of the above technical solution are:

[0105] The present invention connects to the video communication network node of the fluid dynamics expert and sends the fluid space structure information, obtains the return video of the design expert video node to determine the local discussion area of ​​the fluid space structure in the video screen, introduces the preset visualization template of the airflow form, and determines the reasonable airflow form description items according to the discussion content of the experts. According to the association values ​​of the reasonable airflow form description items and their associated airflow forms, a visualization template ranking table is determined for the design expert to select. After the design expert has marked the fluid space structure diagram with the visualization template, the preset interpretation rules of the visualization template are introduced to interpret and describe the standard fluid characteristics, thereby improving the standardization and rationality of the determination of the standard fluid characteristics.

[0106] In one embodiment, according to the first characteristic difference, controlling the target air intake parameter of the air intake port on the side panel of the steam oven includes:

[0107] Obtaining a first current air intake parameter of the air intake port on the side panel of the steam oven; wherein the first current air intake parameter is: an air intake parameter of the air intake port on the side panel of the steam oven, such as: an air intake speed;

[0108] Randomly determine the numerical adjustment direction of the first current intake parameter to adjust the numerical value of the first current intake parameter, and obtain the second current intake parameter; wherein the numerical adjustment direction includes: adjusting in a direction of a larger numerical value and adjusting in a direction of a smaller numerical value, and when randomly adjusting, the adjustment amount of each adjustment is manually preset;

[0109] According to the second current intake parameter, a simulated fluid characteristic is obtained; wherein the extraction rule of the simulated fluid characteristic is the same as the real-time fluid characteristic, and is obtained by simulating a fluid dynamics learning model constructed based on the first intake parameter, the second current intake parameter and the fluid spatial structure information and extracting the fluid characteristic in the simulation result;

[0110] Calculating a second characteristic difference between the simulated fluid characteristic and the standard fluid characteristic;

[0111] When the first characteristic difference is greater than or equal to the second characteristic difference, the randomly determined numerical adjustment direction is used as the target adjustment direction;

[0112] When the first characteristic difference is smaller than the second characteristic difference, the opposite direction of the randomly determined numerical value adjustment direction is used as the target adjustment direction;

[0113] The first current air intake parameter is adjusted according to the target adjustment direction to obtain the target air intake parameter.

[0114] The working principle and beneficial effects of the above technical solution are:

[0115] The present invention obtains a first current air intake parameter of an air intake port on a side panel of a steam oven, firstly, randomly adjusts the first current air intake parameter in a numerical adjustment direction to obtain a second current air intake parameter, characterizes the fluid behavior simulated based on the first air intake parameter, the second current air intake parameter and fluid space structure information to obtain a simulated fluid characteristic, and calculates a second characteristic difference; compares the first characteristic difference with the second characteristic difference, if the first characteristic difference is greater than or equal to the second characteristic difference, it means that the randomly determined numerical adjustment direction is correct, and the randomly determined numerical adjustment direction is used as a target adjustment direction; if the first characteristic difference is less than the second characteristic difference, it means that the randomly determined numerical adjustment direction is wrong, and the opposite direction of the randomly determined numerical adjustment direction is used as a target adjustment direction, and the second air intake parameter is adjusted after the target adjustment direction is determined, thereby improving the adjustment efficiency.

[0116] In one embodiment, adjusting the first current air intake parameter according to the target adjustment direction to obtain the target air intake parameter includes:

[0117] Acquire a third current air intake parameter in real time based on the adjusted first current air intake parameter; wherein the third current air intake parameter is: an air intake parameter generated in real time when the air intake parameter is adjusted on the side panel of the steam oven;

[0118] According to the third current air intake parameter, the adjusted fluid characteristic is obtained; wherein the adjusted fluid characteristic is: a fluid characteristic obtained by characterizing the fluid behavior based on the first air intake parameter, the third current air intake parameter and the fluid spatial structure information simulation;

[0119] Obtaining a first change amount per unit time of the third current intake parameter and a second change amount per unit time of the third characteristic difference of the adjustment fluid characteristic; wherein the first change amount is: the change amount per unit time of the third current intake parameter during the real-time adjustment process; the third characteristic difference is: the characteristic difference between the adjustment fluid characteristic and the standard fluid characteristic; the second change amount is: the change amount per unit time of the third characteristic difference during the real-time adjustment process;

[0120] The first change increment is determined according to the change in the quotient of the first change and the second variable, wherein when the quotient change increases, the first change increment is a positive value, and when the quotient change decreases, the first change increment is a negative value, until the third characteristic difference is zero.

[0121] The working principle and beneficial effects of the above technical solution are:

[0122] The present invention extracts the adjustment fluid characteristic corresponding to the third current intake parameter in the adjustment process, obtains the first change amount per unit time of the third current intake parameter and the second change amount of the third characteristic difference per unit time of the adjustment fluid characteristic, introduces the quotient of the first change amount and the second variable, and when the quotient value changes more, increases the change rate of the first current intake parameter, and when the quotient value changes less, reduces the change rate of the first current intake parameter, determines the adjustment amount according to the feedback of the third characteristic difference, and the fluid adjustment control process is smoother.

[0123] In one embodiment, analyzing the water storage signal to determine whether there is a risk of condensate overflow includes:

[0124] Obtaining water volume prediction basis information of the condensation box; the water volume prediction basis information includes: user cooking habit information and scheduled cooking information; wherein the cooking habit information is: the user's usage habits of the stove steam oven, such as: using the steam box for 20 minutes every morning; the scheduled cooking information is: the scheduled cooking instructions added to the stove steam oven through the smart app;

[0125] According to the water volume prediction basis information and the current time, the condensate volume of the stove steam oven in the next operation is predicted;

[0126] Analyze the water storage signal to obtain the remaining water capacity of the condensate box;

[0127] If the amount of condensed water is greater than the remaining water capacity, it is determined that there is a risk of condensed water overflow.

[0128] The working principle and beneficial effects of the above technical solution are:

[0129] The present invention introduces water volume prediction basis information of the condensation box, and predicts the condensation volume of the stove steam oven in the most recent future operation according to the water volume prediction basis information and the current time. When the predicted remaining water capacity is insufficient to accommodate the most recently predicted condensation volume, it is determined that there is a risk of condensation water overflow, and wastewater treatment is automatically performed before the next operation, thereby avoiding the risk of equipment damage caused by condensation water overflow.

[0130] The embodiment of the present invention provides a condensation box fluid control method for optimizing the treatment of fluid and condensed water, such as Figure 3 As shown, including:

[0131] Step 1: Obtain the first air intake parameter of the steam pipe connected to the condensate box;

[0132] Step 2: Obtain the second air intake parameter of the exhaust pipe connected to the condensation box;

[0133] Step 3: controlling the target air intake parameter of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter;

[0134] Step 4: Obtain the water storage signal of the condensate box in real time, analyze the water storage signal, and determine whether there is a risk of condensate overflow. If so, automatically discharge the waste water in the condensate box.

[0135] In one embodiment, controlling the target air intake parameter of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter includes:

[0136] Obtain fluid space structure information of the stove steam oven;

[0137] Based on the fluid spatial structure information, standard fluid characteristics of the fluid spatial structure are evaluated;

[0138] Constructing a fluid dynamics model according to the first air intake parameter, the second air intake parameter and the fluid space structure information;

[0139] Get real-time fluid characteristics in fluid dynamics models;

[0140] Calculating a first characteristic difference between the real-time fluid characteristic and the standard fluid characteristic;

[0141] According to the first characteristic difference, the air intake parameters of the air intake port on the side panel of the steam oven are controlled.

[0142] In one embodiment, according to the first characteristic difference, controlling the target air intake parameter of the air intake port on the side panel of the steam oven includes:

[0143] Get the first current air intake parameter of the air intake port on the side panel of the steam oven;

[0144] Randomly determine a numerical adjustment direction of the first current air intake parameter to adjust the numerical value of the first current air intake parameter, and obtain a second current air intake parameter;

[0145] acquiring a simulated fluid characteristic according to a second current intake parameter;

[0146] Calculating a second characteristic difference between the simulated fluid characteristic and the standard fluid characteristic;

[0147] When the first characteristic difference is greater than or equal to the second characteristic difference, the randomly determined numerical adjustment direction is used as the target adjustment direction;

[0148] When the first characteristic difference is smaller than the second characteristic difference, the opposite direction of the randomly determined numerical value adjustment direction is used as the target adjustment direction;

[0149] The first current air intake parameter is adjusted according to the target adjustment direction to obtain the target air intake parameter.

[0150] In one embodiment, adjusting the first current air intake parameter according to the target adjustment direction to obtain the target air intake parameter includes:

[0151] acquiring a third current air intake parameter in real time based on the adjusted first current air intake parameter;

[0152] acquiring, according to a third current intake parameter, an adjustment fluid characteristic;

[0153] Obtaining a first change amount per unit time of a third current intake parameter and a second change amount per unit time of a third characteristic difference of the adjusted fluid characteristic;

[0154] The first change amount increment is determined according to the change in the quotient of the first change amount and the second variable.

[0155] In one embodiment, analyzing the water storage signal to determine whether there is a risk of condensate overflow includes:

[0156] Obtaining water volume prediction basis information of the condensation box; the water volume prediction basis information includes: user cooking habit information and scheduled cooking information;

[0157] According to the water volume prediction basis information and the current time, the condensate volume of the stove steam oven in the next operation is predicted;

[0158] Analyze the water storage signal to obtain the remaining water capacity of the condensate box;

[0159] If the amount of condensed water is greater than the remaining water capacity, it is determined that there is a risk of condensed water overflow.

[0160] Obviously, those skilled in the art can make various changes and modifications to the present invention without departing from the spirit and scope of the present invention. Thus, if these modifications and variations of the present invention fall within the scope of the claims of the present invention and their equivalents, the present invention is also intended to include these modifications and variations.

Claims

1. A condensation box for optimizing the treatment of fluid and condensed water, characterized in that: include: A first air intake parameter acquisition subsystem, used to acquire a first air intake parameter of a steam pipe connected to the condensate box; A second air intake parameter acquisition subsystem, used to acquire a second air intake parameter of the exhaust pipe connected to the condensation box; A target air intake parameter control subsystem, used to control the target air intake parameter of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter; The condensate water treatment subsystem is used to obtain the water storage signal of the condensate box in real time, analyze the water storage signal, and determine whether there is a risk of condensate overflow. If so, the waste water in the condensate box is automatically discharged.

2. A condensation box for optimizing the treatment of fluid and condensed water according to claim 1, characterized in that: The target air intake parameter control subsystem controls the target air intake parameters of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter, and performs the following operations: Obtain fluid space structure information of the stove steam oven; Based on the fluid spatial structure information, standard fluid characteristics of the fluid spatial structure are evaluated; Constructing a fluid dynamics model according to the first air intake parameter, the second air intake parameter and the fluid space structure information; Get real-time fluid characteristics in fluid dynamics models; Calculating a first characteristic difference between the real-time fluid characteristic and the standard fluid characteristic; According to the first characteristic difference, the air intake parameters of the air intake port on the side panel of the steam oven are controlled.

3. A condensation box for optimizing the treatment of fluid and condensed water as claimed in claim 2, characterized in that: The target air intake parameter control subsystem controls the target air intake parameters of the air intake port on the side panel of the steam oven according to the first characteristic difference, and performs the following operations: Get the first current air intake parameter of the air intake port on the side panel of the steam oven; Randomly determine a numerical adjustment direction of the first current air intake parameter to adjust the numerical value of the first current air intake parameter, and obtain a second current air intake parameter; Acquiring simulated fluid characteristics according to a second current intake parameter; Calculating a second characteristic difference between the simulated fluid characteristic and the standard fluid characteristic; When the first characteristic difference is greater than or equal to the second characteristic difference, the randomly determined numerical adjustment direction is used as the target adjustment direction; When the first characteristic difference is smaller than the second characteristic difference, the opposite direction of the randomly determined numerical value adjustment direction is used as the target adjustment direction; The first current air intake parameter is adjusted according to the target adjustment direction to obtain the target air intake parameter.

4. A condensation box for optimizing the treatment of fluid and condensed water as claimed in claim 3, characterized in that: The target intake parameter control subsystem adjusts the first current intake parameter according to the target adjustment direction to obtain the target intake parameter and performs the following operations: acquiring a third current air intake parameter in real time based on the adjusted first current air intake parameter; According to a third current intake parameter, obtaining an adjustment fluid characteristic; Obtaining a first change amount per unit time of a third current intake parameter and a second change amount per unit time of a third characteristic difference of the adjusted fluid characteristic; The first change amount increment is determined according to the change in the quotient of the first change amount and the second variable.

5. A condensation box for optimizing the treatment of fluid and condensed water according to claim 1, characterized in that: The condensate treatment subsystem analyzes the water storage signal to determine whether there is a risk of condensate overflow and performs the following operations: Obtaining water volume prediction basis information of the condensation box; the water volume prediction basis information includes: user cooking habit information and scheduled cooking information; According to the water volume prediction basis information and the current time, the condensate volume of the stove steam oven in the next operation is predicted; Analyze the water storage signal to obtain the remaining water capacity of the condensate box; If the amount of condensed water is greater than the remaining water capacity, it is determined that there is a risk of condensed water overflow.

6. A condensation box fluid control method for optimizing the treatment of fluid and condensed water, characterized in that: include: Obtaining a first air intake parameter of a steam pipe connected to the condensate box; Obtain the second air intake parameter of the exhaust pipe connected to the condensation box; Controlling target air intake parameters of the air intake port on the side panel of the steam oven according to the first air intake parameter and the second air intake parameter; The water storage signal of the condensate box is obtained in real time, and the water storage signal is analyzed to determine whether there is a risk of condensate overflow. If so, the waste water in the condensate box is automatically discharged.

7. A condensation box fluid control method for optimizing fluid and condensed water treatment as claimed in claim 6, characterized in that: According to the first air intake parameter and the second air intake parameter, the target air intake parameter of the air intake port on the side panel of the steam oven is controlled, including: Obtain fluid space structure information of the stove steam oven; Based on the fluid spatial structure information, standard fluid characteristics of the fluid spatial structure are evaluated; Constructing a fluid dynamics model according to the first air intake parameter, the second air intake parameter and the fluid space structure information; Get real-time fluid characteristics in fluid dynamics models; Calculating a first characteristic difference between the real-time fluid characteristic and the standard fluid characteristic; According to the first characteristic difference, the air intake parameters of the air intake port on the side panel of the steam oven are controlled.

8. A condensation box fluid control method for optimizing the treatment of fluid and condensed water according to claim 7, characterized in that: According to the first characteristic difference, the target air intake parameters of the air intake port on the side panel of the steam oven are controlled, including: Get the first current air intake parameter of the air intake port on the side panel of the steam oven; Randomly determine a numerical adjustment direction of the first current air intake parameter to adjust the numerical value of the first current air intake parameter, and obtain a second current air intake parameter; Acquiring simulated fluid characteristics according to a second current intake parameter; Calculating a second characteristic difference between the simulated fluid characteristic and the standard fluid characteristic; When the first characteristic difference is greater than or equal to the second characteristic difference, the randomly determined numerical adjustment direction is used as the target adjustment direction; When the first characteristic difference is smaller than the second characteristic difference, the opposite direction of the randomly determined numerical value adjustment direction is used as the target adjustment direction; The first current air intake parameter is adjusted according to the target adjustment direction to obtain the target air intake parameter.

9. A condensation box fluid control method for optimizing fluid and condensed water treatment as claimed in claim 8, characterized in that: Adjusting the first current air intake parameter according to the target adjustment direction to obtain the target air intake parameter includes: acquiring a third current air intake parameter in real time based on the adjusted first current air intake parameter; According to a third current intake parameter, obtaining an adjustment fluid characteristic; Obtaining a first change amount per unit time of a third current intake parameter and a second change amount per unit time of a third characteristic difference of the adjusted fluid characteristic; The first change amount increment is determined according to the change in the quotient of the first change amount and the second variable.

10. A condensation box fluid control method for optimizing fluid and condensed water treatment as claimed in claim 6, characterized in that: Analyze the water storage signal to determine whether there is a risk of condensate overflow, including: Obtaining water volume prediction basis information of the condensation box; the water volume prediction basis information includes: user cooking habit information and scheduled cooking information; According to the water volume prediction basis information and the current time, the condensate volume of the stove steam oven in the next operation is predicted; Analyze the water storage signal to obtain the remaining water capacity of the condensate box; If the amount of condensed water is greater than the remaining water capacity, it is determined that there is a risk of condensed water overflow.

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