JP2019205635A - Deodorization system, method of controlling the same, and information processing device, method of controlling the same, and program, and cleaning device, method of controlling the same, and program - Google Patents

Abstract

To provide a mechanism that can identify a suitable cleaning ability while reducing cost of cleaning.SOLUTION: An information processing device controls a generator that generates cleaning liquid, and a cleaning device that cleans a gas containing a cleaning object by using the cleaning liquid generated by the generator. The information processing device stores a parameter on a cleaning ability of the cleaning liquid; acquires meteorological information on the air containing the gas after cleaned by the cleaning device; and identifies the parameter stored in the storage means, corresponding to the meteorological information acquired by the first acquiring means.SELECTED DRAWING: Figure 1

Description

  Deodorization system capable of providing a mechanism capable of specifying an appropriate cleaning capability while reducing costs related to cleaning, a control method thereof, an information processing device, a control method and program thereof, and a cleaning device and control thereof The present invention relates to a method and a program.

  With increasing environmental awareness, when operating devices or facilities that generate odors, it may be necessary to implement means for reducing odors. As a method for reducing the odor in the exhaust, a method is known in which the odor component in the exhaust is dissolved in water by washing the exhaust with water or a treatment liquid. In addition, a method for improving the odor reduction efficiency by using a treatment liquid having a deodorizing action at this time is also known. For example, the following Patent Document 1 discloses a deodorizing apparatus that reduces odors in the air by spraying hypochlorous acid water to the air fed into the interior and exhausts the air with reduced odors. Has been.

JP 2012-1000071 A

  However, the use concentration of hypochlorous acid water, which is considered desirable in the mechanism described in Patent Document 1, is about 10 to 30 ppm. When deodorizing an intense odor such as a gas generated by fermentation of organic matter including exhaust from a container for storing food waste or human waste, for example, using the mechanism described in Patent Document 1, a higher concentration Increasing the cleaning ability with hypochlorous acid water by using hypochlorous acid water can be mentioned as a means. However, the higher the cleaning ability with hypochlorous acid water, the higher the cost for cleaning.

  Therefore, an object of the present invention is to provide a mechanism that can specify an appropriate cleaning capability while reducing the cost of cleaning.

  In order to achieve the above object, an information processing apparatus according to the present invention is an information processing apparatus that controls a generating apparatus that generates a cleaning liquid for cleaning a gas containing a cleaning target with the cleaning apparatus, and the cleaning capability of the cleaning liquid Corresponding to the weather information acquired by the first acquisition means, storage means for storing parameters relating to, first acquisition means for acquiring weather information of the air containing the gas after cleaning by the cleaning device And specifying means for specifying the parameter stored in the storage means.

  According to the present invention, there is an effect that it is possible to provide a mechanism capable of specifying an appropriate cleaning capability while reducing the cost for cleaning.

It is a system configuration figure showing an example of the composition of the deodorizing system in the embodiment of the present invention. It is a schematic block diagram which shows an example of the deodorizing apparatus in embodiment of this invention. It is a hardware block diagram which shows an example of the hardware structure of the information processing apparatus 100 in embodiment of this invention. It is a block diagram which shows an example of a module structure of the information processing apparatus 100 in embodiment of this invention. It is a flowchart of the deodorizing method in embodiment of this invention. It is a flowchart which shows the detail of the concentration control process of hypochlorous acid water based on the wind direction by the information processing apparatus 100 in embodiment of this invention. It is a flowchart which shows the detail of the flow control process of hypochlorous acid water based on the wind direction by the information processing apparatus 100 in embodiment of this invention. It is a flowchart which shows the detail of the concentration control process of hypochlorous acid water based on the wind speed by the information processing apparatus 100 in embodiment of this invention. It is a flowchart which shows the detail of the flow control process of hypochlorous acid water based on the wind speed by the information processing apparatus 100 in embodiment of this invention. It is a flowchart which shows the detail of the concentration control process of hypochlorous acid water based on the wind direction and ammonia concentration by the information processing apparatus 100 in embodiment of this invention. It is a flowchart which shows the detail of the flow control process of hypochlorous acid water based on the wind direction and ammonia concentration by the information processing apparatus 100 in embodiment of this invention. It is a block diagram which shows an example of a structure of density change mode (1) table in embodiment of this invention. It is a block diagram which shows an example of a structure of the flow volume change mode (1) table in embodiment of this invention. It is a block diagram which shows an example of a structure of density change mode (2) table in embodiment of this invention. It is a block diagram which shows an example of a structure of the flow volume change mode (2) table in embodiment of this invention. It is a block diagram which shows an example of a structure of the density | concentration change mode (3) table in embodiment of this invention. It is a block diagram which shows an example of a structure of the flow volume change mode (3) table in embodiment of this invention. It is a figure which shows the positional relationship of the washing | cleaning apparatus and a house in embodiment of this invention.

  Embodiments of the present invention will be described below with reference to the accompanying drawings. In addition, embodiment described below shows an example at the time of concretely implementing this invention. In particular, the cleaning device, the cleaning system, and the cleaning method according to the embodiment are not limited to a system that aims to deodorize a gas to be deodorized. The cleaning device, the cleaning system, and the cleaning method according to the present embodiment are for cleaning a gas and can be used for various purposes other than deodorization. For example, the cleaning apparatus and the cleaning system according to the present invention can be used for sterilization of a sterilization target in gas. Therefore, the cleaning apparatus, the cleaning system, and the cleaning method according to the present invention include an apparatus, a system, and a method that are mainly used for deodorization but can be used for deodorization. Hereinafter, embodiments of the present invention will be described by taking, as examples, a wet deodorizing apparatus (corresponding to a cleaning apparatus), a deodorizing system (corresponding to a cleaning system), and a deodorizing method whose main purpose is to deodorize a gas to be deodorized. .

  FIG. 1 is a system configuration diagram showing an example of the configuration of a deodorizing system that controls the physical quantity of a cleaning liquid. The deodorization system includes an information processing apparatus 100 that controls the physical amount of the cleaning liquid, a generation apparatus 110 that generates the cleaning liquid, a storage container 120 that stores the cleaning liquid generated in the generation apparatus 110, and a storage container 120 that stores the cleaning liquid. It is comprised with the wet deodorizing apparatus 200 which deodorizes a odor using a washing | cleaning liquid.

  The production | generation apparatus 110 is connected to the three raw material containers which store the raw material of the washing | cleaning liquid through the valve, respectively. The three raw material containers are a first raw material container 101 that stores hypochlorous acid water, a second raw material container 102 that stores water, and a third raw material container 103 that stores carbon dioxide. Indicates. The first raw material container 101 and the generator 110 are connected via a first raw material valve 181. The second raw material container 102 and the generation device 110 are connected via a second raw material valve 182. The third raw material container 103 and the generation device 110 are connected via a third raw material valve 183. The cleaning apparatus 200 is connected to a storage container 120 that stores the cleaning liquid generated by the generation apparatus 110 via a cleaning liquid valve 190. In the present embodiment, the cleaning liquid is generated in the generating device 110 using a carbon dioxide mixing method. The carbon dioxide mixing method is a method of generating hypochlorous acid water by mixing sodium hypochlorite, carbon dioxide, and water. The outlet 111 provided in the generation device 110 is connected to the inlet 121 of the storage container 120, and the cleaning liquid that has flowed out of the outlet 111 of the generation device passes through the inlet 121 of the storage container 120 to the storage container 120. Inflow. Similarly, the outlet 122 provided in the storage container 120 is connected to the inlet 201 of the wet deodorization apparatus, and the cleaning liquid 130 flowing out from the outlet 122 of the storage container 120 passes through the inlet 201 of the wet deodorization apparatus 200. And flows into the wet deodorizing apparatus 200. The deodorizing target gas 2140 is supplied via the odor inflow unit 150, and the deodorizing target gas 140 is deodorized by the cleaning unit in the deodorizing apparatus 200. The cleaning liquid 130 overflowing from the deodorizing apparatus 200 flows out through the cleaning liquid outflow section 170 (repair). The gas after deodorization by the deodorization apparatus 200 is discharged from the odor outflow portion 160. The gas that flows out from the odor outflow portion 160 is referred to as a second gas (corresponding to the cleaned gas). A wind direction sensor 202 that measures the wind direction, a wind speed sensor 203 that measures the wind speed, and an ammonia concentration measuring device 204 that measures the ammonia concentration are provided at a location within 10 m from the odor outflow portion 160.

  In addition, the sensor used in a present Example is an example, and the kind of sensor to be used is not this limitation. Moreover, the apparatus which acquires a wind speed, a wind direction, and an odor component is not restricted to a sensor. For example, weather information such as wind speed and direction may be acquired by the information processing apparatus 100 from the Japan Meteorological Agency or may be input to the information processing apparatus 100 by the user. The place where the sensor and the measuring device are disposed is not limited to the illustrated place as long as the wind direction, wind speed, ammonia concentration, and the like of the air that can contain the gas cleaned by the cleaning device 200 can be acquired. In this embodiment, the ammonia concentration measurement is performed using the ammonia concentration measuring device 204. However, the measurement target is not limited to the ammonia concentration, and it is only necessary to measure the components contained in the gas to be cleaned. For example, the concentration of trimethylamine or the number of virus particles may be used.

  In FIG. 1, the cleaning apparatus is the cleaning apparatus 200, but the information processing apparatus 100, the generation apparatus 110, the storage container 120, the cleaning apparatus 200, and the like may be referred to as a cleaning apparatus.

  Above, description of the system block diagram of the control system shown in FIG. 1 is complete | finished.

  Hereinafter, with reference to FIG. 2 (A) (B), the wet deodorizing apparatus 200 which concerns on this embodiment is demonstrated. 2 (A) and 2 (B) are schematic views each showing a configuration of an example of a wet deodorizing apparatus according to the present embodiment.

  FIG. 2 (A) shows a wet deodorizing apparatus 200A, and FIG. 2 (B) shows a wet deodorizing apparatus 200B. In the present embodiment, it is assumed that the wet deodorizing apparatus 200A is used as a cleaning apparatus. However, the cleaning apparatus is not limited to the wet deodorizing apparatus 200A, and may be a wet deodorizing apparatus 200B, which is an apparatus (not shown) for cleaning gas. I just need it. A gas to be cleaned (deodorized object) flows into these wet deodorizing apparatuses 200A and 200B through the odor inflow portion 150, and the inflowed gas is deodorized by cleaning with the cleaning liquid and flows out through the odor outflow portion 160. To do. In this specification, the gas including the object to be cleaned is referred to as a first gas.

  From the odor inflow section 150, the gas to be deodorized flows into the wet deodorization apparatuses 200A and 200B. For example, the gas to be deodorized can be sent to the odor inflow portion 150 using a pump (not shown). Here, the pump for sending the gas to the odor inflow portion 150 may be disposed either inside or outside the wet deodorization apparatuses 200A and 200B. The type of gas to be deodorized is not particularly limited. The high deodorizing performance of the wet deodorizing apparatuses 200A and 200B according to the present embodiment is suitable for deodorizing a gas having a high odor concentration. For example, the gas to be deodorized includes a gas generated by fermentation of organic matter including exhaust from a container for storing food waste or human waste. Specific examples of the deodorization target include exhaust from a compost (compost production apparatus).

  The odor component to be removed is not particularly limited. Here, examples of odor components in compost include basic components such as ammonia or trimethylamine, sulfide components such as methyl mercaptan, aldehyde components such as acetaldehyde, or carboxylic acid components such as propionic acid, and the like. Can be mentioned. The wet deodorization apparatuses 200A and 200B according to the present embodiment are particularly suitable for reducing the ammonia concentration. For example, in one embodiment, the ammonia concentration of the gas to be deodorized is 100 ppm or more when cooled by a cooler, and is 3000 ppm or more when not cooled by a cooler. Further, the gas to be deodorized flowing from the odor inflow section 150 may be a gas after being processed by another device such as a cooler or a wet deodorizing device located in the preceding stage.

  The cleaning unit 220 cleans the gas to be deodorized that has flowed into the wet deodorizing apparatuses 200 </ b> A and 200 </ b> B with the first cleaning liquid 222. The cleaning part 220 has a contact part 221 where the gas to be deodorized and the first cleaning liquid 222 are in contact with each other, and a part in which the first cleaning liquid 222 is stored. In this embodiment, the 1st washing | cleaning liquid 222 is stored in the lower part of wet deodorizing apparatus 200A, B, Therefore Therefore, the washing | cleaning part 220 is also located in the lower part of wet deodorizing apparatus 200A, B.

  FIG. 2C is an enlarged view of one of the contact portions 221 in FIG. A process for mixing the gas to be deodorized and the first cleaning liquid 222 will be described with reference to FIG. First, the gas to be deodorized is moved toward the flow path constriction 223 by being accelerated by the pump. In the example of FIG. 2A, the gas to be deodorized passes through the flow path constriction 223 provided in the contact portion 221 and close to the liquid surface of the first cleaning liquid 222. At this time, since the flow of the gas to be deodorized is accelerated, the vortex accompanied with the first cleaning liquid 222 is generated after passing through the channel narrowing portion. For this reason, the gas to be deodorized and the first cleaning liquid 222 are efficiently mixed, and the gas to be deodorized is cleaned. As described above, the cleaning unit 220 can mix the gas to be deodorized with the first cleaning liquid 222, and can stir the gas to be deodorized and the first cleaning liquid 222 with each other in one embodiment. . In the example of FIG. 2A, the cleaning unit 220 has two contact portions 221 each having a flow path narrowing portion 223, but the number of contact portions 221 is not particularly limited. For example, the wet deodorization apparatuses 200A and 200B may be provided with three or more contact portions (channel narrowing portions) when it is desired to further improve the deodorization efficiency. Moreover, wet deodorizing apparatus 200A, B can be reduced in size rather than the case where a plurality of contact parts are provided by setting the number of contact parts 221 to one.

  In the example of FIG. 2B, the gas to be deodorized passes through the inside of the first cleaning liquid 222 at the contact portion 221, and at this time, the gas to be deodorized is washed. 2A and 2B, the liquid level of the first cleaning liquid 222 is not uniform because of the pressure of the gas to be deodorized flowing from the odor inflow portion 150. . The height of the liquid surface of the first cleaning liquid 222 is set to be higher than the inflow port 253 and the outflow port 254 and lower than the outflow port 280. In addition, the height of the liquid surface of the first cleaning liquid 222 during the cleaning is close to the channel narrowing portion 223. That is, by discharging the first cleaning liquid 222 from the outlet 280, it is possible to suppress the water level from becoming too high, and it is possible to discharge the first cleaning liquid 222 after being used for cleaning. . By maintaining the water level higher than the inflow port 253 and the outflow port 254, it is possible to supply bubbles to the first cleaning liquid 222.

  But the structure of the washing | cleaning part 220 is not restricted to such a thing. For example, in the cleaning unit 220, the first cleaning liquid 222 may be sprayed. In this case, the gas to be deodorized is cleaned when it passes through the mist of the first cleaning liquid 222. In the cleaning unit 220, the gas to be deodorized flowing from the odor inflow unit 150 may be bubbled into the first cleaning liquid 222. In this case, the gas to be deodorized can also be cleaned with the first cleaning liquid 222.

  From the odor outflow part 160, the gas after being cleaned with the first cleaning liquid 222 flows out. The gas flowing out from the odor outflow portion 160 may be released into the atmosphere, or may be further processed by another device such as a wet deodorizing device. Thus, the odor component of the deodorization target is reduced in the gas after being discharged from the odor outflow part 160 as compared with the gas to be deodorized before flowing in from the odor inflow part 150. Specifically, when the odor to be deodorized is odor from compost, at least the ammonia concentration is reduced by washing treatment with the wet deodorization apparatuses 200A and 200B.

  Next, the internal structure of the wet deodorizing apparatus 200A, B will be described. The insides of the wet deodorization apparatuses 200A and B are classified into several sections. The wet deodorization apparatuses 200 </ b> A and 200 </ b> B have an inflow section 231, and an odor inflow portion 150 is provided in the inflow section 231. The inflow section 231 is a section upstream of the cleaning section 220 where the cleaning with the first cleaning liquid 222 is performed, that is, a section between the odor inflow section 150 and the cleaning section 220. Further, the wet deodorizing apparatuses 200 </ b> A and 200 </ b> B have an outflow section 241, and an odor outflow portion 160 is provided in the outflow section 241. The outflow section 241 is a section downstream of the cleaning section 220 where the cleaning with the first cleaning liquid 222 is performed, that is, a section between the cleaning section 220 and the odor outflow section 160.

  The cleaning liquid supply units 230 and 240 supply a second cleaning liquid (corresponding to the cleaning liquid) different from the first cleaning liquid 222. The cleaning liquid supply units 230 and 240 can supply the second supply liquid so as to be mixed with the first cleaning liquid 222 used for cleaning in the cleaning unit 220. Here, the cleaning liquid supply units 230 and 240 are configured such that the gas to be deodorized is at least one of the second cleaning liquid between the odor inflow unit 150 and the cleaning unit 220 or between the cleaning unit 220 and the odor outflow unit 160. The second cleaning liquid can be supplied so that the second cleaning liquid is cleaned. For example, the cleaning liquid supply units 230 and 240 pass the second cleaning liquid between the odor inflow section 150 and the cleaning section 220 (that is, the inflow section 231) and the cleaning section 220 and the odor outflow section 160. It is possible to spray at least one of a certain space (that is, the outflow section 241).

  As an example, as shown in FIG. 2A, the wet deodorizing apparatus 200A sprays the first cleaning liquid supply unit 230 that sprays the second cleaning liquid onto the inflow section 231 and the second cleaning liquid onto the outflow section 241. A second cleaning liquid supply unit 240. The first cleaning liquid supply unit 230 sprays the second cleaning liquid on the gas flow path from the odor inflow unit 150 to the cleaning unit 220. The first cleaning liquid supply unit 230 sprays the second cleaning liquid on the gas flow path from the cleaning unit 220 toward the odor outflow unit 160. However, it is also possible to employ a configuration in which the second cleaning liquid supply unit 240 is provided and the first cleaning liquid supply unit 230 is not provided as in the wet deodorization apparatus 200B illustrated in FIG. Further, it is not essential that the cleaning liquid supply units 230 and 240 spray the second cleaning liquid. For example, it is possible to adopt a configuration in which the gas to be deodorized passes through the inside of the second cleaning liquid as bubbles.

  The cleaning liquid supply units 230 and 240 are provided so that the second cleaning liquid after cleaning the gas to be deodorized is mixed with the first cleaning liquid used for cleaning in the cleaning unit 220. For example, as shown in FIGS. 2A and 2B, the wet deodorization apparatuses 200 </ b> A and 200 </ b> B can have a single cleaning tank having an odor inflow unit 150, a cleaning unit 220, and an odor outflow unit 160. Then, the cleaning liquid supply units 230 and 240 are arranged so that the liquid level of the first cleaning liquid 222 in the cleaning unit 220 is lower than the supply position of the second cleaning liquid (that is, the position of the cleaning liquid supply units 230 and 240). be able to.

  The cleaning liquid supply units 230 and 240 can supply the second cleaning liquid supplied from the outside of the apparatus, instead of supplying the first cleaning liquid 222 stored in the wet deodorization apparatuses 200A and 200B. According to such a configuration, the cleaning liquid supply units 230 and 240 can supply a fresh cleaning liquid and can clean the gas to be deodorized using the fresh cleaning liquid, so that the odor can be further reduced. Here, the fresh cleaning liquid refers to a cleaning liquid that has not yet been used for cleaning the gas to be deodorized in the wet deodorizing apparatuses 200A and 200B. For example, the fresh cleaning liquid may be a cleaning liquid that does not substantially contain odor components contained in the gas to be deodorized. In addition, the fresh cleaning liquid may be cleaning water that does not substantially contain components other than the cleaning liquid itself. However, if the fresh cleaning liquid is supplied from the outside of the apparatus and has not been used for cleaning in this apparatus, it may be a cleaning liquid after being used for gas cleaning in another wet deodorizing apparatus. By using such a configuration in combination with the cleaning unit 220 that cleans the gas to be deodorized using the first cleaning liquid 222, the odor removal capability can be improved. In particular, the second cleaning liquid supply unit 240 makes it possible to better remove the odor by cleaning the gas after cleaning with the first cleaning liquid 222 with a fresh cleaning liquid. As described above, since the fresh second cleaning liquid is supplied so as to be mixed with the first cleaning liquid 222 used for cleaning in the cleaning unit 220, the components to be cleaned in the first cleaning liquid 222 are further reduced. can do. Further, in the configuration having an outlet 280 described later, the first cleaning liquid 222 is appropriately discharged, so that it is possible to perform cleaning with a fresher cleaning liquid.

  Hereinafter, the first cleaning liquid 222 and the second cleaning liquid will be further described. The second cleaning liquid is not particularly limited. For example, the second cleaning liquid may be water. The second cleaning liquid may be a weakly acidic or acidic aqueous solution having a pH of less than 7 so that the ability to remove basic odor components such as ammonia is improved. Furthermore, in order to improve the deodorizing efficiency, the second cleaning liquid may be an aqueous solution containing a deodorizing agent. The type of deodorizer is not particularly limited, and may be, for example, an oxidizing agent, an antibacterial agent, or a microorganism. Examples of the oxidizing agent include ozone and hypochlorous acid. Examples of antibacterial agents include chitosan or catechin.

  In the present embodiment, an aqueous solution containing hypochlorous acid or hypochlorite ions is used as the second cleaning liquid. In this case, the pH of the second cleaning liquid is not particularly limited, but the pH of the second cleaning liquid can be set to 7 or less so that the activity is improved. Further, from the viewpoint of stability, the pH of the second cleaning liquid can be 5 or more. An aqueous solution containing hypochlorous acid or hypochlorite ions having a pH of 5 or more and 7 or less is known as hypochlorous acid water. From the viewpoint of deodorizing performance, the chlorine concentration in the second cleaning liquid can be 100 ppm or more, or 1000 ppm or more. On the other hand, from the economical viewpoint, the chlorine concentration in the second cleaning liquid may be 10 ppm or more, or may be 500 ppm or less.

  The second cleaning liquid may be hypochlorous acid water containing hypochlorous acid and hydrogen carbonate ions. Such a hypochlorous acid aqueous solution has stable properties because the pH is stable due to a buffering action. Such hypochlorous acid water can be obtained by mixing and diluting sodium hypochlorite and carbon dioxide in water. However, hypochlorous acid water obtained by other methods such as electrolysis of water or mixing of sodium hypochlorite and dilute hydrochloric acid can also be used as the second cleaning liquid.

  The first cleaning liquid 222 is mixed with the second cleaning liquid after being used for cleaning the gas to be deodorized. For this reason, in one embodiment, the composition of the first cleaning liquid 222 is different from that of the second cleaning liquid. For example, the odor component concentration of the first cleaning liquid 222 can be higher than that of the second cleaning liquid. As an example, when hypochlorous acid water is used as the cleaning liquid, the first cleaning liquid 222 and the second cleaning liquid have different pH values. That is, the second cleaning liquid, which is a fresh cleaning liquid, is closer to the ideal pH range of hypochlorous water spray than the first cleaning liquid 222 used for cleaning. Therefore, the second cleaning liquid has a pH value of hypochlorite watering close to the acidic side or the alkaline side depending on the component to be deodorized. Further, the deodorant concentration (for example, chlorine concentration) of the second cleaning liquid can be made higher than that of the first cleaning liquid.

  The liquid property of the first cleaning liquid 222 can be adjusted using a method of adding a cleaning liquid, a method of supplying bubbles, which will be described later, or the like. In one embodiment, the first cleaning liquid 222 is an aqueous solution containing hypochlorous acid or hypochlorite ions. In this case, the pH of the first cleaning liquid 222 is not particularly limited, but the pH of the first cleaning liquid 222 can be set to 7 or less so that the activity is improved. Further, from the viewpoint of stability, the pH of the first cleaning liquid 222 can be 5 or more. From the viewpoint of deodorizing performance, the chlorine concentration in the first cleaning liquid 222 can be 100 ppm or more, or 1000 ppm or more. On the other hand, from the viewpoint of economy, the chlorine concentration in the first cleaning liquid 222 may be 10 ppm or more and 500 ppm or less.

  The bubble supply unit 250 mixes bubbles of a third gas different from the gas (the gas to be deodorized or the first gas) including the object to be cleaned into the first cleaning liquid 222. The bubble supply unit 250 can mix the gas bubbles supplied from the outside of the wet deodorization apparatuses 200A and 200B as the third gas bubbles. Due to the function of the bubble supply unit 250, the contact area between the first cleaning liquid 222 and the gas to be deodorized in the cleaning unit 220 is increased, so that the cleaning efficiency is improved. In one embodiment, the bubble supply unit 250 supplies nanobubbles to the first cleaning liquid 222 in order to further improve the cleaning efficiency. Nanobubbles refer to bubbles with an average bubble diameter of less than 1 μm. The first cleaning liquid 222 can be activated by using nanobubbles. Moreover, generation of sludge in the first cleaning liquid 222 can be suppressed by using nanobubbles. Note that the function of the bubble supply unit 250 is not limited to the function of supplying nanobubbles as long as the function of increasing the contact area between the first cleaning liquid 222 and the gas to be deodorized is provided. As one embodiment, the bubble supply unit 250 may supply microbubbles or millibubbles to the first cleaning liquid 222 or may supply bubbles in which these bubbles are mixed.

  The type of gas supplied by the bubble supply unit 250 is not particularly limited. For example, the bubble supply unit 250 may supply air. On the other hand, the bubble supply unit 250 can mix a gas having an effect of adjusting the liquidity of the first cleaning liquid 222 into the first cleaning liquid 222. An example of such a gas is an acidic gas such as carbon dioxide. By adjusting the liquid property of the first cleaning liquid 222, it is possible to improve the removal efficiency of odor components. For example, the pH of the first cleaning liquid 222 increases when the basic component is absorbed, but the removal efficiency of the basic component can be improved by lowering the pH of the first cleaning liquid 222 using an acidic gas. it can. In particular, when hypochlorous acid water is used as the first cleaning liquid 222 or the second cleaning liquid, the deodorizing activity can be improved by reducing the pH of the first cleaning liquid 222 using an acidic gas. Further, the bubble supply unit 250 can mix a gas having a deodorizing action into the first cleaning liquid 222. Examples of such a gas include ozone. That is, when the gas to be deodorized contains ammonia and hypochlorous acid water is used for the first cleaning liquid 222, it is preferable to use an acidic gas for the bubbles. In such a configuration, it is possible to increase the gas-liquid contact while suppressing the pH of the first cleaning liquid 222 after the deodorizing process.

  The specific configuration of the bubble supply unit 250 is not particularly limited. 2A and 2B show an example of a specific configuration of the bubble supply unit 250. FIG. In these examples, the bubble supply unit 250 includes a circulation path 251 including an inflow port 253 and an outflow port 254, and a discharge unit 252 that mixes bubbles into the first cleaning liquid 222 in the circulation path 251. Yes. The first cleaning liquid 222 stored in the cleaning section 220 flows into the circulation path 251 from the cleaning section 220 via the inflow port 253 that is a connection portion between the circulation path 251 and the cleaning section 220. Further, from the circulation path 251, the first cleaning liquid 222 that has flowed in is supplied again to the cleaning section 220 through an outlet 254 that is a connection portion between the circulation path 251 and the cleaning section 220. According to such a configuration, the first cleaning liquid 222 can be stirred.

  Wet deodorization apparatus 200A, B may have a further configuration. For example, the wet deodorization apparatuses 200 </ b> A and 200 </ b> B may have a charging unit 270 for charging the first cleaning liquid 222. In addition, the wet deodorization apparatuses 200A and 200B may have an outlet 254 through which the first cleaning liquid 222 flows out. In one embodiment, the amount of the first cleaning liquid 222 is limited by the outlet 280. That is, even if the second cleaning liquid is mixed, the first cleaning liquid 222 flows out from the outlet 280 as an overflow, so that the amount of the first cleaning liquid 222 is kept constant. Furthermore, the wet deodorization apparatuses 200A and 200B may have a discharge port 290 at the bottom. The sludge accumulated in the wet deodorizing apparatuses 200A and 200B can be discharged through the discharge port 290. Furthermore, as shown in FIG. 2B, in order to improve the gas-liquid contact efficiency, a filler 295 may be provided at a location where the second cleaning liquid is sprayed and the gas to be deodorized passes.

  Above, description regarding the schematic block diagram of the deodorizing apparatus 200 shown in FIG. 2 is complete | finished.

  Hereinafter, the hardware configuration of the information processing apparatus 100 illustrated in FIG. 1 will be described with reference to FIG.

  As illustrated in FIG. 3, the information processing apparatus 100 includes a central processing unit (CPU) 301, a random access memory (RAM) 302, a read only memory (ROM) 303, an input controller 305, and a video controller 306 via a system bus 304. The memory controller 307, the communication I / F controller 308, etc. are connected.

  The CPU 301 comprehensively controls each device and controller connected to the system bus 304.

  Further, the ROM 303 or the external memory 311 (corresponding to a storage unit) realizes a function executed by each server or each PC, such as a BIOS (Basic Input / Output System) or an OS (Operating System) that is a control program of the CPU 301. Various programs to be described later are stored. Further, information necessary for carrying out the present invention is stored. The external memory may be a database.

  A RAM 302 (corresponding to a storage unit) functions as a main memory, work area, and the like of the CPU 301. The CPU 301 implements various operations by loading a program or the like necessary for executing the processing from the ROM 303 or the external memory 311 to the RAM 302 and executing the loaded program.

  The input controller 305 controls input from a keyboard (KB) 309 or a pointing device such as a mouse (not shown).

  The video controller 306 controls display on a display device such as the display 310. The display device may be a display device such as a liquid crystal display. These are used by the administrator as needed.

  The memory controller 307 is an external storage device (hard disk (HD)), flexible disk (FD), or PCMCIA (Personal Computer) that stores a boot program, various applications, font data, user files, editing files, various data, and the like. Controls access to an external memory 311 (corresponding to storage means) such as a Compact Flash (registered trademark) memory connected to a Memory Card International Association (Card Memory) card slot via an adapter.

  The communication I / F controller 308 connects and communicates with an external device via a network, and executes communication control processing on the network. For example, communication using TCP / IP (Transmission Control Protocol / Internet Protocol) is possible. In the present embodiment, the generator 110 and the wet deodorizing apparatus 200 are communicably connected via a network, but may be connected by a wired cable or the like.

  The CPU 301 can display on the display 310 by executing outline font rasterization processing on a display information area in the RAM 302, for example. Further, the CPU 301 enables a user instruction using a mouse cursor (not shown) on the display 310.

  Various programs to be described later for realizing the present invention are recorded in the external memory 311 and are executed by the CPU 301 by being loaded into the RAM 302 as necessary.

  This is the end of the description regarding the hardware configuration of the information processing apparatus 100 illustrated in FIG. 3. The above configuration is an example, and can be appropriately changed according to the purpose and application.

  Hereinafter, a block diagram illustrating an example of a module configuration of the information processing apparatus 100 illustrated in FIG. 1 will be described with reference to FIG.

  The information processing apparatus 100 includes a first acquisition unit 401, a specifying unit 402, and a second acquisition unit 403.

  The first acquisition unit 401 is a functional unit that performs control so as to acquire meteorological information of air including gas after cleaning by the cleaning device.

  The specifying unit 402 is a functional unit that controls to specify a parameter corresponding to the weather information acquired by the first acquiring unit 401. Furthermore, the specifying unit 402 is a functional unit that controls to specify parameters corresponding to the weather information acquired by the first acquiring unit 401 and the physical quantity acquired by the second acquiring unit 403.

  The second acquisition unit 403 is a functional unit that performs control so as to acquire a physical quantity of air including gas after cleaning by the cleaning device.

  This is the end of the description of the module configuration of the information processing apparatus 100 illustrated in FIG.

  The deodorizing method according to this embodiment will be described with reference to the flowchart of FIG. This deodorization method can be realized using, for example, the wet deodorization apparatus according to the above-described embodiment, but other wet deodorization apparatuses can also be used.

  In step S501, the gas to be deodorized is guided to a cleaning unit that performs cleaning with the first cleaning liquid. For example, the gas to be deodorized can be introduced into the cleaning unit 220 from the odor inflow unit 150. In step S502, gas bubbles different from the gas to be deodorized are mixed with the first cleaning liquid. For example, the bubble supply unit 250 can mix bubbles with the first cleaning liquid 222. In step S503, the gas that has been cleaned with the first cleaning liquid 222 is guided out of the cleaning section. For example, the gas cleaned in the cleaning unit 220 can be led out to the odor outflow unit 160.

  Above, description about the flowchart of the deodorizing method shown in FIG. 5 is complete | finished.

  Hereinafter, the control process of the deodorization system will be described.

  In the present embodiment, in the wet deodorizing apparatus, the deodorizing system, and the deodorizing method as described above, the wind speed and direction around the cleaning apparatus 200 (corresponding to weather information) in order to deodorize the odor with an appropriate cleaning ability. And controlling the concentration and flow rate of hypochlorous acid water according to the wind speed (corresponding to the wind speed information) and the wind direction (corresponding to the wind direction information). In the following first to sixth embodiments, the cleaning liquid is hypochlorous acid water, and the raw material of the cleaning liquid is sodium hypochlorite, water, and carbon dioxide gas, but the cleaning liquid and the raw material of the cleaning liquid are of course only examples. . Moreover, the structure of the wet deodorizing apparatus is only an example. Hypochlorous acid water may be directly supplied from the generation device 110 to the cleaning device 200 without providing the storage container 120.

<First Embodiment>
Hereinafter, the concentration control process of hypochlorous acid water using the wind direction sensor 202 in the first embodiment of the present invention will be described with reference to FIG.

  In the first embodiment, based on the value of the wind direction sensor 202, the flow rate of sodium hypochlorite supplied to the generating device, the flow rate of dilution water supplied to the generating device, and the carbonic acid supplied to the cleaning device. Chlorine concentration control of hypochlorous acid water is performed by changing the setting with the gas flow rate.

  Specifically, the set value of the flow rate of the raw material for generating hypochlorous acid water corresponding to the wind direction measured by the wind direction sensor 202 is specified. The first raw material valve 181 between the first raw material container 101 in which sodium hypochlorite is stored and the production device 110 is produced so as to produce hypochlorous acid water at the specified set value. By controlling 110, the chlorine concentration of hypochlorous acid water can be controlled. In general, there is a correlation between the chlorine concentration of hypochlorous acid water and the cleaning ability of hypochlorous acid water. The higher the chlorine concentration of hypochlorous acid water, the higher the cleaning ability of hypochlorous acid water. Becomes higher.

  A specific example will be described with reference to a diagram showing the relationship between the cleaning device 200 and a house shown in FIG. For example, as shown in FIG. 18, it is assumed that there is a house on the east side of the cleaning apparatus 200 and wind of 270 ° is measured by the wind direction sensor 202. 270 ° is an orientation when the wind direction is indicated by 360 orientations. A wind of 270 ° is a west wind when it is corrected to 16 directions, and indicates a wind blowing from the west. When the wind is directed toward the house from the cleaning device 200, the gas that flows out from the odor outflow part may cause discomfort to the residents. As shown in FIG. 18, when there is a house on the east side of the cleaning device 200 and a wind of 270 ° is blowing, by changing the concentration of hypochlorous acid water and increasing the cleaning capacity, Discomfort due to odor given to residents can be reduced.

  That is, in the present embodiment, by controlling the chlorine concentration of hypochlorous acid water according to the wind direction, hypochlorous acid water having a cleaning ability according to the wind direction can be supplied to the cleaning device.

  In step S601, the CPU 301 of the information processing apparatus 100 acquires the wind direction from the wind direction sensor 202 (corresponding to a first acquisition unit).

  In step S602, the CPU 301 of the information processing apparatus 100 reads the density change mode (1) table 1200 shown in FIG.

  FIG. 12 is a density change mode (1) table 1200 used for mode setting in the first embodiment of the present invention. The wind direction condition 1201 is a condition of the wind direction when setting each mode as described below. The mode 1202 is a mode provided based on the wind direction condition 1201 in the embodiment of the present invention, and the chlorine concentration (corresponding to a parameter) of hypochlorous acid water supplied to the cleaning device is also described. Yes. The set value 1203 is a set value (corresponding to a parameter) of the flow rate of the raw material for generating hypochlorous acid water corresponding to each mode. The flow rate 1204 of sodium hypochlorite supplied to the generator, the flow rate 1205 of dilution water supplied to the generator, and the flow rate 1206 of carbon dioxide supplied to the generator are used to generate hypochlorous acid water, respectively. The flow rate of the raw material.

  In step S603, the CPU 301 of the information processing apparatus 100 reads the setting value 1203 corresponding to the wind direction condition 1201 satisfied by the wind direction acquired in step S601, and the wind direction condition 1201 of the density change mode (1) table 1200 read in step S602. It is specified with reference (corresponding to the specifying means). For example, when the wind direction acquired in step S601 is 270 °, the wind direction is included in 260 ° or more and less than 280 °. That is, when the acquired wind direction is 270 °, the wind direction satisfies the wind direction condition 1201 of “260 ° or more and less than 280 °”, and therefore the setting value 1203 corresponding to the wind direction is stored in the generation device. The flow rate 1204 of sodium hypochlorite supplied is 12.01 mL / min, the flow rate 1205 of dilution water supplied to the generator is 10 L / min, and the flow rate 1206 of carbon dioxide gas supplied to the generator is 10 L / min. Identified. In this case, the mode is the powerful treatment A mode, and the mode is set such that the chlorine concentration of the hypochlorous acid water generated by the generating device, that is, the hypochlorous acid water supplied to the cleaning device is 1200 ppm. It is.

  In step S <b> 604, the CPU 301 of the information processing apparatus 100 transmits the setting value 1203 specified in step S <b> 603 to the CPU 301 of the generation apparatus 110.

  In step S605, the CPU 301 of the generation apparatus 110 receives the setting value 1203 transmitted in step S604.

  In step S606, the CPU 301 of the generating apparatus 110 controls the first raw material valve 181 so as to generate hypochlorous acid water with the set value 1203 received in step S605. The first raw material valve 181 is a valve between the first raw material container 101 in which sodium hypochlorite is stored and the generation device 110. By controlling the first raw material valve 181, the flow rate 1206 of sodium hypochlorite supplied to the generator can be changed. That is, the concentration of hypochlorous acid water generated by the generator can be changed.

  As described above, by controlling the flow rate of the raw material of hypochlorous acid water generated by the generating device with the set value based on the wind direction, it is possible to reduce discomfort due to odors given to neighboring residents. .

  The above is the description regarding the first embodiment of the present invention. In the first embodiment, the information processing apparatus 100 supplies hypochlorous acid water having a cleaning capability according to the wind direction to the cleaning apparatus by controlling the chlorine concentration of the hypochlorous acid water according to the wind direction. Can be controlled.

<Second Embodiment>
Hereinafter, the flow control process of hypochlorous acid water using the wind direction sensor 202 in the second embodiment of the present invention will be described with reference to FIG.

  In 2nd Embodiment, based on the value of the wind direction sensor 202, the flow volume of sodium hypochlorite supplied to a production | generation apparatus, the flow volume of the dilution water supplied to a production | generation apparatus, and the carbonic acid supplied to a washing | cleaning apparatus. By changing the setting with the gas flow rate, the flow rate control of the hypochlorous acid water supplied to the cleaning device is performed.

  Specifically, the set value of the flow rate of the raw material for generating hypochlorous acid water corresponding to the wind direction measured by the wind direction sensor 202 is specified. By controlling the first raw material valve 181, the second raw material valve 182, and the cleaning liquid valve 190 so as to supply hypochlorous acid water at the specified set value, the hypochlorous acid water supplied to the cleaning device is controlled. The flow rate can be controlled.

  In general, there is a correlation between the concentration of hypochlorous acid water and the cleaning ability of hypochlorous acid water. The contact efficiency is improved and the cleaning ability is improved.

  For example, as shown in FIG. 18, when wind of 270 ° is measured by the wind direction sensor 202, the flow rate of hypochlorous acid water is changed and the cleaning ability is increased, so that Can reduce the discomfort caused by odors.

  That is, in this embodiment, by controlling the flow rate of hypochlorous acid water supplied to the cleaning device according to the wind direction, hypochlorous acid water having a cleaning capability according to the wind direction is supplied to the cleaning device. be able to.

  Hereinafter, with respect to the second embodiment, description of parts having the same system configuration, hardware configuration, and module configuration as those of the above-described first embodiment will be omitted, and parts different from those of the first embodiment will be described. To do.

  Since the content of the process of step S601 is the same as that of the first embodiment, description thereof is omitted.

  In step S <b> 701, the CPU 301 of the information processing apparatus 100 reads the flow rate change mode (1) table 1300 shown in FIG. 13 stored in the information processing apparatus 100.

  FIG. 13 is a flow rate change mode (1) table 1300 used for mode setting in the second embodiment of the present invention. The flow rate change mode (1) table 1300 includes a wind direction condition 1201, a mode 1202, a set value 1203, a sodium hypochlorite flow rate 1204 supplied to the generating device, a flow rate 1205 of dilution water supplied to the generating device, and a generating device. It is comprised with the flow volume 1206 of the carbon dioxide gas supplied to. The mode 1202 is a mode provided based on the wind direction condition 1201 in the embodiment of the present invention, and the flow rate (corresponding to the parameter) of hypochlorous acid water supplied to the cleaning device is also described. .

  In step S702, the CPU 301 of the information processing apparatus 100 sets the setting value 1203 corresponding to the wind direction condition 1201 that the wind direction acquired in step S601 satisfies, and the wind direction condition 1201 of the flow rate change mode (1) table 1300 read in step S701. It is specified with reference (corresponding to the specifying means). For example, when the wind direction acquired in step S601 is 270 °, the wind direction is included in 260 ° or more and less than 280 °. In other words, when the acquired wind direction is 270 °, the wind direction satisfies the wind direction condition 1201 of “260 ° or more and less than 280 °”, and therefore the setting value 1203 corresponding to the wind direction is stored in the generation device. The flow rate 1204 of sodium hypochlorite supplied is 12.01 mL / min, the flow rate 1205 of dilution water supplied to the generator is 12 L / min, and the flow rate 1206 of carbon dioxide gas supplied to the generator is 10 L / min. Identified. In this case, the mode is a powerful processing B mode, which is a mode set so that the flow rate of hypochlorous acid water supplied to the cleaning device is 12 L / min.

  In step S703, the CPU 301 of the information processing apparatus 100 transmits the setting value 1203 specified in step S702 to the CPU 301 of the generation apparatus 110.

  In step S704, the CPU 301 of the generation apparatus 110 receives the setting value 1203 transmitted in step S703.

  In step S705, the CPU 301 of the generation apparatus 110 supplies the first raw material valve 181, the second raw material valve 182, and the cleaning liquid valve 190 so as to supply hypochlorous acid water to the cleaning apparatus 200 with the setting value 1203 received in step S704. To control. By controlling the first raw material valve 181, the second raw material valve 182, and the cleaning liquid valve 190, the flow rate of hypochlorous acid water supplied to the cleaning device can be controlled.

  This completes the description of the second embodiment of the present invention. In the second embodiment, by controlling the flow rate of hypochlorous acid water according to the wind direction, hypochlorous acid water having a cleaning ability according to the wind direction can be supplied to the cleaning device.

<Third Embodiment>
Hereinafter, the concentration control process of hypochlorous acid water using the wind speed sensor 203 in the third embodiment of the present invention will be described with reference to FIG.

  In the third embodiment, based on the value of the wind speed sensor 203, the flow rate of sodium hypochlorite supplied to the generating device, the flow rate of dilution water supplied to the generating device, and the carbonic acid supplied to the cleaning device. Chlorine concentration control of hypochlorous acid water is performed by changing the setting with the gas flow rate.

  Specifically, the set value of the flow rate of the raw material for generating hypochlorous acid water corresponding to the wind speed measured by the wind speed sensor 203 is specified. The first raw material valve 181 between the first raw material container 101 in which sodium hypochlorite is stored and the production device 110 is produced so as to produce hypochlorous acid water at the specified set value. By controlling 110, the chlorine concentration of hypochlorous acid water can be controlled. As shown in the first embodiment, generally, there is a correlation between the chlorine concentration of hypochlorous acid water and the cleaning ability of the hypochlorous acid water, and the chlorine concentration of hypochlorous acid water is high. The higher the cleaning ability of hypochlorous acid water is.

  As a specific example, for example, it is assumed that there is a house around the cleaning apparatus 200 and a wind of 15 m / s is measured by the wind speed sensor 203. When wind of 15 m / s is measured, depending on the positional relationship between the cleaning device 200 and the house, the gas that flows out from the odor outflow portion 160 may cause discomfort to the residents. Considering the distance between the cleaning device 200 and the house in advance, and reducing the discomfort due to odors given to neighboring residents by increasing the cleaning ability with hypochlorous acid water when the wind speed is high Can do.

  That is, in this embodiment, hypochlorous acid water having a cleaning ability corresponding to the wind direction can be supplied to the cleaning device by controlling the chlorine concentration of the hypochlorous acid water according to the wind speed.

  In step S801, the CPU 301 of the information processing apparatus 100 acquires the wind speed from the wind speed sensor 203 (corresponding to a first acquisition unit).

  In step S <b> 802, the CPU 301 of the information processing apparatus 100 reads the density change mode (2) table 1400 shown in FIG. 14 stored in the information processing apparatus 100.

  FIG. 14 is a density change mode (2) table 1400 used for mode setting in the third embodiment of the present invention. Concentration change mode (2) table 1400 includes wind speed condition 1401, mode 1202, set value 1203, sodium hypochlorite flow rate 1204 supplied to the generator, dilution water flow rate 1205 supplied to the generator, and generator. It is comprised with the flow volume 1206 of the carbon dioxide gas supplied to. The wind speed condition 1401 is a condition of wind speed when setting each mode. The mode 1202 is a mode provided based on the wind speed condition 1401 in the embodiment of the present invention, and the chlorine concentration (corresponding to the parameter) of hypochlorous acid water supplied to the cleaning device is also described. Yes.

  In step S803, the CPU 301 of the information processing apparatus 100 reads the setting value 1203 corresponding to the wind speed condition 1401 that is satisfied by the wind speed acquired in step S801, and the wind speed condition 1401 of the density change mode (2) table 1400 read in step S802. It is specified with reference (corresponding to the specifying means). For example, when the wind speed acquired in step S801 is 15 m / s, the wind speed is included in 10 m / s or more. That is, when the acquired wind speed is 15 m / s, the wind speed satisfies “10 m / s”, and thus the set value 1203 corresponding to the wind speed is hypochlorous acid supplied to the generator. The flow rate 1204 of sodium acid is specified as 12.01 mL / min, the flow rate 1205 of dilution water supplied to the generator is 10 L / min, and the flow rate 1206 of carbon dioxide gas supplied to the generator is specified as 10 L / min. In this case, the mode is the strong processing C mode, and is a mode in which the chlorine concentration of hypochlorous acid water generated by the generator, that is, the chlorine concentration of hypochlorous acid water supplied to the cleaning device is set to 1200 ppm. It is.

  In step S804, the CPU 301 of the information processing apparatus 100 transmits the setting value 1203 specified in step S803 to the CPU 301 of the generation apparatus 110.

  In step S805, the CPU 301 of the generation apparatus 110 receives the setting value 1203 transmitted in step S804.

  In step S806, the CPU 301 of the generation apparatus 110 controls the first raw material valve 181 so as to generate hypochlorous acid water with the set value 1203 received in step S805. By controlling the first raw material valve 181, the flow rate 1206 of sodium hypochlorite supplied to the generator can be changed. That is, the concentration of hypochlorous acid water generated by the generator can be changed.

  Thus, by controlling the flow rate of the raw material of hypochlorous acid water generated by the generating device with the set value based on the wind speed, it is possible to reduce discomfort due to odor given to neighboring residents. .

The above is the description regarding the third embodiment of the present invention. In the third embodiment, by controlling the chlorine concentration of hypochlorous acid water according to the wind speed, hypochlorous acid water having a cleaning ability according to the wind direction can be supplied to the cleaning device.
<Fourth Embodiment>
Hereinafter, the flow control process of hypochlorous acid water using the wind speed sensor 203 in the fourth embodiment of the present invention will be described with reference to FIG.

  In 4th Embodiment, based on the value of the wind speed sensor 203, the flow volume of sodium hypochlorite supplied to a production | generation apparatus, the flow volume of the dilution water supplied to a production | generation apparatus, and the carbonic acid supplied to a washing | cleaning apparatus. By changing the setting with the gas flow rate, the flow rate control of the hypochlorous acid water supplied to the cleaning device is performed.

  Specifically, the set value of the flow rate of the raw material for generating hypochlorous acid water corresponding to the wind speed measured by the wind speed sensor 203 is specified. By controlling the first raw material valve 181, the second raw material valve 182, and the cleaning liquid valve 190 so as to supply hypochlorous acid water at the specified set value, the hypochlorous acid water supplied to the cleaning device is controlled. The flow rate can be controlled. As shown in the second embodiment, by increasing the flow rate of the hypochlorous acid water, the contact efficiency between the object to be cleaned and the hypochlorous acid water is improved, and the cleaning ability is enhanced.

  For example, as in the third embodiment, it is assumed that there is a house around the cleaning apparatus 200 and wind of 15 m / s is measured by a wind speed sensor. In consideration of the positional relationship between the cleaning device 200 and the house in advance, when the wind speed is high, the cleaning ability with hypochlorous acid water is increased, thereby reducing discomfort due to odor given to neighboring residents. be able to.

  That is, in this embodiment, hypochlorous acid water having a cleaning ability corresponding to the wind direction can be supplied to the cleaning device by controlling the flow rate of the hypochlorous acid water according to the wind speed.

  Hereinafter, with respect to the fourth embodiment, description of parts having the same system configuration, hardware configuration, and module configuration as those of the above-described third embodiment will be omitted, and parts different from those of the third embodiment will be described. To do.

  Since the content of the process of step S801 is the same as that of 3rd Embodiment, description is abbreviate | omitted.

  In step S <b> 901, the CPU 301 of the information processing apparatus 100 reads the flow rate change mode (2) table 1500 illustrated in FIG. 15 stored in the information processing apparatus 100.

  FIG. 15 is a flow rate change mode (2) table 1500 used for mode setting in the fourth embodiment of the present invention. The flow rate change mode (2) table 1500 includes a wind speed condition 1401, a mode 1202, a set value 1203, a sodium hypochlorite flow rate 1204 supplied to the generator, a flow rate 1205 of dilution water supplied to the generator, and a generator. It is comprised with the flow volume 1206 of the carbon dioxide gas supplied to. The mode 1202 is a mode provided based on the wind speed condition 1401 in the embodiment of the present invention, and the flow rate (corresponding to the parameter) of hypochlorous acid water supplied to the cleaning device is also described. .

  In step S902, the CPU 301 of the information processing apparatus 100 reads the setting value 1203 corresponding to the wind speed condition 1401 that the wind speed acquired in step S801 satisfies, and the wind speed condition 1401 of the flow rate change mode (2) table 1500 read in step S901. It is specified with reference (corresponding to the specifying means). For example, when the wind speed acquired in step S801 is 15 m / s, the wind speed is included in 10 L / min. That is, when the acquired wind speed is 15 m / s, the wind speed satisfies “10 m / s”, and thus the set value 1203 corresponding to the wind speed is hypochlorous acid supplied to the generator. The flow rate 1204 of sodium acid is specified as 12.01 mL / min, the flow rate 1205 of dilution water supplied to the generator is 12 L / min, and the flow rate 1206 of carbon dioxide gas supplied to the generator is specified as 10 L / min. In this case, the mode is a powerful processing D mode, which is a mode set so that the flow rate of hypochlorous acid water supplied to the cleaning device is 12 L / min.

  In step S <b> 903, the CPU 301 of the information processing apparatus 100 transmits the setting value 1203 specified in step S <b> 902 to the CPU 301 of the generation apparatus 110.

  In step S904, the CPU 301 of the generation apparatus 110 receives the setting value 1203 transmitted in step S903.

  In step S905, the CPU 301 of the generation apparatus 110 supplies the first raw material valve 181, the second raw material valve 182, and the cleaning liquid valve 190 so as to supply hypochlorous acid water to the cleaning apparatus 200 with the setting value 1203 received in step S904. To control. By controlling the first raw material valve 181, the second raw material valve 182, and the cleaning liquid valve 190, the flow rate of hypochlorous acid water supplied to the cleaning device can be controlled.

  Thus, by controlling the flow rate of the raw material of hypochlorous acid water supplied to the cleaning device with the set value based on the wind speed, it is possible to reduce discomfort due to odor given to neighboring residents. .

  The above is the description regarding the fourth embodiment of the present invention. In the fourth embodiment, by controlling the flow rate of hypochlorous acid water according to the wind speed, hypochlorous acid water having a cleaning ability according to the wind direction can be supplied to the cleaning device.

<Fifth Embodiment>
Hereinafter, the concentration control process of hypochlorous acid water using the wind direction sensor 202 and the ammonia concentration measuring device 204 in the first embodiment of the present invention will be described with reference to FIG.

  In 5th Embodiment, based on the value measured with the wind direction sensor 202 and the ammonia concentration measuring apparatus 204, the flow volume of sodium hypochlorite supplied to a production | generation apparatus, and the dilution water supplied to a production | generation apparatus Chlorine concentration control of hypochlorous acid water is performed by changing the setting of the flow rate and the flow rate of the carbon dioxide gas supplied to the cleaning device. Focusing on ammonia as one of the representative examples of odor, measurement of ammonia concentration (corresponding to physical quantity) is taken in.

  Specifically, a setting value relating to the chlorine concentration of hypochlorous acid water corresponding to the wind direction and the ammonia concentration measured by the wind direction sensor 202 and the ammonia concentration measuring device 204 is specified. By controlling the first raw material valve 181 so as to generate hypochlorous acid water at the specified set value, the chlorine concentration of the hypochlorous acid water can be controlled. In general, there is a correlation between the chlorine concentration of hypochlorous acid water and the cleaning ability of hypochlorous acid water. The higher the chlorine concentration of hypochlorous acid water, the higher the cleaning ability of hypochlorous acid water. Becomes higher.

  In the first embodiment, the chlorine concentration control process of hypochlorous acid water using the wind direction sensor 202 has been described. In the fifth embodiment, by using the ammonia concentration measuring device 204 in addition to the wind direction sensor 202 used in the first embodiment, the chlorine concentration control process of hypochlorous acid water can be appropriately performed without waste. Specifically, when the wind direction sensor 202 measures the wind in the direction from the cleaning device 200 toward the house, and when the wind direction sensor 202 measures the wind in the direction from the house toward the cleaning device 200, the same ammonia concentration is obtained. Assume a measurement. When the ammonia concentration of the same degree is measured, the process of increasing the chlorine concentration of hypochlorous acid water is performed when the wind in the direction from the cleaning device 200 toward the house is measured.

  That is, in this embodiment, by controlling the chlorine concentration of hypochlorous acid water according to the wind direction and ammonia concentration, hypochlorous acid water having a cleaning ability according to the wind direction and ammonia concentration is supplied to the cleaning device. Can be supplied.

  In step S1001, the CPU 301 of the information processing apparatus 100 acquires the wind direction from the wind direction sensor 202 and the ammonia concentration from the ammonia concentration measuring device 204 (corresponding to a first acquisition unit and a second acquisition unit).

  In step S1002, the CPU 301 of the information processing apparatus 100 reads the density change mode (3) table 1600 shown in FIG.

  FIG. 16 is a density change mode (3) table 1600 used for mode setting in the fifth embodiment of the present invention. Concentration change mode (3) table 1600 includes a wind direction condition 1201, an ammonia concentration condition 1601, a mode 1202, a set value 1203, a sodium hypochlorite flow rate 1204 supplied to the generator, and a dilution water supplied to the generator. The flow rate is 1205, and the flow rate is 1206 of carbon dioxide gas supplied to the generator. The ammonia concentration condition 1601 is a condition of ammonia concentration when setting each mode as described below. The mode 1202 is a mode provided based on the wind direction condition 1201 and the ammonia concentration condition 1601 in the embodiment of the present invention, and the chlorine concentration (corresponding to a parameter) of hypochlorous acid water supplied to the cleaning device. Is also described.

  In step S1003, the CPU 301 of the information processing apparatus 100 reads the setting value 1203 corresponding to the wind direction condition 1201 and the ammonia concentration condition 1601 that are satisfied by the wind direction and the ammonia concentration acquired in step S1001, and the concentration change mode ( 3) Specify with reference to the wind direction condition 1201 and the ammonia concentration condition 1601 in the table 1600 (corresponding to the specifying means). For example, when the wind direction acquired in step S1001 is 270 ° and the ammonia concentration is 150 ppm, the wind direction is included in 260 ° or more and less than 280 °, and the ammonia concentration is included in 100 ppm or more. That is, when the obtained wind direction is 260 ° or more and less than 280 ° and the ammonia concentration is 100 ppm or more, the wind direction satisfies the wind direction condition 1201 of “260 ° or more and less than 280 °”, and the ammonia concentration Satisfies the ammonia concentration condition 1601 of “100 ppm or more”, the set value 1203 corresponding to the wind direction and the ammonia concentration is set to a flow rate of sodium hypochlorite 1204 supplied to the generator of 13.02 mL / min. The flow rate 1205 of the dilution water supplied to the generator is specified as 10 L / min, and the flow rate 1206 of the carbon dioxide gas supplied to the generator is specified as 10 L / min. In this case, the mode is an ultra-strong treatment a mode, and is installed such that the chlorine concentration of hypochlorous acid water generated by the generator, that is, the hypochlorous acid water supplied to the cleaning device is 1300 ppm. Mode.

  In step S <b> 1004, the CPU 301 of the information processing apparatus 100 transmits the setting value 1203 specified in step S <b> 1003 to the CPU 301 of the generation apparatus 110.

  In step S1005, the CPU 301 of the generation apparatus 110 receives the setting value 1203 transmitted in step S1004.

  In step S1006, the CPU 301 of the generation apparatus 110 controls the first raw material valve 181 so as to generate hypochlorous acid water with the setting value 1203 received in step S1005. By controlling the first raw material valve 181, the flow rate 1206 of sodium hypochlorite supplied to the generator can be changed. That is, the concentration of hypochlorous acid water generated by the generator can be changed.

  In this way, by controlling the flow rate of the raw material of hypochlorous acid water generated by the generator with a set value based on the wind direction and ammonia concentration, the discomfort due to odor given to neighboring residents is reduced. Can be made.

  The above is the description regarding the fifth embodiment of the present invention. In the fifth embodiment, by controlling the chlorine concentration of hypochlorous acid water according to the wind direction and the ammonia concentration, hypochlorous acid water having a cleaning ability according to the wind direction and the ammonia concentration is supplied to the cleaning device. Can be supplied.

<Sixth Embodiment>
Hereinafter, the flow control process of hypochlorous acid water using the wind direction sensor 202 and the ammonia concentration measuring device 204 in the sixth embodiment of the present invention will be described with reference to FIG.

  In 6th Embodiment, based on the value measured with the wind direction sensor 202 and the ammonia concentration measuring apparatus 204, the flow volume of sodium hypochlorite supplied to a production | generation apparatus, and the dilution water supplied to a production | generation apparatus Chlorine concentration control of hypochlorous acid water is performed by changing the setting of the flow rate and the flow rate of the carbon dioxide gas supplied to the cleaning device. Focusing on ammonia as one of the representative examples of odor, measurement of ammonia concentration is taken in.

  Specifically, a setting value relating to the flow rate of hypochlorous acid water supplied to the cleaning device corresponding to the wind direction and the ammonia concentration measured by the wind direction sensor 202 and the ammonia concentration measuring device 204 is specified. Hypochlorous acid supplied to the cleaning device is controlled by controlling the first raw material valve 181, the second raw material valve 182, and the cleaning liquid valve 190 so as to supply hypochlorous acid water to the cleaning device at the specified set value. The flow rate of the acid water can be controlled.

  In the second embodiment, the flow control process of hypochlorous acid water using the wind direction sensor 202 has been described. In the sixth embodiment, by using the ammonia concentration measuring device 204 in addition to the wind direction sensor 202 used in the second embodiment, the flow control process of hypochlorous acid water can be appropriately performed without waste. Specifically, when the wind direction sensor 202 measures the wind direction in the direction from the cleaning device 200 toward the house and when the wind direction in the direction from the house toward the cleaning device 200 is measured, the ammonia concentration is comparable. Assume a measurement. When the ammonia concentration of the same level is measured, the process of increasing the flow rate of hypochlorous acid water supplied to the cleaning device is performed when the direction of the wind from the cleaning device 200 toward the house is measured. become.

  That is, in this embodiment, hypochlorous acid having a cleaning ability according to the wind direction and the ammonia concentration is controlled by controlling the flow rate of hypochlorous acid water supplied to the cleaning device according to the wind direction and the ammonia concentration. Acid water can be supplied to the cleaning device.

  Since the content of the process of step S1001 is the same as that of the fifth embodiment, description thereof is omitted.

  In step S1101, the CPU 301 of the information processing apparatus 100 reads the flow rate change mode (3) table 1700 shown in FIG.

  FIG. 17 is a flow rate change mode (3) table 1700 used for mode setting in the sixth embodiment of the present invention. The flow rate change mode (3) table 1700 includes a wind direction condition 1201, an ammonia concentration condition 1601, a mode 1202, a set value 1203, a sodium hypochlorite flow rate 1204 supplied to the generator, and a dilution water supplied to the generator. The flow rate is 1205, and the flow rate is 1206 of carbon dioxide gas supplied to the generator. The mode 1202 is a mode provided based on the wind direction condition 1201 and the ammonia concentration condition 1601 in the embodiment of the present invention, and the flow rate (corresponding to the parameter) of hypochlorous acid water supplied to the cleaning device is also the mode 1202. It is also described.

  In step S1102, the CPU 301 of the information processing apparatus 100 reads the set value 1203 corresponding to the wind direction condition 1201 and the ammonia concentration condition 1601 that the wind direction and the ammonia concentration acquired in step S1001 satisfy, and the flow rate change mode read in step S1101. (3) Specify with reference to the wind direction condition 1201 and the ammonia concentration condition 1601 in the table 1700 (corresponding to the specifying means). For example, when the wind direction acquired in step S1001 is 270 ° and the ammonia concentration is 150 ppm, the wind direction is included in 260 ° or more and less than 280 °, and the ammonia concentration is included in 100 ppm or more. That is, when the obtained wind direction is 260 ° or more and less than 280 ° and the ammonia concentration is 100 ppm or more, the wind direction satisfies the wind direction condition 1201 of “260 ° or more and less than 280 °”, and the ammonia concentration Satisfies the ammonia concentration condition 1601 of “100 ppm or more”, the set value 1203 corresponding to the wind direction and the ammonia concentration is set to 15.02 mL / min, the flow rate of sodium hypochlorite 1204 supplied to the generator. The flow rate 1205 of the dilution water supplied to the generating device is specified as 15 L / min, and the flow rate 1206 of the carbon dioxide gas supplied to the generating device is specified as 10 L / min. In this case, the mode is an ultra-strong treatment b mode, which is a mode set so that the flow rate of hypochlorous acid water supplied to the generator is 15 L / min.

  In step S1103, the CPU 301 of the information processing apparatus 100 transmits the setting value 1203 specified in step S1102 to the CPU 301 of the generation apparatus 110.

  In step S1104, the CPU 301 of the generation apparatus 110 receives the setting value 1203 transmitted in step S1103.

  In step S1105, the CPU 301 of the generation apparatus 110 supplies the first raw material valve 181, the second raw material valve 182 and the cleaning liquid valve 190 so as to supply hypochlorous acid water to the cleaning apparatus 200 with the setting value 1203 received in step S1104. To control. By controlling the first raw material valve 181, the second raw material valve 182, and the cleaning liquid valve 190, the flow rate of hypochlorous acid water supplied to the cleaning device can be controlled.

  Thus, by controlling the flow rate of the raw material of hypochlorous acid supplied to the cleaning device with a set value based on the wind direction, it is possible to reduce discomfort due to odor given to neighboring residents. it can.

  The above is the description regarding the sixth embodiment of the present invention. In the sixth embodiment, by controlling the flow rate of hypochlorous acid water according to the wind direction and the ammonia concentration, hypochlorous acid water having a cleaning capability according to the wind direction and the ammonia concentration is supplied to the cleaning device. can do.

<Other embodiments>
In the first to sixth embodiments, the mechanism for supplying hypochlorous acid water having an appropriate cleaning capability to the cleaning apparatus using weather information such as the wind direction and the wind speed acquired from a sensor or the like has been described. Since weather information affects not only the wind direction and wind speed but also how odors spread, the weather information acquired by the CPU 301 of the information processing apparatus 100 includes weather, atmospheric pressure, humidity, precipitation, etc. indicating sunny or rainy conditions. Also good. Since the weather information to be acquired is not limited to the wind direction and the wind speed, hypochlorous acid water having a more appropriate cleaning ability can be supplied to the cleaning device.

  Although seven embodiments related to the present invention have been described above, the chlorine of hypochlorous acid water to be generated in consideration of a plurality of weather information such as a combination of the first embodiment and the third embodiment. The concentration may be determined. Further, in the fifth embodiment and the sixth embodiment, the wind direction sensor 202 and the ammonia concentration measuring device 204 are combined, but the wind speed sensor 203 may be combined, and not the wind direction sensor 202 but the wind speed sensor 203. May be used. In the concentration control and flow rate control of hypochlorous acid water, control was performed by changing the flow rate of each raw material and cleaning liquid. However, the change is not limited to the flow rate, and other amounts such as volume and weight can be changed. Good.

  In the six embodiments relating to the present invention, it is assumed that hypochlorous acid water having a chlorine concentration of usually about 1000 ppm is generated by the generator 110. When hypochlorous acid water having a chlorine concentration of about 1000 ppm is generated by the generator 110, the flow rate 1204 of sodium hypochlorite supplied to the generator is higher than the flow rate 1205 of dilution water supplied to the generator. It can be said that it is extremely small. Therefore, in this embodiment, the flow rate 1205 of the dilution water supplied to the production | generation apparatus and the flow rate of hypochlorous acid water supplied to a washing | cleaning apparatus are considered to be the same.

  For example, the dilution water flow rate 1205 supplied to the generation device is 10 L / min dilution water, the sodium hypochlorite flow rate 1204 supplied to the generation device is 10.01 mL / min sodium hypochlorite, It is assumed that hypochlorous acid water is generated by the generation device 110 by mixing with carbon dioxide gas. In this case, hypochlorous acid water having a chlorine concentration of 1000 ppm is generated by the generation device 110 and supplied to the cleaning device 200 at a flow rate of 10 L / min that is the same flow rate as the flow rate 1205 of the dilution water supplied to the generation device. It is considered to be done.

  The sensor and the measuring device may be provided in different places as long as the wind direction, wind speed, ammonia concentration, and the like of the air that can contain the gas cleaned by the cleaning device 200 can be acquired.

  Although the generation device 110 performs control of the valve, the generation device 110 such as the information processing device 100 or the storage container 120 may perform control. The valve controls the flow rate. However, the valve may not be a valve as long as the device can adjust the flow rate, such as a pump instead of a valve.

  Although three raw material containers are provided, the number of raw material containers may be changed depending on the type of cleaning liquid generated by the generation device 110 and the generation method. The number of valves may be changed according to the number of raw material containers.

  Although the object to be cleaned is exhausted from the compost production apparatus, there are various objects to be cleaned, such as air in the living room and cut vegetables. Although the cleaning liquid is hypochlorous acid water and the method of generating hypochlorous acid water is a carbon dioxide gas mixing method, other cleaning liquids and other generation methods may of course be used.

  Information included in tables and the like stored in the information processing apparatus 100 illustrated in FIGS. 12 to 17 is not limited to the values described in the table of the present embodiment. Further, the modes are not limited to the modes shown in FIGS. 12 to 17, and a larger number of modes may be provided, or the number of modes may be reduced. In addition, table items may be rewritten.

  In the second, fourth, and sixth embodiments, the first raw material valve 181, the second raw material valve 182, and the cleaning liquid valve 190 are controlled in order to change the flow rate of hypochlorous acid water. Controlling the cleaning liquid valve 190 may cause the hypochlorous acid water in the storage container 120 to overflow or the hypochlorous acid water to become insufficient. By controlling not only the cleaning liquid valve 190 but also the valves for controlling the supply of the raw materials such as the first raw material valve 181 and the second raw material valve 182, the hypochlorous acid water can be supplied without delay. Of course, the first material valve 181 and the second material valve 182 may not be controlled as necessary.

  Moreover, in 2nd, 4th, 6th embodiment, the flow volume of sodium hypochlorite supplied to a production | generation apparatus is very small compared with the flow volume of the dilution water supplied to a production | generation apparatus. Even when the flow rate of diluting water is controlled without controlling the flow rate of sodium hypochlorite, it may be considered that the chlorine concentration of hypochlorous acid water is fixed and only the flow rate is changed.

  Above, the description regarding the control process of a deodorizing system is complete | finished.

  As described above, according to the present invention, it is possible to provide a mechanism capable of specifying an appropriate cleaning capability while reducing the cost for cleaning.

  The present invention can be implemented as a system, apparatus, method, program, storage medium, or the like, and can be applied to a system including a plurality of devices. You may apply to the apparatus which consists of one apparatus. Note that the present invention includes a software program that implements the functions of the above-described embodiments directly or remotely from a system or apparatus. The present invention also includes a case where the information processing apparatus of the system or apparatus is achieved by reading and executing the supplied program code.

  Therefore, the program code itself installed in the information processing apparatus in order to realize the functional processing of the present invention with the information processing apparatus also realizes the present invention. That is, the present invention includes a computer program itself for realizing the functional processing of the present invention.

  In that case, as long as it has the function of a program, it may be in the form of object code, a program executed by an interpreter, script data supplied to the OS, and the like.

  Examples of the recording medium for supplying the program include a flexible disk, hard disk, optical disk, magneto-optical disk, MO, CD-ROM, CD-R, and CD-RW. In addition, there are magnetic tape, nonvolatile memory card, ROM, DVD (DVD-ROM, DVD-R), and the like.

  As another program supply method, a browser on a client computer is used to connect to an Internet home page. The computer program of the present invention itself or a compressed file including an automatic installation function can be supplied from the homepage by downloading it to a recording medium such as a hard disk.

  It can also be realized by dividing the program code constituting the program of the present invention into a plurality of files and downloading each file from a different homepage. That is, the present invention also includes a WWW server that allows a plurality of users to download a program file for realizing the functional processing of the present invention with an information processing apparatus.

  In addition, the program of the present invention is encrypted, stored in a storage medium such as a CD-ROM, distributed to users, and key information for decryption is downloaded from a homepage via the Internet to users who have cleared predetermined conditions. Let The downloaded key information can be used to execute the encrypted program and install it in the information processing apparatus.

  Further, the functions of the above-described embodiment are realized by the information processing apparatus executing the read program. In addition, based on the instructions of the program, the OS or the like operating on the information processing apparatus performs part or all of the actual processing, and the functions of the above-described embodiments can be realized by the processing.

  Further, the program read from the recording medium is written in a memory provided in a function expansion board inserted into the information processing apparatus or a function expansion unit connected to the information processing apparatus. Thereafter, the CPU of the function expansion board or function expansion unit performs part or all of the actual processing based on the instructions of the program, and the functions of the above-described embodiments are realized by the processing.

  The above-described embodiments are merely examples of implementation in carrying out the present invention, and the technical scope of the present invention should not be construed as being limited thereto. That is, the present invention can be implemented in various forms without departing from the technical idea or the main features thereof.

100 Information processing device 301 CPU
302 RAM
303 ROM
304 system bus 305 input controller 306 video controller 307 memory controller 308 communication I / F controller 309 keyboard 310 display 311 external memory

Claims (18)

An information processing apparatus that controls a generating apparatus that generates a cleaning liquid for cleaning a gas including a cleaning target with a cleaning apparatus,
Storage means for storing parameters relating to the cleaning ability of the cleaning liquid generated by the generating device;
First acquisition means for acquiring weather information of air containing the gas after being cleaned by the cleaning device;
An information processing apparatus comprising: specifying means for specifying the parameter stored in the storage means corresponding to the weather information acquired by the first acquisition means. A second acquisition means for acquiring a physical quantity of air containing the gas after being cleaned by the cleaning device;
The specifying means specifies the parameter stored in the storage means corresponding to the weather information acquired by the first acquisition means and the physical quantity acquired by the second acquisition means. The information processing apparatus according to claim 1.   The information processing apparatus according to claim 2, wherein the storage unit stores the parameter based on the weather information or the physical quantity.   The information processing apparatus according to claim 2, wherein the physical quantity is a concentration of a component contained in the cleaned gas.   The information processing apparatus according to claim 1, wherein the weather information is wind direction information.   The information processing apparatus according to claim 1, wherein the weather information is wind speed information.   The information processing apparatus according to claim 1, wherein the object to be cleaned is ammonia.   The information processing apparatus according to claim 1, wherein the cleaning liquid is hypochlorous acid water.   The information processing apparatus according to claim 1, wherein the parameter is a concentration of the cleaning liquid generated by the generation apparatus.   The information processing apparatus according to claim 1, wherein the parameter is an amount of a raw material for generating the cleaning liquid in the generation apparatus.   The information processing apparatus according to claim 1, wherein the parameter is an amount of the cleaning liquid supplied to the cleaning apparatus. An information processing apparatus that controls a generating apparatus that generates a cleaning liquid for cleaning a gas including a cleaning target with a cleaning apparatus, and a control method for the information processing apparatus that includes a storage unit that stores parameters relating to the cleaning ability of the cleaning liquid. There,
A first acquisition step of acquiring weather information of air containing the gas after being cleaned by the cleaning device;
And a specifying step of specifying the parameter stored in the storage unit corresponding to the weather information acquired in the first acquisition step. An information processing apparatus that controls a generation apparatus that generates a cleaning liquid for cleaning a gas including a cleaning target with a cleaning apparatus, and that can be executed by the information processing apparatus including a storage unit that stores parameters relating to the cleaning ability of the cleaning liquid A program,
The information processing apparatus;
First acquisition means for acquiring weather information of air containing the gas after being cleaned by the cleaning device;
A program executable by the information processing apparatus, wherein the program is caused to function as a specifying unit that specifies the parameter stored in the storage unit, corresponding to the weather information acquired by the first acquisition unit. A deodorizing system comprising: a generating device that generates a cleaning liquid; and a cleaning device that cleans a gas including an object to be cleaned using the cleaning liquid generated by the generating device,
Storage means for storing parameters relating to the cleaning ability of the cleaning liquid;
First acquisition means for acquiring weather information of air containing the gas after being cleaned by the cleaning device;
Specifying means for specifying the parameter stored in the storage means, corresponding to the weather information acquired by the first acquisition means,
A deodorizing system for controlling the cleaning device to clean the gas based on the parameter specified by the specifying means. A deodorizing system including a generation device that generates a cleaning liquid, and a cleaning device that cleans a gas including a cleaning target using the cleaning liquid generated by the generation device, and storage means that stores parameters relating to the cleaning ability of the cleaning liquid A control method for the deodorizing system comprising:
A first acquisition step of acquiring weather information of air containing the gas after being cleaned by the cleaning device;
Specifying the parameter stored in the storage means corresponding to the weather information acquired in the first acquisition step, and
A control method for a deodorizing system, wherein the cleaning device controls the gas to be cleaned based on the parameter specified in the specifying step. A cleaning device for cleaning a gas including a cleaning target with a cleaning liquid,
First acquisition means for acquiring weather information of air containing the gas after being cleaned by the cleaning device;
A cleaning device comprising: cleaning means for cleaning the gas with a cleaning ability determined based on the weather information acquired by the first acquisition means. A control method of a cleaning apparatus for cleaning a gas including a cleaning target with a cleaning liquid,
A first acquisition step of acquiring weather information of air containing the gas after being cleaned by the cleaning device;
A cleaning step of cleaning the gas with a cleaning capability determined based on the weather information acquired by the first acquisition step. A program that can be executed by a cleaning device that cleans a gas including a cleaning target with a cleaning liquid,
The cleaning device,
First acquisition means for acquiring weather information of air containing the gas after being cleaned by the cleaning device;
A program executable by the cleaning apparatus, wherein the cleaning apparatus functions as a cleaning unit that cleans the gas with a cleaning capability determined based on the weather information acquired in the first acquisition step.

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