CN111001281A - Aldehyde removing method and device - Google Patents
Aldehyde removing method and device Download PDFInfo
- Publication number
- CN111001281A CN111001281A CN201911105041.6A CN201911105041A CN111001281A CN 111001281 A CN111001281 A CN 111001281A CN 201911105041 A CN201911105041 A CN 201911105041A CN 111001281 A CN111001281 A CN 111001281A
- Authority
- CN
- China
- Prior art keywords
- chlorine dioxide
- reaction
- formaldehyde
- fan
- flow
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/76—Gas phase processes, e.g. by using aerosols
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/346—Controlling the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/72—Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
- B01D2251/108—Halogens or halogen compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/06—Polluted air
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
Abstract
The invention discloses a method and a device for removing aldehyde, wherein the method comprises the following steps: presetting operation time and reaction parameter values; detecting an initial formaldehyde value in a current space; calculating the dosage of the chlorine dioxide to be synthesized according to the reaction parameter value and the initial formaldehyde value; and controlling the chlorine dioxide synthesis agent to be blended in a chlorine dioxide synthesis bin according to the amount of the medicament to be synthesized and the running time. Through presetting a reaction parameter value and detecting an initial formaldehyde value, calculating the dosage of chlorine dioxide required to be generated for removing formaldehyde, and controlling the chlorine dioxide with the corresponding dosage generated by the chlorine dioxide synthesis bin, the technical problem that the chlorine dioxide is easily used excessively to influence health is solved, the chlorine dioxide with the corresponding dosage is automatically generated according to the formaldehyde amount, the formaldehyde removal automation is labor-saving and rapid, and the health of people is not influenced.
Description
Technical Field
The invention relates to an air formaldehyde removal technology, in particular to a formaldehyde removal method and device.
Background
In catering, hotels, schools, homes and other occasions, formaldehyde smell is easily generated when the occasions are started to be installed, formaldehyde is colorless and has pungent taste, and the formaldehyde gas easily harms the bodies of people, so various formaldehyde removing methods appear in the market.
At present, two methods for removing formaldehyde are available on the market, one is a physical method and the other is a chemical method, the physical method is a photocatalyst atomization method for purification, or furniture containing formaldehyde is sealed by a sealing agent to inhibit volatilization, and the methods are quite complex to use, time-consuming and labor-consuming, and cannot completely remove formaldehyde. The physical method also can remove formaldehyde by an adsorption mode, wherein the adsorption mode mainly adopts active recovery and a purifier, but the formaldehyde removal effect is not ideal. The chemical method mainly uses photocatalyst, chlorine dioxide and the like to atomize and synthesize and remove aldehyde, wherein formaldehyde pollution in air is removed through volatilization of the chlorine dioxide, but once the slow release mode is opened for use, the reaction cannot be stopped, the slow release mode is easily used in an excessive way, so that a human body feels uncomfortable, or the excessive way can cause health influence.
Disclosure of Invention
The present invention is directed to solving at least one of the problems of the prior art. Therefore, the invention provides an aldehyde removing method, which can automatically generate the dosage of the chlorine dioxide for removing formaldehyde according to the formaldehyde value of air, can automatically control the generation of chlorine dioxide to remove formaldehyde, and can generate chlorine dioxide with the dosage corresponding to the formaldehyde to be removed, so that the formaldehyde is removed simply and healthily.
The invention also provides an aldehyde removing device.
In a first aspect, one embodiment of the invention provides a method for removing aldehydes: presetting operation time and reaction parameter values;
detecting an initial formaldehyde value in a current space;
calculating the dosage of the chlorine dioxide to be synthesized according to the reaction parameter value and the initial formaldehyde value;
and controlling the chlorine dioxide synthesis agent to be blended in a chlorine dioxide synthesis bin according to the amount of the medicament to be synthesized and the running time.
The aldehyde removal method provided by the embodiment of the invention at least has the following beneficial effects: through presetting a reaction parameter value and detecting an initial formaldehyde value, calculating the dosage of chlorine dioxide required to be generated for removing formaldehyde, and controlling the chlorine dioxide with the corresponding dosage generated by the chlorine dioxide synthesis bin, the technical problem that the chlorine dioxide is easily used excessively to influence health is solved, the chlorine dioxide with the corresponding dosage is automatically generated according to the formaldehyde amount, the formaldehyde removal automation is labor-saving and rapid, and the health of people is not influenced.
According to other embodiments of the present invention, the reaction parameter values include: reaction time, area of the current space, height of the current space, reaction temperature.
According to further embodiments of the present invention, the aldehyde removing method further comprises:
after the chlorine dioxide is synthesized in the chlorine dioxide synthesizing bin, the accelerated reaction controller for accelerating the volatilization of the chlorine dioxide solution is started;
presetting an operation gear of the accelerated reaction controller, and controlling the accelerated reaction controller to operate according to the operation gear and the reaction temperature.
According to further embodiments of the present invention, the aldehyde removing method further comprises:
receiving a self-starting instruction and a preset single dose, and controlling the direct reaction of the single dose of the medicament according to the self-starting instruction;
and receiving a stopping instruction, and stopping the reaction of the chlorine dioxide synthetic agent according to the stopping instruction.
According to further embodiments of the present invention, the aldehyde removing method further comprises:
detecting the reaction temperature of the medicament reaction, the first operation speed of the flow expansion fan, the second operation speed of the turbulent flow fan and the residual amount of the medicament;
displaying the reaction temperature, the first operation rate, the second operation rate and the residual amount;
displaying the preset running time and the single dose.
In a second aspect, one embodiment of the present invention provides an aldehyde removal device: the method comprises the following steps:
the setting module is used for presetting operation time and reaction parameter values;
the detection module is used for automatically detecting an initial formaldehyde value in the current space;
the calculation module is used for calculating the dosage of the medicine to be synthesized according to the reaction parameter value and the initial formaldehyde value;
and the control module is used for controlling the chlorine dioxide synthesis bin to synthesize the chlorine dioxide with the medicament amount to be synthesized in the running time according to the medicament amount to be synthesized.
The aldehyde removing device provided by the embodiment of the invention at least has the following beneficial effects: the corresponding reaction parameters are set through the setting module, the calculation module calculates the dosage of the to-be-synthesized medicine of the chlorine dioxide needing to react with the formaldehyde after the detection module detects the initial formaldehyde value, and then the control module controls the chlorine dioxide reaction bin to generate the chlorine dioxide with the corresponding dosage so as to more accurately remove the formaldehyde in the air.
According to the aldehyde removing device of other embodiments of the present invention, the aldehyde removing device further comprises an accelerated reaction controller, wherein the accelerated reaction controller comprises a heating auxiliary device, a flow expansion fan and a turbulent fan;
the setting module is also used for presetting the operation gears of the flow expansion fan and the flow disturbing fan;
the control module controls the heating assistor to operate according to the reaction parameter value;
the control module controls the flow expansion fan and the flow disturbance fan to operate according to the operating gears.
Drawings
FIG. 1 is a block diagram of an embodiment of an aldehyde removal device in an embodiment of the present invention;
FIG. 2 is a schematic flow diagram of one embodiment of a method for removing aldehydes in an embodiment of the present invention;
fig. 3 is a schematic view of a specific embodiment of the aldehyde removal method according to the embodiment of the invention.
Description of the drawings: 100. setting a module; 200. a detection module; 300. a calculation module; 400. a control module; 500. an accelerated reaction controller; 510. a heating aid; 520. a flow-expanding fan; 530. a turbulent fan; 600. a self-starting key; 700. a self-starting module; 800. and a display module.
Detailed Description
The concept and technical effects of the present invention will be clearly and completely described below in conjunction with the embodiments to fully understand the objects, features and effects of the present invention. It is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments, and those skilled in the art can obtain other embodiments without inventive effort based on the embodiments of the present invention, and all embodiments are within the protection scope of the present invention.
In the description of the present invention, if an orientation description is referred to, for example, the orientations or positional relationships indicated by "upper", "lower", "front", "rear", "left", "right", etc. are based on the orientations or positional relationships shown in the drawings, only for convenience of describing the present invention and simplifying the description, but not for indicating or implying that the referred device or element must have a specific orientation, be constructed and operated in a specific orientation, and thus should not be construed as limiting the present invention. If a feature is referred to as being "disposed," "secured," "connected," or "mounted" to another feature, it can be directly disposed, secured, or connected to the other feature or indirectly disposed, secured, connected, or mounted to the other feature.
In the description of the embodiments of the present invention, if "a number" is referred to, it means one or more, if "a plurality" is referred to, it means two or more, if "greater than", "less than" or "more than" is referred to, it is understood that the number is not included, and if "greater than", "lower" or "inner" is referred to, it is understood that the number is included. If reference is made to "first" or "second", this should be understood to distinguish between features and not to indicate or imply relative importance or to implicitly indicate the number of indicated features or to implicitly indicate the precedence of the indicated features.
The first embodiment is as follows: referring to fig. 1, the embodiment of the invention discloses an aldehyde removing device, which mainly removes formaldehyde gas in air through chlorine dioxide, wherein the chlorine dioxide is an internationally recognized safe and nontoxic green disinfectant. A large number of foreign experimental studies show that chlorine dioxide is a safe and nontoxic disinfectant, has no 'three-cause' effect (carcinogenesis, teratogenesis and mutagenesis), and does not generate chlorination reaction with organic matters during disinfection to generate organic chloride or other toxic substances which can generate 'three-cause' effect. However, chlorine dioxide has extremely strong chloridizing ability and is used at a high concentration (>500ppm) which should be avoided.
In the air, the use of chlorine dioxide as a product for sterilization and disinfection is the safest and most effective means, but the synthesis of chlorine dioxide is limited to the synthesis and activation of solid tablets or medicinal powder and liquid at present, so that the accurate dosage control cannot be realized, and the dynamic synthesis of chlorine dioxide according to actual needs cannot be realized.
In this embodiment, the aldehyde-removing device comprises: the device comprises a setting module 100, a detection module 200, a calculation module 300, a control module 400 and an accelerated reaction controller 500, wherein the setting module 100 is used for setting operation time and reaction parameter values, the detection module 200 is used for automatically detecting an initial formaldehyde value in the current space, the calculation module 300 is used for calculating the dosage of a medicine to be synthesized according to the reaction parameter values and the initial formaldehyde value, and the control module 400 is used for controlling a chlorine dioxide synthesis bin to synthesize chlorine dioxide with corresponding dosage in the operation time according to the dosage of the medicine to be synthesized. The setting module 100 is further configured to set an operation gear of the acceleration-response controller 500, and the control module 400 controls the acceleration-response controller 500 to execute within the corresponding operation gear and the corresponding response parameter value according to the operation gear. According to the reaction parameter value set by the operator and the initial formaldehyde value detected by the detection module 200, the calculation module 300 calculates the amount of the to-be-synthesized medicament which needs to react out chlorine dioxide according to the reaction parameter value and the initial formaldehyde value, the control module 400 controls the chlorine dioxide synthesis bin to synthesize chlorine dioxide with a corresponding dose in the operation time according to the dose of the to-be-synthesized medicament, so that the amount of chlorine dioxide for removing formaldehyde gas in the current space is accurately calculated, the formaldehyde gas in the current space can be clearly and cleanly removed, and the mode for removing the formaldehyde gas has no harmful substances. After the setting module 100 reads the operation gear, the control module 400 controls the accelerated reaction controller 500 to operate in the operation gear, and controls the chlorine dioxide solution to be rapidly volatilized through the accelerated reaction controller, so that the formaldehyde concentration in the air can be rapidly eliminated by being synthesized with formaldehyde in the air more rapidly.
The reaction parameter values comprise reaction time, the area of the current space, the height of the current space and reaction temperature, wherein the reaction time is also running time, the time for starting and running the aldehyde removing device set by an operator is obtained through the setting module 100 to obtain the reaction time, and the reaction time read through the setting module 100 is mainly used for setting the specific time for executing the generation of chlorine dioxide. An operator inputs the reaction time, the area of the current space, the height of the current space and the reaction temperature through an input device of the aldehyde removing device, and the setting module 100 reads the reaction time, the area of the current space, the height of the current space and the reaction temperature. The operator also inputs the operating range of the accelerated response controller 500 through the input device, and the setting module 100 reads the operating range corresponding to the operator input.
The detection module 200 is configured to detect an initial formaldehyde value in the current space, where the initial formaldehyde value is a formaldehyde concentration of 1 cubic volume, and a molecular formula of a reaction between chlorine dioxide and formaldehyde is such that a balanced mass ratio of formaldehyde to chlorine dioxide is about 1 to 2, so that it is only known how many doses of chlorine dioxide are needed to eliminate formaldehyde in the current space after the detection module 200 detects the corresponding formaldehyde value. The calculating module 300 calculates the amount of the to-be-synthesized chemical required to be reacted according to the initial formaldehyde value detected by the detecting module 200 and the reaction parameter value read by the setting module 100, where the amount of the to-be-synthesized chemical is the generated amount of chlorine dioxide. The calculation formula for generating chlorine dioxide once is as follows: (1+ T) × (1+ W) × 2 × M × S × H, wherein T is the reaction time, Z is the dose of chlorine dioxide required to be synthesized at a single time, W is the reaction temperature, M is the initial formaldehyde value, S is the area of the current room, and H is the height of the current room. The dosage of the chlorine dioxide generated in a single time is calculated by the calculation formula of the chlorine dioxide, and then the chlorine dioxide synthetic agent which needs to react to generate the chlorine dioxide can be determined, so that the dosage of the chlorine dioxide for eliminating the formaldehyde in the current space can be calculated more accurately. In the embodiment, the chlorine dioxide synthetic agent is mainly synthesized by parent and activator double liquids, the controllable volatilization in the air is successfully realized, and the concentration time is also controllable. The control module 400 calculates the dosage of the chlorine dioxide synthetic agent corresponding to the dosage control of the medicine to be synthesized according to the calculation module 300, and the chlorine dioxide synthetic agent starts to react in the chlorine dioxide synthetic bin, so that the chlorine dioxide automatically starts to react with formaldehyde in the air after the automatic generation of the carbon dioxide flow.
Set up module 100, calculation module 300 and control module 400 are all that long-range removing aldehyde APP sends corresponding instruction to chlorine dioxide synthesis storehouse and reacts, set up module 100, calculation module 300 and control module 400 are integrated on the master control table or long-range backstage, so that at the synthetic high concentration chlorine dioxide of unmanned occasion, avoid high concentration chlorine dioxide to cause human discomfort, and can avoid operating personnel to inhale too much formaldehyde, so that easily apply to food and drink, the hotel, places such as school and house, and the sterilization under the mainly used 0.1 ppm.
Preferably, the accelerated reaction controller 500 includes a heating auxiliary device 510, a diffuser fan 520 and a spoiler fan 530, the heating auxiliary device 510 is mainly used for accelerating rapid evaporation of chlorine dioxide, the diffuser fan 520 is mainly used for volatilizing the chlorine dioxide generated by the aldehyde removing device so that the chlorine dioxide rapidly reacts with formaldehyde in the air, and the spoiler fan 530 is mainly used for assisting generation of chlorine dioxide. The control module 400 controls the diffusion fan 520 and the turbulent fan 530 to operate according to the operation gear after the chlorine dioxide synthesis bin starts to operate according to the operation gear acquired by the setting module 100, so that the diffusion fan 520 and the turbulent fan 530 can control the gear according to the requirement of an operator. The control module 400 controls the heating auxiliary device 510 to heat the temperature control heating layer of the chlorine dioxide reaction chamber to a set reaction temperature according to the reaction temperature so as to rapidly evaporate the chlorine dioxide medicament, and the temperature control of the temperature control heating layer in the chlorine dioxide reaction chamber is kept at 50-120 ℃ as much as possible so as to rapidly evaporate the chlorine dioxide, thereby generating a formaldehyde reaction between the chlorine dioxide and the air and rapidly removing the formaldehyde.
Preferably, the aldehyde removing device further comprises a self-starting button 600, a self-starting module 700 and a display module 800, the setting module 100 is further configured to set a single dose, when an operator presses the self-starting button 600, the self-starting module 700 obtains a self-starting instruction of the operator, the control module 400 controls the chlorine dioxide synthesizing agent in the chlorine dioxide synthesizing bin to start to react according to the self-starting instruction, and when the operator does not press the self-starting button 600, the self-starting module 700 does not obtain all self-starting instructions, and the control module 400 does not control the chlorine dioxide synthesizing agent to start to react. When the self-starting button 600 is pressed, the corresponding chlorine dioxide synthesis agent is matched according to the single dose set by the setting module 100, and the operator manually controls the chlorine dioxide synthesis until the operator does not press the self-starting button 600, so that on one hand, the operator can automatically generate chlorine dioxide with the corresponding dose according to the self-demand, and on the other hand, the whole device is prevented from being paralyzed due to the fact that the automatic detection module 200 cannot automatically generate chlorine dioxide when in fault, and manual control is facilitated.
The display module 800 is mainly used for displaying the reaction time, the reaction temperature, the operation gear, the single dose, the operation days and the remaining amount of the medicament, which are acquired by the setting module 100, wherein the display module 800 is mainly an LCD display, and the operation gear matches the first operation rate of the flow expanding fan 520 and the second operation rate of the flow disturbing fan 530. The control module 400 calculates the number of days that the device has been operated and starts to display through the display module 800, and the chlorine dioxide synthesis bin is internally provided with a liquid level sensor for detecting the chlorine dioxide synthesis agent, and the liquid level sensor detects the surplus of the chlorine dioxide at the dosage liquid level of the chlorine dioxide synthesis agent and displays the surplus through the display module 800, so that an operator can accurately master the state data of the current aldehyde removing device.
In summary, the setting module 100 sets the corresponding reaction time, reaction temperature, area of the current space, height of the current space, and operation gear, and according to the initial formaldehyde value of the current space detected by the detecting module 200, the calculating module 300 obtains the amount of chlorine dioxide to be generated by the reaction according to the reaction time, the reaction temperature, the area of the current space, the height of the current space, and the initial formaldehyde value, so as to obtain the required amount of the chlorine dioxide synthesizing agent, and the control module 400 starts the chlorine dioxide synthesizing agent to react in the operation time according to the amount of the carbon dioxide synthesizing agent, and simultaneously starts the heating auxiliary 510, the flow expanding fan 520, and the turbulent fan 530 to react the generated chlorine dioxide with formaldehyde in the air rapidly, so as to remove formaldehyde rapidly and accurately. When the detection module 200 detects a failure, an operator presses the self-starting button 600 to automatically control the reaction of the chlorine dioxide synthesis agent in the chlorine dioxide synthesis bin, and the operator stops the reaction of the chlorine dioxide synthesis agent when knowing that the operator does not press the self-starting button 600, so that the aldehyde can be removed manually and automatically.
Example two: referring to fig. 2 and 3, the embodiment of the invention discloses an aldehyde removing method, which is mainly executed by an aldehyde removing robot, and the aldehyde removing robot is controlled in a remote control mode to set the following mode and is remotely executed by a WiFi remote control aldehyde removing robot.
The aldehyde removing method specifically comprises the following steps:
presetting operation time and reaction parameter values, wherein the reaction parameter values comprise: reaction time, area of the current space, height of the current space and reaction temperature;
detecting an initial formaldehyde value in the current space, wherein the initial formaldehyde value in the current space is obtained in the example and is a formaldehyde concentration value in each cube, and the formaldehyde concentration value is automatically obtained to save manpower and reduce excessive formaldehyde inhaled by people; the detected initial formaldehyde value is transmitted to a remote control end through WIFI, and is on a remote APP.
Calculating the dosage of the chlorine dioxide to be synthesized according to the reaction parameter value and the initial formaldehyde value, and calculating by a chlorine dioxide generation dosage formula according to the reaction time, the area of the current space, the height of the current space, the reaction temperature and the initial formaldehyde value, wherein the calculation formula is as follows: (1+ T) x (1+ W) x 2 xM xSxH, wherein T is reaction time, W is reaction temperature, M is an initial formaldehyde value, S is the area of the current room, and H is the height of the current room, the dosage of the to-be-synthesized agent needing to be generated by chlorine dioxide is calculated through a calculation formula of the dosage of chlorine dioxide, and then the dosage of the chlorine dioxide synthesizing agent needing to participate in the reaction is obtained, so that the to-be-synthesized agent can accurately react with formaldehyde in the air, and the formaldehyde can be more completely removed.
The preparation of the chlorine dioxide synthesis agent in the chlorine dioxide synthesis bin is controlled according to the dosage of the medicine to be synthesized and the operation time, the chlorine dioxide synthesis agent in the chlorine dioxide synthesis bin is controlled to start to react after the dosage of the chlorine dioxide synthesis agent which does not need to react is calculated, and the reaction time is the same when the chlorine dioxide synthesis agent reacts to the preset operation time, so that the reaction can be carried out according to the operation time set by an operator, and the operator can know the formaldehyde removal time in the air conveniently.
Preferably, the method for removing aldehydes further comprises the steps of:
when the chlorine dioxide synthesis bin starts to react, the accelerated reaction controller for controlling the diffusion speed of chlorine dioxide starts, and the accelerated reaction controller comprises: the chlorine dioxide-free air purifier comprises a heating auxiliary device, a flow expansion fan and a flow disturbing fan, wherein the heating auxiliary device is favorable for the evaporation of chlorine dioxide, and the flow expansion fan and the flow disturbing fan can accelerate the diffusion of the chlorine dioxide so as to rapidly react with formaldehyde in the air to rapidly eliminate the formaldehyde.
The operation gear of the reaction accelerating controller is preset, the reaction accelerating controller operates under the operation gear and the reaction temperature according to control, and the formaldehyde is removed through the preset operation gear so as to accelerate more quickly according to the will of an operator.
Preferably, the aldehyde removal method further comprises:
receiving a self-starting instruction and a preset single dose, and controlling the direct reaction of the single dose of the medicament according to the self-starting instruction; and receiving a stopping instruction, and stopping the reaction of the chlorine dioxide synthesis agent according to the stopping instruction. When the operation of automatically detecting the concentration of formaldehyde in the current space is damaged or the generation of chlorine dioxide cannot be automatically started, the reaction of the dioxide synthetic agent can be manually controlled, the generation of chlorine dioxide with single dose can be automatically controlled by setting the pressing of the self-starting key, and the automatic control fault can also be manually controlled.
Preferably, the aldehyde removal method further comprises:
detecting the reaction temperature of the medicament reaction, the first operation speed of the flow expansion fan, the second operation speed of the turbulent flow fan and the residual amount of the medicament;
the method comprises the steps of displaying the reaction temperature, the first operation speed, the second operation speed and the surplus, and displaying the preset operation time and the single dose, wherein the first operation speed and the second operation speed correspond to the operation gears of the flow expansion fan and the turbulent flow fan, so that the operation gears of the turbulent flow fan and the flow expansion fan are displayed to facilitate an operator to master the operation gears of the current turbulent flow fan and the current flow expansion fan. The residual amount of the medicament is displayed by directly detecting the liquid level of the chlorine dioxide synthetic agent through a liquid level meter, so that the current residual amount of the chlorine dioxide can be known, the current residual amount of the medicament can be displayed through a display, an operator can conveniently know the residual amount of the medicament, and the state of the current formaldehyde removing robot can be conveniently determined by the operator through the display of each parameter.
The embodiments of the present invention have been described in detail with reference to the accompanying drawings, but the present invention is not limited to the above embodiments, and various changes can be made within the knowledge of those skilled in the art without departing from the gist of the present invention. Furthermore, the embodiments of the present invention and the features of the embodiments may be combined with each other without conflict.
Claims (8)
1. A method for removing aldehydes, comprising:
presetting operation time and reaction parameter values;
detecting an initial formaldehyde value in a current space;
calculating the dosage of the chlorine dioxide to be synthesized according to the reaction parameter value and the initial formaldehyde value;
and controlling the chlorine dioxide synthesis agent to be blended in a chlorine dioxide synthesis bin according to the amount of the medicament to be synthesized and the running time.
2. The method of claim 1, wherein the reaction parameter values comprise: reaction time, area of the current space, height of the current space, reaction temperature.
3. The method for removing aldehydes according to claim 2, further comprising:
after the chlorine dioxide is synthesized in the chlorine dioxide synthesizing bin, the accelerated reaction controller for accelerating the volatilization of the chlorine dioxide solution is started;
presetting an operation gear of the accelerated reaction controller, and controlling the accelerated reaction controller to operate according to the operation gear and the reaction temperature.
4. The method for removing aldehydes according to claim 3, wherein the accelerated reaction controller comprises: the heating auxiliary device, the flow-expanding fan and the flow-disturbing fan.
5. The method for removing aldehydes according to claim 4, further comprising:
receiving a self-starting instruction and a preset single dose, and controlling the direct reaction of the single dose of the medicament according to the self-starting instruction;
and receiving a stopping instruction, and stopping the reaction of the chlorine dioxide synthetic agent according to the stopping instruction.
6. The method for removing aldehydes according to claim 5, further comprising:
detecting the reaction temperature of the medicament reaction, the first operation speed of the flow expansion fan, the second operation speed of the turbulent flow fan and the residual amount of the medicament;
displaying the reaction temperature, the first operation rate, the second operation rate and the residual amount;
displaying the preset running time and the single dose.
7. An aldehyde removal device, comprising:
the setting module is used for presetting operation time and reaction parameter values;
the detection module is used for automatically detecting an initial formaldehyde value in the current space;
the calculation module is used for calculating the dosage of the medicine to be synthesized according to the reaction parameter value and the initial formaldehyde value;
and the control module is used for controlling the chlorine dioxide synthesis bin to synthesize the chlorine dioxide within the running time according to the dosage of the medicine to be synthesized.
8. The aldehyde removing device according to claim 7, further comprising an accelerated reaction controller, wherein the accelerated reaction controller comprises a heating auxiliary device, a flow expansion fan and a flow disturbance fan;
the setting module is also used for presetting the operation gears of the flow expansion fan and the flow disturbing fan;
the control module controls the heating assistor to operate according to the reaction parameter value;
the control module controls the flow expansion fan and the flow disturbance fan to operate according to the operating gears.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911105041.6A CN111001281A (en) | 2019-11-13 | 2019-11-13 | Aldehyde removing method and device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911105041.6A CN111001281A (en) | 2019-11-13 | 2019-11-13 | Aldehyde removing method and device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111001281A true CN111001281A (en) | 2020-04-14 |
Family
ID=70113065
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201911105041.6A Pending CN111001281A (en) | 2019-11-13 | 2019-11-13 | Aldehyde removing method and device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111001281A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101949564A (en) * | 2010-10-15 | 2011-01-19 | 太原和瑞环保科技有限公司 | Central air-conditioning sterilizing device capable of realizing chlorine dioxide dosage dynamic control |
| US20160016114A1 (en) * | 2012-01-09 | 2016-01-21 | Robert George RICHARDSON | Removal of atmospheric pollutants from gas, related apparatus, processes and uses thereof |
| CN106322671A (en) * | 2016-08-30 | 2017-01-11 | 深圳市潜能环保实业有限公司 | Air purifying method and device |
| CN107115777A (en) * | 2017-05-19 | 2017-09-01 | 深圳市橘井舒泉技术有限公司 | Air disinfection purifier and its control method except formaldehyde, device and storage medium |
| CN108654345A (en) * | 2018-03-16 | 2018-10-16 | 安徽科浦环保科技有限公司 | The sterilizing equipment decontaminating apparatus and remove carbaldehyde Method that indoor formaldehyde is removed |
| CN209438353U (en) * | 2019-01-04 | 2019-09-27 | 广东净威环保科技有限公司 | A kind of equipment for removing indoor formaldehyde |
-
2019
- 2019-11-13 CN CN201911105041.6A patent/CN111001281A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101949564A (en) * | 2010-10-15 | 2011-01-19 | 太原和瑞环保科技有限公司 | Central air-conditioning sterilizing device capable of realizing chlorine dioxide dosage dynamic control |
| US20160016114A1 (en) * | 2012-01-09 | 2016-01-21 | Robert George RICHARDSON | Removal of atmospheric pollutants from gas, related apparatus, processes and uses thereof |
| CN106322671A (en) * | 2016-08-30 | 2017-01-11 | 深圳市潜能环保实业有限公司 | Air purifying method and device |
| CN107115777A (en) * | 2017-05-19 | 2017-09-01 | 深圳市橘井舒泉技术有限公司 | Air disinfection purifier and its control method except formaldehyde, device and storage medium |
| CN108654345A (en) * | 2018-03-16 | 2018-10-16 | 安徽科浦环保科技有限公司 | The sterilizing equipment decontaminating apparatus and remove carbaldehyde Method that indoor formaldehyde is removed |
| CN209438353U (en) * | 2019-01-04 | 2019-09-27 | 广东净威环保科技有限公司 | A kind of equipment for removing indoor formaldehyde |
Non-Patent Citations (1)
| Title |
|---|
| 张清洁等: "《动物检疫与卫生监督》", 30 April 2011, 中原农民出版社 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| AU2022201077B2 (en) | Insufflation apparatus and methods and a gas generating cartridge therefor | |
| US8282891B2 (en) | Apparatus for the generation of gases | |
| US20230044304A1 (en) | Nitric oxide generation, dilution, analysis, and topical application compositions, systems, apparatus and methods | |
| JP6306420B2 (en) | Decontamination method and apparatus | |
| KR100966933B1 (en) | Method and apparatus for ozone steriliza tion | |
| US20160206767A1 (en) | Sterilizing apparatus and sterilizing method using wet gaseous chlorine dioxide | |
| US6269810B1 (en) | Pulmonary dosing system and method | |
| US20170348450A1 (en) | Method and apparatus for producing nitrogen oxide gas | |
| US8696981B2 (en) | Apparatus and methods for disinfecting spaces | |
| US7608217B2 (en) | Apparatus and method for humidifying a sterilization chamber | |
| CN106322671A (en) | Air purifying method and device | |
| CN205145190U (en) | Special sterilizing machine of breathing machine | |
| CN212464681U (en) | Automatic disinfectant allocation instrument | |
| CN111001281A (en) | Aldehyde removing method and device | |
| CN102178968B (en) | Chlorine dioxide gas disinfection device | |
| CN207562133U (en) | A kind of Gas sterilizing device | |
| CN207370875U (en) | A kind of intelligence Chinese medicine part device for fumigation | |
| WO2021068137A1 (en) | Anesthesia machine and method for controlling anesthetic vaporizer | |
| US9492580B2 (en) | System and method for the safe provision of ozone | |
| JP6325882B2 (en) | Decontamination method and apparatus | |
| JP2000288075A (en) | Electrolytic water spraying device | |
| CN111631229B (en) | Automatic disinfectant dispensing instrument and automatic disinfectant dispensing method | |
| RU2769219C1 (en) | Universal automatic mobile disinfector | |
| CN205472642U (en) | Chlorine dioxide solution preparation facilities | |
| JP2006081697A (en) | Sterilizer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20200414 |