CN213609056U - Multi-channel respiratory tract treatment equipment - Google Patents

Abstract

The utility model relates to the technical field of medical equipment, a multichannel respiratory track treatment facility is disclosed, can realize that a plurality of fog components export the treatment medium simultaneously with the atomization frequency that corresponds. The utility model discloses a controller, raw materials output module, electrolysis trough, storage part, atomization component and inhale fog part, still include the atomization frequency regulator with atomization component electric connection, the utility model discloses with an atomization component, an atomization frequency regulator, an inhale fog part and constitute a set of branch road to communicate with same storage part, realize one and drag many effects, can implement the treatment for a plurality of patients simultaneously, can effectively improve treatment efficiency, reduce and doctorse and nurses manpower working strength, accessible atomization frequency adjusts the control that realizes treatment medium deposit position, in order to reach the higher treatment concentration of focus position, promotes treatment.

Description

Multi-channel respiratory tract treatment equipment

Technical Field

The utility model relates to the technical field of medical equipment, especially a multichannel respiratory track treatment facility.

Background

At present, all domestic oxidation potential water generating equipment is provided with a water storage tank for storing and mixing oxidation potential liquid which is prepared by electrolysis, and chlorine gas is gathered in the storage process along with the increase of the storage time, so that potential safety hazards are generated in the operation and maintenance processes, and the oxidation potential water generating equipment cannot be applied to the treatment of human respiratory tracts.

Therefore, the atomization frequency of the current oxidation potential water generating equipment is constant. Because the atomization frequency directly affects the particle size of the atomization, and the particle size is a decisive factor of the deposition part of the atomized particles (such as oral cavity, throat and lung), the atomization frequency cannot be adjusted, so that the local drug treatment concentration at the application part and the effective fixed-point treatment aiming at the focus part are difficult to control.

At present, tertiary hospital generally all possesses the special treatment room of breathing atomizing room to central embedded compressed air atomizing is leading, and the following hospital of second grade does not possess special room of atomizing and atomizing pipe-line system mostly, uses the unit version atomizer to give first place to, and atomizing treatment process complex operation consumes a large amount of nursing manpower resources. And respiratory infectious diseases are mostly seasonal outbreaks, the concentration of infected people is high, the single treatment room can not accommodate the crowd who concentrates the doctor, and fixed atomizing system can not remove yet, and hospital treatment throughput is obviously limited to room overall arrangement.

Therefore, there is a need for a respiratory tract treatment device which can act on the respiratory tract of a human body, has high safety and effectiveness, and has a larger treatment coverage.

SUMMERY OF THE UTILITY MODEL

The utility model discloses aim at solving one of the technical problem that exists among the prior art at least. Therefore, the utility model provides a multichannel respiratory tract treatment equipment, equipment can be through multiplexed output treatment medium, for a plurality of patients implement the treatment, improve treatment efficiency and treatment coverage by a wide margin, and can be according to patient individual difference treatment demand, carry out independent control to the atomizing frequency of each group fog-absorbing part, with this control treatment medium most concentrated deposit at the focus position, in order to obtain local higher treatment effective concentration, reach and improve treatment, reduce the purpose of side reaction, the invention can be applied to common respiratory infectious disease of human body and new issue infectious disease, have the broad, show that effect is fast, the small side effect, the characteristics of security height.

The multi-channel respiratory tract treatment equipment according to the embodiment of the utility model comprises a controller, a raw material output module, an electrolytic bath, a storage part, at least two atomization components, at least two fog absorption parts and at least two atomization frequency regulator controllers; the raw material output module is provided with a raw material output port; the electrolytic cell is provided with a first water outlet and a second water outlet, and the input end of the electrolytic cell is communicated with the raw material output port; the storage component is provided with a gas output end, a liquid input end and at least two liquid output ends, and the liquid input end is communicated with the first water outlet; the input end of each atomization assembly is communicated with the corresponding liquid output end; the input end of each mist suction part is communicated with the output end of the corresponding atomization component; each atomization frequency regulator is electrically connected with the corresponding atomization assembly; the controller is respectively electrically connected with the raw material output module, the electrolytic bath, the storage component, the atomization assembly and the atomization frequency regulator.

According to the utility model discloses multichannel respiratory track treatment facility has following beneficial effect at least: an atomization component, an atomization frequency regulator and a mist suction component form a group of branches which are respectively communicated with the same storage component, so that the effect of one-to-many treatment is realized, the occupied space can be reduced, a plurality of patients can be treated at the same time, the ward circulation rate and the treatment efficiency can be effectively improved, and the labor intensity of medical care is reduced; and each atomization component is independently connected with an atomization frequency regulator, so that the atomization frequency of each group of the atomization components can be independently regulated and controlled according to individual treatment requirements of patients, most of treatment media are controlled to be intensively deposited on the focus part, local high treatment effective concentration is obtained, and the aims of improving treatment effect and reducing side effects are fulfilled.

According to some embodiments of the invention, the raw material output module comprises a water pretreatment part, a water flow rate control part and a brine output part: the input end of the water flow rate control part is communicated with the output end of the water pretreatment part through a pipeline; the input end of the brine output component is communicated with the output end of the water pretreatment component through a pipeline; wherein, the output end of the brine output part is communicated with the output end of the water flow-rate control part to form the raw material output port.

According to some embodiments of the utility model, the water pretreatment components including loop through the pipeline intercommunication and respectively with controller electric connection's water purifier and demineralized water treatment ware, demineralized water treatment ware's output respectively with water flow rate control unit's input and salt water output unit's input intercommunication.

According to some embodiments of the utility model, the water flow rate control part including loop through the pipeline intercommunication and respectively with controller electric connection's relief pressure valve, first solenoid valve and flow sensor, the input of relief pressure valve with the output intercommunication of water pretreatment parts, flow sensor's output with the input intercommunication of electrolysis trough.

According to some embodiments of the utility model, the salt solution output part includes salt solution tank and measuring pump through the pipeline intercommunication, the input of salt solution tank pass through the second solenoid valve with the output intercommunication of pretreatment of water part, the output of measuring pump with the input intercommunication of electrolysis trough, the second solenoid valve with the measuring pump respectively with controller electric connection.

According to some embodiments of the utility model, the brine tank is equipped with the wet return with self intercommunication, be equipped with on the wet return with controller electric connection's first water pump.

According to some embodiments of the present invention, the storage component comprises a water storage tank and at least two second water pumps, the gas output end and the liquid input end are respectively provided at an upper end of the water storage tank; the input end of each second water pump is communicated with the bottom of the water storage tank, the output end of each second water pump is communicated with the corresponding liquid output end, and the second water pumps are electrically connected with the controller.

According to some embodiments of the present invention, the atomizing assembly comprises an atomizing chamber, an atomizer and an air pump, wherein an input end of the atomizing chamber is communicated with the corresponding liquid output end, and an output end of the atomizing chamber is communicated with an input end of the corresponding mist absorbing member; the atomizer is arranged at the bottom of the atomization box and is electrically connected with the controller; the air pump pass through the pipeline with the upper end intercommunication of atomizer box and with controller electric connection.

Additional aspects and advantages of the invention will be set forth in part in the description which follows and, in part, will be obvious from the description, or may be learned by practice of the invention.

Drawings

The above and/or additional aspects and advantages of the present invention will become apparent and readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings of which:

fig. 1 is a schematic structural view of a multi-channel respiratory tract treatment device according to an embodiment of the present invention.

Reference numerals: the water pretreatment device 100, the water filter 110, the water softener 120, the water flow rate control device 200, the pressure reducing valve 210, the first electromagnetic valve 220, the flow sensor 230, the brine output device 300, the brine tank 310, the metering pump 320, the second electromagnetic valve 330, the first water pump 340, the electrolytic bath 400, the three-way electromagnetic valve 410, the storage device 500, the water storage tank 510, the second water pump 520, the atomization assembly 600, the atomization tank 610, the atomizer 620, the air pump 630, the mist absorption device 700, the third electromagnetic valve 710, the controller 800, the chlorine purifier 900 and the atomization frequency regulator 1000.

Detailed Description

This section will describe in detail the embodiments of the present invention, preferred embodiments of the present invention are shown in the attached drawings, which are used to supplement the description of the text part of the specification with figures, so that one can intuitively and vividly understand each technical feature and the whole technical solution of the present invention, but they cannot be understood as the limitation of the protection scope of the present invention.

In the description of the present invention, a plurality of means are one or more, a plurality of means are two or more, and the terms greater than, less than, exceeding, etc. are understood as not including the number, and the terms greater than, less than, within, etc. are understood as including the number. If any description to first, second and third is only for the purpose of distinguishing technical features, it is not to be understood as indicating or implying relative importance or implicitly indicating the number of technical features indicated or implicitly indicating the precedence of the technical features indicated.

In the description of the present invention, unless there is an explicit limitation, the words such as setting, installation, connection, etc. should be understood in a broad sense, and those skilled in the art can reasonably determine the specific meanings of the above words in combination with the specific contents of the technical solution.

Referring to fig. 1, the multi-channel respiratory tract treatment device according to the embodiment of the present invention comprises a raw material output module, an electrolytic bath 400, a storage part 500, at least two atomization assemblies 600, at least two mist absorption parts 700, and at least two atomization frequency regulators 1000 and a controller 800; the raw material output module is provided with a raw material output port; the electrolytic cell 400 is provided with a first water outlet and a second water outlet, and the input end of the electrolytic cell 400 is communicated with the raw material output port; the storage component 500 has a gas output, a liquid input, and at least two liquid outputs, the liquid input being in communication with the first water outlet; the input end of each atomization assembly 600 is communicated with the corresponding liquid output end; the input end of each fog absorbing part 700 is communicated with the output end of the corresponding atomization assembly 600; each atomization frequency adjuster 1000 is electrically connected with a corresponding atomization assembly 600; the controller 800 is electrically connected to the raw material output module, the electrolytic cell 400, the storage part 500, the atomizing assembly 600, and the atomizing frequency adjuster 1000, respectively.

Each atomization assembly 600, the atomization frequency regulator 1000 and the mist absorption part 700 are a group, which can respectively provide treatment media with corresponding parameters to corresponding patients with corresponding atomization frequency, the raw material output module provides raw materials to the electrolytic cell 400, the electrolytic cell 400 transports neutral oxidation potential water to the same storage part 500, and then the neutral oxidation potential water is transported to each atomization assembly 600 by the storage part 500, so that the effect of one-to-many atomization is realized, the treatment media can be provided to a plurality of patients with different atomization frequencies, and the device can be effectively prevented from occupying too much space. Specifically, referring to fig. 1, in the present embodiment, four branches are provided, each branch is composed of an atomizing assembly 600, an atomizing frequency adjuster 1000, and a mist absorbing component 700, and each branch can independently provide neutral oxidation potential water with corresponding atomizing frequency and corresponding parameters to the corresponding mist absorbing component 700.

The utility model discloses in, the raw materials output module includes pretreatment of water part 100, water velocity of flow control part 200 and salt solution output part 300: the input end of the water flow rate control part 200 is communicated with the output end of the water pretreatment part 100 through a pipeline; the input end of the brine output part 300 is communicated with the output end of the water pretreatment part 100 through a pipeline; wherein, the output end of the brine output part 300 is communicated with the output end of the water flow rate control part 200 to form a raw material output port.

Wherein, the water pretreatment unit 100 is mainly used for filtering and softening a water source to reduce water hardness, and the water flow rate control unit 200 is used for making water flow into the electrolytic cell 400 at a stable water flow rate, and part of the water passing through the water pretreatment unit 100 enters the brine output unit 300 to form saturated brine, and the brine output unit 300 is used for inputting brine into the electrolytic cell 400 at a set water flow rate, and it should be noted that, before the brine and the water flow enter the electrolytic cell 400, the brine with low concentration is formed after mixing in an external pipeline and then enters the electrolytic cell 400, and then the electrode plates of the electrolytic cell 400 are electrified to electrolyze the saturated brine between the two electrode plates into water with neutral oxidation potential, and the water with neutral oxidation potential is transported to the storage unit 500 for storage, and during treatment, the atomization assembly 600 is transported from the storage unit 500 for atomization, and transmits the treatment medium to the patient through the mist suction member 700 to achieve an effective treatment effect.

The water flow rate control part 200 outputs water flow at a speed of 2-4L/min, the brine output part 300 outputs water flow at a speed of 1-5 ml/min, the current value of the electrolytic cell 400 is 6A-14A, and the voltage of the electrolytic cell 400 is 5-24V. Wherein the electrode pitch of the electrolytic cell 400 is 4mm,current density 60ma/cm²The effective area of the electrode is 100cm². By utilizing the above parameter ranges, the pH value of the neutral oxidation potential water generated by the electrolytic cell 400 is 5-7, the oxidation-reduction potential of the neutral oxidation potential water is +500 to +1000mV, and the available chlorine content of the neutral oxidation potential water is 10-50 mg/L. The neutral oxidation potential water with the parameters can synchronously kill pathogenic microorganisms of the respiratory tract, wherein the pathogenic microorganisms comprise viruses and bacteria, and the viruses mainly comprise rhinoviruses, coronaviruses, adenoviruses, influenza H1N1, H3N2, parainfluenza viruses, respiratory syncytial viruses and the like; the bacteria mainly comprise hemolytic streptococcus, haemophilus influenzae, pneumococcus, staphylococcus, etc., and can be used for treating respiratory infectious diseases, including upper respiratory infection and lower respiratory infection, including rhinitis, pharyngitis, laryngitis; lower respiratory tract infection includes trachea, bronchitis, pneumonia, etc.

The neutral oxidation potential water with the parameters has unique physical and chemical double mechanisms. ORP (oxidation-reduction potential) physical sterilization is mainly used, and ACC (available chlorine) chemical action sterilization is used as an auxiliary; the synergistic bactericidal action of the two is far greater than the single action. The atomized neutral oxidation potential water generates an electron-withdrawing effect at the moment of contacting pathogenic microorganisms, interferes the balance of pathogenic microorganism membranes, changes the potential difference inside and outside the cell membranes, the permeability of the membranes and the osmotic pressure inside and outside the membranes, and causes the rupture of the cell membranes, the cytoplasm overflow inside the cell membranes and the change of the ultrastructure, thereby leading the pathogenic cells to die.

The available chlorine of the neutral oxidation potential water in the embodiment is mainly HC1O, and HClO is further decomposed to form nascent oxygen [ O ]. The nascent oxygen has strong oxidizability, and can change the cell permeability of bacteria and viruses or mechanically break a biological membrane to promote the intracellular solute to seep outwards, so that the bacteria die.

The clinical properties of the invention for producing neutral oxidation potential water having the above parameters are described in detail below:

firstly, the antibacterial spectrum is wide:

has wide antibacterial spectrum, is suitable for common respiratory tract infection types, treats independently and does not need synchronous use of medicaments. Can synchronously and efficiently kill virus, bacteria and mould; the antibacterial spectrum is obviously superior to that of the traditional atomized antibiotic medicine, and the defect that the traditional atomized antibiotic medicine has no treatment effect on virus type infection is overcome.

Secondly, the effect is shown to be rapid:

the medicine can quickly relieve symptoms after being treated for 15min for the first time, and has strong effect; the treatment course is short (2-4 times), and the treatment duration is shortened by half compared with the traditional atomized antibiotic medicine. In vitro testing: the killing rate of staphylococcus aureus, candida albicans and escherichia coli reaches 99.99 percent in 3 min. The spore can be killed within 10 min.

Thirdly, the method is safe and effective:

the treatment medium is non-toxic and non-irritant, does not produce anaphylactic reaction, has pH close to neutral, adapts to the colloid osmotic pressure of tissues, completely meets the use requirements of atomized medicament treatment, and has no medicament resistance. Has the advantages of high local drug concentration, direct effect on focus parts, quick response, small side effect and the like.

Fourth, compatibility and popularity:

the utility model discloses collect medicine preparation and atomizing function in an organic whole, can prepare the atomizing medicine medium, have the function of atomizer again concurrently, solved traditional atomizing medicine and must be equipped with the environment restriction that the atomizer could use, the existing system usefulness, stability is good.

Fifthly, personalized treatment:

the atomization frequency of each group of the fog absorbing parts 700 can be independently regulated and controlled according to individual treatment requirements of patients, so that most of treatment media are controlled to be intensively deposited on the focus part, and local high treatment effective concentration is obtained, thereby achieving the purposes of improving treatment effect and reducing side effects.

Sixthly, multiplexed output, equipment is portable, increases the treatment coverage:

the device can treat a plurality of patients at the same time, effectively improve the ward transfer rate and the treatment efficiency, and reduce the labor intensity of medical care; the equipment is movable and is not limited by the fixed room environment; can meet the requirement of treatment flow of seasonal respiratory tract infectious diseases.

In some embodiments of the present invention, the chlorine purifier 900 is further connected to the controller 800, and the input of the chlorine purifier 900 is connected to the gas output. The chlorine gas released from the storage unit 500 can be effectively treated by the chlorine gas purifier 900, so that the chlorine gas can be prevented from polluting the environment or damaging the human body.

In some embodiments of the present invention, the water pretreatment unit 100 includes a water filter 110 and a water softener 120 that are respectively electrically connected to the controller 800 through a pipeline, and the output end of the water softener 120 is respectively connected to the input end of the water flow rate control unit 200 and the input end of the brine output unit 300. Impurities in water can be removed by the water filter 110, and calcium and magnesium ions in the water can be removed and water quality can be activated by the water softener 120, so that water hardness can be reduced.

In some embodiments of the present invention, the water flow rate control unit 200 includes a pressure reducing valve 210, a first solenoid valve 220 and a flow sensor 230 which are sequentially connected through a pipeline and electrically connected to the controller 800, respectively, an input end of the pressure reducing valve 210 is connected to an output end of the water pretreatment unit 100, and an output end of the flow sensor 230 is connected to an input end of the electrolytic bath 400. The pressure reducing valve 210 can be used to adjust the speed of the water flow, the first solenoid valve 220 can be used to control the water flow passage of the water flow control unit 200, and the flow sensor 230 can be used to detect the water flow, so as to ensure the water flow is within the limited range. Specifically, the water flow rate adjusted by the pressure reducing valve 210 in the embodiment is 2-4L/min.

Wherein, the electrolysis trough 400 can be followed first delivery port and flowed neutral oxidation potential water when the electrolysis, simultaneously, at the exhaust in-process of neutral oxidation potential water, alkaline water then can be discharged in step to the second delivery port, and alkaline water then directly flows to the waste water mouth through the pipeline to concentrate the collection processing with alkaline water. In this embodiment, a three-way electromagnetic valve 410 is further disposed between the first water outlet and the second water outlet and the output end of the storage component 500, the first interface and the first water outlet of the three-way electromagnetic valve 410 are communicated, the second interface of the three-way electromagnetic valve 410 is communicated with the input end of the storage component 500, the first interface and the second water outlet of the first three-way electromagnetic valve 410 are connected and communicated with the wastewater outlet through a pipeline, in practical use, the second interface of the first three-way electromagnetic valve 410 can be closed, and the first water outlet discharges alkaline water and the second water outlet discharges neutral oxidation potential water by switching the polarity of the electrolytic cell 400.

In some embodiments of the present invention, the brine output unit 300 includes a brine tank 310 and a metering pump 320 which are connected through a pipe, an input end of the brine tank 310 is connected to an output end of the water pretreatment unit 100 through a second solenoid valve 330, an output end of the metering pump 320 is connected to an input end of the electrolytic bath 400, and the second solenoid valve 330 and the metering pump 320 are electrically connected to the controller 800 respectively. Specifically, the water flow rate of the metering pump 320 in this embodiment is 1-5 ml/min.

In some embodiments of the present invention, the brine tank 310 is provided with a water return pipe communicated with itself, and the water return pipe is provided with the first water pump 340 electrically connected to the controller 800. By using the first water pump 340, the brine in the brine tank 310 may be circularly mixed, so that the salt in the brine tank 310 may be sufficiently dissolved.

In some embodiments of the present invention, the storage part 500 includes a water storage tank 510 and at least two second water pumps 520, and the gas output end and the liquid input end are respectively disposed at the upper end of the water storage tank 510; the input end of each second water pump 520 is communicated with the bottom of the water storage tank 510, the output end of each second water pump 520 is communicated with the corresponding liquid output end, and the second water pumps 520 are electrically connected with the controller 800. By using the water storage tank 510, the generated neutral oxidation potential water can be stored in the water storage tank 510 before treatment, and then the neutral oxidation potential water is transported to the atomization assembly 600 for atomization by using the second water pump 520 when in use, and finally the atomized neutral oxidation potential water is output through the mist absorption part 700. Because the neutral oxidation potential water can release chlorine in the process of being stored for a long time, the chlorine can be discharged to the chlorine purifier 900 for purification through the gas output end at the upper end. Specifically, be equipped with four second water pumps 520 in this embodiment, can make the water velocity of flow that the treatment water route that each group corresponds remains stable provide neutral oxidation potential water to the atomization component 600 who corresponds, can avoid too big water pressure to lead to the utility model discloses an atomization component 600's atomizing frequency can't in time atomize to the water level that causes atomization component 600 is too high, makes the neutral oxidation potential water of liquid directly discharge with liquid state, causes the condition of chocking the wound to patient.

In some embodiments of the present invention, a gas pump is further disposed between the gas output end and the chlorine purifier 900 to effectively discharge chlorine gas, meanwhile, the air pump is electrically connected with the controller 800, the air pumping frequency of the air pump can be controlled, in addition, a chlorine concentration detector can be arranged at the upper end inside the water storage tank 510, so as to effectively monitor the concentration of the chlorine gas in the water storage tank 510 in real time, and can effectively discharge the chlorine gas by matching with the air pump, and at the same time, a liquid level detection sensor can be further arranged at the bottom inside the water storage tank 510 to monitor the liquid level of the water storage tank 510 in real time, so as to avoid the liquid level being lower than the horizontal height position of the output port of the water storage tank 510 connected with the second water pump 520, so that the chlorine gas can be prevented from being discharged toward the atomizing assembly 600 and the mist absorbing member 700, thereby avoiding the harm to the respiratory tract of the patient or the pollution caused by the direct discharge of the respiratory tract into the atmosphere.

In some embodiments of the present invention, the atomization assembly 600 comprises an atomization assembly 600 comprising an atomization box 610, an atomizer 620 and an air pump 630, wherein the input end of the atomization box 610 is communicated with the corresponding liquid output end, and the output end of the atomization box 610 is communicated with the input end of the corresponding mist suction component 700; the atomizer 620 is arranged at the bottom of the atomization box 610 and electrically connected with the controller 800; the air pump 630 is communicated with the upper end of the atomization box 610 through a pipeline and is electrically connected with the controller 800. In cooperation with the atomization assembly 600 and the water storage tank 510, the corresponding atomization assembly 600 can be activated during treatment. Specifically, in the present embodiment, the output end of the atomization box 610 is communicated with the corresponding mist suction component 700 through a third electromagnetic valve; the atomizer 620 is arranged at the bottom of the atomization box 610 and electrically connected with the controller 800; the air pump 630 is communicated with the upper end of the atomization box 610 through a pipeline and is electrically connected with the controller 800. The atomizer 620 is an ultrasonic atomization device, an embedded atomizer or a throw-in atomizer can be selected as required, and a corresponding atomization sheet is selected according to the type of the atomizer 620, specifically, the ultrasonic frequency of the atomizer 620 in the embodiment is 1.7-3 MHz, the atomization amount is not less than 0.1ml/min, the output pressure of the atomization gas of the atomization water tank is 5-40 kPa, and the output flow is 1-5L/min. Specifically, in the present embodiment, the atomizer 620 is electrically connected to the atomization frequency adjuster 1000, so as to adjust the atomization frequency of the atomizer 620.

Wherein, the utility model provides a water pretreatment component 100, the relief pressure valve 210, first solenoid valve 220, flow sensor 230, measuring pump 320, second solenoid valve 330, first water pump 340, electrolysis trough 400, three-way solenoid valve 410, second water pump 520, atomizer 620, air pump 630, the third solenoid valve, chlorine purifier 900, atomizing frequency regulator 1000, the aspiration pump, chlorine concentration detector and level sensor equally divide do not with controller 800 electric connection, by the operating condition of each parts above the controller 800 control, wherein, flow sensor 230 still feeds back the detected signal of discharge to controller 800, chlorine concentration detector feeds back the detected signal of chlorine concentration and the detected signal of level sensor to controller 800 feedback liquid level to controller 800.

It is conceivable that the mist suction member 700 may be a mouthpiece type, a nasal cavity type, or a mask type mist suction attachment according to the treatment requirement when the present invention is applied to the treatment of upper respiratory tract infection such as acute rhinitis, pharyngitis, laryngitis, bronchitis, etc.

The generation and characteristics of neutral oxidation potential water are further described by combining a specific processing scheme as follows:

the first scheme is as follows: NaCl is added into the brine tank 310, so that NaCl crystals are deposited at the bottom of the brine tank 310, the current of the electrolytic cell 400 is 10A, the voltage is 12V, the pressure reducing valve 210 is adjusted to enable the water flow to be 3L/min, the frequency of the metering pump 320 is adjusted to enable the brine flow to be 4ml/min, the pH value of neutral oxidation potential water is measured to be 5.2, the ORP (oxidation reduction potential) is 967mV, and the ACC (available chlorine content) is measured to be 46.5 mg/L.

Scheme II: NaCl is added into the brine tank 310, so that NaCl crystals are deposited at the bottom of the brine tank 310, the current of the electrolytic cell 400 is 10A, the voltage is 12V, the pressure reducing valve 210 is adjusted to enable the water flow to be 3L/min, the frequency of the metering pump 320 is adjusted to enable the brine flow to be 3ml/min, the pH value of neutral oxidation potential water is measured to be 5.7, the ORP (oxidation reduction potential) is 923mV, and the ACC (available chlorine content) is measured to be 38.4 mg/L.

The third scheme is as follows: NaCl is added into the brine tank 310, so that NaCl crystals are deposited at the bottom of the brine tank 310, the current of the electrolytic cell 400 is 10A, the voltage is 12V, the pressure reducing valve 210 is adjusted to enable the water flow to be 3L/min, the frequency of the metering pump 320 is adjusted to enable the brine flow to be 2ml/min, the pH value of neutral oxidation potential water is measured to be 6.3, the ORP (oxidation reduction potential) is 878mV, and the ACC (available chlorine content) is measured to be 30.1 mg/L.

And the scheme is as follows: NaCl is added into the brine tank 310, so that NaCl crystals are deposited at the bottom of the brine tank 310, the current of the electrolytic cell 400 is 8A, the voltage is 12V, the pressure reducing valve 210 is adjusted to enable the water flow to be 3L/min, the frequency of the metering pump 320 is adjusted to enable the brine flow to be 2ml/min, the pH value of neutral oxidation potential water is measured to be 6.5, the ORP (oxidation reduction potential) is 759mV, and the ACC (available chlorine content) is measured to be 22.3 mg/L.

And a fifth scheme: NaCl is added into the brine tank 310, so that NaCl crystals are deposited at the bottom of the brine tank 310, the current of the electrolytic cell 400 is 8A, the voltage is 12V, the pressure reducing valve 210 is adjusted to enable the water flow to be 3L/min, the frequency of the metering pump 320 is adjusted to enable the brine flow to be 1.5ml/min, the pH value of neutral oxidation potential water is measured to be 6.8, the ORP is 621mV, and the ACC (available chlorine content) is measured to be 14.1 mg/L.

According to the utility model discloses multichannel respiratory tract treatment equipment, through so setting, some effects as following at least can be reached, the utility model discloses with an atomizing component 600, an atomizing frequency regulator 1000, a fog part 700 constitution a set of branch road is inhaled to one, and communicate with same storage part 500 respectively, realize one and drag many effects, not only can reduce the occupation of land space, still can realize that two at least fog parts 700 can provide the course of treatment of disinfecting for two at least patients simultaneously, and an atomizing frequency regulator 1000 is connected alone to each atomizing component 600, can be according to patient's treatment demand, adjust the atomizing frequency that corresponds atomizing component 600, realize the control at treatment medium deposit position, and with this higher treatment effective concentration in focus position, promote treatment effect's purpose.

In the description herein, references to the description of the term "one embodiment," "some embodiments," "an illustrative embodiment," "an example," "a specific example," or "some examples" or the like mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the present invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.

While embodiments of the present invention have been shown and described, it will be understood by those of ordinary skill in the art that: various changes, modifications, substitutions and alterations can be made to the embodiments without departing from the principles and spirit of the invention, the scope of which is defined by the claims and their equivalents.

Claims (8)

1. A multi-pathway respiratory therapy apparatus, comprising:

the raw material output module is provided with a raw material output port;

the electrolytic cell is provided with a first water outlet and a second water outlet, and the input end of the electrolytic cell is communicated with the raw material output port;

a storage component having a gas output, a liquid input, and at least two liquid outputs, the liquid input communicating with the first water outlet;

the input end of each atomization assembly is communicated with the corresponding liquid output end;

the input end of each fog absorbing part is communicated with the output end of the corresponding atomization assembly;

at least two atomization frequency regulators, each atomization frequency regulator is electrically connected with the corresponding atomization assembly

And the controller is respectively electrically connected with the raw material output module, the electrolytic tank, the storage part, the atomization assembly and the atomization frequency regulator.

2. The multi-pathway respiratory therapy apparatus of claim 1, wherein the feedstock output module comprises:

a water pretreatment component;

the input end of the water flow rate control part is communicated with the output end of the water pretreatment part through a pipeline;

the input end of the brine output component is communicated with the output end of the water pretreatment component through a pipeline;

wherein, the output end of the brine output part is communicated with the output end of the water flow-rate control part to form the raw material output port.

3. The multi-pathway respiratory therapy apparatus of claim 2, wherein: the water pretreatment component comprises a water filter and a softened water processor which are sequentially communicated through a pipeline and are respectively and electrically connected with the controller, and the output end of the softened water processor is respectively communicated with the input end of the water flow speed control component and the input end of the brine output component.

4. The multi-pathway respiratory therapy apparatus of claim 2, wherein: the water flow rate control part comprises a pressure reducing valve, a first electromagnetic valve and a flow sensor which are sequentially communicated through a pipeline and are respectively electrically connected with the controller, the input end of the pressure reducing valve is communicated with the output end of the water pretreatment part, and the output end of the flow sensor is communicated with the input end of the electrolytic cell.

5. The multi-pathway respiratory therapy apparatus of claim 2, wherein: the brine output part comprises a brine tank and a metering pump which are communicated through a pipeline, the input end of the brine tank is communicated with the output end of the water pretreatment part through a second electromagnetic valve, the output end of the metering pump is communicated with the input end of the electrolytic cell, and the second electromagnetic valve and the metering pump are respectively electrically connected with the controller.

6. The multi-pathway respiratory therapy apparatus of claim 5, wherein: the brine tank is provided with a water return pipe communicated with the brine tank, and the water return pipe is provided with a first water pump electrically connected with the controller.

7. The multi-pathway respiratory therapy apparatus according to claim 1, wherein the storage component comprises:

the gas output end and the liquid input end are respectively arranged at the upper end of the water storage tank;

the input end of each second water pump is communicated with the bottom of the water storage tank, the output end of each second water pump is communicated with the corresponding liquid output end, and the second water pumps are electrically connected with the controller.

8. The multi-pathway respiratory therapy apparatus according to claim 1, wherein said nebulizing assembly comprises:

the input end of the atomization box is communicated with the corresponding liquid output end, and the output end of the atomization box is communicated with the input end of the corresponding mist suction component;

the atomizer is arranged at the bottom of the atomization box and is electrically connected with the controller;

the air pump, through the pipeline with the upper end intercommunication of atomizer box and with controller electric connection.

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