CN213609054U - Multi-channel new oxidation potential water treatment equipment - Google Patents
Multi-channel new oxidation potential water treatment equipment Download PDFInfo
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- CN213609054U CN213609054U CN202021728928.9U CN202021728928U CN213609054U CN 213609054 U CN213609054 U CN 213609054U CN 202021728928 U CN202021728928 U CN 202021728928U CN 213609054 U CN213609054 U CN 213609054U
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Abstract
The utility model relates to the technical field of medical equipment, a new oxidation potential water treatment facilities of multichannel is disclosed, can realize that a plurality of treatments contact member export treatment medium simultaneously. The utility model comprises a raw material output module, a controller, an electrolytic bath, a water flow direction control part, a first water pump, a treatment contact part and an atomization component, wherein the raw material output module is provided with at least two raw material output ports; constitute a set of branch road with electrolysis trough, water flow direction control unit, first water pump, treatment contact member and atomization component, electrolysis trough on each branch road communicates with same raw materials output module respectively, realizes the effect that one drags many, but every electrolysis trough autonomous working carries out the treatment for a plurality of patients, improves clinical treatment efficiency and treatment coverage, reduces and doctorss and nurses the manpower configuration, practices thrift the acquisition cost.
Description
Technical Field
The utility model relates to the technical field of medical equipment, in particular to a multi-channel new oxidation potential water treatment device.
Background
Acidic Electrolyzed Oxidizing Water (EOW) is liquid with high Oxidation Reduction Potential (ORP), low pH value, low concentration of available chlorine (ACC), active oxygen and hypochlorous acid, and has strong oxidizing ability and rapid microorganism killing effect. EOW has quickly gained acceptance by the national academy since 1995 when it entered the Chinese market. Through years of research and practice, the characteristics of broad-spectrum antibiosis, quick sterilization, safety, reliability, low cost, no toxic or side effect on human bodies, no residue and the like are commonly recognized, and the application field of the disinfectant is gradually expanded to the clinical treatment field along with the continuous and deep research.
At present, domestic oxidation potential water generating equipment can only be singly matched with one treatment contact part for treatment, when a plurality of patients exist, the actual treatment efficiency is lower, the waiting patients cannot be treated in time, meanwhile, the domestic oxidation potential water generating equipment is provided with a water storage tank for storing the electrolyzed oxidation potential water, so that the equipment volume is easy to cause overlarge, if a plurality of pieces of equipment are arranged for treatment, a larger space is needed for placing, in addition, as the storage time is increased, parameters of the acidic oxidation potential water can be rapidly reduced along with the increase of the storage time, and the disinfection and sterilization performance of the acidic oxidation potential water is greatly reduced. Therefore, the electrolyzed oxidizing water is suitable for being prepared and used at present, and the shorter the time interval between the preparation and the use is, the better the time interval between the preparation and the use is, so as to obtain the optimal disinfection concentration. Meanwhile, the traditional oxidation potential water generating equipment is provided with a water storage tank, and the preparation process of the water storage tank enables the newly prepared solution and the prepared solution to be continuously mixed, so that the mixing proportion is difficult to master, the mixing balance degree is low, the parameter stability is poor and the like; and the water storage tank is large in size, cannot be portable and light, occupies a large amount of hospital site resources, and seriously influences the use convenience and the popularity of the products.
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 new oxidation potential water treatment facilities of multichannel, can generate the treatment medium that has extremely strong killing effect to pathogenic microorganisms such as virus, bacterium, mould, and get rid of the stock solution link, effectively shorten preparation and time interval of use, in order to obtain the highest ORP value and the best bactericidal concentration, still realize multichannel concurrent therapy simultaneously, can implement the treatment for a plurality of patients simultaneously, improve clinical treatment efficiency and treatment coverage greatly, reduce and nurse the manpower configuration, practice thrift hospital's equipment acquisition cost, make gynaecology's physics anti-infection treatment realize the popularization, and realize equipment volume lightweight, improve user's convenience and popularization and application.
The multi-channel new oxidation potential water treatment equipment comprises a raw material output module, a controller, at least two electrolytic tanks, at least two water flow direction control parts, at least two first water pumps, at least two treatment contact parts and at least two atomization components, wherein the raw material output module is provided with at least two raw material output ports; each electrolytic cell is provided with a first water outlet and a second water outlet, and the input end of each electrolytic cell is respectively communicated with the corresponding raw material output port; each water flow direction control component is provided with a first water inlet end, a second water inlet end, a first water outlet end, a second water outlet end and a waste water end, each first water inlet end is communicated with the corresponding first water outlet, each second water inlet end is communicated with the corresponding second water outlet, and each water flow direction control component can control the communication between the first water inlet end of the water flow direction control component and the first water outlet end or the second water outlet end or the waste water end or the communication between the second water inlet end and the first water outlet end or the second water outlet end or the waste water end; the output end of each first water pump is communicated with the corresponding first water outlet end; the input end of each treatment contact component is communicated with the output end of the corresponding first water pump; the input end of each atomization component is communicated with the second water outlet end, and the output end of each atomization component is communicated with the input end of the treatment contact component; the controller is respectively and electrically connected with the raw material output module, the electrolytic bath, the water flow direction control part, the first water pump and the atomization assembly.
According to the utility model discloses new oxidation potential water treatment facilities of multichannel has following beneficial effect at least: the electrolysis bath, the water flow direction control part, the first water pump, the treatment contact part and the atomization assembly form a group of branches which are respectively communicated with the same raw material output module, so that the effect of one-to-many treatment is realized, the occupied space can be reduced, the treatment course of sterilization and disinfection treatment can be provided for at least two patients by at least two treatment contact parts, each electrolysis bath can work independently, and personalized treatment parameters can be provided according to the treatment requirements of different patients; the multi-channel setting can be used for treating a plurality of patients simultaneously, the ward circulation rate and the treatment efficiency can be effectively improved, the labor intensity of medical care is reduced, and the equipment acquisition cost of hospitals is saved.
According to some embodiments of the invention, the raw material output module comprises a water pretreatment component, a water flow rate control component, and a brine output component; the water flow rate control part is provided with at least two water raw material output ports, and 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 brine output component is provided with at least two brine output ports, and the input end of the brine output component is communicated with the output end of the water pretreatment component through a pipeline; wherein one of the water feedstock output ports is in communication with one of the brine output ports to form the feedstock 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 demineralized water treatment ware and heater, the output of heater with the input intercommunication of water velocity control part, the output of demineralized water treatment ware with the input intercommunication of salt solution output part.
According to some embodiments of the invention, the water flow rate control means comprises a pressure reducing valve, at least two first solenoid valves and at least two flow sensors electrically connected to the controller, respectively; the input end of the pressure reducing valve is communicated with the output end of the water pretreatment component; the first connecting port of each first electromagnetic valve is communicated with the output end of the pressure reducing valve; the input end of each flow sensor is communicated with the corresponding second connecting port of the first electromagnetic valve, and the output end of each flow sensor is communicated with the corresponding input end of the electrolytic cell.
According to some embodiments of the utility model, the salt solution output part includes the salt solution case and at least two measuring pumps that communicate with the salt solution case respectively, the input of salt solution case pass through the second solenoid valve with the output intercommunication of pretreatment of water part, each the output of measuring pump with correspond the electrolysis trough input intercommunication, second solenoid valve and each 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 second water pump.
According to some embodiments of the utility model, each water flow direction control part include respectively with controller electric connection's first three-way solenoid valve, second three-way solenoid valve, third three-way solenoid valve and fourth three-way solenoid valve: a first connecting port of the first three-way electromagnetic valve is communicated with the corresponding first water outlet, and a third connecting port of the first three-way electromagnetic valve is communicated with the corresponding waste water end; a first connecting port of the second three-way electromagnetic valve is communicated with the corresponding first water outlet, and a third connecting port of the second three-way electromagnetic valve is communicated with the corresponding waste water end; the first connecting port of the third three-way electromagnetic valve is respectively communicated with the second connecting port of the second three-way electromagnetic valve and the second connecting port of the first three-way electromagnetic valve, and the third connecting port of the third three-way electromagnetic valve is communicated with the corresponding input end of the atomization assembly; and a first connecting port of the fourth three-way electromagnetic valve is communicated with a third connecting port of the third three-way electromagnetic valve, a second connecting port of the fourth three-way electromagnetic valve is communicated with the corresponding first water pump, and a third connecting port of the fourth three-way electromagnetic valve is communicated with the corresponding waste water end.
According to some embodiments of the present invention, a fifth three-way solenoid valve is provided between the input of each of the therapeutic contact members, each of the first water pump and each of the output of the atomizing assembly.
According to some embodiments of the utility model, each atomization component include air pump, atomized water tank and set up in the atomizer of atomized water tank bottom, atomized water tank's upper end pass through the pipeline with the air pump intercommunication, atomized water tank's input with correspond the second goes out the water end intercommunication, atomized water tank's output with correspond treatment contact element's input intercommunication, the air pump with the atomizer respectively 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 neooxidation potential water treatment device according to an embodiment of the present invention.
Reference numerals: the device comprises a raw material output module 100, a water pretreatment component 110, a water softening processor 111, a heater 112, a water flow rate control component 120, a pressure reducing valve 121, a first electromagnetic valve 122, a flow sensor 123, a brine output component 130, a brine tank 131, a metering pump 132, a second electromagnetic valve 133, a second water pump 134, an electrolytic tank 200, a water flow direction control component 300, a first three-way electromagnetic valve 310, a second three-way electromagnetic valve 320, a third three-way electromagnetic valve 330, a fourth three-way electromagnetic valve 340, a first water pump 400, a treatment contact component 500, a fifth three-way electromagnetic valve 510, an atomization assembly 600, an air pump 610, an atomization water tank 620, an atomizer 630 and a controller 700.
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, it should be understood that the orientation or positional relationship indicated with respect to the orientation description, such as up, down, front, rear, left, right, etc., is based on the orientation or positional relationship shown in the drawings, and is only for convenience of description and simplification of description, and does not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting 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 there is a description of the first, second, third, fourth and fifth only for the purpose of distinguishing between 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 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 electrolyzed oxidizing water treatment apparatus according to the embodiment of the present invention comprises a raw material output module 100, a controller 700, at least two electrolysis baths 200, at least two water flow direction control components 300, at least two first water pumps 400, at least two treatment contact components 500, and at least two atomization components 600, wherein the raw material output module 100 is provided with at least two raw material output ports; each electrolytic cell 200 is provided with a first water outlet and a second water outlet, and the input end of each electrolytic cell 200 is respectively communicated with the corresponding raw material output port; each water flow direction control component 300 is provided with a first water inlet end, a second water inlet end, a first water outlet end, a second water outlet end and a waste water end, each first water inlet end is communicated with the corresponding first water outlet, each second water inlet end is communicated with the corresponding second water outlet, and each water flow direction control component 300 can control the communication between the first water inlet end of the water flow direction control component and the first water outlet end or the second water outlet end or the waste water end or the communication between the second water inlet end and the first water outlet end or the second water outlet end or the waste water end; the output end of each first water pump 400 is communicated with the corresponding first water outlet end; the input end of each treatment contact part 500 is communicated with the output end of the corresponding first water pump 400; the input end of each atomization assembly 600 is communicated with the second water outlet end, and the output end of each atomization assembly 600 is communicated with the input end of the treatment contact member 500; the controller 700 is electrically connected to the raw material output module 100, the electrolytic cell 200, the water flow direction control unit 300, the first water pump 400, and the atomizing assembly 600.
Each of the electrolysis cells 200, the water flow control unit 300, the first water pump 400, the atomization assembly 600 and the treatment contact unit 500 are in a group and provide treatment media with corresponding parameters to corresponding patients, and the raw material output module 100 provides raw materials to each group of electrolysis cells 200 individually, so that a dragging effect is achieved, and excessive space occupation of the device can be effectively avoided while treatment media are provided to a plurality of patients. Specifically, referring to fig. 1, in the present embodiment, there are four sets of branches consisting of the electrolytic cell 200, the water flow control unit 300, the first water pump 400, the atomizing assembly 600 and the treatment contact unit 500, and each branch can individually provide electrolyzed oxidizing water to the corresponding treatment contact unit 500.
In some embodiments of the present invention, the raw material output module 100 includes a water pretreatment part 110, a water flow rate control part 120, and a brine output part 130; the water flow rate control part 120 is provided with at least two water raw material output ports, and the input end of the water flow rate control part 120 is communicated with the output end of the water pretreatment part 110 through a pipeline; the brine output component 130 is provided with at least two brine output ports, and the input end of the brine output component 130 is communicated with the output end of the water pretreatment component 110 through a pipeline; wherein, a water raw material delivery outlet and a salt water delivery outlet intercommunication form the raw materials delivery outlet.
Wherein, the water pretreatment unit 110 is mainly used for softening or heating a water source to reduce water hardness, and the water flow rate control unit 120 is used for making the water flow into the corresponding electrolytic cell 200 at a stable water flow rate, and at the same time, part of the water passing through the water pretreatment unit 110 enters the brine output unit 130 to form saturated brine, and at the same time, the brine output unit 130 is used for inputting brine into the corresponding electrolytic cell 200 at a set water flow rate, and before the brine and the water flow enter the electrolytic cell 200, the brine and the water flow are mixed in an external pipeline to form low-concentration brine, and then the low-concentration brine enters the electrolytic cell 200, and then the electrode plates of the electrolytic cell 200 are electrified to make the low-concentration brine between the two electrode plates generate acidic electrolyzed-oxidized water, and then the water flow direction control unit 300 and the first water pump 400 are used for making the generated acidic electrolyzed-oxidized water flow to the treatment contact unit 500 or to the control unit 300 and the atomization assembly through the water flow direction 600 and then to the treatment contact member 500.
Simultaneously, through the first water pump 400 and the water flow rate control unit 120 that the cooperation corresponds, can make every treatment water route that corresponds keep stable water flow rate, still can avoid too big water pressure to lead to the utility model discloses a water route is overloaded, not only can make the water flow of the utility model is stable, can make the fluctuation range of the discharge of control be less than 10%, cooperates rivers to control unit 300 in addition, can be according to electrolysis trough 200 polarity transform and atomizing needs to the flow direction of adjustment acid oxidation potential water.
In some embodiments of the present invention, the water pretreatment unit 110 includes a water softening treatment device 111 and a heater 112 which are respectively electrically connected to the controller 700 through pipeline communication, the output end of the heater 112 is communicated with the input end of the water flow rate control unit 120, and the output end of the water softening treatment device 111 is communicated with the input end of the brine output unit 130. The softened water processor 111 can reduce water hardness to remove calcium and magnesium ions in water and activate water quality, and the heater 112 is matched to heat water, so that the temperature of the generated electrolyzed oxidizing water can be kept at 26-38 ℃, which is close to the body temperature of a human body, the treatment process is more comfortable, and the stability of the electrolyzed oxidizing water in the electrolytic cell 200 can be ensured, and the change of treatment parameters can be influenced because the temperature of the electrolyzed oxidizing water is too high or too low.
In some embodiments of the present invention, the water flow rate control part 120 includes a pressure reducing valve 121, at least two first solenoid valves 122, and at least two flow sensors 123 electrically connected to the controller 700, respectively; an input end of the pressure reducing valve 121 is communicated with an output end of the water pretreatment part 110, and specifically, an input end of the pressure reducing valve 121 is communicated with an output end of the heater 112; the first connection port of each first solenoid valve 122 is communicated with the output end of the pressure reducing valve 121; the input end of each flow sensor 123 is communicated with the second connection port of the corresponding first electromagnetic valve 122, and the output end of each flow sensor 123 is communicated with the input end of the corresponding electrolytic cell 200. The pressure reducing valve 121 can be used to adjust the speed of the water flow, and the first solenoid valve 122 can be used to control the water flow passage of the water flow rate control unit 120, and the flow sensor 123 can be used to detect the water flow rate, so as to ensure the water flow rate is within the limited range. Specifically, referring to fig. 1, in the present embodiment, four sets of branches are provided, so when one branch works, the water flow rate adjusted by the pressure reducing valve 121 is 2-4L/min; when two branches work simultaneously, the water flow regulated by the pressure reducing valve 121 is 4-4L/min, and when three branches work simultaneously, the water flow regulated by the pressure reducing valve 121 is 6-12L/min; when the four branches work simultaneously, the water flow regulated by the pressure reducing valve 121 is 8-16L/min; namely, the water flow at the output end of each flow sensor 123 is controlled to be 2-4L/min.
In some embodiments of the present invention, the brine output component 130 includes a brine tank 131 and at least two metering pumps 132 respectively communicated with the brine tank 131, an input end of the brine tank 131 is communicated with an output end of the water pretreatment component 110 through a second electromagnetic valve 133, specifically, an input end of the brine tank 131 is communicated with an output end of the water softening device 111 through the second electromagnetic valve 133, an output end of each metering pump 132 is communicated with an input end of the corresponding electrolytic cell 200, and the second electromagnetic valve 133 and each metering pump 132 are respectively electrically connected with the controller 700. Specifically, the water flow rate of each metering pump 132 in the embodiment is 5-10 ml/min.
In some embodiments of the present invention, the brine tank 131 is provided with a water return pipe communicated with itself, and the water return pipe is provided with the second water pump 134 electrically connected to the controller 700. By using the second water pump 134, the brine in the brine tank 131 can be circularly mixed, so that the salt in the brine tank 131 can be sufficiently dissolved.
In some embodiments of the present invention, each water flow direction control part 300 includes a first three-way solenoid valve 310, a second three-way solenoid valve 320, a third three-way solenoid valve 330, and a fourth three-way solenoid valve 340 electrically connected to the controller 700, respectively: a first connecting port of the first three-way electromagnetic valve 310 is communicated with a corresponding first water outlet, and a third connecting port of the first three-way electromagnetic valve 310 is communicated with a corresponding waste water end; a first connecting port of the second three-way electromagnetic valve 320 is communicated with a corresponding first water outlet, and a third connecting port of the second three-way electromagnetic valve 320 is communicated with a corresponding waste water end; the first connection port of the third three-way electromagnetic valve 330 is respectively communicated with the second connection port of the second three-way electromagnetic valve 320 and the second connection port of the first three-way electromagnetic valve 310, and the third connection port of the third three-way electromagnetic valve 330 is communicated with the input end of the corresponding atomization assembly 600; the first connection port of the fourth three-way solenoid valve 340 is communicated with the third connection port of the third three-way solenoid valve 330, the second connection port of the fourth three-way solenoid valve 340 is communicated with the corresponding first water pump 400, and the third connection port of the fourth three-way solenoid valve 340 is communicated with the corresponding waste water end.
Specifically, by controlling the states of the first three-way solenoid valve 310, the second three-way solenoid valve 320, the third three-way solenoid valve 330 and the fourth three-way solenoid valve 340 of each water flow control unit 300, the flow direction of the acidic oxidation water generated by the corresponding electrolytic cell 200 can be mainly in the following four states:
a. the acidic water of the electrolytic cell 200 flows to the treatment contact part 500 through the first water outlet, the first water inlet end, the first water outlet end and the first water pump 400, and at this time, the alkaline water of the electrolytic cell 200 flows to the wastewater end through the second water outlet and the second water inlet end;
b. the acidic water of the electrolytic cell 200 flows to the treatment contact member 500 through the first water outlet, the first water inlet end, the second water outlet end and the atomization assembly 600, and at this time, the alkaline water of the electrolytic cell 200 flows to the waste water end through the second water outlet and the second water inlet end;
c. the acidic water of the electrolytic cell 200 flows to the treatment contact part 500 through the second water outlet, the second water inlet end, the first water outlet end and the first water pump 400, and at this time, the alkaline water of the electrolytic cell 200 flows to the wastewater end through the first water outlet and the first water inlet end;
d. the acidic water of the electrolytic cell 200 flows to the treatment contact member 500 through the second water outlet, the second water inlet, the second water outlet and the atomization assembly 600, and at this time, the alkaline water of the electrolytic cell 200 flows to the waste water end through the first water outlet and the first water inlet.
In some embodiments of the present invention, a fifth three-way solenoid valve 510 is disposed between the input of each corresponding treatment contact member 500, each first water pump 400, and the output of each atomization assembly 600. The fifth three-way solenoid valve 510 is provided to control the therapeutic contact member 500 to communicate with the corresponding first water pump 400 or with the corresponding atomization assembly 600. The fifth three-way solenoid valve 510 is electrically connected to the controller 700, and the controller 700 controls the valve state of the fifth three-way solenoid valve 510.
It should be noted that the above-mentioned acidic water is acidic electrolyzed oxidizing water, and is a treatment medium for sterilization.
The controller 700 controls the water flow rate control part 120 and each first water pump 400, so that the water outlet flow of each electrolytic cell 200 can be kept consistent with the flow of the corresponding first water pump 400, the condition that the water tank needs to be temporarily stored because the water outlet flow of the electrolytic cell 200 is not equal to the output flow of the treatment contact part 500 can be avoided, and when the polarity of the electrolytic cell 200 is switched, the acidity and the alkalinity of the water outlet of the electrolytic cell 200 can be exchanged, so that the flow direction of the acidic electrolyzed oxidizing water generated by the electrolytic cell 200 can be controlled by matching with the corresponding water flow direction control component, and the acidic electrolyzed oxidizing water is ensured to continuously flow to the treatment contact part 500 or the atomization component 600; utilize rivers to control assembly, get rid of the stock solution link, not only can reduce the utility model discloses an equipment volume more can effectively shorten preparation and time interval who uses to acquire the highest ORP value and the best bactericidal concentration, can reduce simultaneously the utility model discloses the tie point of internal plant pipeline to reduced the safe risk that the pipe connection point leaked, and the utility model discloses the acidic oxidation potential water that generates has extremely strong effect of killing to pathogenic microorganisms such as virus, bacterium, mould.
In some embodiments of the present invention, each of the atomization components 600 includes an air pump 610, an atomization water tank 620 and an atomizer 630 disposed at the bottom of the atomization water tank 620, the upper end of the atomization water tank 620 is communicated with the air pump 610 through a pipeline, the input end of the atomization water tank 620 is communicated with the corresponding second water outlet end, the output end of the atomization water tank 620 is communicated with the corresponding input end of the treatment contact component 500, and the air pump 610 and the atomizer 630 are respectively electrically connected with the controller 700. The atomizer 630 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 630, specifically, the ultrasonic frequency of the atomizer 630 in this 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 620 is 5-40 kPa, and the output flow is 1-5L/min.
Wherein, the utility model provides a softened water treater 111, heater 112, relief pressure valve 121, first solenoid valve 122, flow sensor 123, measuring pump 132, second solenoid valve 133, second water pump 134, electrolysis trough 200, first three-way solenoid valve 310, second three-way solenoid valve 320, third three-way solenoid valve 330, fourth three-way solenoid valve 340, first water pump 400, fifth three-way solenoid valve 510, air pump 610 and atomizer 630 equally divide respectively with controller 700 electric connection, the operating condition of each parts more than the control of controller 700, wherein flow sensor 123 still feeds back the detected signal of discharge to controller 700.
In some embodiments of the present invention, the therapeutic contact member 500 is a disposable therapeutic head, and the disposable therapeutic head adopts a threaded tube made of medical PVC soft plastic material to increase the swirling drainage, so as to thoroughly flush the secretion; the air outlet and the tube body form an angle of 35-45 degrees to form a hole, so that the liquid outlet is not directly sprayed to the uterine orifice, and the infection of the ascending reproductive tract caused by the flushing of pathogenic secretion to the ascending reproductive tract is avoided; of course, the straight tube made of PC or PE material can be adopted, and the air outlet and the tube body are opened at an angle of 90 degrees.
In some embodiments of the present invention, the output water flow rate of each flow sensor 123 is 2-4L/min, the output water flow rate of each metering pump 132 is 5-10 ml/min, the current value of each electrolytic cell 200 is 6A-14A, and the voltage of each electrolytic cell 200 is 5-24V. Wherein the electrode distance of each electrolytic cell 200 is 4mm, and the current density is 60ma/cm2The effective area of the electrode is 100cm2. By utilizing the parameter range, the pH value of the electrolyzed oxidizing water generated by the electrolytic cell 200 is 2.5-4.5, the oxidation-reduction potential of the electrolyzed oxidizing water is +1000 to +1300mV, and the available chlorine content of the electrolyzed oxidizing water is 70-150 mg/L. At the moment, the acidic electrolyzed oxidizing water is mainly used for the genital tract of women, and the genital tract of women is sterilized and disinfected by the acidic electrolyzed oxidizing water with the parameters, so that the pH value of the vagina can be reduced to the initial state of the normal pH value of women of childbearing age; creates a slightly acidic environment which is beneficial to the recovery growth of the lactobacillus acidophilus. Meanwhile, ORP physical sterilization is taken as the leading factor, so that the absolute storage of the lactobacillus is selectively kept to the maximum extent while the pathogenic bacteria are killed. Thereby keeping the slightly acidic environment of the vagina from being damaged, and being beneficial to the continuous and recovery growth of lactobacillus and the reconstruction of the microecological environment of the vagina. At present, a large number of researches prove that the morbidity of common people and different patients with cervical lesions is obviously related to the change of the environment in the vagina and the distribution of flora such as vaginitis, fungal infection, candida infection and the like; is related to the interaction of chlamydia trachomatis, mycoplasma, herpes simplex virus and the like; the difference in incidence is statistically significant. The flora adjustment effect of the acidic oxidation potential water generated by the utility model can greatly reduce the HPV infection incidence rate and greatly reduce the probability of inducing cervical lesion due to HPV expression. Since genital tract is wrinkled, vaginal administration schemes such as gynecological lotion, suppository, effervescent tablet, etc. are commonly used withoutCan be disintegrated and fully contact with the focus part, and the atomization component 600 can enable the acidic oxidation potential water to exist in a fog state by adopting an ultrasonic atomization device, so that the focus part is fumigated, and the aim of treating without dead angles is fulfilled.
It is conceivable that the pH, oxidation-reduction potential, and available chlorine content of the electrolyzed oxidizing water may be adjusted in accordance with the sterilization and disinfection requirements, so as to be adaptable to the sterilization and disinfection effects of the respective portions.
It can be imagined that when being applied to the skin sterilization, the utility model can be applied to the treatment contact part 500 which can adopt an ultrasonic debridement system device, a negative pressure drainage device, a high-voltage pulse device, an automatic suction liquid level protection device, an electronic temperature control device, an ultrasonic handle and a medicine basin, when the treatment contact part 500 adopts the components, the utility model can form a comprehensive debridement treatment system, can effectively remove necrotic tissues, can remove large-area pollutants and bacteria at a deep sterilization speed by low-frequency ultrasonic waves and oxidation potential liquid, prevent infection and infection, and promote the regeneration of skin tissues; can be used for treating skin gangrene and diabetic foot.
It is conceivable that when the utility model is applied to oral disease treatment (periodontitis, gingivitis, oral ulcer) and oral cleaning and disinfection, mobile phone and impression sterilization and disinfection, the treatment contact part 500 can adopt a water-air foot switch, an air brake balance arm, a spray gun, a saliva aspirator, a strong aspirator, a negative pressure suction device and a mobile phone (a high-speed turbine mobile phone and a low-speed motor straight-bending mobile phone); when the treatment contact part 500 adopts the above components and is matched with the oral cavity cold light lamp and the film observing lamp, the utility model can form a micro-acidic oxidation potential oral cavity comprehensive treatment system.
It can be imagined that when will the utility model discloses be applied to upper respiratory infection, when treating such as acute rhinitis, pharyngitis, laryngitis, bronchitis, treatment contact part 500 can adopt ultrasonic frequency regulator, air duct, inhale fog annex (suction nozzle formula, nostril formula, face guard formula) and T type director, when treatment contact part 500 adopts above-mentioned subassembly, can make the utility model discloses constitute respiratory tract aerosol therapy appearance.
According to the multi-channel new oxidation potential water treatment equipment provided by the embodiment of the utility model, through the arrangement, at least the following effects can be achieved, one electrolytic cell 200, one water flow direction control part 300, one first water pump 400, one treatment contact part 500 and one atomization component 600 are combined and respectively communicated with the same raw material output module 100, so that the effect of one-driving-more is realized, the occupied space can be reduced, the treatment course of sterilization and disinfection treatment can be provided for at least two patients by at least two treatment contact parts 500, each electrolytic cell 200 can work independently, individualized parameter treatment can be provided according to the treatment requirements of different patients, the treatment medium output by each treatment contact part 500 can meet the requirements of different patients, the lightweight multi-channel arrangement is adopted, and the treatment can be carried out for a plurality of patients simultaneously, the patient is prevented from waiting for a long time, the clinical treatment efficiency and the treatment coverage are greatly improved, the medical manpower configuration is reduced, and the hospital equipment acquisition cost is saved.
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 (9)
1. A multi-channel neooxidation potential water treatment device is characterized by comprising:
the raw material output module is provided with at least two raw material output ports;
each electrolytic cell is provided with a first water outlet and a second water outlet, and the input end of each electrolytic cell is respectively communicated with the corresponding raw material output port;
each water flow direction control component is provided with a first water inlet end, a second water inlet end, a first water outlet end, a second water outlet end and a waste water end, each first water inlet end is communicated with the corresponding first water outlet, each second water inlet end is communicated with the corresponding second water outlet, and each water flow direction control component can control the communication between the first water inlet end of the water flow direction control component and the first water outlet end, the second water outlet end or the waste water end, or the communication between the second water inlet end and the first water outlet end, the second water outlet end or the waste water end;
the output end of each first water pump is communicated with the corresponding first water outlet end;
the input end of each treatment contact component is communicated with the output end of the corresponding first water pump;
at least two atomization assemblies, wherein the input end of each atomization assembly is communicated with the second water outlet end, and the output end of each atomization assembly is communicated with the input end of the treatment contact component;
and the controller is respectively electrically connected with the raw material output module, the electrolytic tank, the water flow direction control part, the first water pump and the atomization assembly.
2. The multi-pass neoxidation potentiometric water treatment apparatus of claim 1, wherein the raw material output module comprises:
a water pretreatment component;
the water flow rate control part is provided with at least two water raw material output ports, and 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 brine output component is provided with at least two brine output ports, and the input end of the brine output component is communicated with the output end of the water pretreatment component through a pipeline;
wherein one of the water feedstock output ports is in communication with one of the brine output ports to form the feedstock output port.
3. The multi-pass neoxidation potentiometric water treatment apparatus of claim 2, wherein: the water pretreatment component comprises a water softening processor and a heater which are communicated through a pipeline in sequence and are respectively electrically connected with the controller, the output end of the heater is communicated with the input end of the water flow rate control component, and the output end of the water softening processor is communicated with the input end of the brine output component.
4. The multi-channel neoxidation potentiometric water treatment apparatus of claim 2 wherein the water flow rate control means comprises:
the input end of the pressure reducing valve is communicated with the output end of the water pretreatment component;
the first connecting port of each first electromagnetic valve is communicated with the output end of the pressure reducing valve;
the input end of each flow sensor is communicated with the corresponding second connecting port of the first electromagnetic valve, and the output end of each flow sensor is communicated with the corresponding input end of the electrolytic cell.
5. The multi-pass neoxidation potentiometric water treatment apparatus of claim 2, wherein: the brine output part comprises a brine tank and at least two metering pumps which are respectively communicated with the brine tank, 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 each metering pump is communicated with the input end of the corresponding electrolytic cell, and the second electromagnetic valve and each metering pump are respectively electrically connected with the controller.
6. The multi-pass neoxidation potentiometric water treatment 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 second water pump electrically connected with the controller.
7. The multi-channel neoxidation potentiometric water treatment apparatus of claim 1 wherein each of the water flow control assemblies comprises:
a first connecting port of the first three-way electromagnetic valve is communicated with the corresponding first water outlet, and a third connecting port of the first three-way electromagnetic valve is communicated with the corresponding waste water end;
a first connecting port of the second three-way electromagnetic valve is communicated with the corresponding first water outlet, and a third connecting port of the second three-way electromagnetic valve is communicated with the corresponding waste water end;
a first connecting port of the third three-way electromagnetic valve is respectively communicated with the second connecting port of the second three-way electromagnetic valve and the second connecting port of the first three-way electromagnetic valve, and a third connecting port of the third three-way electromagnetic valve is communicated with the corresponding input end of the atomization assembly;
and a first connecting port of the fourth three-way electromagnetic valve is communicated with a third connecting port of the third three-way electromagnetic valve, a second connecting port of the fourth three-way electromagnetic valve is communicated with the corresponding first water pump, and a third connecting port of the fourth three-way electromagnetic valve is communicated with the corresponding waste water end.
8. The multi-pass neoxidation potentiometric water treatment apparatus of claim 1, wherein: and a fifth three-way electromagnetic valve is arranged between the input end of each corresponding treatment contact component and the output ends of each first water pump and each atomization assembly.
9. The multi-pass neoxidation potentiometric water treatment apparatus of claim 1, wherein: each atomization component includes air pump, atomized water tank and set up in the atomizer of atomized water tank bottom, atomized water tank's upper end pass through the pipeline with the air pump intercommunication, atomized water tank's input with correspond the second goes out water end intercommunication, atomized water tank's output with correspond the input intercommunication of treatment contact member, the air pump with the atomizer respectively with controller electric connection.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021728928.9U CN213609054U (en) | 2020-08-18 | 2020-08-18 | Multi-channel new oxidation potential water treatment equipment |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202021728928.9U CN213609054U (en) | 2020-08-18 | 2020-08-18 | Multi-channel new oxidation potential water treatment equipment |
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| CN213609054U true CN213609054U (en) | 2021-07-06 |
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