CN107082517B - Water treatment system for phased array focusing ultrasonic hysteromyoma treatment system - Google Patents
Water treatment system for phased array focusing ultrasonic hysteromyoma treatment system Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61N—ELECTROTHERAPY; MAGNETOTHERAPY; RADIATION THERAPY; ULTRASOUND THERAPY
- A61N7/00—Ultrasound therapy
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/003—Wastewater from hospitals, laboratories and the like, heavily contaminated by pathogenic microorganisms
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
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- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Public Health (AREA)
- Radiology & Medical Imaging (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Veterinary Medicine (AREA)
- Hydrology & Water Resources (AREA)
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Abstract
The invention discloses a water treatment system for a phased array focusing ultrasonic hysteromyoma treatment system, which comprises a water purification device, an RO reverse osmosis waste water reflux device, an ultraviolet lamp sterilization device, an ultra-pure deionization device, a degasification water device, a condensed water and water vapor separation device, a condensed water recycling device, a condensed water automatic drainage device, a degasification water tank management device, a treatment head component, a water bag water pressure adjusting module device and a constant-temperature degasification water proportion mixing and recycling device. The invention does not need an additional water and electricity heating device, utilizes the accumulated heat generated in the working process of the ultrasonic transducer to pass through a booster pump, a condensate water device, a cold-hot water mixing ratio three-way valve and a pipeline, neutralizes to reach constant temperature deaerated water, a reverse osmosis waste water backflow module, reduces the requirement of tap water quantity, detects the dissolved oxygen value, the water temperature value, the conductivity, the deaerated water quantity, the pressure value of a water collector and the water pressure in real time in the whole running process of the system, thereby achieving the purposes of water and electricity saving, low power consumption, long service life, small volume and stable deaerated water.
Description
Technical Field
The invention relates to the field of high-intensity focusing ultrasonic treatment equipment, in particular to a water treatment system for a phased array focusing ultrasonic hysteromyoma treatment system.
Background
A phased array focusing ultrasonic hysteromyoma treatment system is characterized in that ultrasonic waves emitted by a phased array ultrasonic transducer can be coupled into tissues to be focused only through medium water, the degassed water has good acoustic permeability and is low in price, the commonly used degassed water is used as the medium water, when a treatment head works at high intensity and high power, the degassing completeness of the degassed water and the temperature in the treatment process increase the dissolved oxygen content of the degassed water, the acoustic impedance of the transducer is seriously influenced, the ultrasonic waves emitted by the treatment head are attenuated, the clinical radiation dose is unexpectedly changed, and the size of side lobes cannot be controlled. The degassing degree and the supply of medium water become key factors influencing treatment, and in order to meet relevant national standard and performance requirements, two methods are usually adopted in the current industry, namely a heating atomization vacuumizing method and a vacuum pumping method by matching a filter element and a reverse osmosis membrane degassing membrane.
The conventional equipment at present has the following defects:
the vacuum pump has high negative pressure, the booster pump has large volume and large power, the noise is large, the quantity of water tanks is large, the water tanks have large volume, return water recycling devices and ultra-purification devices are avoided, electric heating is needed before water treatment, the water consumption is high, the power consumption is high, the pump is easy to age, the leakage safety risk and the failure rate are increased, the water quality conversion efficiency is low, pipeline parts are easy to corrode and age, the types and the quantity of filters are large, the size is large, and the integration, the miniaturization and the portability are inconvenient; the reverse osmosis membrane has no waste water reflux device, the degassed water quality detection adopts a common membrane method for sampling detection, the actual measurement result error caused by flow rate and temperature is overlarge, no ultraviolet lamp irradiation is caused, the total organic carbon is higher, microorganisms are bred on the tube wall, no condensation collecting device is arranged, no constant-temperature degassed water recycling device is arranged, and no automatic drainage device for a degassed water tank, a pipeline and a water collector is arranged.
The requirements cannot be really met.
Disclosure of Invention
In view of the above-mentioned deficiencies in the prior art, it is an object of the present invention to provide a water treatment system for a phased array focused ultrasound uterine fibroid treatment system.
The invention is realized by the following technical scheme.
The utility model provides a be used for phased array focus supersound uterus myoma treatment system water processing system, includes water purification installation, RO reverse osmosis abandons water reflux unit, ultraviolet lamp sterilizing equipment, super purification deionization device, degasification water installation, comdenstion water steam separator, comdenstion water cyclic utilization device, degasification water tank management device, treatment head subassembly, water pocket water pressure adjusting module device, constant temperature degasification water proportional mixing recycles device and comdenstion water automatic drainage device, wherein:
water purification installation links to each other with RO reverse osmosis abandon water reflux unit, RO reverse osmosis abandon water reflux unit links to each other with ultraviolet lamp sterilizing equipment, comdenstion water cyclic utilization device, the mixed device of recycling of constant temperature degasification water proportion and comdenstion water automatic drainage device respectively, ultraviolet lamp sterilizing equipment links to each other with super purification deionization device, super purification deionization device links to each other with degasification water installation, degasification water installation links to each other with comdenstion water vapor separation device and degasification water tank management device respectively, comdenstion water vapor separation device links to each other with comdenstion water cyclic utilization device, comdenstion water cyclic utilization device links to each other with degasification water installation, degasification water tank management device links to each other with the treatment head subassembly, the treatment head subassembly links to each other with water bag water pressure regulation module device, water bag water pressure regulation module device links to each other with the mixed device of constant temperature degasification water proportion.
The water purification device comprises a water inlet pipeline J100, a water inlet electromagnetic valve KM1 and a PP filter Z100; wherein:
the water inlet pipeline J100 is connected with a water inlet electromagnetic valve KM1, the water inlet electromagnetic valve KM1 is connected with a PP filter Z100, and the output end of the PP filter Z100 is connected with an RO reverse osmosis waste water reflux device.
The RO reverse osmosis waste water reflux device comprises a pressure regulating valve T100, a waste water reflux module Z106, a booster pump Z101, an RO reverse osmosis membrane, a three-way joint T200, an electromagnetic valve KM6 and a four-way joint T400; wherein:
the input port 21 of the pressure regulating valve T100 is connected with a water purifying device, the first output port of the pressure regulating valve T100 is connected with the output end of a wastewater backflow module Z106, the input end of the waste water backflow module Z106 is connected with the input port 25 of the connected three-way joint T200, the first output port 26 of the three-way joint T200 is connected with the solenoid valve KM6, the second output port 23 of the pressure regulating valve T100 is connected with the input end of the booster pump Z101, the output end of the booster pump Z101 is connected with the input port 9 of the RO reverse osmosis membrane, the output port 11 of the RO reverse osmosis membrane is connected with the second output port 24 of the three-way joint T200, the solenoid valve KM6 is connected with the input port 12 of the four-way joint T400, the first output port 15 of the four-way joint T400 is connected with a condensed water automatic drainage device, the second output port 13 of the four-way joint T400 is connected with a condensed water recycling device, and the third output port 14 of the four-way joint T400 is connected with a constant-temperature degassed water proportional mixing recycling device.
The ultraviolet lamp sterilization device comprises a dual-wavelength ultraviolet lamp Z104, the output end of the dual-wavelength ultraviolet lamp Z104 is connected with an ultra-purification deionization device, and the input end of the dual-wavelength ultraviolet lamp Z104 is connected with an RO reverse osmosis waste water reflux device.
The ultra-purification deionization device comprises an ultra-purification water column Z105, a conductivity sensor Z107 and a water pressure sensor T107; wherein:
the output end of the ultra-pure water column Z105 is connected with the input end of a conductivity sensor Z107, the output end of the conductivity sensor Z107 is connected with the input end of a water pressure sensor T107, and the output end of the water pressure sensor T107 is connected with a water degassing device.
The degassing water device comprises a three-way electromagnetic valve Q106, a liquid degassing membrane Z108, a semiconductor condenser L100 and an electromagnetic valve KM3; the condensed water and water-vapor separation device comprises a water collector J200, a water collection position sensor TS100, an electromagnetic valve KM5, a water collection membrane J201, a pressure release valve M201, a pressure sensor M202, an electromagnetic valve KM4, a three-way electromagnetic valve Q101, a vacuum pump Z103, a three-way electromagnetic valve Q102 and a polymer silencer X100; the condensate water recycling device comprises a through type electromagnetic valve KM7, a three-way electromagnetic valve Q104 and a three-way electromagnetic valve Q105; the automatic condensed water drainage device comprises a wastewater electromagnetic valve KM8 and a wastewater pipeline F100; wherein:
an input port P of the three-way electromagnetic valve Q106 is connected with the ultra-purification deionization device, an input port T of the three-way electromagnetic valve Q106 is communicated with an output port A of the three-way electromagnetic valve Q106, the output port A of the three-way electromagnetic valve Q106 is connected with an input port 1 of a liquid degassing membrane Z108, and an output port 2 of the liquid degassing membrane Z108 is connected with a degassed water tank management device; a first degassing port 3B of a liquid degassing membrane Z108 is connected with an input end of a semiconductor condenser L100, an output end of the semiconductor condenser L100 is connected with a solenoid valve KM3, the solenoid valve KM3 is connected with an input port 16 of a water collector J200, an output port 40 of the water collector J200 is connected with a through solenoid valve KM7, an output port 19 of the water collector J200 is connected with a through solenoid valve KM4, an output port 20 of the water collector J200 is connected with a solenoid valve KM5, the solenoid valve KM5 is connected with an output port P of a three-way solenoid valve Q102, a pressure relief port 17 of the water collector J200 is provided with a pressure relief valve M201, a pressure transmission port 18 of the water collector J200 is provided with a pressure sensor M202, a water collection position sensor TS100 and a water collection membrane J201 are arranged inside the water collector J200, the water collection membrane J201 is transversely filled in the water collector J200, the input port T of the three-way solenoid valve Q101 is connected with an input port T of the three-way solenoid valve Q101, an input port T of the three-way solenoid valve Q101 is communicated with an output port A of the three-way solenoid valve Q101, an output port A of the three-way solenoid valve Q101 is connected with an input port Q102 of a vacuum pump Z103, an output port Q102, an output port of the vacuum pump Z102, and an output port of the three-way solenoid valve Q102X of the three-way solenoid valve Q102 is communicated with an X of the three-way solenoid valve Q102; the penetration type electromagnetic valve KM7 is connected with an input port A of a three-way electromagnetic valve Q104, the input port A of the three-way electromagnetic valve Q104 is communicated with an output port T of the three-way electromagnetic valve Q104, the output port T of the three-way electromagnetic valve Q104 is connected with an input port T of a three-way electromagnetic valve Q105, the input port T of the three-way electromagnetic valve Q105 is communicated with the output port A of the three-way electromagnetic valve Q105, and the output port A of the three-way electromagnetic valve Q105 is connected with an input port T of a three-way electromagnetic valve Q106; an output port P of the three-way electromagnetic valve Q104 is connected with an RO reverse osmosis waste water reflux device; an input port P of the three-way electromagnetic valve Q105 is connected with the constant-temperature degassing water proportional mixing recycling device; the electromagnetic valve KM8 is arranged on a wastewater water pipe F100, and the input end of the wastewater water pipe F100 is connected with an RO reverse osmosis waste water reflux device.
The degassed water tank management device comprises a degassed water tank W100, a fluorescence detection head W101, a dissolved oxygen transmitter W103, a liquid level sensor W102, a drain PK1, a three-way joint T500 and a peristaltic pump W104; wherein:
the fluorescence detection head W101 and the liquid level sensor W102 are respectively arranged in the degassed water tank W100; fluorescence method detecting head W101 outer end links to each other with dissolved oxygen changer W103, degassed water tank W100 lateral wall links to each other with peristaltic pump and degassed water device respectively through the pipeline, degassed water tank W100's top is equipped with gas vent PK1, gas vent PK1 is connected through the input of tube coupling three way connection T500, and evacuation pipe K100 and water pocket water pressure regulation module device are connected respectively to three way connection T500's two outputs.
The treatment head component comprises a treatment head, wherein the treatment head comprises a telescopic silica gel water bag H100, an aluminum casting substrate SH100 and a B-ultrasonic probe B100; wherein:
the telescopic silica gel water bag H100 is arranged on the aluminum cast substrate SH100, and the B ultrasonic probe B100 is arranged inside the aluminum cast substrate SH 100; the aluminum casting substrate SH100 is respectively connected with a degassed water tank management and water bag water pressure regulation module device.
Water pocket water pressure regulation module device, including water pocket water pressure regulation water column module SY100 and elevator motor module M200, wherein, water pocket water pressure regulation water column module SY100 includes two regulation water columns that communicate each other, and wherein the built-in high water position trigger TS101 of first regulation water column, the top of first regulation water column are equipped with evacuation mouth PK2, evacuation mouth PK2 is connected with degasification water tank management device, and the bottom of first regulation water column is passed through the pipeline and is connected with the treatment head subassembly, and the second is adjusted the water column and is recycled the device with elevator motor module M200 and constant temperature degasification water proportional mixing respectively and is connected. Constant temperature degasification water proportional mixing recycles device, including booster pump Z102 and three-way solenoid valve Q103, wherein:
the input end of the booster pump is connected with the water bag water pressure adjusting module device, the output end of the booster pump is connected with the input port A of the three-way electromagnetic valve Q103, the input port A of the three-way electromagnetic valve Q103 is communicated with the output port T of the three-way electromagnetic valve Q103, the output port T of the three-way electromagnetic valve Q103 is connected with the condensate water recycling device, and the output port P of the three-way electromagnetic valve Q103 is connected with the RO reverse osmosis waste water backflow device.
The water treatment system for the phased array focused ultrasound hysteromyoma treatment system further comprises a central control unit, a multi-path power supply module, a communication module, an upper computer and a display and input unit; wherein:
the multi-path power supply module is connected with the central control unit, and the central control unit is connected with the upper computer through the communication module; the display and input unit is connected with the central control unit;
the central control unit is respectively in control connection with the water purification device, the RO reverse osmosis waste water reflux device, the ultraviolet lamp sterilization device, the ultra-purification deionization device, the deaerating water device, the condensed water and vapor separation device, the condensed water recycling device, the condensed water automatic drainage device, the deaerating water tank management device, the treatment head assembly, the water bag water pressure adjusting module device and the constant-temperature deaerating water proportion mixing recycling device; and the multi-path power supply module and the peristaltic pump of the degassed water tank management device are respectively connected with an external conducting wire.
Compared with the prior art, the invention has the following beneficial effects:
1. the invention adopts a fluorescence method probe and a multi-wavelength technology to thoroughly and completely solve the influence of flow rate and temperature; and for the problems of overlarge volume and excessive quantity of the water tank, the RO reverse osmosis waste water backflow technology is adopted, and the service life of the RO reverse osmosis membrane is prolonged by reducing the loss of waste water and increasing the water yield.
2. The invention adopts the design of the water collector, atomized water vapor brought by a degassing membrane can be changed into water drops through semiconductor condensation and enters the water collector together with pipeline water, the water vapor is retained in the water collector by adopting the water-collecting membrane, the pipeline pumped by the vacuum pump does not contain the water vapor, the service life of the vacuum pump is prolonged, the phenomenon that gas discharged from the pipeline does not contain the water vapor is eliminated, the oxidation of the water vapor to a metal structure is reduced, the vacuum pump is connected with the polymer silencer, the noise of equipment is reduced, the service life of the equipment is prolonged, the polymer silencer with small volume is used, the size is small, the installation is convenient, the attenuation is low, and the comfort of the equipment is enhanced. The low-temperature condensed water in the water collector is used, so that the constant temperature of the degassing water is kept, the service life of a degassing membrane is prolonged, and the water quantity requirement of equipment is reduced.
3. By using the pumping and beating dual-purpose vacuum pump, the low-temperature condensed water in the water collector can be added into the constant-temperature degassing water recirculation pipeline through the cold-hot water mixing ratio three-way electromagnetic valve for degassing again, the service life of the degassing membrane is prolonged, and the condensed water in the water collector can be pushed out of the wastewater pipeline.
4. The pressure of the water bag of the energy conversion disc is adjusted by the corrugated telescopic water bag and the water column pressure adjusting device, the pressure of the water bag is continuously adjusted, the treatment focus is adjustable, the structure is simple, and the reliability is high. The ultra-pure degassing water circulating device has high circulating supply pressure, low requirement on pipeline structure design, strong adaptability of pipeline installation and high automatic control degree. The pp filter replaces the traditional filter of traditional activated carbon, filling cotton and soft water resin, and has the advantages of high filtering efficiency, long service life, low filtering cost, high safety and strong adaptability. By adopting the dual-wavelength ultraviolet lamp for illumination, TOC (total organic carbon) can be degraded, and bacteria can be prevented from breeding on the tube wall.
Drawings
FIG. 1 is a schematic diagram of a water treatment system for a phased array focused ultrasound uterine fibroid treatment system in accordance with the present invention;
FIG. 2 is a schematic control diagram of a water treatment system for a phased array focused ultrasound hysteromyoma treatment system of the present invention.
Detailed Description
The following examples illustrate the invention in detail: the embodiment is implemented on the premise of the technical scheme of the invention, and a detailed implementation mode and a specific operation process are given. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the inventive concept, which falls within the scope of the present invention.
Examples
The working principle and the process of the invention of the system are explained in detail by combining the attached drawings in the invention, and the system comprises water purification equipment, an RO reverse osmosis waste water reflux device, an ultraviolet lamp sterilization device, a deaerating water device, a condensed water and water-vapor separation device, a condensed water recycling device, an ultra-purification deionization device, a deaerating water tank management device, a treatment head assembly, a water bag water pressure adjusting module device, a constant-temperature deaerating water proportion mixing and recycling device and a condensed water automatic drainage device.
To phased array focus supersound hysteromyoma treatment system's water processing system, the filter is bulky, the kind, in large quantity, the effect is poor, the life-span is short, maintain difficult, this embodiment adopts polypropylene PP filter to replace the tradition to adopt the cotton packing, activated carbon, soft water resin, the design contains inlet channel J100, the water inlet solenoid valve KM1 who links to each other with inlet channel J100, the polypropylene PP filter Z100 who links to each other with inlet channel KM1, polypropylene PP filter Z100 output and pressure regulating valve T100 mouth 21.
The water treatment system for the phased array focused ultrasound hysteromyoma treatment system is high in water consumption, low in water yield, high in RO membrane vacuum degree requirement and short in service life, and the embodiment comprises a wastewater backflow module Z106 output end connected with a 22 port on a pressure regulating valve T100, a three-way joint T200 port 25 connected with the wastewater backflow module Z106, a solenoid valve KM6 connected with a 26 port on the three-way joint T200, a booster pump Z101 input end connected with a 23 port on the pressure regulating valve T100, a booster pump Z101 works, an RO reverse osmosis membrane port 9 connected with the output end of the booster pump Z101, a three-way joint T200 port 24 connected with an RO reverse osmosis membrane port 11, a solenoid valve KM6 communicated with a 26 port on the three-way joint T200, a four-way joint T400 port 12 connected with the solenoid valve KM6, and a wastewater solenoid valve KM8 communicated with a 15 port on the four-way joint T400.
To phased array focus supersound hysteromyoma treatment system's water treatment system, total organic carbon of TOC is on the high side, and the pipe wall easily breeds the microorganism, and this embodiment contains the dual wavelength ultraviolet lamp Z104 who links to each other with RO reverse osmosis membrane mouth 10, adopts the dual wavelength ultraviolet lamp to shine, reduces the TOC quantity, reduces water pollution, reduces the TOC, prevents that the microorganism from nourishing.
In the embodiment, through an ultra-pure water column Z105 connected with an output port of a dual-wavelength ultraviolet lamp Z104, a conductivity sensor Z107 connected with an output end of the ultra-pure water column Z105, a water pressure sensor T107 connected with an output end of the conductivity sensor Z107, a three-way electromagnetic valve Q106 port P connected with the water pressure sensor T107, the conductivity value detected by the conductivity sensor Z107 after ultra-purification is transmitted to a central control unit CPU200, the pipeline pressure abnormality in the ultra-purification process is detected by the water pressure sensor T107 and transmitted to the central control unit CPU200 for processing, and the instability of water supply pressure and air intake, which cause the instability of conductivity after ultra-purification, of the water treatment system of the phased array focusing ultrasonic hysteromyoma treatment system are prevented.
In the water treatment system aiming at the phased array focused ultrasound hysteromyoma treatment system, the vacuum pump has high negative pressure, high power, large volume of a vacuum bottle, high noise, low use efficiency of a degassing membrane, no low-temperature condensed water recovery device, no water collection membrane design, short service life of the degassing membrane, and the quality of the degassed water is easily influenced by the measured flow rate and temperature shadow, the service life of the vacuum pump is influenced by water vapor in scavenging gas of a liquid degassing membrane, and the water vapor discharged by the vacuum pump is easily aged and rusted by a metal structure in the equipment, in the embodiment, a three-way electromagnetic valve Q106 port P is communicated with a Q106 port A, a liquid degassing membrane Z108 port 1 connected with the Q106 port A end of the three-way electromagnetic valve Q106, a degassed water tank W100 port 4 connected with a Z108 port 2 of the liquid degassing membrane, a semiconductor condenser L100 connected with a Z108 port 3B of the liquid degassing membrane is opened, an electromagnetic valve KM3 connected with the semiconductor condenser L100 is communicated, a water collector J200 port 16 connected with the electromagnetic valve KM3, and a run-through electromagnetic valve KM7 connected with a port 40 of the water collector J200 is disconnected, the device comprises a solenoid valve KM4 connected with a port 19 of a water collector J200, a solenoid valve KM5 disconnected connected with a port 20 of the water collector J200, a pressure relief valve M201 connected with a port 17 of the water collector J200, the pressure relief valve M201 is used for protecting pressure abnormity, a pressure sensor M202 connected with a port 18 of the water collector J200 is used for pressure detection and transmission to a central control unit CPU200, a water collection position sensor TS100 arranged inside the water collector J200 is used for detecting and transmitting low-temperature condensed water quantity to the central control unit CPU200 for processing, a water collection film J201 arranged inside the water collector J200 and connected up and down, the water collection film J201 is used for absorbing low-temperature condensed water vapor to the bottom of the water collector J200, a three-way solenoid valve Q101 port T connected with the solenoid valve KM4, a three-way solenoid valve Q101 port T is communicated with a port A, a vacuum pump Z103 input end connected with the three-way solenoid valve Q101 port A, the vacuum pump Z103 is opened, and a three-way solenoid valve Q102 port A connected with the vacuum pump Z103 output end, the three-way electromagnetic valve Q102 port A is communicated with the port T, a high polymer silencer X100 connected with the three-way electromagnetic valve Q102 port T is used for condensing cleaning air containing a large amount of water vapor from a liquid degassing membrane Z108 port 3 into low-temperature condensate water, the low-temperature condensate water enters a water collector through a pipeline electromagnetic valve KM3 through a port 16 of a water collector J200, a water collecting membrane J201 is installed on the water collector, the low-temperature condensate water is sucked by the water collecting membrane J201 to the bottom of the water collector J200, the air without the water vapor is communicated with the three-way electromagnetic valve Q101 port T through an electromagnetic valve KM4 after coming out through a port 19 of the water collector J200, the port T of the three-way electromagnetic valve Q101 is connected, the port A of the three-way electromagnetic valve Q101 is connected with the input end of a vacuum pump Z103, the output end of the vacuum pump Z103 is connected with the port A of the three-way electromagnetic valve Q102, the air without the water vapor is connected with the high polymer silencer X100 through the port T of the three-way electromagnetic valve Q102 port T, the high polymer silencer X100 is small in size, high attenuation is high in noise is low, the installation is convenient, the air without the high polymer silencer X100 discharges the air without the moisture, and the metal silencer X100, and the comfort level of metal structure of the metal aging of the internal equipment is reduced.
The water treatment system aims at a phased array focused ultrasound hysteromyoma treatment system, detection is carried out by a common membrane method, errors of actual measurement results are overlarge due to flow rate and temperature, water quantity of a degassed water tank is inaccurate to control, and a treatment interruption waiting phenomenon often occurs.
Aiming at the water treatment system of the phased array focusing ultrasonic hysteromyoma treatment system, the pressure of a water bag is not adjusted, the comfort level is poor, the embodiment comprises a treatment head connected with a peristaltic pump W104, the treatment head comprises a telescopic silica gel water bag H100, an aluminum casting substrate SH100 and an ultrasonic B probe B100, the aluminum casting substrate SH100 is used for fixing a phased array seismic source, the ultrasonic B probe B100 is used for collecting the lesion status in tissues and transmitting the lesion status to an upper computer, the output end of the treatment head is connected with a mouth 6 of a water bag water pressure adjusting water column module SY100, the water pressure of the treatment head influences the length of the telescopic silica gel water bag, namely the control is the treatment focal range, a high water position trigger TS101 is arranged on the water bag water pressure adjusting water column module SY100, the high water level trigger TS101 detects a high water level signal and transmits the high water level signal to the central control unit CPU200 for processing, the evacuation port PK2 is connected with a three-way joint T500 port 501, a port 8 of a water bag water pressure adjusting water column module SY100 is connected with an overflow water booster pump Z102, the water bag water pressure adjusting water column module SY100 is fixed on a lifting motor module M200, the lifting motor module M200 controls the liquid level difference between the liquid level of the water bag water pressure adjusting water column module SY100 and a treatment head, so that the expansion length of the telescopic silica gel water bag H100 is controlled, namely the telescopic silica gel water bag H100 is controlled to be at a treatment focal length position, the high water level trigger is used for preventing the liquid level from being too high, the booster pump Z102 timely processes excessive overflow deaerated water or high-temperature deaerated water generated in a treatment process, and accordingly the expansion length of the telescopic silica gel water bag H100 is kept constant and the pressure is moderate.
Aiming at a water treatment system of a phased array focusing ultrasonic hysteromyoma treatment system, electric heating is needed before water treatment, the water consumption is large, the dissolved oxygen content of high-temperature degassed water for treatment is high, the high-temperature degassed water is required to be replaced in time, a degassed water constant-temperature backwater recycling device is not needed, a degassing membrane and a pump are quick in aging, and the electric safety risk and the failure rate are high; in the embodiment, in the treatment process of the treatment head, a peristaltic pump W104 provides degassed water for the treatment head according to the calculated required set flow, the degassed water is heated in the radiation process of the ultrasonic treatment head, the temperature of the thermal degassing water rises, the dissolved oxygen content rises and needs to be continuously discharged out of the treatment head, after passing through a water bag water pressure regulating water column module SY100, the degassed water is sent to a three-way electromagnetic valve Q103 port T by a booster pump Z102, flows to a cold and hot water mixing three-way electromagnetic valve Q105 port P through the three-way electromagnetic valve Q103 port T, the amount of condensed water in a water collector J200 is detected by a water collecting position sensor TS100 and is transmitted to a central control unit CPU200 for processing, the pressure in the water collector J200 is detected and transmitted by a pressure sensor M202, the overpressure in a pressure relief valve M201 in the water collector J200 is used for abnormal protection, a semiconductor condenser L100 is closed, the electromagnetic valve KM3 is broken, the electromagnetic valve KM4 is broken, the three-way electromagnetic valve Q101 port P is connected with a vacuum pump Z103 powered on, the vacuum pump Z103 is powered on, the three-way electromagnetic valve Q102, the port P is connected with the electromagnetic valve KM5, a through type electromagnetic valve KM7 is communicated, a port T of a port A of a three-way electromagnetic valve Q104 is communicated, low-temperature condensed water is sent to a port T of the three-way electromagnetic valve Q105, the three-way electromagnetic valve Q105 is used for switching and mixing the low-temperature condensed water of the port T and thermal degassing water of a port P of the port Q105 according to a certain proportion, constant-temperature degassing water is communicated from the port A of the three-way electromagnetic valve Q105 to the port T of the three-way electromagnetic valve Q106, the port A of the port T of the three-way electromagnetic valve Q106 and the port A of the three-way electromagnetic valve Q106 are communicated with a water inlet port 1 of a liquid degassing membrane Z108 for degassing circulation again, the temperature and the content of the dissolved oxygen after constant temperature is maintained again are detected by a fluorescence detection probe W101 and sent to a dissolved oxygen transmitter W103 and sent to a central control unit CPU200 for processing, a main control system accurately calculates and adjusts the proportion of the port P of the port T of the three-way electromagnetic valve Q105 according to adjust the mixing proportion, thereby achieving accurate constant-temperature control, because the dissolved oxygen content of the constant-temperature water entering the constant-temperature of the port Z108 of the liquid degassing water entering the degassing membrane is far lower than the dissolved oxygen from a treated ultra-pure degassing water column Z105, the burden of the liquid degassing membrane Z108 is reduced, the service life of the liquid degassing membrane Z108 is prolonged, electricity and water are saved, the constant temperature is comfortable, and the requirement on pipeline layout is low.
Aiming at a water treatment system of a phased array focusing ultrasonic hysteromyoma treatment system, condensed water in a degassed water tank, a pipeline and a water collector is not automatically discharged; in the embodiment, the amount of condensed water in the water collector J200 is detected by the water collecting position sensor TS100 and transmitted to the central controller CPU200, the pressure in the water collector J200 is detected by the pressure sensor M202 and transmitted to the central control unit CPU200, the pressure relief valve M201 in the water collector J200 is used for pressure abnormality protection, the semiconductor condenser L100 is turned off, the solenoid valve KM3 is turned off, the solenoid valve KM4 is turned off, the port a of the three-way solenoid valve Q101 is connected to the port P of the three-way solenoid valve Q101, the vacuum pump Z103 is powered on and operated, the port P of the three-way solenoid valve Q102 is connected to the port a, the solenoid valve KM5 is connected to the port KM7, the port P of the three-way solenoid valve Q104 is connected to the port P of the three-way solenoid valve Q104 and is connected to the port T400 13, the solenoid valve KM6 is connected to the port 12 of the four-way solenoid valve T400, the port T400 is connected to the port T14 of the port a three-way solenoid valve Q103, the port a port P15 of the four-way solenoid valve T is connected to the solenoid valve KM8 and the solenoid valve KM8 is connected to the solenoid valve KM8, and the vacuum pump Z103 is connected to the output end, and the air pressure generated by the output end of the vacuum pump Z103 discharges the low-temperature condensed water out of the pipeline F100. The water quantity in a degassing water tank W100 is detected by a liquid level sensor W102 and is transmitted to a central control unit CPU200, the degassing water in the water tank is communicated with a peristaltic pump W104 through a degassing water W101 port 5, the W104 peristaltic pump transmits the degassing water to a treatment head, the water flows into a water bag water pressure regulating water column SY100 port 6, a water bag water pressure regulating water column SY100 port 8 flows out and enters an input end of a booster pump Z102, an output end of the booster pump Z102 is connected with a three-way electromagnetic valve Q103 port A, a three-way electromagnetic valve Q103 port A port P, a three-way electromagnetic valve Q103 port P is communicated with a four-way joint T400 port 14 and is disconnected with a four-way joint T400 port 12 electromagnetic valve KM6, a four-way joint T400 port 13 is communicated with a three-way electromagnetic valve Q104 port P, a three-way electromagnetic valve Q104 port A port T is communicated with a four-way joint T400 port 15 KM8, the peristaltic pump W104 works, and the booster pump Z102 discharges the water from the degassing water tank W100, the treatment head, the water bag water pressure regulating water column SY100 and the water collecting and the waste water discharging function of the pipeline, thereby realizing the low-temperature condensation water collecting and automatic waste water discharging function of the water tank.
The water treatment system for the phased array focusing ultrasonic uterine fibroid treatment system provided by the embodiment comprises control components including a solenoid valve KM1, a solenoid valve KM2, a solenoid valve KM3, a solenoid valve KM4, a solenoid valve KM5, a solenoid valve KM6, a penetrating solenoid valve KM7, a solenoid valve KM8, a three-way solenoid valve Q103, a three-way solenoid valve Q104, a three-way solenoid valve Q105, a three-way solenoid valve Q106, a conductivity sensor Z107, a dissolved oxygen transmitter W103, a fluorescence probe W101, a liquid level sensor W102, a pressure sensor M202, a lifting motor module M200, a booster pump Z100, a booster pump Z101, an ultraviolet lamp Z104, a semiconductor condenser L100, a high water position trigger TS101, a water collection position sensor TS100, a main control chip CPU200, a multi-path power supply module PWR100, a communication module COM1, a superior system PC1 (upper computer), a display and key input IO200, and power supply leads L, N and PE.
The system provided by the embodiment does not need an additional water and electricity heating device, accumulated heat generated in the working process of the ultrasonic transducer passes through the booster pump, the condensate water device, the cold and hot water mixing proportion three-way valve and the pipeline, neutralization reaches constant-temperature degassed water, the reverse osmosis abandoned water backflow module reduces the requirement on the water volume of tap water, the dissolved oxygen value, the water temperature value, the conductivity, the degassed water volume, the water collector pressure value in the whole running process of the system are detected in real time, and therefore the purposes of water and electricity saving, low power consumption, long service life, small volume and stable degassed water are achieved.
The above examples are intended to cover by those of ordinary skill in the art all such modifications and variations as may be within the scope of the present claims.
The foregoing description of specific embodiments of the present invention has been presented. It is to be understood that the present invention is not limited to the specific embodiments described above, and that various changes and modifications may be made by one skilled in the art within the scope of the appended claims without departing from the spirit of the invention.
Claims (9)
1. A water treatment system for a phased array focusing ultrasonic hysteromyoma treatment system is characterized by comprising a water purification device, an RO reverse osmosis waste water reflux device, an ultraviolet lamp sterilization device, an ultra-purification deionization device, a deaerating water device, a condensed water and water separation device, a condensed water recycling device, a condensed water automatic drainage device, a deaerating water tank management device, a treatment head component, a water bag water pressure adjusting module device and a constant-temperature deaerating water proportion mixing recycling device;
wherein: the water purification device is connected with an RO reverse osmosis waste water reflux device, the RO reverse osmosis waste water reflux device is respectively connected with an ultraviolet lamp sterilization device, a condensed water recycling device, a constant-temperature deaerated water proportional mixing and recycling device and a condensed water automatic drainage device, the ultraviolet lamp sterilization device is connected with an ultra-purification deionization device, the ultra-purification deionization device is connected with a deaerated water device, the deaerated water device is respectively connected with a condensed water-vapor separation device and a deaerated water tank management device, the condensed water-vapor separation device is connected with the condensed water recycling device, the condensed water recycling device is connected with a deaerated water device, the deaerated water tank management device is connected with a treatment head assembly, the treatment head assembly is connected with a water bag water pressure regulation module device, and the water bag water pressure regulation module device is connected with a constant-temperature deaerated water proportional mixing and recycling device;
the degassing water device comprises a three-way electromagnetic valve Q106, a liquid degassing membrane Z108, a semiconductor condenser L100 and an electromagnetic valve KM3; the condensed water and water-vapor separation device comprises a water collector J200, a water collection position sensor TS100, an electromagnetic valve KM5, a water collection membrane J201, a pressure release valve M201, a pressure sensor M202, an electromagnetic valve KM4, a three-way electromagnetic valve Q101, a vacuum pump Z103, a three-way electromagnetic valve Q102 and a polymer silencer X100; the condensate water recycling device comprises a through type electromagnetic valve KM7, a three-way electromagnetic valve Q104 and a three-way electromagnetic valve Q105; the automatic condensed water drainage device comprises a wastewater electromagnetic valve KM8 and a wastewater pipeline F100; wherein:
an input port P of the three-way electromagnetic valve Q106 is connected with an ultra-purification deionization device, an input port T of the three-way electromagnetic valve Q106 is communicated with an output port A of the three-way electromagnetic valve Q106, the output port A of the three-way electromagnetic valve Q106 is connected with an input port (1) of a liquid degassing membrane Z108, and an output port (2) of the liquid degassing membrane Z108 is connected with a degassed water tank management device; a first degassing port 3B of a liquid degassing membrane Z108 is connected with an input end of a semiconductor condenser L100, an output end of the semiconductor condenser L100 is connected with a solenoid valve KM3, the solenoid valve KM3 is connected with a first input port (16) of a water collector J200, a second output port (40) of the water collector J200 is connected with a through solenoid valve KM7, a first output port (19) of the water collector J200 is connected with a solenoid valve KM4, a second input port (20) of the water collector J200 is connected with a solenoid valve KM5, the solenoid valve KM5 is connected with an output port P of a three-way solenoid valve Q102, a pressure relief port (17) of the water collector J200 is provided with a pressure relief valve M201, a pressure transmission port (18) of the water collector J200 is provided with a pressure sensor M202, a water collection position sensor TS100 and a water collection J201 are arranged in the water collector J200, the water collection membrane J201 is transversely filled in the water collector J200, the solenoid valve KM4 is connected with an input port T of the three-way solenoid valve Q101, an input port T of the three-way solenoid valve Q101 is communicated with an output port A of the solenoid valve Q101, an output port A103 of a vacuum pump Q100 of the three-way solenoid valve Q101, an output port of a vacuum pump Z103, and a high-molecular solenoid valve Q102 of the three-way solenoid valve Q100, and a high-way solenoid valve Q102, the three-way solenoid valve Q102; the penetration type electromagnetic valve KM7 is connected with an input port A of a three-way electromagnetic valve Q104, the input port A of the three-way electromagnetic valve Q104 is communicated with an output port T of the three-way electromagnetic valve Q104, the output port T of the three-way electromagnetic valve Q104 is connected with an input port T of a three-way electromagnetic valve Q105, the input port T of the three-way electromagnetic valve Q105 is communicated with the output port A of the three-way electromagnetic valve Q105, and the output port A of the three-way electromagnetic valve Q105 is connected with an input port T of a three-way electromagnetic valve Q106; an output port P of the three-way electromagnetic valve Q104 is connected with an RO reverse osmosis waste water reflux device; an input port P of the three-way electromagnetic valve Q105 is connected with the constant-temperature degassing water proportional mixing recycling device; the electromagnetic valve KM8 is arranged on a waste water pipeline F100, and the input end of the waste water pipeline F100 is connected with an RO reverse osmosis waste water reflux device;
constant temperature degasification water proportional mixing recycles device, including booster pump Z102 and three-way solenoid valve Q103, wherein:
the input end of the booster pump Z102 is connected with the water bag water pressure adjusting module device, the output end of the booster pump Z102 is connected with the input port A of the three-way electromagnetic valve Q103, the input port A of the three-way electromagnetic valve Q103 is communicated with the output port T of the three-way electromagnetic valve Q103, the output port T of the three-way electromagnetic valve Q103 is connected with the condensate water recycling device, and the output port P of the three-way electromagnetic valve Q103 is connected with the RO reverse osmosis water-discarding backflow device.
2. The water treatment system for phased array focused ultrasound uterine fibroid treatment system as claimed in claim 1, wherein said water purification means comprises a water inlet line J100, a water inlet solenoid valve KM1 and a PP filter Z100; wherein:
the water inlet pipeline J100 is connected with a water inlet electromagnetic valve KM1, the water inlet electromagnetic valve KM1 is connected with a PP filter Z100, and the output end of the PP filter Z100 is connected with an RO reverse osmosis waste water reflux device.
3. The water treatment system for phased array focused ultrasound uterine fibroid treatment system as claimed in claim 1, wherein said RO reverse osmosis reject water return means comprises a pressure regulating valve T100, a wastewater return module Z106, a booster pump Z101, an RO reverse osmosis membrane, a three-way joint T200, a solenoid valve KM6, and a four-way joint T400; wherein:
the utility model discloses a condensate water circulation utilization device, including pressure regulating valve T100, waste water backflow module Z106, booster pump Z101, condensate water automatic drainage device, pressure regulating valve T400, pressure regulating valve T100's input port (21) and water purification installation link to each other, pressure regulating valve T100's first input port (22) link to each other with waste water backflow module Z106's output, waste water backflow module Z106's input links to each other with three way connection T200's second output port (25), three way connection T200's first output port (26) link to each other with solenoid valve KM6, pressure regulating valve T100's second output port (23) are connected with booster pump Z101's input, and booster pump Z101's output links to each other with RO's input port (9), and RO's output port (11) link to each other with three way connection T200's second input port (24), and solenoid valve KM6 link to each other with four way connection T400's input port (12), and four way connection T400's first output port (15) link to each other with condensate water automatic drainage device, and four way connection T400's second input port (13) of four way connection T400) link to each other with condensate water circulation utilization device, and four way connection T400's constant temperature input port (14) and degasification water proportional mixing reuse device link to each other.
4. The water treatment system for phased array focused ultrasound uterine fibroid treatment system according to claim 1, wherein said ultraviolet lamp sterilizing device comprises a dual wavelength ultraviolet lamp Z104, the output of said dual wavelength ultraviolet lamp Z104 is connected with an ultra-pure deionization device, and the input of said dual wavelength ultraviolet lamp Z104 is connected with an RO reverse osmosis reject water reflux device.
5. The water treatment system for a phased array focused ultrasound uterine fibroid treatment system according to claim 1, wherein said ultra-purification deionization device comprises ultra-pure water column Z105, conductivity sensor Z107 and water pressure sensor T107; wherein:
the output end of the ultra-pure water column Z105 is connected with the input end of a conductivity sensor Z107, the output end of the conductivity sensor Z107 is connected with the input end of a water pressure sensor T107, and the output end of the water pressure sensor T107 is connected with a water degassing device.
6. The water treatment system for phased array focused ultrasound uterine fibroid treatment system according to claim 1, wherein said degassed water tank management device comprises a degassed water tank W100, a fluorometric probe W101, a dissolved oxygen transducer W103, a level sensor W102, a drain PK1, a tee fitting T500, and a peristaltic pump W104; wherein:
the fluorescence detection head W101 and the liquid level sensor W102 are respectively arranged in the degassed water tank W100; fluorescence method detecting head W101 outer end links to each other with dissolved oxygen changer W103, degassed water tank W100 lateral wall links to each other with peristaltic pump and degassed water device respectively through the pipeline, degassed water tank W100's top is equipped with gas vent PK1, gas vent PK1 passes through the input of tube coupling three way connection T500, and evacuation pipe K100 and water pocket water pressure regulation module device are connected respectively to two output of three way connection T500.
7. The water treatment system for the phased array focused ultrasound hysteromyoma treatment system of claim 1, wherein the treatment head assembly comprises a treatment head, the treatment head comprises a telescopic silica gel water sac H100, an aluminum casting substrate SH100 and an ultrasonic B probe B100; wherein:
the telescopic silica gel water bag H100 is arranged on the aluminum cast substrate SH100, and the B ultrasonic probe B100 is arranged inside the aluminum cast substrate SH 100; the aluminum casting substrate SH100 is connected to a degassed water tank management device and a water bag water pressure regulation module device, respectively.
8. The system of claim 1, wherein the water bladder water pressure regulating module means comprises a water bladder water pressure regulating water column module SY100 and a lift motor module M200, wherein the water bladder water pressure regulating water column module SY100 comprises two mutually communicated regulating water columns, wherein a first regulating water column is internally provided with a high water position trigger TS101, the top of the first regulating water column is provided with an evacuation port PK2, the evacuation port PK2 is connected with the degassed water tank management device, the bottom of the first regulating water column is connected with the treatment head assembly through a pipeline, and a second regulating water column is respectively connected with the lift motor module M200 and the constant temperature degassed water proportional mixing and recycling device.
9. The water treatment system for a phased array focused ultrasound uterine fibroid treatment system according to any one of claims 1 to 8, further comprising a central control unit, a multi-way power module, a communication module, an upper computer, and a display and input unit; wherein:
the multi-path power supply module is connected with the central control unit, and the central control unit is connected with the upper computer through the communication module; the display and input unit is connected with the central control unit;
the central control unit is respectively in control connection with the water purification device, the RO reverse osmosis waste water reflux device, the ultraviolet lamp sterilization device, the ultra-purification deionization device, the deaerating water device, the condensed water and vapor separation device, the condensed water recycling device, the condensed water automatic drainage device, the deaerating water tank management device, the treatment head assembly, the water bag water pressure adjusting module device and the constant-temperature deaerating water proportion mixing recycling device;
and the multi-path power supply module and the degassed water tank management device are respectively connected with an external conducting wire.
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