CN211911785U - High-low temperature composite ablation operation system - Google Patents

Abstract

The utility model relates to a high low temperature complex melts operation system relates to freezing low temperature treatment technical field for improve the safe validity of treatment. The utility model discloses a high low temperature complex melts operation system, including the host computer unit and with the needle is melted to the cold and heat that the host computer unit links to each other, the host computer unit includes cold working medium supply system, hot working medium supply system and working medium distribution system, and working medium distribution system can control cold working medium supply system respectively and melt the needle and carry cold working medium to the cold and heat to and control hot working medium supply system melts the needle and carry hot working medium to the cold and heat, consequently can carry out quick rewarming to the treatment area after accomplishing low temperature treatment, thereby provide the basis for the promotion of operation security, economic nature and convenience.

Description

High-low temperature composite ablation operation system

Technical Field

The utility model relates to a freezing low temperature treatment technical field especially relates to a high low temperature complex melts operation system.

Background

At present, cryotherapy techniques are becoming the main approach for interventional tumor therapy. The technology belongs to pure physical therapy, and has the advantages of definite therapeutic effect, no tumor cell diffusion during treatment, minimal invasion, no pain during treatment, quick recovery, no damage to normal tissues and the like compared with radiotherapy and chemotherapy. Clinical data show that the body immunity of the patient treated by the technology is obviously improved compared with that before treatment, and the long-term survival rate is obviously improved. Has obvious advantages in the aspect of treating solid tumors such as lung cancer, liver cancer, breast cancer, kidney cancer, prostate cancer and the like.

The mechanism of cryotherapy is as follows:

1. the mechanical damage to the tumor cells caused by the growth of ice crystals and the dehydration of cells

2. Tumor tissue hypoxia death caused by blood embolism

3. Reversible damage, causing apoptosis

4. Freezing can stimulate immunoregulation to produce waterfall type ectopic tumor inhibition effect

In the prior art, a typical cryotherapeutic apparatus is represented by Cryocare surgery System (developed by Endocare corporation in usa) and VISUAL-ICE Cryoablation System (developed by Galil corporation in israel), and is generally called argon-helium knife because argon and helium are used as working media. The effect of cryotherapy is achieved by the principle of Joule-Thomson effect (temperature change phenomenon caused by gas expansion through a porous plug), the lowest low-temperature ablation temperature can reach-150 to-160 ℃, and the highest rewarming temperature can reach about 40 ℃. It is easy to find that the low-temperature treatment equipment only has one refrigeration mechanism, and the working temperature area is limited by the refrigeration principle and the characteristics of the working medium, so that the low-temperature treatment equipment only can provide treatment with a single function. In addition, due to the limitation of the working mechanism, the low-temperature treatment equipment has high working pressure (12-22 MPa), potential safety hazards exist in the operation, and the noise is relatively large; the working medium is expensive (high-purity argon and helium, wherein helium is one of indispensable rare strategic materials for national defense military industry and high-tech industry development), is not easy to obtain, and cannot be widely popularized; in addition, the high-pressure argon gas bottle and the helium gas bottle are required to be connected in the operation process, and the operation is inconvenient in an operation room with limited space. To date, no fully functional high-low temperature treatment equipment with wide temperature range exists at home and abroad.

SUMMERY OF THE UTILITY MODEL

The utility model provides a high low temperature complex melts operation system can combine the heating treatment function of higher intensity on satisfying the prerequisite of basic cryotherapy functional requirement to promote for operation security, economic nature and convenience provides the basis.

The utility model provides a high-low temperature composite ablation operation system, which comprises a main machine unit and a cold-hot ablation needle connected with the main machine unit, wherein the cold-hot ablation needle is used for treating the focus of a patient;

the host unit includes:

the cold working medium supply system is used for conveying cold working medium to the cold and hot ablation needle;

a hot working medium supply system for delivering a hot working medium to the hot and cold ablation needle; and

and the working medium distribution system is respectively connected with the cold working medium supply system and the hot working medium supply system, and is used for controlling the cold working medium supply system to convey cold working medium to the cold and hot ablation needle and controlling the hot working medium supply system to convey hot working medium to the cold and hot ablation needle.

In one embodiment, the working fluid distribution system comprises:

the phase separator is connected with the cold working medium supply system; and

the precooler is provided with a gas channel and a liquid channel, the input side of the gas channel is communicated with the gas outlet end of the phase separator, and the input side and the output side of the liquid channel are respectively communicated with the liquid outlet end of the phase separator and the cold and hot ablation needle;

wherein the gas in the gas channel is used for pre-cooling the liquid in the liquid channel.

In one embodiment, the gas channel is configured as a labyrinth-like channel.

In one embodiment, the host unit further comprises a recovery system connected to the output port of the ablation needle, and the recovery system is connected to the cold working medium supply system and the hot working medium supply system, respectively, and is configured to collect the treated cold working medium or hot working medium, or collect the cold working medium discharged from the cold working medium supply system or the hot working medium discharged from the hot working medium supply system due to overpressure.

In one embodiment, the recovery system comprises a heat exchanger connected with the output port of the ablation needle, and the heat exchanger is used for heating the cold working medium output by the ablation needle and returning the cold working medium to the atmosphere, or cooling the hot working medium output by the ablation needle and recovering the hot working medium.

In one embodiment, the cold working medium supply system comprises a cold tank for carrying cold working medium, and the cold tank is used for conveying the cold working medium with pressure to the cold and hot ablation needle conveying belt.

In one embodiment, a pressurization pipeline is connected to the cold tank, and the pressurization pipeline is used for realizing self pressurization of the cold working medium in the cold tank.

In one embodiment, the hot working medium supply system comprises a hot tank for carrying the hot working medium, the hot tank being adapted to convey the pressurized hot working medium to the hot and cold ablation needles.

In one embodiment, a heating device is disposed on the hot tank, and the heating device is used for vaporizing and pressurizing the hot working medium in the hot tank.

In one embodiment, the host unit further includes an electrical control system and an interaction system electrically connected to each other, and the electrical control system is electrically connected to the cold working medium supply system, the hot working medium supply system, and the working medium distribution system, respectively, to control the working process of the working medium.

Compared with the prior art, the utility model has the advantages of: the working medium distribution system can respectively control the cold working medium supply system to convey cold working medium to the cold-heat ablation needle and control the hot working medium supply system to convey hot working medium to the cold-heat ablation needle, so that the treatment area can be quickly rewarmed after the low-temperature treatment is completed, and a foundation is provided for the improvement of the operation safety, the economy and the convenience.

Drawings

The present invention will be described in more detail hereinafter based on embodiments and with reference to the accompanying drawings.

Fig. 1 is a schematic structural diagram of a high-low temperature composite ablation surgical system according to an embodiment of the present invention;

fig. 2 is a schematic connection diagram of the cold working medium supply system and the hot working medium supply system in the embodiment of the present invention;

FIG. 3 is a schematic diagram of the connection of the cold medium supply system according to the embodiment of the present invention;

fig. 4 is a schematic connection diagram of a hot working medium supply system according to an embodiment of the present invention;

fig. 5 is a schematic block diagram of a high-low temperature composite ablation surgical system according to an embodiment of the present invention;

FIGS. 6 and 7 are schematic views of the connection of the working medium distribution system according to an embodiment of the present invention;

fig. 8 and 9 are schematic structural diagrams of a host unit in an embodiment of the present invention;

fig. 10 and fig. 11 are schematic structural diagrams of the host unit after the housing is partially hidden according to the embodiment of the present invention;

FIG. 12 is a schematic view of a piping connection of the working medium distribution system according to an embodiment of the present invention;

fig. 13 is a schematic structural diagram of a precooler in an embodiment of the present invention;

fig. 14 and 15 are schematic structural diagrams of a heat exchanger according to an embodiment of the present invention.

Fig. 16 is a schematic structural view of a cold-hot ablation needle according to an embodiment of the present invention;

fig. 17 is an enlarged view of fig. 16 at I.

Reference numerals:

100-a host unit;

200-a cold-hot ablation needle; 2010, a working medium input pipe; 202-working medium return pipe; 203-vacuum tube; 204-vacuum layer;

300-a cold working medium supply system; 400-hot working medium supply system; 500-a working medium distribution system; 600-a recovery system; 700-an electrical control system; 800-an interactive system;

210-a probe delivery tube; 220-temperature measuring probe;

310-automatic cold working medium filling system; 320-a cold working medium pressure control system;

311-cold working medium storage tank; 312-an output valve; 313-interface detection switch; 314-a perfusion interface; 315-a charging valve; 316-one-way valve;

321-a cold tank; 322-a booster circuit; 323-pressure increasing valve; 324,426-pressure sensor; 325,425-safety valve; 326-liquid charging air release valve; 327,428,512-manual valve; 328-a deflation valve; 329,427-pressure gauge; 330, 430-liquid level meter; 331-a filter;

410-automatic hot working medium filling system; 420-a hot working medium pressure control system;

411-hot working medium storage tank; 412-a fill port; 413-a filling pump; 414-a fill valve;

421-a hot tank; 422, 513-temperature sensor; 423-temperature switch; 424-a heater; 429-a purge valve;

510-a phase separator; 511-phase separation valve;

520-a precooler; 521-gas channel; 522-upper plate; 523-lower plate;

610-a heat exchanger; 611-fins; 612-a fan; 613-PTC heaters; 620-recovery tank; 621-a weighing sensor;

810-a display; 820-a functional keyboard;

910-a housing; 911-power-assisted wheel; 912-an electrically controlled wheel; 913-a handle; 914-wireless tablet; 915-scram button.

Detailed Description

The present invention will be further explained with reference to the accompanying drawings.

As shown in fig. 1, the present invention provides a high-low temperature combined ablation surgical system, which includes a main unit 100 and a cold-hot ablation needle 200 connected to the main unit 100, wherein the cold-hot ablation needle 200 is used for treating a lesion of a patient.

Therein, the main unit 100 comprises a cold working medium supply system 300, a hot working medium supply system 400 and a working medium distribution system 500.

Specifically, the cold working medium supply system 300 is used for delivering cold working medium to the cold and hot ablation needle 200; a hot working medium supply system 400 for delivering a hot working medium to the thermal ablation needle 200; the working medium distribution system 500 is respectively connected with the cold working medium supply system 300 and the hot working medium supply system 400, and the working medium distribution system 500 is used for controlling the cold working medium supply system 300 to deliver cold working medium to the cold and hot ablation needle 200 or controlling the hot working medium supply system 400 to deliver hot working medium to the cold and hot ablation needle 200.

The utility model provides a high low temperature complex melts operation system shows the function of low temperature and rewarming clinically. It comprises two stages of treatment, namely a low-temperature treatment stage and a rewarming stage. Specifically, in the low-temperature treatment stage, the cold and hot ablation needle 200 is inserted into the focus of a patient, the cold working medium is conveyed to the cold and hot ablation needle 200 through the cold working medium supply system 300, the cold working medium rapidly passes through the ablation needle and is evaporated to absorb heat, a large amount of cold energy is instantly supplied to the lesion tissue, and the tissue is rapidly frozen and destroyed to achieve the treatment purpose. After the low-temperature treatment stage is completed, the hot working medium is delivered to the thermal ablation needle 200 through the hot working medium supply system 400, so that the high-temperature hot working medium steam reaches the treatment part of the thermal ablation needle 200, and a large amount of heat is released instantly, so that the treatment area is rapidly rewarming.

The cold working medium can be single substances such as liquid nitrogen (-196 ℃, boiling point under the normal pressure), liquid oxygen (-183 ℃, boiling point under the normal pressure), liquid methane (-161 ℃, boiling point under the normal pressure), liquid argon (-186 ℃, boiling point under the normal pressure), liquid neon (-246 ℃, boiling point under the normal pressure), liquid helium (-269 ℃, boiling point under the normal pressure), liquefied nitrous (-88.5 ℃, boiling point under the normal pressure), liquefied carbon dioxide (-79 ℃, boiling point under the normal pressure) and freon 22(-50 ℃, boiling point under the normal pressure), and can also be a mixture of the substances.

The hot working medium of the present invention may be a single substance such as water vapor (100 ℃, boiling point under normal pressure), methanol vapor (64.7 ℃, boiling point under normal pressure), formic acid vapor (100.8 ℃, boiling point under normal pressure), ethanol vapor (78 ℃, boiling point under normal pressure), acetic acid vapor (117.9 ℃, boiling point under normal pressure), ethyl ester vapor (54.3 ℃, boiling point under normal pressure), propanol vapor (82.5 ℃, boiling point under normal pressure), propionic acid vapor (141.1 ℃, boiling point under normal pressure), propylene ester vapor (101.6 ℃, boiling point under normal pressure), or a mixture of the above-mentioned substances. It should be noted that the boiling point temperature does not represent the rewarming temperature, and in some embodiments, for example, a steam pressurization method is used as a power to deliver the hot working medium to the thermal ablation needle 200, and the treatment temperature may be higher than the boiling point of the selected hot working medium.

Therefore, the cold working medium and the hot working medium of the utility model have wide sources and lower cost, and the temperature range covered by the cold working medium and the hot working medium is wider, thereby providing a foundation for the promotion of the safety, the economy and the convenience of the surgical operation.

In addition, each pipeline for conveying cold working medium or hot working medium is provided with a heat insulation part, so that the lowest temperature can reach the required cryotherapy temperature when the cold working medium is output to the needle point of the cold and hot ablation needle 200.

The following describes each part of the present invention.

Cooling medium supply system 300

As shown in fig. 2 and 3, cold medium supply system 300 includes an automatic cold medium filling system 310 and a cold medium pressure control system 320.

Specifically, the cold working medium automatic filling system 310 includes a cold working medium storage tank 311 for storing cold working medium, the cold working medium pressure control system 320 includes a cold tank 321 for delivering cold working medium to the cold-hot ablation needle 200, and the cold working medium storage tank 311 is connected with the cold tank 321 through a pipeline so as to deliver the cold working medium therein to the cold tank 321.

An output valve 312, an interface detection switch 313 and a filling interface 314 are sequentially arranged on a pipeline connecting the cold working medium storage tank 311 and the cold tank 321, and the interface detection switch 313 is used for opening or closing the filling interface 314 so as to connect or disconnect the cold working medium storage tank 311 and the cold tank 321.

A charging valve 315 and a one-way valve 316 are sequentially arranged on the pipeline between the filling interface 314 and the cold tank 321 to prevent the working medium from flowing backwards.

The cold tank 321 can be used to convey pressurized cold working fluid into the cold and hot ablation needle 200. Optionally, a pressure boost pipeline 322 is connected to the cold tank 321, and the pressure boost pipeline 322 is used for realizing self-pressurization of the cold medium in the cold tank 321.

Specifically, the two ends of the pressurization line 322 are connected to the cold tank 321 to form a closed loop. The pressure increasing pipeline 322 is provided with a pressure increasing valve 323, when the pressure increasing valve 323 is opened, the working medium in the cold tank 321 enters the pressure increasing pipeline 322, and is vaporized through heat exchange between the pipe wall and the outside, and the volume is expanded violently, so that the self-pressurization is realized.

The cold tank 321 is a vacuum heat-insulated stainless steel pressure vessel.

In addition, some optional embodiments can realize that the cold tank 321 conveys the cold working medium with pressure to the hot and cold ablation needle 200. For example, air is pressurized by pressing air into the cold tank 321 by an air compressor; or the high-pressure gas with the boiling point not higher than that of the cold working medium is charged into the cold tank 321 for pressurization; or by heating the cold working medium to vaporize it.

In addition, a more direct way to provide power is to pump the cold working fluid in the cold tank 321 through a cryogenic pump, and to regulate the mass flow rate of the delivered cold working fluid by controlling the pump speed or power.

The cold tank 321 is further provided with a pressure sensor 324 and two safety valves 325 to detect the pressure of the cold tank 321 and avoid the pressure of the cold tank 321 from being too high through the safety valves 325. By providing two safety valves 325, a certain redundancy can be ensured, thereby further improving the reliability of the cold tank 321.

The cold tank 321 is also connected to a recovery system 600, mentioned below.

Specifically, a liquid charging and discharging valve 326, a pressure sensor 324 and a safety valve 325 are sequentially arranged on a pipeline between the cold working medium automatic filling system 310 and the recovery system 600, the pressure sensor 324 is used for detecting the pressure in the pipeline, and overpressure protection is performed through the safety valve 325.

A manual valve 327 and a purge valve 328 are provided in parallel on a line through which the cold tank 321 is purged to the recovery system 600. And a pressure gauge 329 is connected in series to the pipe on which the manual valve 327 is provided, so that the pressure of the pipe is manually controlled by the pressure gauge 329 and the manual valve 327. The bleed valve 328 may be implemented as a conventional pressure control valve of the prior art, and the relief valve 325 provides effective pressure relief in the event of a failure.

The liquid charging vent valve 326 and the vent valve 328 can both be normally open valves, i.e. the device can be automatically opened to release pressure when power is off, and the device is in a safe state without pressure.

In the process of filling cold working medium into the cold tank 321 from the cold working medium storage tank 311, when the pipeline pressure exceeds a certain value, the pressure can be relieved through the liquid feeding air relief valve 326; relief may be provided by relief valve 325 if the charge relief valve 326 fails; thereby ensuring the safety in the perfusion process. When the pressure sensor 324 and the safety valve 325 fail, the pressure gauge 329 can read the pressure and operate the manual valve 327 to release the pressure, so as to ensure the safety of the equipment.

Further, a liquid level meter 330 for identifying the liquid level thereof is provided in the cold tank 321.

In addition, a filter 331 is disposed at the bottom of the output pipeline connected to the working medium distribution system 500 in the cold tank 321, so as to prevent impurities from entering the working medium distribution system 500 or the conveying pipeline to cause blockage, thereby improving the effectiveness of the device treatment.

The operation of the automatic cold medium filling system 310 will be described in detail below.

Firstly, the cold working medium storage tank 311 is connected with the filling interface 314, and after the interface detection switch 313 detects that the connection of the filling interface 314 is completed, the charging valve 315 is opened, and the charging vent valve 326 is closed.

Secondly, an output valve 312 of the cold working medium storage tank 311 is opened, and the cold working medium is continuously injected into the cold tank 321; when the liquid level meter 330 detects that the cold working medium liquid adding is finished, the liquid adding valve 315 is closed, the liquid adding vent valve 326 is opened, and meanwhile, the output valve 312 of the cold working medium storage tank 311 is closed; the fill interface 314 is then disconnected, thereby completing the priming operation.

The operation of cold medium pressure control system 320 is described in detail below.

When the device is ready to operate, the pressure in the cold tank 321 needs to be increased to provide power for the output treatment of the cold working medium.

Therefore, firstly, the pressure increasing valve 323 is opened, the working medium in the cold tank 323 enters the pressure increasing pipeline 322, and is vaporized through heat exchange between the pipe wall and the outside, and the volume is expanded violently, so that the self-pressurization is realized.

Secondly, in order to achieve the effectiveness and consistency of treatment, the pressure of the cold working medium needs to be accurately controlled, so that the pressure in the cold tank 323 is monitored in real time, and when the pressure exceeds the working pressure, the air release valve 328 is opened to release the pressure. In order to achieve smooth pressure, the opening of the pressure increasing valve 323 and the air releasing valve 328 can be controlled according to different strategies and different working conditions.

An alternative pressure control method is as follows: setting the working pressure to be P, and when the pressure in the cold tank 321 is far less than P, opening the pressure increasing valve 323 and closing the air release valve 328; when the pressure reaches P-ap 0, the pressure increasing valve 323 is closed, the current pressure is checked after a certain period of time, if it is farther from the set pressure P, the pressure increasing valve 323 is re-opened, and the above process is repeated to gradually approach the set pressure P.

Since the leakage heat of the cold tank 321 inevitably exists, the pressure in the cold tank 321 will also increase slowly, and when the pressure reaches P + Δ P0, the release valve 328 is opened to release the pressure until the pressure is released to P and closed. Meanwhile, in the treatment process, with the continuous consumption of the cold working medium, the gas phase space in the cold tank 321 is enlarged, and the pressure in the cold tank may also continuously decrease, so that when the pressure is lower than P- Δ P1, the pressure increasing valve 323 of the cold tank 321 needs to be opened until the pressure reaches P + Δ P1, and the pressure increasing valve 323 is closed.

The values of delta P0 and delta P1 are determined by a large number of experiments, and delta P1 is smaller than delta P0; in addition, the values of Δ P0 and Δ P1 are also related to the liquid level of the cold tank 321, so the control strategies at different liquid levels can be adjusted as required.

(II) Hot working Medium supply System 400

As shown in fig. 2 and 4, the hot working medium supply system 400 includes an automatic hot working medium filling system 410 and a hot working medium pressure control system 420.

Specifically, the automatic hot working medium filling system includes a hot working medium storage tank 411 for storing hot working medium, the hot working medium pressure control system 420 includes a hot tank 421 for delivering hot working medium to the ablation needles 200, and the hot working medium storage tank 411 is connected to the hot tank 421 through a pipeline to deliver the hot working medium therein to the cold tank 421.

A charging port 412, a charging pump 413 and a charging valve 414 are sequentially connected in series on a pipeline between the hot working medium storage tank 411 and the hot working medium storage tank 421.

The hot tank 421 is used to convey a pressurized hot working medium to the cold-hot ablation needle 200. One of the alternative ways is to heat the hot tank 421 to cause the hot working medium to produce steam to pressurize it. For example, a heating device such as a heating rod or a heating sheet may be provided inside the hot tank 421, or ceramics coated on the inner cylinder of the hot tank 421 and the outer wall of the transfer line may be provided to heat the hot tank, or a microwave heating method may be used to directly heat the working medium.

In one embodiment of the present disclosure, a temperature sensor 422, a temperature switch 423 and a heater 424 are disposed in the hot tank 421. The hot working medium in the hot tank 421 is heated by the heater 424 to be pressurized. And controls the temperature of the hot working medium through a temperature switch 423 and a temperature sensor 422. When the medium in the hot tank 421 is too little, if the heater 424 works, the temperature switch 422 will be turned off after the temperature rises to the starting temperature of the temperature switch 422, and the heater 424 is forcibly stopped to work, so as to prevent dry burning, thereby improving the safety of the equipment.

Further, a liquid level meter 430 (liquid level sensor) is provided in the hot tank 421. In the automatic filling process of hot working medium from hot working medium storage tank 411 to hot tank 421, level gauge 430 can monitor the liquid level of hot tank 421 at any time, if the liquid level does not change in a period of time, the operator will be reminded to change hot working medium storage tank 411, avoid liquid feeding pump 413 empty pump, reduce wear.

The hot tank 421 adopts a vacuum heat-insulating stainless steel pressure container, so that heat leakage is reduced, and the efficiency of the equipment is improved.

The hot tank 421 is also connected to a recovery system 600 mentioned below.

A safety valve 425, a pressure sensor 426, a pressure gauge 427 and a manual valve 428 are connected in series on a pipeline connecting the hot tank 421 and the recovery system 600 in sequence, and a release valve 429 is connected in parallel on the manual valve 428.

The bleed valve 429 is a conventional pressure control valve and the relief valve 425 will provide an effective pressure bleed in the event of its failure. In addition, when the pressure sensor 426 and the safety valve 425 both fail, the pressure gauge 426 may read the pressure and timely release the pressure by operating the manual valve 428, so as to ensure the safety of the equipment.

The operation of the automatic hot-working-medium filling system 410 will be described in detail below.

First, the hot working medium storage tank 411 is connected to the filling opening 412, wherein a common silicone hose can be used for connection.

Then, a liquid adding operation is performed. The filling valve 414 is opened, and the filling pump 413 is started at the same time, so that the hot working medium is continuously filled into the hot tank 421; when the liquid level meter 430 detects that the hot working medium charging is completed, the filling valve 414 is closed, the charging pump 413 is closed, and then the charging port 412 is disconnected, so that the charging action is completed.

The operation of the thermal medium pressure control system 420 is described in detail below.

When the apparatus is ready to operate, the pressure in the hot tank 421 needs to be increased to power the output therapy of the hot working medium.

According to above-mentioned optional scheme, the utility model discloses a mode of heating vaporization promotes the pressure of hot jar 421, and the energy source for high temperature treatment is hot steam.

In order to achieve the effectiveness and consistency of treatment, precise control of the pressure of hot pot 421 is required: therefore, the pressure in the hot tank 421 needs to be monitored in real time, and when the pressure exceeds the working pressure, the air release valve 429 needs to be opened for pressure release. To achieve pressure leveling, the opening of the heater 424 and the bleed valve 429 may be controlled in different ways depending on the strategy and operating conditions.

Since the saturated vapor pressure of a hot working medium is temperature dependent, an alternative control method is to use temperature PID regulation to regulate the pressure.

Working medium distribution system 500

As shown in fig. 5-7 and 14, working fluid distribution system 500 includes a phase separator 510. Because the cold working medium is gasified by heat exchange with the outside through the pipe wall in the conveying process, if the gaseous specific gravity in the cold working medium conveyed to the cold and hot ablation needle 200 is large, the low-temperature treatment effect can be influenced, and most of the cold working medium conveyed to the cold and hot ablation needle 200 is liquid through the phase separator 510.

Specifically, the cold tank 321 is connected to the phase separator 510 through a pipe, and the lower end of the phase separator 510 is connected to the cold and hot ablation needle 200 through a pipe. A phase separation valve 511 and a manual valve 512 are sequentially arranged on a pipeline between the upper end of the phase separator 510 and the recovery system 600, the upper end of the phase separator 510 is provided with a hole, the gasified cold working medium is discharged out of the system through the phase separation valve 511 and the manual valve 512, and the liquid working medium is input into the cold-hot ablation needle 200 through a valve, so that the purpose of gas-liquid separation is realized.

The manual valve 512 can also adjust the flow resistance of the pipeline, and a balance is achieved between liquid nitrogen consumption and gas-liquid separation.

In addition, a temperature sensor 513 is arranged at the downstream of the phase separation valve 511, when the nitrogen passing through the phase separator 510 is exhausted and then goes out of liquid nitrogen, the phase separation valve 510 can be closed, and loss of liquid nitrogen at the phase separator 510 is reduced.

The working medium distribution system 500 further comprises a precooler 520 connected with the phase separator 510, a gas channel 521 and a liquid channel are arranged on the precooler 520, the input side of the gas channel 521 is communicated with the gas outlet end of the phase separator 510, and the input side and the output side of the liquid channel are respectively communicated with the liquid outlet end of the phase separator 510 and the cold-hot ablation needle 520; wherein the gas in the gas channel 521 is used for pre-cooling the liquid in the liquid channel.

In other words, the gaseous working medium and the liquid working medium are separated by the phase separation valve 511, but the gaseous working medium also has a certain amount of cold, so that the cold is wasted if the gaseous working medium is directly recovered or discharged. Therefore, the gaseous working medium passes through the gas channel 521 of the precooler 520, and simultaneously, the liquid working medium passes through the liquid channel of the precooler, and the gaseous channel 521 can at least cover a part of the liquid channel, so that the cold energy of the gaseous working medium can be utilized in the circulation of the gaseous working medium and the liquid working medium, so as to ensure the temperature of the liquid working medium input into the cold-hot ablation needle 200.

Further, the gas channel 521 is configured as a labyrinth-shaped channel to increase the flow path of the gas, so that the cold energy of the gas can be more fully utilized.

Specifically, as shown in fig. 15, the precooler 520 includes an upper plate 522 and a lower plate 523, and the upper plate 522 and the lower plate 523 are connected by a locking screw. The lower plate 523 is provided with a labyrinth-like passage, i.e., a gas passage 521. The upper plate 522 and the lower plate 523 are provided with liquid channels, and the gaseous working medium can cool the upper plate 522 and the lower plate 523, so that the liquid working medium can be precooled by using the cold energy of the gaseous working medium, and the utilization efficiency of the cold working medium is improved.

The liquid passage of the precooler 520 is provided with a plurality of output connections (bayonet fittings) so that the output of each passage can be controlled independently.

(IV) recovery System 600

The utility model discloses in, to cold working medium or the hot working medium of input in the cold and hot ablation needle 200, after the treatment, all can retrieve through its output, retrieve through recovery system 600 promptly.

Specifically, as shown in fig. 2, the recovery system 600 includes a heat exchanger 610 connected to each other, the heat exchanger 610 is connected to the output end of the ablation needle 200, and the heat exchanger 610 is used to discharge the cold working medium output by the ablation needle 200 into the atmosphere after performing a temperature rise process on the cold working medium, or to recover the hot working medium output by the ablation needle 200 after cooling the hot working medium.

The cold working medium or the hot working medium output from the output end of the cold and hot ablation needle 200 is input into the heat exchanger 610 through a pipeline. For the cold working medium, the heat exchanger 610 heats the cold working medium, so that the temperature of the cold working medium is increased, and excessive condensation white mist is avoided. For the hot working medium, the hot working medium steam is condensed by heat exchange with air through the fins 611 of the heat exchanger 610, so as to avoid diffusion of the steam in the environment.

As shown in fig. 16 and 17, the heat exchanger 610 is an air-cooled heat exchanger, and hot air is blown to the fins 611 by a fan 612 to condense hot working medium vapor. In which the air-cooled heat exchanger is integrated with a PTC heater 613. The PTC heater 613 can improve its heat dissipation rate by using U-shaped corrugated fins. And moreover, the advantages of adhesion and mechanical type are combined, various thermal and electrical phenomena of the PTC heater 613 during working are fully considered, and the PTC heater is strong in binding force, excellent in heat conduction and heat dissipation performance, high in efficiency, safe and reliable.

In addition, the PTC heater 613 has the advantages of low thermal resistance and high heat exchange efficiency, and is an automatic constant temperature and power saving electric heater. The safety performance of the heater is characterized in that when the fan stops due to failure, the power of the PTC heater 613 can be automatically and rapidly reduced because the PTC heater 613 cannot fully dissipate heat, and the surface temperature of the heater is maintained at about Curie temperature (generally about 250 ℃), so that the surface of the heater such as an electric heating tube heater is prevented from being red, the heat exchange efficiency is greatly improved, and the safety is high.

Meanwhile, the cold working medium discharged from the cold working medium supply system 300 due to overpressure or the hot working medium discharged from the hot working medium supply system 400 due to overpressure can be input into the heat exchanger 610 for treatment and recovery.

The recycling system 600 further includes a recycling tank 620 disposed below the heat exchanger 610, and the hot working medium condensed by the heat exchange between the fins of the heat exchanger 610 and the air enters the recycling tank 620 for recycling.

Retrieve and be provided with weighing sensor 621 under jar 620, when retrieving jar 620 interior hot working medium of condensation and reach a quantitative, weighing sensor 621 reports to the police and reminds the user in time to handle, avoids overflowing of working medium.

(V) Electrical control System 700 and Interactive System 800

As shown in fig. 8-13, the host unit 100 further includes an electrical control system 700 and an interactive system 800, which are electrically connected, and the electrical control system 700 is electrically connected to the cold working medium supply system 300, the hot working medium supply system 400 and the working medium distribution system 500, respectively, to control the working process of the working medium.

The electrical control system 700 includes a power supply system and a computer control system, wherein the power supply system includes an air switch, a filter, a soft start circuit, an isolation transformer and a switching power supply, and is powered by a lithium battery. The computer control system is communicatively connected to electrical devices such as pressure sensors 324,426, temperature sensor 422,513, level gauges 330,430, load cell 621, etc. to collect signals such as pressure, temperature, level, weight and position, etc. and to the switches of the actuators such as valves, pumps, heater 424, blower 512, etc. as mentioned above.

The electrical control system 700 may be implemented by means of a PCBA or a PLC, etc.

The interactive system 800 includes a display (touch screen) 810, a function pad 820, and a wireless tablet 914 disposed on a housing 910 for performing surgical operations, all of which may be operated independently. The system has the functions of displaying the three-color lamp, displaying the battery power, displaying the operation output state, identifying the RFID and the like, helps a user to use the system better, and improves the usability of the system.

The interactive system 800 can integrate a 5G communication module, and after the interactive system is connected with the Internet, a medical appliance manufacturer can monitor the use state of the system through an enterprise server, collect data of equipment which is put on the market, and provide conditions for maintenance and optimization of the equipment.

In addition, an emergency stop button 915 is provided on the housing 910.

The rear side of the housing 910 is also provided with four output ports 916 connected to the temperature probe 220 and the probe feed tube 210, respectively.

The host unit 100 also includes a power assist system 900. The power assisting system 900 comprises a power assisting wheel 911, an electric control wheel 912, a lithium battery and a handle 913 which are arranged on a shell 910. The power-assisted wheel 911 provides power for the movement of the main unit 100, the electric control wheel 912 is used for automatically locking the housing 910 when the housing 910 stops, and the handle 913 is integrated with a torque sensor, so that a hospital nurse can conveniently move the device.

The cold working medium supply system 300, the hot working medium supply system 400, the working medium distribution system 500, the recovery system 600 and the electrical control system 700 are all integrated in the shell 910, and can be conveniently moved by matching with the mobile power assisting system 900.

(VI) Cold-Heat ablation needle 200

As shown in fig. 1, the cold-hot ablation needle 200 is connected with the cold working medium supply system 300 and the hot working medium supply system 400 through the probe delivery pipe 210, and the probe delivery pipe 210 has a vacuum heat insulation layer, so that an operator is not affected by low temperature or high temperature during use.

The probe conveying pipe 210 can convey and recycle the working medium in the probe conveying pipe 210, wherein the probe conveying pipe 210 is soft, so that an operator can conveniently rotate and bend in the using process, and the operability in the operation process is greatly improved.

Furthermore, the probe delivery pipe 210 and the cold and hot ablation needle 200 as well as the cold working medium supply system 300 and the hot working medium supply system 400 are connected in a quick-insertion manner, so that the operation of an operator is facilitated, the connection confirmation is carried out, and the connection is firm.

Also connected to the host unit 100 is a temperature probe 220 for detecting the temperature of tissue during surgery, and a temperature sensor (e.g., a T-type thermocouple) is disposed within the needle.

The diameter of the needle tube of the temperature probe 220 is 0.5 mm-3 mm; the interface between the lead and the host unit 100 is a coupling multi-core connector, which is convenient for plugging and unplugging and has anti-loose design.

The cold and hot ablation needle 200 and the temperature probe 220 are disposable sterile products, and are integrated with an electronic encryption chip, so that the RFID card reader of the interaction system 800 can be matched to effectively identify the cold and hot ablation needle and is used in a limited time, and repeated use of the disposable sterile products is avoided. The chip can also record parameters such as production batch number, validity period, specification and the like of the cold and hot ablation needle 200 or the temperature measuring probe 220.

In addition, the diameter of the needle tube of the cold-hot ablation needle 200 is generally 1mm to 8 mm.

Specifically, as shown in fig. 16 and 17, the cold-hot ablation needle 200 includes a working medium input pipe 201 and a working medium return pipe 202 sleeved outside the working medium input pipe 201, wherein the working medium input pipe 201 is connected to the cold working medium supply system 300 or the hot working medium supply system 400, respectively, and the cold working medium or the hot working medium can be input to the working medium input pipe 201 through the cold working medium supply system 300 or the hot working medium supply system 400 (as shown by an arrow in fig. 17, a flow direction when the working medium is input).

After the cold working medium or the hot working medium in the working medium input pipe 201 reaches the needle point of the cold-hot ablation needle 200, the treatment area is treated, and after the treatment is completed, the cold working medium or the hot working medium is output to the recovery system 600 along the working medium return pipe 202 (as shown by an arrow in fig. 17, the flow direction of the working medium during output is shown). That is, the flow directions of the working medium in working medium return pipe 202 and working medium input pipe 201 are opposite.

Therefore, the cold-hot ablation needle 200 of the present invention can integrate the input (inflow) and the output (backflow) by sleeving the pipelines, so that the working medium input pipe 201 and the working medium backflow pipe 202 do not need to be matched with an external connection pipe; the structure of the connecting lines and the medium storage device is greatly simplified.

In addition, the working medium input pipe 201 and the working medium return pipe 202 are both constructed into a bent pipe structure, that is, the extending directions of the working medium input pipe 201 and the working medium return pipe 202 are changed, as shown in fig. 16, the cold-hot ablation needle 200 integrally forms an L-shaped structure, so that the cold-hot ablation needle 200 is not oversized in one direction as a whole; in addition, it is particularly important that, even if sudden disturbance or vibration is applied to the handle portion of the ablation needle body, the acting force is not immediately transmitted to the needle tip portion of the ablation needle 200 to affect the patient, so that the disturbance of unstable factors such as disturbance to the needle tip portion of the ablation needle 200 can be reduced by the bent tube structure, thereby improving the treatment stability of the ablation needle 200.

Further, the thermal ablation needle 200 further includes a vacuum tube 203, wherein the vacuum tube 203 is sleeved outside the working medium return tube 202, and the vacuum tube 203 at least covers a part of the outer wall of the working medium return tube 202, so that a vacuum layer 204 is formed between at least a part of the outer wall of the working medium return tube 202 and at least a part of the inner wall of the vacuum tube 203, as shown in fig. 17. The vacuum layer 204 can better realize that the thermal ablation needle 200 has good vacuum insulation performance in the non-treatment area part (so as to prevent the non-treatment area part from frostbite normal skin tissue of a human body or contacting with an operation operator in the non-treatment area part of the ablation needle when the targeted tissue is cryogenically treated).

In addition, as shown in fig. 5, a temperature sensor is disposed at an inlet of the working medium input pipe 201, and a temperature sensor is also disposed at an outlet of the working medium return pipe 202 to detect a temperature of the working medium.

The high-low temperature composite ablation operation system of the utility model can adopt the working pressure below the critical point of the working medium, and if the temperature is low enough at the same time, the working medium is in a liquid state; if at the same time the temperature is sufficiently high, the working substance is in the gaseous state. It is understood that working pressures above the critical point of the working fluid may also be used, in which case the working fluid is in the supercritical state.

Taking working medium as nitrogen as an example for explanation:

critical temperature Tc of nitrogen is 126.2K (-147 deg.C), critical pressure Pc is 3.4MPa, and critical density is 313.3kg/m 3. Nitrogen has an abnormally large thermal expansion coefficient, a large specific heat capacity and a relatively small viscosity near a near critical point, and a high heat exchange coefficient can be obtained when the temperature difference is small. In the supercritical nitrogen transmission process, the temperature is higher than the liquid nitrogen temperature, so the loss of the refrigerating capacity along the way is small. The working pressure is high, the integral density is high, and the mass flow is high. Therefore, the utility model preferably adopts nitrogen as the cold working medium.

The utility model discloses the circulation route of well cold working medium as follows:

the cold working medium in the cold working medium storage tank 311 sequentially passes through the output valve 312, the filling interface 314, the liquid adding valve 315 and the one-way valve 316 to enter the cold tank 321 to complete liquid adding.

The cold working medium in the cold tank 321 is input to the cold-heat ablation needle 200 along the main pipeline for treatment; and is input to the heat exchanger 610 along a branch for recovery.

Specifically, after entering the probe delivery pipe 210 sequentially through the output valve, the phase separator 510 and the precooler 520 along the main pipeline, the cold working medium in the cold tank 321 enters the cold-hot ablation needle 200 through the input port of the cold-hot ablation needle 200. The cold working medium entering the cold and hot ablation needle 200 returns to the output port after the treatment is completed in the treatment area. And the cold working medium at the output port of the cold and hot ablation needle 200 enters the heat exchanger 610 to be heated, and the heated cold working medium is treated and then discharged.

Cold working medium (gas state) in the cold tank 321 enters the heat exchanger 610 along the branch through the manual valve 327 or the release valve 328 for overpressure release.

The utility model discloses well hot working medium's circulation route is as follows:

the hot working medium in the hot working medium storage tank 411 sequentially enters the hot tank 421 through the liquid filling port 412, the filling pump 413 and the filling valve 414 to complete liquid filling.

The hot working medium in the hot tank 421 is input to the cold-hot ablation needle 200 along the main pipeline for treatment; and is input to the heat exchanger 610 along a branch for recovery.

Specifically, after entering the probe delivery pipe 210 sequentially through the output valve, the phase separator 510 and the precooler 520 along the main pipeline, the hot working medium in the hot tank 421 enters the cold-hot ablation needle 200 through the input port of the cold-hot ablation needle 200. The hot working medium entering the cold-hot ablation needle 200 returns to the output port thereof after the treatment is completed in the treatment area. The hot working medium at the output port of the cold-hot ablation needle 200 enters the heat exchanger 610 to be cooled, and the cooled hot working medium enters the recovery tank 620.

The hot working medium (when the pressure is over-pressure) in the hot tank 421 passes through the manual valve 428 or the air release valve 429 along the branch to enter the heat exchanger 610 for recovery.

While the invention has been described with reference to a preferred embodiment, various modifications may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In particular, the technical features mentioned in the embodiments can be combined in any way as long as there is no structural conflict. The present invention is not limited to the particular embodiments disclosed herein, but encompasses all technical solutions falling within the scope of the claims.

Claims (10)

1. A high-low temperature combined ablation surgical system, which is characterized by comprising a host unit (100) and a cold-hot ablation needle (200) connected with the host unit (100), wherein the cold-hot ablation needle (200) is used for treating a lesion of a patient;

the host unit (100) comprises:

a cold working medium supply system (300) for delivering cold working medium to the cold and hot ablation needle (200);

a hot working medium supply system (400) for delivering a hot working medium to the needle (200); and

the working medium distribution system (500) is respectively connected with the cold working medium supply system (300) and the hot working medium supply system (400), and the working medium distribution system (500) is used for controlling the cold working medium supply system (300) to convey cold working medium to the cold and hot ablation needle (200) and controlling the hot working medium supply system (400) to convey hot working medium to the cold and hot ablation needle (200).

2. The high-low temperature composite ablation surgical system according to claim 1, wherein the working medium distribution system (500) comprises:

a phase separator (510) connected to the cold medium supply system (300); and

a precooler (520) provided with a gas channel (521) and a liquid channel, wherein the input side of the gas channel (521) is communicated with the gas outlet end of the phase separator (510), and the input side and the output side of the liquid channel are respectively communicated with the liquid outlet end of the phase separator (510) and the cold-hot ablation needle (200);

wherein the gas in the gas channel (521) is used for pre-cooling the liquid in the liquid channel.

3. The high-low temperature composite ablation surgical system according to claim 2, wherein the gas channel (521) is configured as a labyrinth-like channel.

4. The high-low temperature composite ablation surgical system according to any one of claims 1 to 3, characterized in that the host unit (100) further comprises a recovery system (600) connected to the output port of the cold-hot ablation needle (200), and the recovery system (600) is respectively connected to the cold working medium supply system (300) and the hot working medium supply system (400) for collecting the cold working medium or the hot working medium after the treatment, or collecting the cold working medium discharged from the cold working medium supply system (300) or the hot working medium discharged from the hot working medium supply system (400) due to overpressure.

5. The high-low temperature composite ablation surgical system according to claim 4, wherein the recovery system (600) comprises a heat exchanger (610) connected with each other, the heat exchanger (610) is connected with an output port of the cold-hot ablation needle (200), and the heat exchanger (610) is used for returning cold working medium output by the cold-hot ablation needle (200) to the atmosphere after heating up, or recovering hot working medium output by the cold-hot ablation needle (200) after cooling down.

6. The high-low temperature composite ablation surgical system according to any one of claims 1 to 3, wherein the cold working medium supply system (300) comprises a cold tank (321) for carrying cold working medium, and the cold tank (321) is used for conveying the pressurized cold working medium to the cold-hot ablation needle (200).

7. The high-low temperature composite ablation surgical system as claimed in claim 6, wherein a pressurizing pipeline (322) is connected to the cold tank (321), and the pressurizing pipeline (322) is used for realizing self-pressurization of the cold working medium in the cold tank (321).

8. The high-low temperature composite ablation surgical system according to any one of claims 1 to 3, wherein the hot working medium supply system (400) comprises a hot tank (421) for carrying a hot working medium, and the hot tank (421) is used for conveying the hot working medium with pressure to the cold-hot ablation needle (200).

9. The high-low temperature composite ablation surgical system according to claim 8, characterized in that a heating device is arranged on the hot tank (421), and the heating device is used for vaporizing and pressurizing the hot working medium in the hot tank (421).

10. The high-low temperature composite ablation surgical system according to any one of claims 1 to 3, wherein the host unit (100) further comprises an electrical control system (700) and an interaction system (800) which are electrically connected, and the electrical control system (700) is electrically connected with the cold working medium supply system (300), the hot working medium supply system (400) and the working medium distribution system (500) respectively so as to control the working process of the working medium.

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