Oxidation and Antioxidant Medical System

Abstract

The present application relates to the fields of ozone medicine and hydrogen medicine and their interactive applications, and specifically discloses an oxidation and antioxidant medical system. The oxidation and antioxidant medical system includes ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment, oxidation and antioxidant saline generation equipment, oxidation and antioxidant intestinal flora reconstruction and fecal bacteria transplantation equipment, oxidation and antioxidant gynecological treatment equipment, oxidation and antioxidant burn and scald infiltration treatment equipment, and oxidation and antioxidant hemodialysis treatment equipment. The system generates ozone dialysis water and hydrogen-rich dialysis water by electrolyzing dialysis water in a dedicated electrolytic cell, and further configures it into ozone and hydrogen-rich dialysis saline. It can be applied to intestinal flora for intestinal flora reconstruction and fecal bacteria transplantation, and is applied to the treatment of gynecological diseases and infiltration rehabilitation treatment of patients with burns and scalds, cleaning treatment of difficult-to-heal tissues, treatment of gangrene, treatment of oral inflammation, and treatment of skin infections and skin diseases caused by fungi and bacteria.

Description

Technical Field

[0001] The present application relates to the fields of ozone medicine and hydrogen medicine and their interactive applications, and specifically to an oxidation and antioxidant medical system composed of several innovative medical devices. Background Art

[0002] Ozone water has strong oxidizing properties and is a good disinfectant. Its bactericidal ability is significantly greater than that of alcohol and chlorine, and its disinfection effect is also better than that of iodine disinfectants. Ozone water has a significant therapeutic effect on diseases caused by skin infections. Frequent use of ozone water to rinse wounds can prevent wound infection and promote wound healing.

[0003] The medical ozone therapy device produced in Germany is connected to the medical oxygen cylinder, and generates 0-80µg / ml ozone gas through high-voltage discharge. A small amount of ozone gas is injected into the bone joints to treat arthritis. The human blood is drawn into a special blood transfusion bag, and then a small amount of ozone gas is injected into the blood transfusion bag through a syringe and fully mixed with the blood before being injected back into the human body to achieve the purpose of treating a variety of diseases. This therapy is called major autohemotherapy or minor autohemotherapy. The ozone gynecological therapy device produces ozone water for gynecological cleaning to achieve the purpose of treating gynecological diseases.

[0004] The biological effects of hydrogen medicine and ozone medicine are similar and their indications highly overlap. Both have a wide range of biological effects. Currently, there is no medical system that uses hydrogen and ozone interactively.

[0005] Studies have shown that intestinal flora has a significant impact on human health and longevity. Japanese scholars have confirmed through research that the amount of hydrogen produced by the intestinal flora of Japanese centenarians is more than three times that of normal people. Hydrogen is an endogenous gas in the human body and a longevity gas. The medical community uses fecal microbiota transplantation (FMT) to treat a variety of diseases and treats colitis by introducing ozone gas into the large intestine. The effectiveness of drinking hydrogen-rich water to treat constipation is more than 80%. The human intestinal flora can produce hydrogen that is absorbed by the human body and has beneficial effects. Infusing or injecting hydrogen-rich saline into the human body to achieve the purpose of treatment has become a safe treatment method. Tongji Hospital has studied a new treatment for allergic rhinitis, namely the treatment of saline containing hydrogen, with an effectiveness of 86%, which is not inferior to drug treatment. This new treatment is not only safe and effective, but also low-cost, bringing good news to many allergic rhinitis patients. This research result also won the third prize of Shanghai Medical Science and Technology. Summary of the invention

[0006] Since there is no medical system that uses ozone and hydrogen interactively, and ozone has an oxidizing effect and hydrogen has an antioxidant effect, this application proposes an oxidation and antioxidant medical system composed of the following oxidation and antioxidant equipment.

[0007] The oxidation and antioxidant medical system is specifically composed of ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment to provide ozone water and hydrogen-rich water, and specifically generates oxidation and antioxidant saline generation equipment at the back end, oxidation, antioxidant intestinal flora reconstruction and fecal microbiota transplantation equipment, oxidation and antioxidant gynecological treatment equipment, oxidation and antioxidant burn infiltration treatment equipment and oxidation and antioxidant hemodialysis treatment equipment. These five interrelated innovative medical devices constitute the oxidation and antioxidant medical system. The specific scheme adopted by this system is as follows.

[0008] An oxidation and antioxidant medical system, including ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment; the ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment includes a hydrogen-rich cathode sanitary pure water tank, an ozone anode sanitary pure water tank, a dedicated electrolyzer, a hydrogen-rich cathode dissolved gas cutting pump, an ozone anode dissolved gas cutting pump, a hydrogen-rich dialysis water supply dedicated pipeline and an ozone dialysis water supply dedicated pipeline. The water outlet of the hydrogen-rich cathode sanitary pure water tank is connected to the lower inlet of the cathode side of the dedicated electrolyzer, and the water outlet of the hydrogen-rich cathode sanitary pure water tank is also connected to the water inlet of the hydrogen-rich cathode dissolved gas cutting pump; the upper outlet of the cathode side of the dedicated electrolyzer is connected to the negative pressure port of the hydrogen-rich cathode dissolved gas cutting pump; the water outlet of the hydrogen-rich cathode dissolved gas cutting pump is connected to the hydrogen-rich dialysis water supply dedicated pipeline, and the hydrogen-rich dialysis water supply dedicated pipeline is connected to the water outlet of the hydrogen-rich cathode sanitary pure water tank to form a closed loop. The water outlet of the ozone anode sanitary pure water tank is connected to the lower inlet of the anode side of the dedicated electrolytic cell, and the water outlet of the ozone anode sanitary pure water tank is also connected to the water inlet of the ozone anode dissolved gas cutting pump; the upper outlet on the anode side of the dedicated electrolytic cell is connected to the negative pressure port of the ozone anode dissolved gas cutting pump, and the water outlet of the ozone anode dissolved gas cutting pump is connected to the dedicated water supply pipeline for ozone dialysis water, and the dedicated water supply pipeline for ozone dialysis water is connected to the water outlet of the ozone anode sanitary pure water tank to form a closed loop.

[0009] By adopting the above technical solution, when the equipment is running, two sanitary pure water tanks first ensure a certain liquid level, and two dissolved air cutting pumps run for a certain period of time at the same time to circulate the two water circuits in the equipment, and the cathode and anode in the special electrolytic cell are also in circulation. At this time, the circuit control supplies a certain direct current to the special electrolytic cell to put it in an electrolysis working state. At this time, a mixture of hydrogen bubbles and dialysis water is generated in the cathode side water circuit of the special electrolytic cell, and the hydrogen bubbles are broken up by the hydrogen-rich cathode dissolved air cutting pump and dissolved into the dialysis water to generate high-concentration hydrogen-rich dialysis water. A mixture of oxygen and ozone bubbles and dialysis water is generated in the anode side water circuit of the special electrolytic cell, and the oxygen and ozone bubbles are broken up by the ozone anode dissolved air cutting pump and dissolved into the dialysis water to generate high-concentration ozone dialysis water, which are respectively supplied to each treatment room and treatment station through special pipelines for further use.

[0010] Preferably, an online ultrasonic dissolved gas probe and a flow-through ultraviolet lamp are installed on the dedicated water supply pipeline for hydrogen-rich dialysis water; another online ultrasonic dissolved gas probe is installed on the dedicated water supply pipeline for ozone dialysis water.

[0011] By adopting the above technical solution, the online ultrasonic dissolved air probe emits ultrasound into the pipeline, and uses ultrasonic cavitation to further break the micron bubbles in the micro-nano bubble water output by the dissolved air cutting pump into nano bubbles for further dissolution in the water. The over-flow ultraviolet lamp not only plays a role in sterilization and disinfection, but also can eliminate possible ozone.

[0012] Preferably, the oxidation and antioxidant medical system includes multiple groups of medical equipment, each group of medical equipment is connected to the dedicated water supply pipeline for hydrogen-rich dialysis water and the dedicated water supply pipeline for ozone dialysis water; the multiple groups of medical equipment include oxidation and antioxidant saline production equipment, oxidation and antioxidant intestinal flora reconstruction and fecal bacteria transplantation equipment, oxidation and antioxidant gynecological treatment equipment, oxidation and antioxidant burn infiltration treatment equipment, and oxidation and antioxidant hemodialysis treatment equipment.

[0013] Preferably, the oxidation and antioxidant medical system includes multiple groups of medical equipment; the multiple groups of medical equipment include oxidation and antioxidant saline production equipment, oxidation and antioxidant intestinal flora reconstruction and fecal microbiota transplantation equipment, oxidation and antioxidant gynecological treatment equipment, oxidation and antioxidant burn and scald infiltration treatment equipment, and oxidation and antioxidant hemodialysis treatment equipment. The oxidation and antioxidant saline solution generating equipment is connected to the hydrogen-rich dialysis water supply dedicated pipeline and the ozone dialysis water supply dedicated pipeline; the oxidation and antioxidant intestinal flora reconstruction and fecal bacteria transplantation equipment is connected to the hydrogen-rich dialysis water supply dedicated pipeline and the ozone dialysis water supply dedicated pipeline; the oxidation and antioxidant gynecological treatment equipment is connected to the hydrogen-rich dialysis water supply dedicated pipeline and the ozone dialysis water supply dedicated pipeline; the oxidation and antioxidant hemodialysis treatment equipment is connected to the hydrogen-rich dialysis water supply dedicated pipeline and the ozone dialysis water supply dedicated pipeline; the oxidation and antioxidant saline solution generating equipment outputs hydrogen-rich dialysis saline solution and ozone dialysis saline solution; the oxidation and antioxidant burn and scald infiltration treatment equipment introduces the hydrogen-rich dialysis saline solution and ozone dialysis saline solution output by the oxidation and antioxidant saline solution generating equipment.

[0014] By adopting the above technical solutions, multiple groups of medical devices are used to treat different diseases.

[0015] Preferably, the first structure of the oxidation and antioxidant saline production equipment is that the oxidation and antioxidant saline production equipment includes a hydrogen-rich dialysis water inlet solenoid valve, multiple one-way valves, a hydrogen-rich dialysis water proportional pump, multiple saline concentration conductivity probes and display meters, an ozone dialysis water inlet solenoid valve, an ozone dialysis water proportional pump, and a supersaturated concentrated brine supply device. The hydrogen-rich dialysis water supply dedicated pipeline is connected to the hydrogen-rich dialysis water inlet solenoid valve, the hydrogen-rich dialysis water inlet solenoid valve is connected to the hydrogen-rich dialysis water proportional pump through a one-way valve, and the salt intake port of the hydrogen-rich dialysis water proportional pump is connected to the supersaturated concentrated brine supply device through a hose, and the outlet of the hydrogen-rich dialysis water proportional pump outputs hydrogen-rich dialysis saline through a saline concentration conductivity probe and a display meter. The dedicated water supply pipeline for ozone dialysis water is connected to the ozone dialysis water inlet solenoid valve, and the ozone dialysis water inlet solenoid valve is connected to the ozone dialysis water proportional pump through another one-way valve, and the salt intake port of the ozone dialysis water proportional pump is connected to the supersaturated concentrated brine supply equipment through a hose, and the outlet of the ozone dialysis water proportional pump outputs ozone dialysis saline through another saline concentration conductivity probe and display instrument.

[0016] By adopting the above technical scheme, the oxidation and antioxidant saline generation equipment mixes ozone dialysis water and hydrogen-rich dialysis water with supersaturated injection concentrated saline formed by dissolving injection salt in dialysis water in a certain proportion to form hypotonic, mesotonic and hypertonic saline, which can be directly used for various medical applications and the treatment of diseases. The oxidation and antioxidant saline generation equipment includes an injection Nacl salt dissolution container and a supersaturated injection Nacl concentrated saline storage container, which respectively introduce ozone dialysis water and hydrogen-rich dialysis water at about 35°C through a proportional pump or a combination of a proportional pump and a metering pump. After a certain amount of supersaturated injection physiological Nacl concentrated saline is inhaled and mixed, the concentration and conductivity of the physiological saline are displayed simultaneously on the instrument, and the metering pump is manually adjusted or automatically controlled to generate the corresponding hypotonic, mesotonic and hypertonic saline.

[0017] Preferably, the second structure of the oxidation and antioxidant saline production equipment is that the oxidation and antioxidant saline production equipment includes a hydrogen-rich dialysis saline output pipeline and an ozone dialysis saline output pipeline. The hydrogen-rich dialysis water supply dedicated pipeline is connected to the hydrogen-rich dialysis saline output pipeline; the hydrogen-rich dialysis saline output pipeline is sequentially installed with a hydrogen-rich dialysis water inlet solenoid valve, a one-way valve, a hydrogen-rich dialysis water proportional pump and a saline concentration conductivity probe and display instrument along the water flow direction; the salt intake port of the hydrogen-rich dialysis water proportional pump is connected to the supersaturated concentrated brine equipment through a one-way valve and a metering pump; the outlet of the hydrogen-rich dialysis water proportional pump outputs hydrogen-rich dialysis saline through the saline concentration conductivity probe and display instrument. The ozone dialysis water supply dedicated pipeline is connected to the ozone dialysis saline output pipeline; the ozone dialysis saline output pipeline is sequentially installed with an ozone dialysis water inlet solenoid valve, a one-way valve, an ozone dialysis water proportional pump, and a saline concentration conductivity probe and display instrument along the water flow direction; the salt intake port of the ozone dialysis water proportional pump is connected to the supersaturated concentrated brine equipment through a one-way valve and a metering pump; the outlet of the ozone dialysis water proportional pump outputs ozone dialysis saline through the saline concentration conductivity probe and display instrument. The oxidation and antioxidant saline generation equipment also includes a connecting pipeline; the two ends of the connecting pipeline are respectively connected to the inlet of the hydrogen-rich dialysis water proportional pump of the hydrogen-rich dialysis saline output pipeline and the inlet of the ozone dialysis water inlet solenoid valve of the ozone dialysis saline output pipeline; another ozone dialysis water inlet solenoid valve, another metering pump and another one-way valve are installed on the connecting pipeline; the one-way valve on the connecting pipeline allows water to flow to the inlet of the hydrogen-rich dialysis water proportional pump.

[0018] By adopting the above technical solution, the introduced high-concentration ozone dialysis water and high-concentration hydrogen-rich dialysis water enter the water inlet solenoid valve and proportional pump respectively, and the liquid suction port of the proportional pump is respectively equipped with a metering pump, and the output of the proportional pump is respectively equipped with a display instrument showing the concentration of physiological saline and conductivity, and there is an analog data output. The output salt concentration is set by circuit control to automatically control the salt absorption of the metering pump, so that the output of the proportional pump reaches the set salt concentration, respectively. The hypotonic, mesotonic and hypertonic physiological saline concentrations or any required concentration in between can be set. In this way, there are two outputs of high-concentration ozone dialysis physiological saline and high-concentration hydrogen-rich dialysis physiological saline. Further, a thin tube micro-branch is added at the water supply of high-concentration ozone dialysis water, which is connected to the front of the hydrogen-rich dialysis water proportional pump through the solenoid valve, metering pump and one-way valve. When the micro-branch solenoid valve and metering pump are opened, a small amount of ozone dialysis water is mixed with the hydrogen-rich dialysis water to obtain hydrogen-rich ozone mixed physiological saline.

[0019] Preferably, the oxidation, antioxidant intestinal flora reconstruction and fecal bacteria transplantation equipment includes: a hydrogen-rich circuit, an ozone circuit, a mixing circuit, a salt circuit, an intestinal bacteria circuit and a fecal bacteria circuit. The mixing circuit is sequentially installed with an ozone hydrogen-rich dialysis water mixing ratio pump, a saline concentration conductivity probe and a display instrument, a pressure controller, a pressure gauge, a one-way valve and a special intestinal treatment flushing head. The front end of the hydrogen-rich circuit is connected to the dedicated water supply pipeline for hydrogen-rich dialysis water, and the rear end is connected to the ozone hydrogen-rich dialysis water mixing ratio pump of the mixing circuit. The hydrogen-rich circuit is installed with a hydrogen-rich dialysis water inlet solenoid valve and a one-way valve. The front end of the ozone circuit is connected to the dedicated water supply pipeline for ozone dialysis water, and the rear end is bifurcated into two branches connected to the ozone hydrogen-rich dialysis water mixing ratio pump of the mixing circuit; one branch of the ozone circuit is sequentially installed with an ozone dialysis water inlet solenoid valve, a metering pump and a one-way valve, and the other branch is sequentially installed with an ozone dialysis water inlet solenoid valve and a one-way valve. The salt line is equipped with supersaturated brine supply equipment, metering pumps, one-way valves and salt absorption solenoid valves in sequence. The salt absorption solenoid valve is connected to the salt absorption port of the ozone hydrogen-rich dialysis water mixing proportion pump in the mixing line. The intestinal bacteria line is equipped with intestinal probiotic liquid barrels, peristaltic pumps and one-way valves in sequence; the one-way valve of the intestinal bacteria line is connected to the intestinal treatment flushing head. The fecal bacteria line is equipped with fecal bacteria transplantation liquid barrels, peristaltic pumps and one-way valves in sequence; the one-way valve of the fecal bacteria line is connected to the intestinal treatment flushing head.

[0020] By adopting the above technical scheme, the suction port below the ozone hydrogen-rich dialysis water mixing proportion pump is provided with a solenoid valve, a one-way valve and a metering pump. After the circuit control is opened, a certain amount of supersaturated injection concentrated saline is input to configure the appropriate concentration of injection saline. The metering pump can also be removed to adjust the proportion pump to fix the configuration of hypotonic saline. When this salt absorption solenoid valve is closed, the supersaturated injection concentrated saline will not enter the proportion pump. At this time, the equipment can control the output of three different dialysis waters, namely: 1. High-concentration hydrogen-rich dialysis water, 2. Mixed water of high-concentration hydrogen-rich dialysis water and a small amount of high-concentration ozone dialysis water, 3. High-concentration ozone dialysis water. When the circuit controls the salt absorption solenoid valve to open, the equipment outputs the appropriate concentration of saline for the above dialysis water. The use of the equipment is ① first use high-concentration hydrogen-rich dialysis water at about 35°C or its configured saline to clean the intestines. ② Then control the mixing of a small amount of high-concentration ozone dialysis water to clean the intestines to kill some intestinal flora. ③ Use high-concentration ozone dialysis water or its specific concentration of physiological saline to clean the intestine according to the condition to completely kill the unbalanced flora in the intestine. ④ Then repeat step ① to clean the killed intestinal flora and the ozone in the intestine, so as to facilitate the colonization and reconstruction of intestinal probiotics and the effect of fecal transplantation. ⑤ Control the start of the peristaltic pump for delivering probiotic liquid to input the intestinal probiotic liquid into the intestine for intestinal probiotic colonization, or start the peristaltic pump for delivering fecal transplant liquid to input the fecal transplant liquid into the intestine for fecal transplantation. Step ⑤ can be performed separately for several days to enhance the colonization of intestinal probiotics and the fixed value of fecal bacteria, or it can be performed crosswise to obtain a richer reconstruction and transplantation of intestinal flora that is beneficial to health. In this way, the process of oxidation, antioxidant intestinal flora reconstruction and fecal transplantation is completed.

[0021] Preferably, the oxidation and anti-oxidation burn and scald infiltration treatment equipment comprises: a patient infiltration water tank, an LED immersion ultraviolet sterilization lamp, a hydrogen nano-aeration device, a medical ultrapure hydrogen source, a heating and heat preservation device, an ozone concentration probe, a waste liquid buffer tank, a drain solenoid valve, a manual drain valve and a saline concentration conductivity probe. The patient infiltration water tank introduces hydrogen-rich dialysis saline and ozone dialysis saline output by the oxidation and anti-oxidation saline generation device. The LED immersion ultraviolet sterilization lamps are distributed under the lower part and the side liquid surface of the patient immersion water tank, the hydrogen nano aeration devices are distributed at the bottom of the two longitudinal sides of the patient immersion water tank, and the medical ultrapure hydrogen source is connected to each hydrogen nano aeration device; the heating and insulation device is arranged at the outer bottom of the patient immersion water tank; the ozone concentration probe is arranged at the inner bottom of the patient immersion water tank, the physiological saline concentration conductivity probe is arranged at the inner bottom of the patient immersion water tank, and the waste liquid buffer tank is arranged on the lower movable bracket of the patient immersion water tank; the drain solenoid valve is arranged at the bottom of the patient immersion water tank, and the drain solenoid valve leads to the waste liquid buffer tank; a manual drain valve is arranged between the bottom of the patient immersion water tank and the waste liquid buffer tank; another manual drain valve is arranged at the bottom of the waste liquid buffer tank.

[0022] By adopting the above technical scheme, the immersion treatment equipment is suitable for the safe passage and rehabilitation treatment of patients with large-area severe burns and scalds during the dangerous infection period. When in use, the patient with severe burns and scalds lies flat in the patient's immersion and soaking tank, first injects a high-concentration hydrogen-rich hypotonic dialysis saline at about 35°C for antioxidant treatment, and then mixes a small amount of high-concentration ozone dialysis saline for infection prevention and control treatment. According to the condition, if a burn infection occurs, a high-concentration ozone hypotonic saline at about 35°C can be gradually injected for strong sterilization, disinfection, and immersion treatment. Then alternately inject high-concentration hydrogen-rich hypotonic saline, and the distribution of LED immersion ultraviolet sterilization lamps can be turned on or off according to the situation. Since ultraviolet rays have the effect of deozone, the ultraviolet lamp is turned off when ozone is needed, and the ultraviolet lamp can be controlled to turn on when ozone deozone and disinfection are needed. The control treatment plan is set according to the patient's condition to make the equipment operate normally. The oxidation and anti-oxidation burn and scald immersion treatment equipment provides a treatment method and survival possibility for patients with severe burns and scalds, which can improve their survival rate.

[0023] Preferably, the oxidation and anti-oxidation hemodialysis treatment equipment comprises: a hydrogen-rich dialysis water outlet valve, an ozone dialysis water outlet valve, an ozone dialysis water inlet solenoid valve, a metering pump, a one-way valve and a hemodialysis machine. The hydrogen-rich dialysis water outlet valve is connected to the inlet of the hemodialysis machine through a one-way valve; the ozone dialysis water outlet valve is connected to the metering pump through the ozone dialysis water inlet solenoid valve, and then connected to the inlet of the hemodialysis machine through a one-way valve.

[0024] By adopting the above technical scheme, the hose of the branch valve connected to the high-concentration hydrogen-rich dialysis water pipeline is connected to the hemodialysis machine, and the hose here is further connected to a micro-branch and connected to the branch valve of the high-concentration ozone dialysis water through a one-way valve, a metering pump, and a solenoid valve. By controlling the solenoid valve and the metering pump, a trace amount of high-concentration ozone dialysis water and high-concentration hydrogen-rich dialysis water are mixed and supplied to the hemodialysis machine. At the beginning of dialysis, high-concentration hydrogen-rich dialysis water is first used for hemodialysis. At an appropriate time, the micro-branch solenoid valve and the metering pump are controlled to open to control a trace amount of high-concentration ozone dialysis water to mix in for hemodialysis. After a certain period of time, the micro-branch solenoid valve and the metering pump are controlled to close, and the high-concentration hydrogen-rich dialysis water is continued to be used for hemodialysis until the machine is finished, or the micro-branch is not closed until the machine is finished.

[0025] This application uses the strong oxidation sterilization and oxygenation effects of high-concentration ozone dialysis water and the configured high-concentration ozone dialysis saline, as well as the safety, permeability, and selective antioxidant effects of high-concentration hydrogen-rich dialysis water and the configured high-concentration hydrogen-rich dialysis saline, and is comprehensively applied to the treatment of human diseases! This system can be used for cleaning and accelerating healing of difficult-to-heal tissues, treating skin infections and skin diseases caused by fungi and bacteria, infiltration rehabilitation treatment of burns and scalds, battlefield rescue wound cleaning and disinfection to prevent infection, treatment of diabetes and treatment of oral inflammation. This system also promotes patient recovery and people's health through oxidation, antioxidant intestinal flora reconstruction and fecal bacteria transplantation, etc. BRIEF DESCRIPTION OF THE DRAWINGS

[0026] Figure 1 Connection diagram of the ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment, which is the basic equipment of the oxidation and antioxidant medical system.

[0027] Figure 2 A connection diagram for scheme 1 of an oxidative and antioxidant saline solution generating device in an oxidative and antioxidant medical system.

[0028] Figure 3 This is a connection diagram for scheme 2 of an oxidative and antioxidant saline solution generating device in an oxidative and antioxidant medical system.

[0029] Figure 4 A connection diagram of the oxidative and antioxidant intestinal flora reconstruction and fecal microbiota transplantation devices within the oxidative and antioxidant medical system.

[0030] Figure 5 This is the connection diagram of the oxidation and antioxidant burn infiltration treatment equipment in the oxidation and antioxidant medical system.

[0031] Figure 6 for Figure 5 A top-down connection diagram of some structures of the oxidation and anti-oxidation burn and scald infiltration treatment equipment.

[0032] Figure 7 This is a connection structure diagram of the oxidation and antioxidant hemodialysis treatment equipment in the oxidation and antioxidant medical system.

[0033] Figure symbols: hydrogen-rich cathode sanitary pure water tank 1; ozone anode sanitary pure water tank 2; heating sleeve 101; liquid level sensing rod 102; immersion ultraviolet lamp 103; degassed water inlet solenoid valve 37; special electrolytic cell 3; cathode side 301; anode side 302; hydrogen-rich cathode dissolved gas cutting pump 4-1; ozone anode dissolved gas cutting pump 4-2; hydrogen-rich water supply dedicated pipeline 5; ozone water supply dedicated pipeline 6; online ultrasonic dissolved gas probe 7; flow-through ultraviolet lamp 8; pressure gauge 9; back pressure valve 10; hydrogen-rich dialysis water outlet valve 11; ozone dialysis water outlet valve 12; hydrogen-rich dialysis water inlet solenoid valve 13; one-way valve 14; hydrogen-rich dialysis water proportional pump 15; physiological saline concentration conductivity probe and display instrument 16; ozone dialysis water inlet solenoid valve 17; proportional pump for ozone dialysis water 18; metering pump 19; supersaturated concentrated brine supply equipment 20; supersaturated concentrated brine tank 20-1; salt absorption rod 20-2; salt tank for injection 20-3; supersaturated concentrated brine for injection 20-4; ozone hydrogen-rich dialysis water mixing proportional pump 21; salt absorption solenoid valve 22; pressure controller 23; peristaltic pump 24; intestinal special probiotic barrel 25; fecal bacteria transplantation liquid barrel 26; intestinal special treatment flushing head 27; patient infiltration immersion tank 28; LED immersion ultraviolet sterilization lamp 29; hydrogen nano aeration device 30; medical ultrapure hydrogen source equipment 31; heating and insulation device 32; ozone concentration probe 33; waste liquid buffer tank 34; drain solenoid valve 35; manual drain valve 36; physiological saline concentration conductivity probe 38. DETAILED DESCRIPTION

[0034] The oxidation and antioxidant medical system of the present application is described in detail below with reference to the accompanying drawings.

[0035] The oxidation and antioxidant medical system includes ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment. The oxidation and antioxidant medical system also includes multiple groups of medical equipment. The multiple groups of medical equipment include oxidation and antioxidant saline generation equipment, oxidation and antioxidant intestinal flora reconstruction and fecal bacteria transplantation equipment, oxidation and antioxidant gynecological treatment equipment, oxidation and antioxidant burn and scald infiltration treatment equipment, and oxidation and antioxidant hemodialysis treatment equipment.

[0036] Among them, the oxidation and antioxidant saline generation equipment is connected to the ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment; the oxidation and antioxidant intestinal flora reconstruction and fecal microbiota transplantation equipment is connected to the ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment; the oxidation and antioxidant gynecological treatment equipment is connected to the ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment; the oxidation and antioxidant hemodialysis treatment equipment is connected to the ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment. The oxidation and antioxidant saline generation equipment outputs hydrogen-rich dialysis saline and ozone dialysis saline. The oxidation and antioxidant burn and scald infiltration treatment equipment is connected to the oxidation and antioxidant saline generation equipment, and introduces the hydrogen-rich dialysis saline and ozone dialysis saline output by the oxidation and antioxidant saline generation equipment.

[0037] Please refer to Figure 1 The ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment includes: a hydrogen-rich cathode sanitary pure water tank 1, an ozone anode sanitary pure water tank 2, a heating sleeve 101, a liquid level sensing rod 102, an immersion ultraviolet lamp 103, a degassed water inlet solenoid valve 37, a special electrolytic cell 3, a hydrogen-rich cathode dissolved gas cutting pump 4-1, an ozone anode dissolved gas cutting pump 4-2, a hydrogen-rich water supply dedicated pipeline 5, an ozone water supply dedicated pipeline 6, an online ultrasonic dissolved gas probe 7, a flow-through ultraviolet lamp 8, a pressure gauge 9, and a back pressure valve 10.

[0038] The outlet of the hydrogen-rich cathode sanitary pure water tank 1 is connected to the lower inlet of the cathode side 301 of the dedicated electrolyzer 3 and the water inlet of the hydrogen-rich cathode dissolved gas cutting pump 4-1. The upper outlet of the cathode side 301 is connected to the negative pressure port of the hydrogen-rich cathode dissolved gas cutting pump 4-1, and the outlet of the hydrogen-rich cathode dissolved gas cutting pump 4-1 leads to the dedicated hydrogen-rich water supply pipeline 5, on which the dedicated hydrogen-rich water supply pipeline 5 is installed with an online ultrasonic dissolved gas probe 7, a flow-through ultraviolet lamp 8, a pressure gauge 9, and a back pressure valve 10. The dedicated hydrogen-rich water supply pipeline 5 flows back to the outlet of the hydrogen-rich cathode sanitary pure water tank 1 to form a cycle. The dedicated hydrogen-rich water supply pipeline 5 outputs high-concentration hydrogen-rich dialysis water at about 35°C.

[0039] The outlet of the ozone anode sanitary pure water tank 2 is connected to the lower inlet of the anode side 302 of the dedicated electrolyzer 3 and the water inlet of the ozone anode dissolved gas cutting pump 4-2, and the upper outlet of the anode side 302 is connected to the negative pressure port of the ozone anode dissolved gas cutting pump 4-2. The outlet of the ozone anode dissolved gas cutting pump 4-2 leads to the dedicated ozone water supply pipeline 6, on which the dedicated ozone water supply pipeline 6 is installed with an online ultrasonic dissolved gas probe 7, an ozone dialysis water outlet valve 12, a pressure gauge 9, and a back pressure valve 10. The dedicated ozone water supply pipeline 6 returns to the outlet of the ozone anode sanitary pure water tank 2 to form a cycle. The dedicated ozone water supply pipeline 6 outputs high-concentration ozone dialysis water at about 35°C.

[0040] The hydrogen-rich water supply dedicated pipeline 5 can be installed with a hydrogen-rich dialysis water outlet valve 11, and the ozone water supply dedicated pipeline 6 can be installed with an ozone dialysis water outlet valve 12 to connect to the hemodialysis machine. The hydrogen-rich water supply dedicated pipeline 5 can also directly output hydrogen-rich water through other valves, and the ozone water supply dedicated pipeline 6 can also directly output ozone water through other valves for direct use in related treatments.

[0041] The main body of the hydrogen-rich cathode sanitary pure water tank 1 and the ozone anode sanitary pure water tank 2 is cylindrical, and the lower part is conical or arc-shaped to facilitate emptying. A heating sleeve 101 can be set on the outside for heating and insulation, and a liquid level sensing rod 102 is set inside. The liquid level sensing rod 102 is connected to the circuit control system. When the liquid level is low, the control system controls the opening of the degassed water inlet solenoid valve 37 to replenish the dialysis water degassed at about 35°C. When the liquid level is full, the degassed water inlet solenoid valve 37 is controlled to be closed.

[0042] Since the ultraviolet germicidal lamp has both the function of disinfection and sterilization and the function of de-ozonation, an immersion type ultraviolet lamp 103 is set in the hydrogen-rich cathode sanitary pure water tank 1 on the cathode circulation side and a flow type ultraviolet lamp 8 is set on the hydrogen-rich water supply dedicated pipeline 5, which not only plays the role of disinfection and sterilization but also can eliminate the ozone that may be mixed in. The online ultrasonic dissolved gas probe 7 emits ultrasound into the pipeline and uses ultrasonic cavitation to further break the micron bubbles in the micro-nano bubble water output by the dissolved gas cutting pump into nano bubbles for further dissolution in the water. The back pressure valve 10 can adjust the water pressure in the pipeline to maintain a certain water pressure in the pipeline, and the pressure gauge 9 is used to display the water pressure in the pipeline. The hydrogen-rich cathode dissolved gas cutting pump 4-1 and the ozone anode dissolved gas cutting pump 4-2 can use frequency conversion control, and the adjustment of the back pressure valve 10 can make the water supply pressure in the pipeline more stable.

[0043] When the ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment is in operation, the two sanitary pure water tanks are first filled with dialysis water, and then the two dissolved gas cutting pumps are started at the same time, so that the dialysis water on the cathode side and the anode side of the special electrolyzer is circulated and delayed for a certain time, and then the special electrolyzer 3 is powered on and the ultrasonic dissolved gas probe 7 is controlled to work. The immersion ultraviolet lamp 103 and the over-current ultraviolet lamp 8 are turned on for irradiation. At this time, the equipment is in a normal working state, and the cathode side 301 of the special electrolyzer 3 produces a mixture of hydrogen bubbles and dialysis water, which is sucked into the negative pressure port of the hydrogen-rich cathode dissolved gas cutting pump 4-1 and mixed with the water inlet of the cutting pump, and then cut by the dissolved gas impeller to break the hydrogen bubbles into micro-nano bubbles, and then break the micron bubbles into nano bubbles through the ultrasonic cavitation of the online ultrasonic dissolved gas probe 7 for further dissolution, and then return to the outlet of the cathode sanitary pure water tank 1 through the hydrogen-rich water supply special pipeline 5 to form a cycle, thereby increasing the hydrogen concentration.

[0044] The anode side 302 of the dedicated electrolytic cell 3 produces a mixture of ozone (20%) and oxygen (80%) bubbles and dialysis water, which are then cut by a dissolved air impeller to break the bubbles into micro-nano bubbles, which are then further dissolved by ultrasonic cavitation by an online ultrasonic dissolved air probe 7, and then returned to the outlet of the ozone anode sanitary pure water tank 2 through an ozone water supply dedicated pipeline 6 to form a cycle, thereby increasing the ozone concentration.

[0045] When the liquid level of the dialysis water in the sanitary pure water tank reaches the water shortage warning position, the device controls to stop the operation of the dedicated electrolytic cell 3, and at the same time stops the operation of the dissolved air cutting pump and the operation of the online ultrasonic dissolved air probe 7. When the liquid level returns to normal, the device will operate normally. When the device is not in operation, the device is in a dormant state and runs regularly to prevent bacterial growth.

[0046] There are two options for the oxidation and antioxidant saline generation equipment in the oxidation and antioxidant medical system.

[0047] Option 1, reference Figure 2 The first structure of the oxidation and antioxidant saline generation equipment in the oxidation and antioxidant medical system includes: the oxidation and antioxidant saline generation equipment includes three hydrogen-rich saline pipelines and three ozone saline pipelines. The hydrogen-rich water supply dedicated pipeline 5 is connected to the three hydrogen-rich saline pipelines, and the three hydrogen-rich saline pipelines respectively output low-tonic high-concentration hydrogen-rich dialysis saline, medium-tonic high-concentration hydrogen-rich dialysis saline, and hypertonic high-concentration hydrogen-rich dialysis saline. The ozone water supply dedicated pipeline 6 is connected to the three ozone saline pipelines, and the three ozone saline pipelines respectively output low-tonic high-concentration ozone dialysis saline, medium-tonic high-concentration ozone dialysis saline, and hypertonic high-concentration ozone dialysis saline.

[0048] refer to Figure 2 The oxidation and anti-oxidation physiological saline production equipment includes a supersaturated concentrated saline supply equipment 20.

[0049] Each hydrogen-rich saline pipeline is sequentially installed with a hydrogen-rich dialysis water inlet solenoid valve 13, a one-way valve 14, a hydrogen-rich dialysis water proportional pump 15 and a physiological saline concentration conductivity probe and display instrument 16.

[0050] Each ozone saline pipeline is sequentially installed with an ozone dialysis water inlet solenoid valve 17, a one-way valve 14, an ozone dialysis water proportional pump 18 and a physiological saline concentration conductivity probe and display instrument 16.

[0051] The salt intake ports of the three hydrogen-rich dialysis water proportional pumps 15 and the salt intake ports of the three ozone dialysis water proportional pumps 18 are all connected to the supersaturated concentrated brine supply equipment 20 .

[0052] On the three-way hydrogen-rich saline pipeline, high-concentration hydrogen-rich dialysis water at about 35°C enters three solenoid valves 13, one-way valve 14, hydrogen-rich dialysis water proportional pump 15, and saline concentration conductivity probe and display instrument 16 to the outlet water respectively, and the salt absorption of the three hydrogen-rich dialysis water proportional pumps 15 is adjusted respectively, so that the three-way output is respectively hypotonic high-concentration hydrogen-rich dialysis saline, mesotonic high-concentration hydrogen-rich dialysis saline and hypertonic high-concentration hydrogen-rich dialysis saline and fixed. In this way, high-concentration hydrogen-rich dialysis saline has three outputs. If you want to use whichever one, control which solenoid valve 13 to open and output saline of that concentration.

[0053] On the three-way ozone saline pipeline, high-concentration ozone dialysis water at about 35°C enters three solenoid valves 17, one-way valve 14, ozone dialysis water proportional pump 18, and saline concentration and conductivity probe and display instrument 16 to the outlet water, respectively, and the salt absorption of the three ozone dialysis water proportional pumps 18 is adjusted respectively, so that the three-way output is respectively low-osmotic high-concentration ozone dialysis saline, medium-osmotic high-concentration ozone dialysis saline, and hypertonic high-concentration ozone dialysis saline and fixed, so that high-concentration ozone dialysis saline has three outputs, and whichever one you want to use is controlled by which solenoid valve 17 to open and output that concentration. In this way, Scheme 1 has six kinds of saline outputs for different applications.

[0054] Option 2, reference Figure 3 The oxidation and antioxidant saline production equipment includes a hydrogen-rich dialysis saline output pipeline and an ozone dialysis saline output pipeline.

[0055] The hydrogen-rich dialysis water supply dedicated pipeline 5 is connected to the hydrogen-rich dialysis saline output pipeline. The hydrogen-rich dialysis saline output pipeline is sequentially installed with a hydrogen-rich dialysis water inlet solenoid valve 13, a one-way valve 14, a hydrogen-rich dialysis water proportional pump 15 and a saline concentration conductivity probe and display instrument 16 along the water flow direction. The salt intake port of the hydrogen-rich dialysis water proportional pump 15 is connected to the supersaturated concentrated brine supply device 20 through a one-way valve 14 and a metering pump 19. The outlet of the hydrogen-rich dialysis water proportional pump 15 outputs hydrogen-rich dialysis saline through the saline concentration conductivity probe and display instrument 16.

[0056] The ozone dialysis water supply dedicated pipeline 6 is connected to the ozone dialysis saline output pipeline. The ozone dialysis saline output pipeline is sequentially installed with an ozone dialysis water inlet solenoid valve 17, a one-way valve 14, an ozone dialysis water proportional pump 18 and a saline concentration conductivity probe and display instrument 16 along the water flow direction; the salt intake port of the ozone dialysis water proportional pump 18 is connected to the supersaturated concentrated brine supply device 20 through a one-way valve 14 and a metering pump 19; the outlet of the ozone dialysis water proportional pump 18 outputs ozone dialysis saline through the saline concentration conductivity probe and display instrument 16.

[0057] The oxidation and antioxidant saline production device also includes a connecting pipeline. The two ends of the connecting pipeline are respectively connected to the inlet of the hydrogen-rich dialysis water proportional pump 15 of the hydrogen-rich dialysis saline output pipeline and the inlet of the ozone dialysis water inlet solenoid valve 17 of the ozone dialysis saline output pipeline. Another ozone dialysis water inlet solenoid valve 17, another metering pump 19 and another one-way valve 14 are installed on the connecting pipeline. The one-way valve 14 on the connecting pipeline allows water to flow to the inlet of the hydrogen-rich dialysis water proportional pump 15.

[0058] In the hydrogen-rich dialysis saline output pipeline, high-concentration hydrogen-rich dialysis water at about 35°C passes through the hydrogen-rich dialysis water inlet solenoid valve 13, the one-way valve 14, the hydrogen-rich dialysis water proportional pump 15, and the saline concentration conductivity probe and display instrument 16 to the outlet. The salt absorption port of the hydrogen-rich dialysis water proportional pump 15 is downwardly connected to the one-way valve 14 and the metering pump 19 to the supersaturated concentrated brine supply equipment 20. The salt absorption amount of the metering pump 19 is set and controlled by the circuit control so that the output is low-tonic, medium-tonic or hypertonic high-concentration hydrogen-rich dialysis saline.

[0059] In the ozone dialysis saline output pipeline, high-concentration ozone dialysis water at about 35°C passes through the solenoid valve 17, the one-way valve 14, the ozone dialysis water proportional pump 18, the saline concentration conductivity probe and the display instrument 16 to the water outlet, and the salt intake port of the proportional pump 18 is downwardly connected to the one-way valve 14 and the metering pump 19 to the supersaturated concentrated brine supply equipment 20. The circuit control sets and controls the salt intake of the metering pump 19 so that the output is low-tonic, medium-tonic and hypertonic high-concentration ozone dialysis saline.

[0060] On the connecting pipeline, high-concentration ozone dialysis water at about 35°C is connected to the water inlet of the hydrogen-rich dialysis water proportional pump 15 through the solenoid valve 17, the metering pump 19, and the one-way valve 14. The solenoid valve 17 is opened and the metering pump 19 is operated through circuit control to control a small amount or even a trace amount of high-concentration ozone dialysis water to be mixed into the high-concentration hydrogen-rich dialysis water. At this time, the output of the hydrogen-rich dialysis water proportional pump 15 is high-concentration hydrogen-rich dialysis saline mixed with a small amount or even a trace amount of ozone to obtain a third type of saline output for future application.

[0061] The supersaturated brine supply equipment 20 consists of a supersaturated brine tank 20-1, a salt absorption rod 20-2 and an injection salt tank 20-3. The injection salt tank 20-3 is used to place injection salt so that the injection salt fills the injection salt tank 20-3 and the supersaturated brine tank 20-1 is filled with supersaturated injection brine 20-4. Supersaturated injection brine needs to be injected into the supersaturated brine tank 20-1 at any time to keep it at the required high liquid level.

[0062] refer to Figure 4 The oxidative and antioxidant intestinal flora reconstruction and fecal bacteria transplantation equipment in the oxidative and antioxidant medical system include: hydrogen-rich path, ozone path, mixed path, salt path, intestinal bacteria path and fecal bacteria path.

[0063] The mixing line is sequentially equipped with an ozone hydrogen-rich dialysis water mixing ratio pump 21, a physiological saline concentration conductivity probe and display instrument 16, a pressure controller 23, a pressure gauge 9, a one-way valve 14 and a special intestinal treatment flushing head 27.

[0064] The front end of the hydrogen-rich path is connected to the dedicated hydrogen-rich dialysis water supply pipeline 5, and the rear end is connected to the ozone hydrogen-rich dialysis water mixing ratio pump 21 of the mixing path. The hydrogen-rich dialysis water inlet electromagnetic valve 13 and the one-way valve 14 are installed on the hydrogen-rich path.

[0065] The front end of the ozone circuit is connected to the ozone dialysis water supply dedicated pipeline 6, and the rear end is bifurcated into two branches connected to the ozone hydrogen-rich dialysis water mixing proportion pump 21 of the mixing circuit; the first branch of the ozone circuit is installed with the ozone dialysis water inlet solenoid valve 17, the metering pump 19 and the one-way valve 14 in sequence, and the second branch is installed with the ozone dialysis water inlet solenoid valve 17 and the one-way valve 14 in sequence.

[0066] The salt line is sequentially installed with a supersaturated brine supply device 20, a metering pump 19, a one-way valve 14 and a salt absorption solenoid valve 22, and the salt absorption solenoid valve 22 is connected to the salt absorption port of the ozone hydrogen-rich dialysis water mixing proportion pump 21 of the mixing line.

[0067] The intestinal bacteria path is sequentially installed with a probiotic liquid barrel 25 for the intestinal tract, a peristaltic pump 24 and a one-way valve 14; the one-way valve 14 of the intestinal bacteria path is connected to a special intestinal treatment flushing head 27.

[0068] The fecal bacteria path is sequentially installed with a fecal bacteria transplantation liquid barrel 26, a peristaltic pump 24 and a one-way valve 14; the one-way valve 14 of the fecal bacteria path is connected to a special intestinal treatment flushing head 27.

[0069] When the oxidation, antioxidant intestinal flora reconstruction and fecal microbiota transplantation equipment starts working, first open the hydrogen-rich dialysis water inlet solenoid valve 13, use high-concentration hydrogen-rich dialysis water to enter the ozone hydrogen-rich dialysis water mixing proportion pump 21 to the intestinal special treatment flushing head 27, and the intestinal special treatment flushing head 27 is placed in the patient's large intestine to perform enema cleansing on the large intestine, so that the large intestine has an antioxidant hydrogen-rich environment. Secondly, the ozone dialysis water inlet solenoid valve 17 and the metering pump 19 are opened to allow a small amount or even a trace amount of high-concentration ozone dialysis water to be mixed with the high-concentration hydrogen-rich dialysis water for enema cleaning of the large intestine, thereby partially killing the unbalanced intestinal flora in the large intestine. Alternatively, the hydrogen-rich dialysis water inlet solenoid valve 13 may be closed according to the actual situation of the patient, the ozone dialysis water inlet solenoid valve 17 and the metering pump 19 of the first branch are closed, and the ozone dialysis water inlet solenoid valve 17 of the second branch is opened to directly use the high-concentration ozone dialysis water to completely kill the harmful flora in the large intestine, and then the ozone dialysis water inlet solenoid valve 17 of the second branch is closed. , open the hydrogen-rich dialysis water inlet solenoid valve 13, use high-concentration hydrogen-rich dialysis water to perform enema cleaning on the patient to remove ozone in the large intestine, and finally close the hydrogen-rich dialysis water inlet solenoid valve 13, open the peristaltic pump 24 under the intestinal special probiotic liquid barrel 25, and inject the prepared intestinal special probiotic liquid into the large intestine to reconstruct the intestinal flora, or open the peristaltic pump 24 under the fecal microbiota transplantation liquid barrel 26, and inject the prepared fecal microbiota transplantation liquid into the large intestine for fecal microbiota transplantation. Intestinal special probiotic liquid or fecal microbiota transplantation liquid can be injected separately every few days to consolidate the effects of intestinal flora reconstruction and fecal microbiota transplantation, or they can be performed alternately.

[0070] During the above enema cleaning process, the salt absorption solenoid valve 22 and the metering pump 19 of the salt circuit can be opened according to the situation, and the output can be set to hypotonic, mesotonic and hypertonic saline through circuit control to increase the effect of flora reconstruction and fecal microbiota transplantation. The metering pump 19 under the salt absorption solenoid valve 22 can also be removed, and the output of the fixed ozone hydrogen-rich dialysis water mixing ratio pump 21 is adjusted to be hypotonic saline. Then, the salt absorption solenoid valve 22 is opened in a certain process through circuit control so that the ozone hydrogen-rich dialysis water mixing ratio pump 21 outputs hypotonic saline. The human intestinal flora oxidation, antioxidant reconstruction technology and oxidation, antioxidant fecal microbiota transplantation technology can improve the human intestinal flora reconstruction effect and the treatment prospect of fecal microbiota transplantation, improve the human immune level, and treat various diseases caused by intestinal flora imbalance and unhealthy conditions, such as some chronic diseases, difficult diseases and rare diseases.

[0071] Continue to refer Figure 4The oxidation and antioxidant gynecological treatment equipment in the oxidation and antioxidant medical system has a structural composition that is basically the same as the oxidation and antioxidant intestinal flora reconstruction and fecal microbiota transplantation equipment, except that the intestinal special treatment flushing head 27 is changed into a gynecological special treatment flushing head, and the intestinal special probiotic liquid barrel 25 is changed into a gynecological special probiotic liquid barrel, which contains gynecological special probiotic liquid, and the fecal microbiota transplantation liquid barrel 26 is changed into a gynecological special medicine liquid barrel, which contains gynecological special medicine liquid. The usage method is also basically the same, except that the last infusion is the gynecological special probiotic liquid, or the treatment is terminated without the final infusion process.

[0072] refer to Figure 5 and Figure 6 The oxidation and antioxidant burn infiltration treatment equipment in the oxidation and antioxidant medical system includes: a patient infiltration tank 28, an LED immersion ultraviolet sterilization lamp 29, a hydrogen nano aeration device 30, a medical ultrapure hydrogen source 31, a heating and insulation device 32, an ozone concentration probe 33, a waste liquid buffer box 34, a drain solenoid valve 35, a manual drain valve 36 and a physiological saline concentration conductivity probe 38.

[0073] The patient infiltration water tank 28 introduces hydrogen-rich dialysis saline and ozone dialysis saline output by the oxidation and antioxidant saline production device.

[0074] The LED immersion ultraviolet sterilization lamp 29 is distributed under the lower part and side liquid surface of the patient infiltration tank 28, the hydrogen nano aeration device 30 is distributed at the bottom of the two longitudinal sides of the patient infiltration tank 28, and the medical ultrapure hydrogen source 31 is connected to each hydrogen nano aeration device 30; the heating and insulation device 32 is arranged at the outer bottom of the patient infiltration tank 28; the ozone concentration probe 33 is arranged at the inner bottom of the patient infiltration tank 28, the physiological saline concentration conductivity probe 38 is arranged at the inner bottom of the patient infiltration tank 28, and the waste liquid buffer tank 34 is arranged on the lower movable bracket of the patient infiltration tank 28; the drainage solenoid valve 35 is arranged at the bottom of the patient infiltration tank 28, and the drainage solenoid valve 35 leads to the waste liquid buffer tank 34; a manual drainage valve 36 is arranged between the bottom of the patient infiltration tank 28 and the waste liquid buffer tank 34; another manual drainage valve 36 is arranged at the bottom of the waste liquid buffer tank 34.

[0075] When the oxidation and anti-oxidation burn and scald infiltration treatment equipment is in operation, the severely burned and scalded patient lies flat in the patient infiltration tank 28, and first injects high-concentration hypotonic hydrogen-rich dialysis saline at about 35°C to infiltrate the patient. According to the patient's infection situation, high-concentration hypotonic ozone dialysis saline is injected to control the patient's bacterial infection. If you want to quickly eliminate ozone, you can turn on the LED immersion ultraviolet sterilization lamp 29 to maintain the hydrogen concentration of the hypotonic saline in the patient's infiltration tank 28. You can turn on the medical ultrapure hydrogen source 31 and connect it to the patient through a hose. A hydrogen nano-aeration device 30 is connected to generate hydrogen micro-nano bubbles at the bottom of both sides of the patient infiltration tank 28. When the hypotonic saline in the patient infiltration tank 28 needs to be updated, the drain solenoid valve 35 is opened to drain the waste liquid while controlling the injection of new corresponding dialysis saline and maintaining a certain liquid level. After the treatment is completed and the patient infiltration tank 28 is cleaned and disinfected, the manual drain valve 36 can be opened to empty the patient infiltration tank 28. The waste liquid buffer tank 34 plays the role of temporarily storing the waste liquid, which can be directly discharged into the sewer if conditions permit.

[0076] Oxidation and anti-oxidation burn infiltration treatment equipment is suitable for patients with severe and large-area burns and scalds to get through the critical period. It uses the powerful biological effects of hypotonic high-concentration hydrogen-rich dialysis saline and hypotonic high-concentration ozone dialysis saline to control large-area infection, facilitate burn and scald healing, patient recovery, and reduce mortality.

[0077] refer to Figure 7 The oxidation and anti-oxidation hemodialysis treatment equipment includes: a hydrogen-rich hemodialysis water outlet valve 11, an ozone hemodialysis water outlet valve 12, an ozone hemodialysis water inlet electromagnetic valve 17, a metering pump 19, a one-way valve 14 and a hemodialysis machine.

[0078] The hydrogen-rich dialysis water outlet valve 11 is connected to the inlet of the hemodialysis machine through a one-way valve 14; the ozone dialysis water outlet valve 12 is connected to the metering pump 19 through the ozone dialysis water inlet solenoid valve 17, and then connected to the inlet of the hemodialysis machine through the one-way valve 14.

[0079] When performing oxidation and antioxidant hemodialysis, the hydrogen-rich hemodialysis water outlet valve 11 and the ozone hemodialysis water outlet valve 12 are in the open state, and the ozone hemodialysis water inlet electromagnetic valve 17 is in the closed state. Hemodialysis is first performed with high-concentration hydrogen-rich hemodialysis water for a certain period of time, and then the ozone hemodialysis water inlet electromagnetic valve 17 and the metering pump 19 are controlled to open, so that a trace amount of ozone is mixed into the hydrogen-rich hemodialysis water for hemodialysis. Depending on the situation, the hemodialysis can be performed to the end, or the ozone hemodialysis water inlet electromagnetic valve 17 and the metering pump 19 can be closed halfway and the hydrogen-rich hemodialysis water is used until the end of the hemodialysis. A capillary can also be used instead of the metering pump 19, the purpose of which is to mix a trace amount of ozone hemodialysis water into the hydrogen-rich hemodialysis water.

[0080] In the above oxidation and antioxidant hemodialysis treatment equipment, hydrogen-rich water has weak reducing properties and selective antioxidant effects, and ozone water has strong oxidizing properties and is a strong bactericidal disinfectant. However, the temperature for the reaction between ozone and hydrogen must reach above 200°C, and the ozone dialysis water and hydrogen-rich dialysis water are mixed with each other. No redox reaction will occur at room temperature, and each plays its own role. The hydrogen-rich dialysis water used for hemodialysis is mixed with a trace amount of ozone dialysis water so that the ozone content is 0-80µg / ml. After mixing, it is supplied to the hemodialysis machine and can be used for the treatment of systemic bacterial and viral infections in the human body, such as hepatitis, HIV, leprosy, and sepsis.

[0081] During treatment, the patient can first use hydrogen-rich dialysis water for dialysis for a certain period of time, and then mix in a small amount of ozone dialysis water for hemodialysis treatment until the end. The mixing of ozone dialysis water can also be disconnected midway, and the dialysis can be continued with hydrogen-rich dialysis water until the end. Alternatively, only hydrogen-rich dialysis water can be used for treatment from beginning to end.

[0082] This application utilizes the strong oxidative sterilization and oxygenation effects of ozone water, as well as the safety, permeability and selective antioxidant effects of hydrogen-rich water, and is comprehensively applied to the treatment of human diseases, cleaning of difficult-to-heal tissues, treatment of gangrene, skin infections caused by fungi and bacteria, treatment of skin diseases, infiltration rehabilitation treatment of burns and scalds, cleaning of trauma, cleaning and disinfection of battlefield rescue wounds, and treatment of oral inflammation. It has a positive impact on human health through oxidation, antioxidant intestinal flora reconstruction and fecal bacteria transplantation, and can be used for the treatment and rehabilitation of chronic diseases, difficult diseases and rare diseases in the human body.

[0083] The above are only some embodiments of the present application. The protection scope of the present application is not limited to the above embodiments. For ordinary technicians in this technical field, several improvements and modifications without departing from the creative design of the present application should also fall within the protection scope of the present application.

Claims

1. Oxidation and antioxidant medical system, characterized in that: It comprises ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment; the ozone and hydrogen-rich hemodialysis treatment water generation and supply equipment comprises a hydrogen-rich cathode sanitary pure water tank (1), an ozone anode sanitary pure water tank (2), a dedicated electrolyzer (3), a hydrogen-rich cathode dissolved gas cutting pump (4-1), an ozone anode dissolved gas cutting pump (4-2), a hydrogen-rich dialysis water supply dedicated pipeline (5) and an ozone dialysis water supply dedicated pipeline (6); The water outlet of the hydrogen-rich cathode sanitary pure water tank (1) is connected to the lower inlet of the cathode side (301) of the dedicated electrolyzer (3), and the water outlet of the hydrogen-rich cathode sanitary pure water tank (1) is also connected to the water inlet of the hydrogen-rich cathode dissolved gas cutting pump (4-1); the upper outlet of the cathode side (301) of the dedicated electrolyzer (3) is connected to the negative pressure port of the hydrogen-rich cathode dissolved gas cutting pump (4-1); the water outlet of the hydrogen-rich cathode dissolved gas cutting pump (4-1) is connected to the dedicated pipeline (5) for supplying hydrogen-rich dialysis water, and the dedicated pipeline (5) for supplying hydrogen-rich dialysis water is connected to the water outlet of the hydrogen-rich cathode sanitary pure water tank (1) to form a closed loop; The water outlet of the ozone anode sanitary pure water tank (2) is connected to the lower inlet of the anode side (302) of the dedicated electrolytic cell (3), and the water outlet of the ozone anode sanitary pure water tank (2) is also connected to the water inlet of the ozone anode dissolved gas cutting pump (4-2); the upper outlet of the anode side (302) of the dedicated electrolytic cell (3) is connected to the negative pressure port of the ozone anode dissolved gas cutting pump (4-2), and the water outlet of the ozone anode dissolved gas cutting pump (4-2) is connected to the dedicated water supply pipeline (6) for ozone dialysis water, and the dedicated water supply pipeline (6) for ozone dialysis water is connected to the water outlet of the ozone anode sanitary pure water tank (2) to form a closed loop; A mixed product of hydrogen bubbles and dialysis water is generated in the water path on the cathode side (301) of the dedicated electrolytic cell (3), and the hydrogen bubbles are broken up by a hydrogen-rich cathode dissolved gas cutting pump (4-1) and dissolved into the dialysis water to generate hydrogen-rich dialysis water. A mixed product of oxygen and ozone bubbles and dialysis water is generated in the water path on the anode side (302) of the dedicated electrolytic cell (3), and the oxygen and ozone bubbles are broken up by an ozone anode dissolved gas cutting pump (4-2) and dissolved into the dialysis water to generate ozone dialysis water.

2. The oxidation and antioxidant medical system according to claim 1, characterized in that: An online ultrasonic dissolved gas probe (7) and a flow-through ultraviolet lamp (8) are installed on the dedicated hydrogen-rich dialysis water supply pipeline (5); another online ultrasonic dissolved gas probe (7) is installed on the dedicated ozone dialysis water supply pipeline (6).

3. The oxidation and antioxidant medical system according to claim 1, characterized in that: The oxidation and antioxidant medical system includes one of the following groups of medical equipment: oxidation and antioxidant physiological saline generation equipment, oxidation and antioxidant intestinal flora reconstruction and fecal bacteria transplantation equipment, oxidation and antioxidant gynecological treatment equipment, oxidation and antioxidant burn and scald infiltration treatment equipment, oxidation and antioxidant hemodialysis treatment equipment; The oxidation and antioxidant saline generation equipment is connected to the hydrogen-rich dialysis water supply pipeline (5) and the ozone dialysis water supply pipeline (6); the oxidation and antioxidant intestinal flora reconstruction and fecal microbiota transplantation equipment is connected to the hydrogen-rich dialysis water supply pipeline (5) and the ozone dialysis water supply pipeline (6); the oxidation and antioxidant gynecological treatment equipment is connected to the hydrogen-rich dialysis water supply pipeline (5) and the ozone dialysis water supply pipeline (6); the oxidation and antioxidant hemodialysis treatment equipment is connected to the hydrogen-rich dialysis water supply pipeline (5) and the ozone dialysis water supply pipeline (6); The oxidation and antioxidant saline generation equipment outputs hydrogen-rich dialysis saline and ozone dialysis saline; the oxidation and antioxidant burn and scald infiltration treatment equipment introduces the hydrogen-rich dialysis saline and ozone dialysis saline output by the oxidation and antioxidant saline generation equipment.

4. The oxidation and antioxidant medical system according to claim 3, characterized in that: A first structure of the oxidation and antioxidant saline production device is that the oxidation and antioxidant saline production device comprises a hydrogen-rich dialysis water inlet solenoid valve (13), a plurality of one-way valves (14), a hydrogen-rich dialysis water proportional pump (15), a plurality of saline concentration conductivity probes and display instruments (16), an ozone dialysis water inlet solenoid valve (17), an ozone dialysis water proportional pump (18), and a supersaturated concentrated saline supply device (20); The hydrogen-rich dialysis water supply dedicated pipeline (5) is connected to the hydrogen-rich dialysis water inlet electromagnetic valve (13), and the hydrogen-rich dialysis water inlet electromagnetic valve (13) is connected to the hydrogen-rich dialysis water proportional pump (15) through a one-way valve (14), and the salt intake port of the hydrogen-rich dialysis water proportional pump (15) is connected to the supersaturated concentrated salt water supply device (20) through a hose, and the outlet of the hydrogen-rich dialysis water proportional pump (15) outputs hydrogen-rich dialysis saline through a saline concentration conductivity probe and display instrument (16); The ozone dialysis water supply dedicated pipeline (6) is connected to the ozone dialysis water inlet electromagnetic valve (17), and the ozone dialysis water inlet electromagnetic valve (17) is connected to the ozone dialysis water proportional pump (18) through another one-way valve (14), and the salt intake port of the ozone dialysis water proportional pump (18) is connected to the supersaturated concentrated salt water supply device (20) through a hose, and the outlet of the ozone dialysis water proportional pump (18) outputs ozone dialysis saline through another saline concentration conductivity probe and display instrument (16).

5. The oxidation and antioxidant medical system according to claim 3, characterized in that: The second structure of the oxidation and anti-oxidation saline production equipment is that the oxidation and anti-oxidation saline production equipment includes a hydrogen-rich dialysis saline output pipeline and an ozone dialysis saline output pipeline; The hydrogen-rich dialysis water supply dedicated pipeline (5) is connected to the hydrogen-rich dialysis saline output pipeline; the hydrogen-rich dialysis saline output pipeline is sequentially installed with a hydrogen-rich dialysis water inlet solenoid valve (13), a one-way valve (14), a hydrogen-rich dialysis water proportional pump (15) and a saline concentration conductivity probe and display instrument (16) along the water flow direction; the salt intake port of the hydrogen-rich dialysis water proportional pump (15) is connected to the supersaturated concentrated salt water supply device (20) through a one-way valve (14) and a metering pump (19); the outlet of the hydrogen-rich dialysis water proportional pump (15) outputs the hydrogen-rich dialysis saline through the saline concentration conductivity probe and display instrument (16); The ozone dialysis water supply dedicated pipeline (6) is connected to the ozone dialysis saline output pipeline; the ozone dialysis saline output pipeline is sequentially installed with an ozone dialysis water inlet solenoid valve (17), a one-way valve (14), an ozone dialysis water proportional pump (18) and a saline concentration conductivity probe and display instrument (16) along the water flow direction; the ozone dialysis water proportional pump (18) is connected to the supersaturated concentrated brine supply device (20) through a one-way valve (14) and a metering pump (19); the ozone dialysis water proportional pump (18) outputs ozone dialysis saline through the saline concentration conductivity probe and display instrument (16); The oxidation and antioxidant saline production device further comprises a connecting pipeline; the two ends of the connecting pipeline are respectively connected to the inlet of the hydrogen-rich dialysis water proportional pump (15) of the hydrogen-rich dialysis saline output pipeline and the inlet of the ozone dialysis water inlet solenoid valve (17) of the ozone dialysis saline output pipeline; another ozone dialysis water inlet solenoid valve (17), another metering pump (19) and another one-way valve (14) are installed on the connecting pipeline; the one-way valve (14) on the connecting pipeline allows water to flow to the inlet of the hydrogen-rich dialysis water proportional pump (15).

6. The oxidation and antioxidant medical system according to claim 3, characterized in that: The oxidation, antioxidant intestinal flora reconstruction and fecal bacteria transplantation equipment includes: a hydrogen-rich path, an ozone path, a mixed path, a salt path, an intestinal bacteria path and a fecal bacteria path; The mixing line is sequentially equipped with an ozone hydrogen-rich dialysis water mixing ratio pump (21), a physiological saline concentration conductivity probe and display instrument (16), a pressure controller (23), a pressure gauge (9), a one-way valve (14) and a special intestinal treatment flushing head (27); The front end of the hydrogen-enriched circuit is connected to the dedicated hydrogen-enriched dialysis water supply pipeline (5), and the rear end is connected to the ozone hydrogen-enriched dialysis water mixing ratio pump (21) of the mixing circuit. The hydrogen-enriched circuit is equipped with a hydrogen-enriched dialysis water inlet solenoid valve (13) and a one-way valve (14); The front end of the ozone path is connected to the ozone dialysis water supply dedicated pipeline (6), and the rear end is bifurcated into two branches connected to the ozone hydrogen-rich dialysis water mixing ratio pump (21) of the mixing path; one branch of the ozone path is sequentially installed with an ozone dialysis water inlet solenoid valve (17), a metering pump (19) and a one-way valve (14), and the other branch is sequentially installed with an ozone dialysis water inlet solenoid valve (17) and a one-way valve (14); The salt line is sequentially installed with a supersaturated concentrated brine supply device (20), a metering pump (19), a one-way valve (14) and a salt absorption solenoid valve (22), and the salt absorption solenoid valve (22) is connected to the salt absorption port of the ozone hydrogen-enriched dialysis water mixing proportion pump (21) in the mixing line; The intestinal bacteria path is sequentially equipped with an intestinal probiotic liquid barrel (25), a peristaltic pump (24) and a one-way valve (14); the one-way valve (14) of the intestinal bacteria path is connected to a special intestinal treatment flushing head (27); The fecal bacteria path is sequentially equipped with a fecal bacteria transplantation liquid barrel (26), a peristaltic pump (24), and a one-way valve (14); the one-way valve (14) of the fecal bacteria path is connected to a special intestinal treatment flushing head (27).

7. The oxidation and antioxidant medical system according to claim 3, characterized in that: The oxidation and anti-oxidation burn and scald infiltration treatment equipment comprises: a patient infiltration water tank (28), an LED immersion ultraviolet sterilization lamp (29), a hydrogen nano-aeration device (30), a medical ultrapure hydrogen source (31), a heating and heat preservation device (32), an ozone concentration probe (33), a waste liquid buffer tank (34), a drain solenoid valve (35), a manual drain valve (36) and a physiological saline concentration conductivity probe (38); The patient infiltration water tank (28) is introduced with hydrogen-rich dialysis saline and ozone dialysis saline output by the oxidation and antioxidant saline generation device; the LED immersion ultraviolet sterilization lamp (29) is distributed below the liquid surface at the bottom and side of the patient infiltration water tank (28); the hydrogen nano-aeration device (30) is distributed at the bottom of both sides of the patient infiltration water tank (28); the medical ultrapure hydrogen source (31) is connected to each hydrogen nano-aeration device (30); the heating and heat preservation device (32) is arranged at the outer bottom of the patient infiltration water tank (28); the ozone concentration probe (33) is arranged at the patient The patient infiltration tank (28) is provided at the bottom of the interior of the patient infiltration tank (28); the physiological saline concentration conductivity probe (38) is provided at the bottom of the interior of the patient infiltration tank (28); the waste liquid buffer tank (34) is provided on a lower movable bracket of the patient infiltration tank (28); a liquid discharge solenoid valve (35) is provided at the bottom of the patient infiltration tank (28); the liquid discharge solenoid valve (35) leads to the waste liquid buffer tank (34); a manual liquid discharge valve (36) is provided between the bottom of the patient infiltration tank (28) and the waste liquid buffer tank (34); and another manual liquid discharge valve (36) is provided at the bottom of the waste liquid buffer tank (34).

8. The oxidation and antioxidant medical system according to claim 3, characterized in that: The oxidation and anti-oxidation hemodialysis treatment equipment comprises: a hydrogen-rich hemodialysis water outlet valve (11), an ozone hemodialysis water outlet valve (12), an ozone hemodialysis water inlet solenoid valve (17), a metering pump (19), a one-way valve (14) and a hemodialysis machine; The hydrogen-rich dialysis water outlet valve (11) is connected to the inlet of the hemodialysis machine through a one-way valve (14); the ozone dialysis water outlet valve (12) is connected to the metering pump (19) through the ozone dialysis water inlet solenoid valve (17), and then connected to the inlet of the hemodialysis machine through the one-way valve (14).

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