CN108315755A - A kind of hydrogen-rich cup - Google Patents
A kind of hydrogen-rich cup Download PDFInfo
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- CN108315755A CN108315755A CN201810159115.3A CN201810159115A CN108315755A CN 108315755 A CN108315755 A CN 108315755A CN 201810159115 A CN201810159115 A CN 201810159115A CN 108315755 A CN108315755 A CN 108315755A
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 108
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 108
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 99
- 239000001301 oxygen Substances 0.000 claims abstract description 147
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 147
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 123
- 238000000926 separation method Methods 0.000 claims abstract description 98
- 239000012528 membrane Substances 0.000 claims abstract description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 51
- 150000002431 hydrogen Chemical class 0.000 claims abstract description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 40
- 238000005070 sampling Methods 0.000 claims description 19
- 238000001514 detection method Methods 0.000 claims description 18
- 229920001296 polysiloxane Polymers 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 16
- 238000007599 discharging Methods 0.000 claims description 14
- 238000003860 storage Methods 0.000 claims description 9
- 230000003020 moisturizing effect Effects 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000000741 silica gel Substances 0.000 claims description 6
- 229910002027 silica gel Inorganic materials 0.000 claims description 6
- 230000005611 electricity Effects 0.000 claims 4
- 241000628997 Flos Species 0.000 claims 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims 2
- 229910052710 silicon Inorganic materials 0.000 claims 2
- 239000010703 silicon Substances 0.000 claims 2
- 229960001866 silicon dioxide Drugs 0.000 claims 2
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 239000007787 solid Substances 0.000 claims 1
- 241000190070 Sarracenia purpurea Species 0.000 abstract description 18
- 238000005063 solubilization Methods 0.000 abstract description 17
- 230000007928 solubilization Effects 0.000 abstract description 17
- 230000003381 solubilizing effect Effects 0.000 abstract description 6
- 238000007789 sealing Methods 0.000 description 16
- 238000010586 diagram Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 238000009423 ventilation Methods 0.000 description 5
- 238000004880 explosion Methods 0.000 description 4
- -1 hydroxyl radicals Chemical class 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000009434 installation Methods 0.000 description 3
- 150000003254 radicals Chemical class 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 230000004308 accommodation Effects 0.000 description 2
- 230000035622 drinking Effects 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000004792 oxidative damage Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 208000017667 Chronic Disease Diseases 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004590 computer program Methods 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000006806 disease prevention Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000001225 therapeutic effect Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000010023 transfer printing Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
- C25B9/73—Assemblies comprising two or more cells of the filter-press type
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/02—Process control or regulation
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Automation & Control Theory (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
本发明公开了富氢水杯,包括控压增溶杯盖,杯体和氢氧分离电解系统,杯体杯口设置杯盖接口,控压增溶杯盖与杯体通过杯盖接口可拆卸连接,控压增溶杯盖上设有透气孔,透气孔中设置有隔水透气膜,氢氧分离电解系统设置在杯体底部。本发明的富氢水杯通过控压增溶杯盖,可以实现杯体保持在一定的压力下,增加氢气溶解到水中的浓度,同时控制杯体的压力不会太大造成危险。
The invention discloses a hydrogen-rich water cup, which comprises a pressure-controlled solubilizing cup cover, a cup body and a hydrogen-oxygen separation electrolysis system. , The lid of the pressure-controlled solubilization cup is provided with air holes, and a water-proof and breathable membrane is arranged in the air holes, and the hydrogen-oxygen separation electrolysis system is arranged at the bottom of the cup body. The hydrogen-rich water cup of the present invention can maintain the cup body under a certain pressure through the pressure-controlled solubilizing cup cover to increase the concentration of hydrogen dissolved in water, and at the same time control the pressure of the cup body so that it will not be too high to cause danger.
Description
技术领域technical field
本发明涉及电解技术领域,尤其涉及可以制作富氢水的富氢水杯。The invention relates to the technical field of electrolysis, in particular to a hydrogen-rich water cup capable of producing hydrogen-rich water.
背景技术Background technique
科学研究证明,人体几乎所有慢性疾病均与自由基氧化损伤有密切关系。自2007年日本太田成男教授发表权威论文,证实氢气具有选择性中和羟自由基以及亚硝酸阴离子等有毒有害自由基,从而发挥选择性抗氧化作用以来,氢医学在健康产业中迅速发展。随着生活质量的提供,人们对自身的健康更加关注。Scientific research has proved that almost all chronic diseases in the human body are closely related to free radical oxidative damage. Since the authoritative paper published by Professor Shigeo Ota in Japan in 2007, proving that hydrogen can selectively neutralize toxic and harmful free radicals such as hydroxyl radicals and nitrite anions, thereby exerting a selective antioxidant effect, hydrogen medicine has developed rapidly in the health industry. With the provision of quality of life, people pay more attention to their own health.
人体摄取氢气的主要方式有饮用富氢水、注射氢生理盐水、直接吸入氢气等,其中氢应用最早的富氢水领域。目前市面的产品主要为富氢水杯,它是通过氢气溶存于水中,通过直接饮用获取氢气。该方式比较方便,但是常温常压下氢气在水中溶存度很低,一般为0.5-0.8ppm(质量浓度为百万分之零点五至百万分之零点八),要发挥其治疗效果,需要饮用大量的氢气水。The main ways for the human body to absorb hydrogen include drinking hydrogen-rich water, injecting hydrogen saline, and inhaling hydrogen directly. Among them, the earliest application of hydrogen is in the field of hydrogen-rich water. The current products on the market are mainly hydrogen-rich water cups, which dissolve hydrogen in water and obtain hydrogen by drinking directly. This method is more convenient, but the solubility of hydrogen in water at normal temperature and pressure is very low, generally 0.5-0.8ppm (mass concentration is 0.5-0.8ppm), and its therapeutic effect must be exerted. , Need to drink a lot of hydrogen water.
现有技术提供的富氢水杯,要么不提供对水杯中的水增压,使得溶于水中的氢气有限,同时造成了大部分生成的氢气散发到空气中,造成浪费。要么虽然提供了增压设备,但是没有合适的释压机制,使得杯体的压力越来越大,容易产生危险。The hydrogen-rich water cup provided by the prior art either does not provide pressurization of the water in the water cup, so that the hydrogen dissolved in the water is limited, and at the same time, most of the generated hydrogen is emitted into the air, resulting in waste. Or although a pressurization device is provided, there is no suitable pressure release mechanism, so that the pressure of the cup is increasing, which is prone to danger.
发明内容Contents of the invention
针对现有富氢水杯的问题,本发明实施例提供富氢水杯,可以增加水的一定压力,使氢气在水中的浓度得到极大提高。同时在压力超过一定值时,氢气可以从杯子排出,避免杯中压力太大造成危险。Aiming at the problems of the existing hydrogen-rich water cup, the embodiment of the present invention provides a hydrogen-rich water cup, which can increase a certain pressure of the water and greatly increase the concentration of hydrogen in the water. At the same time, when the pressure exceeds a certain value, hydrogen can be discharged from the cup to avoid danger caused by too much pressure in the cup.
本发明实施例提供的一种富氢水杯,包括控压增溶杯盖,杯体和氢氧分离电解系统,杯体杯口设置杯盖接口,控压增溶杯盖与杯体通过杯盖接口可拆卸连接,控压增溶杯盖上设有透气孔,透气孔中设置有隔水透气膜,氢氧分离电解系统设置在杯体底部。A hydrogen-rich water cup provided by an embodiment of the present invention includes a pressure-controlled solubilization cup cover, a cup body and a hydrogen-oxygen separation electrolysis system, the cup mouth is provided with a cup cover interface, and the pressure-controlled solubilization cup cover and the cup body pass through the cup cover The interface can be detachably connected, and the cover of the pressure-controlled solubilization cup is provided with a vent hole, and a water-proof and breathable membrane is arranged in the vent hole, and the hydrogen-oxygen separation electrolysis system is arranged at the bottom of the cup body.
本发明实施例提供的富氢水杯,通过提供控压增溶杯盖,控压增溶杯盖中设置通气孔,同时在透气孔中设置隔水透气膜。隔水透气膜的特点是只有在压力超过0.1MPa时,气体才会从隔水透气膜中排出,而且不会漏水。在压力不足 0.1MPa时,气体不能排出,从而保证了杯体内的工作压力始终维持在接近 0.1MPa。这既可以通过压力充分增加氢在水中的溶解度,提高单位工作时间内富氢水浓度,又可以稳定维持杯体内的压力,确保了杯子的使用安全。从而避免了氢氧混合可能发生爆炸、压力过大容器漏水或爆炸的危险,以及压力过低单位时间内富氢水浓度过低的不足。本发明提供的富氢水杯,没有复杂的电子或者控制结构,设备简单,组装实现工艺简单,工作稳定可靠。The hydrogen-rich water cup provided by the embodiment of the present invention provides a pressure-controlled solubilization cup cover, and a vent hole is provided in the pressure-controlled solubilization cup cover, and a water-proof and breathable film is provided in the vent hole. The characteristic of the water-proof and breathable membrane is that only when the pressure exceeds 0.1MPa, the gas will be discharged from the water-proof and breathable membrane, and there will be no water leakage. When the pressure is less than 0.1MPa, the gas cannot be discharged, thus ensuring that the working pressure in the cup is always maintained close to 0.1MPa. This can not only fully increase the solubility of hydrogen in water through pressure, increase the concentration of hydrogen-rich water per unit working time, but also maintain the pressure in the cup stably, ensuring the safety of the cup. This avoids the risk of hydrogen-oxygen mixture explosion, water leakage or explosion in the container with too high pressure, and the problem of too low concentration of hydrogen-rich water per unit time when the pressure is too low. The hydrogen-rich water cup provided by the present invention has no complicated electronic or control structure, simple equipment, simple assembly and realization process, and stable and reliable operation.
优选地,控压增溶杯盖包括上盖和下盖,上盖和下盖相对应位置均设置有透气孔,隔水透气膜设置在所述上盖、下盖之间,并与透气孔对应设置,下盖固定在上盖底面。Preferably, the pressure control solubilization cup cover includes an upper cover and a lower cover, and the corresponding positions of the upper cover and the lower cover are provided with vent holes, and the water-proof and breathable film is arranged between the upper cover and the lower cover, and is connected with the vent holes. Corresponding to the setting, the lower cover is fixed on the bottom surface of the upper cover.
优选地,上盖包括透气孔外柱,下盖包括透气孔内柱,隔水透气膜紧密贴合在透气孔内柱的气孔上,透气孔内柱插入透气孔外柱。Preferably, the upper cover includes an outer post of the vent hole, the lower cover includes an inner post of the vent hole, the water-proof and breathable membrane is closely attached to the air hole of the inner post of the vent hole, and the inner post of the vent hole is inserted into the outer post of the vent hole.
优选地,控压增溶杯盖还包括第四密封硅胶圈,第四密封硅胶圈中间设置有通孔,第四密封硅胶圈通过通孔嵌套在下盖上。Preferably, the pressure control solubilization cup cover further includes a fourth sealing silicone ring, a through hole is provided in the middle of the fourth sealing silicone ring, and the fourth sealing silicone ring is nested on the lower cover through the through hole.
优选地,氢氧分离电解系统包括氢氧分离电解装置和氢氧分离电解装置控制系统;氢氧分离电解装置控制系统设置在所述氢氧分离电解装置的底部并与下固定板密封连接。Preferably, the hydrogen-oxygen separation electrolysis system includes a hydrogen-oxygen separation electrolysis device and a hydrogen-oxygen separation electrolysis device control system; the hydrogen-oxygen separation electrolysis device control system is arranged at the bottom of the hydrogen-oxygen separation electrolysis device and is sealingly connected with the lower fixing plate.
氢氧分离电解装置,包括电解发生器、上固定板和下固定板,电解发生器包括阴极片、阳极片、选择性质子透过膜,阴极片设置阴极接线端,阴极接线端外接电源负极,阳极片设置阳极接线端,阳极接线端外接电源正极,下固定板上设置电极孔,阳极接线端和阴极接线端穿过电极孔,上固定板的底面和所述下固定板的顶面设置与阴极片、选择性质子透过膜、阳极片形状匹配的容置空腔,下固定板与上固定板可拆卸连接,阴极片、选择性质子透过膜、阳极片固定在上固定板和下固定板之间的容置空腔内,阴极片与选择性质子透过膜之间形成氢气生成区,阳极片和选择性质子透过膜之间形成氧气生成区,氢气生成区设置氢气排放口供氢气排出氢气生成区和水进入氢气生成区,氧气生成区设置氧气排放口供氧气排出氧气生成区。The hydrogen-oxygen separation electrolysis device includes an electrolytic generator, an upper fixed plate and a lower fixed plate. The electrolytic generator includes a cathode sheet, an anode sheet, and a selective proton permeable membrane. The anode sheet is provided with an anode terminal, the anode terminal is externally connected to the positive pole of the power supply, an electrode hole is arranged on the lower fixed plate, the anode terminal and the cathode terminal pass through the electrode hole, the bottom surface of the upper fixed plate and the top surface of the lower fixed plate are arranged with The cathode sheet, the selective proton permeable membrane, and the anode sheet have matching cavity in shape, the lower fixed plate is detachably connected to the upper fixed plate, and the cathode sheet, the selective proton permeable membrane, and the anode sheet are fixed on the upper fixed plate and the lower fixed plate. In the accommodation cavity between the fixed plates, a hydrogen generation area is formed between the cathode sheet and the selective proton permeable membrane, an oxygen generation area is formed between the anode sheet and the selective proton permeable membrane, and a hydrogen gas discharge port is set in the hydrogen generation area for Hydrogen gas exits the hydrogen generation area and water enters the hydrogen generation area, and an oxygen discharge port is provided in the oxygen generation area for oxygen to exit the oxygen generation area.
优选地,氢氧分离电解装置还包括电板旋盖,下固定板对应电解发生器区域设置通孔,电板旋盖设置在通孔内,电板旋盖可沿所述通孔上下移动。Preferably, the hydrogen-oxygen separation electrolysis device further includes an electric plate screw cover, the lower fixing plate is provided with a through hole corresponding to the area of the electrolysis generator, the electric plate screw cover is arranged in the through hole, and the electric plate screw cover can move up and down along the through hole.
优选地,阴极片和阳极片上设置多个透气孔。Preferably, a plurality of ventilation holes are provided on the cathode sheet and the anode sheet.
优选地,阴极片、阳极片、选择性质子透过膜、上固定板和下固定板均设置为大小匹配的圆形,阴极片、选择性质子透过膜、阳极片按从上到下的顺序固定在上固定板和下固定板之间,氧气排放口设置在下固定板上,阳极片、选择性质子透过膜和下固定板之间密封连接。Preferably, the cathode sheet, the anode sheet, the selective proton permeable membrane, the upper fixed plate and the lower fixed plate are all arranged in a circular shape with matching sizes, and the cathode sheet, the selective proton permeable membrane, and the anode sheet are arranged in a top-to-bottom order. They are sequentially fixed between the upper fixing plate and the lower fixing plate, the oxygen discharge port is arranged on the lower fixing plate, and the anode sheet, the selective proton permeable membrane and the lower fixing plate are sealed and connected.
优选地,选择性质子透过膜为自增湿型质子透过膜。Preferably, the selective proton permeable membrane is a self-humidifying proton permeable membrane.
优选地,还包括保湿硅胶垫,所述保湿硅胶垫可拆卸地设置在氢氧分离电解装置上。Preferably, it also includes a moisturizing silica gel pad, which is detachably arranged on the hydrogen-oxygen separation electrolysis device.
优选地,氢氧分离电解装置控制系统,包括微处理器、存储器、自动调压模块和开关电路,微处理器分别连接存储器、自动调压模块和开关电路,自动调压模块电源输入端外接电源,自动调压模块电源输出端正极外接氢氧分离电解装置的阳极,自动调压模块电源输出端负极外接氢氧分离电解装置的阴极;Preferably, the hydrogen-oxygen separation electrolysis device control system includes a microprocessor, a memory, an automatic voltage regulation module and a switch circuit, the microprocessor is respectively connected to the memory, the automatic voltage regulation module and the switch circuit, and the power supply input end of the automatic voltage regulation module is connected to an external power supply , the positive pole of the power output terminal of the automatic voltage regulation module is externally connected to the anode of the hydrogen-oxygen separation electrolysis device, and the negative pole of the power output terminal of the automatic voltage regulation module is externally connected to the cathode of the hydrogen-oxygen separation electrolysis device;
存储器存储有根据氢氧分离电解装置工作电压预设的开机电压检测值,控制电压步进值和计算机可执行程序,微处理器读取存储器中的计算机可执行程序并实现以下控制方法:The memory stores the start-up voltage detection value preset according to the operating voltage of the hydrogen-oxygen separation electrolysis device, the control voltage step value and the computer executable program. The microprocessor reads the computer executable program in the memory and implements the following control methods:
开机电压检测步骤:检测外接电源的电源电压,若所述电源电压低于开机电压检测值,停止工作并提示电压不足,否则,执行下一步骤;Start-up voltage detection step: detect the power supply voltage of the external power supply, if the power supply voltage is lower than the start-up voltage detection value, stop working and prompt that the voltage is insufficient, otherwise, go to the next step;
自动升压步骤:控制自动调压模块以预设的控制电压步进值逐步提高输入至氢氧分离电解装置阴极和阳极的电压,直到氢氧分离电解装置阴极和阳极的实际工作电压达到开机电压检测值。Automatic boosting step: control the automatic voltage regulation module to gradually increase the voltage input to the cathode and anode of the hydrogen-oxygen separation electrolysis device with the preset control voltage step value until the actual working voltage of the cathode and anode of the hydrogen-oxygen separation electrolysis device reaches the start-up voltage detection value.
优选地,氢氧分离电解装置控制系统,还包括取样比较电路,取样比较电路输入端分别连接自动调压模块电源输出端正极和负极,取样比较电路输出端连接微处理器,取样比较电路获取氢氧分离电解装置的实际工作电压,并输入至微处理器,微处理器执行计算机可执行程序实现以下控制方法:Preferably, the hydrogen-oxygen separation electrolysis device control system also includes a sampling comparison circuit, the input terminal of the sampling comparison circuit is respectively connected to the positive pole and the negative pole of the output terminal of the automatic voltage regulation module power supply, the output terminal of the sampling comparison circuit is connected to the microprocessor, and the sampling comparison circuit obtains hydrogen The actual working voltage of the oxygen separation electrolysis device is input to the microprocessor, and the microprocessor executes the computer executable program to realize the following control method:
自动调压步骤:比较所述实际工作电压与所述开机电压检测值的大小,如果实际工作电压大于所述开机电压检测值,控制自动调压模块降低输出至氢氧分离电解装置的电压,直至所述实际工作电压等于开机电压检测值,如果实际工作电压小于开机电压检测值,控制自动调压模块升高输出至氢氧分离电解装置的电压,直至实际工作电压等于开机电压检测值。Automatic voltage regulation step: compare the actual working voltage with the detected value of the start-up voltage, if the actual working voltage is greater than the detected value of the start-up voltage, control the automatic voltage regulation module to reduce the voltage output to the hydrogen-oxygen separation electrolysis device until The actual working voltage is equal to the detection value of the starting voltage. If the actual working voltage is lower than the detection value of the starting voltage, the automatic voltage regulation module is controlled to increase the voltage output to the hydrogen-oxygen separation electrolysis device until the actual working voltage is equal to the detection value of the starting voltage.
优选地,氢氧分离电解装置控制系统还包括充放电管理模块和蓄电池,自动调压模块通过充放电管理模块外接电源,蓄电池通过充放电管理模块分别连接外接电源和自动调压模块,充放电管理模块在外接电源时,用于根据蓄电池的电容调节充电电压和充电电流;充放电管理模块在蓄电池供电时,用于对蓄电池进行过流或过载保护。Preferably, the hydrogen-oxygen separation electrolysis device control system also includes a charging and discharging management module and a storage battery. When the module is connected to an external power supply, it is used to adjust the charging voltage and charging current according to the capacitance of the battery; when the charging and discharging management module is powered by the battery, it is used to protect the battery from overcurrent or overload.
优选地,氢氧分离电解装置控制系统还包括灯光显示装置,灯光显示装置与微处理器连接,灯光显示装置用于接收微处理器的信号,并显示工作状态,工作状态包括开机检测、自动升压、自动调压或者电源电压不足。Preferably, the hydrogen-oxygen separation electrolysis device control system also includes a light display device, which is connected to the microprocessor, and the light display device is used to receive signals from the microprocessor and display the working status. The working status includes power-on detection, automatic upgrade voltage, automatic voltage regulation, or insufficient power supply voltage.
本发明实施例提供的富氢水杯,通过控压增溶杯盖,可以实现杯体保持在一定的压力下,增加氢气溶解到水中的浓度,同时控制杯体的压力不会太大造成危险。The hydrogen-rich water cup provided by the embodiment of the present invention can keep the cup body under a certain pressure by controlling the pressure-controlled solubilizing cup cover, increase the concentration of hydrogen dissolved in water, and control the pressure of the cup body so that it will not be too high to cause danger.
附图说明Description of drawings
图1为本发明实施例中一种富氢水杯结构示意图;Fig. 1 is a schematic structural diagram of a hydrogen-rich water cup in an embodiment of the present invention;
图2为本发明实施例中控压增溶杯盖结构示意图;Fig. 2 is a schematic diagram of the structure of the pressure-controlled solubilizing cup cover in the embodiment of the present invention;
图3为本发明实施例中氢氧分离电解装置控制系统结构示意图;3 is a schematic structural diagram of the control system of the hydrogen-oxygen separation electrolysis device in the embodiment of the present invention;
图4为本发明实施例中氢氧分离电解装置控制系统优选实施方案结构示意图;Fig. 4 is a schematic structural diagram of a preferred embodiment of the control system of the hydrogen-oxygen separation electrolysis device in the embodiment of the present invention;
图5为本发明实施例中氢氧分离电解装置分解图结构示意图;Fig. 5 is a schematic structural diagram of an exploded view of a hydrogen-oxygen separation electrolysis device in an embodiment of the present invention;
图6为本发明实施例中氢氧分离电解装置组装结构示意图。Fig. 6 is a schematic diagram of the assembly structure of the hydrogen-oxygen separation electrolysis device in the embodiment of the present invention.
附图中:100、氢氧分离电解装置;111、阴极片;1112、阴极接线端;1113、阴极片凸台;112、阳极片;1122、阳极接线端;1123、阳极片凸台;113、选择性质子透过膜;121、下固定板;122、电极孔;131、上固定板;132、固定旋盖;133、电极卡槽;134、容置空腔;135、卡销;141、电板旋盖;142、氧气排放口;151、第一密封硅胶圈;152、第二密封硅胶圈;153、第三密封硅胶圈; 154、第四密封硅胶圈;161、氢气生成区;162、氧气生成区;170、保湿硅胶垫;200、氢氧分离电解装置控制系统;210、微处理器;220、自动调压模块; 230、存储器;240、开关电路;250、取样比较电路;260、充放电管理模块; 270、蓄电池;280、灯光显示装置;290、倾斜感应装置;300、杯体;310、控制底座;400、外接电源;500、控压增溶杯盖;510、上盖;511、透气孔外柱;520、下盖;521、透气孔内柱;530、隔水透气膜。In the drawings: 100, hydrogen and oxygen separation electrolysis device; 111, cathode piece; 1112, cathode terminal; 1113, cathode piece boss; 112, anode piece; 1122, anode terminal; 1123, anode piece boss; 113, Selective proton permeable membrane; 121, lower fixing plate; 122, electrode hole; 131, upper fixing plate; 132, fixing screw cap; 133, electrode slot; 134, accommodating cavity; Electrical plate screw cap; 142, oxygen discharge port; 151, first sealing silicone ring; 152, second sealing silicone ring; 153, third sealing silicone ring; 154, fourth sealing silicone ring; 161, hydrogen generation area; 162 . Oxygen generation area; 170. Moisturizing silica gel pad; 200. Hydrogen and oxygen separation electrolysis device control system; 210. Microprocessor; 220. Automatic voltage regulation module; 230. Memory; 240. Switching circuit; 250. Sampling comparison circuit; , charging and discharging management module; 270, storage battery; 280, light display device; 290, tilt sensing device; 300, cup body; 310, control base; 400, external power supply; ; 511, the outer column of the ventilation hole; 520, the lower cover; 521, the inner column of the ventilation hole; 530, the water-proof and breathable membrane.
具体实施方式Detailed ways
下面,结合附图以及具体实施方式,对本发明做进一步描述,需要说明的是,在不相冲突的前提下,以下描述的各实施例之间或各技术特征之间可以任意组合形成新的实施例。Below, the present invention will be further described in conjunction with the accompanying drawings and specific implementation methods. It should be noted that, under the premise of not conflicting, the various embodiments described below or the technical features can be combined arbitrarily to form new embodiments. .
本发明实施例提供的一种富氢水杯。氢氧分离电解系统包括氢氧分离电解装置,用于日常生活中制取富氢水,以满足人们使用富氢水进行疾病预防和调理身体,避免体内的自由基氧化损伤的问题。A hydrogen-rich water cup provided by an embodiment of the present invention. The hydrogen-oxygen separation electrolysis system includes a hydrogen-oxygen separation electrolysis device, which is used to produce hydrogen-rich water in daily life, so as to meet the problem of people using hydrogen-rich water for disease prevention and body conditioning, and to avoid free radical oxidative damage in the body.
实施例1:Example 1:
如图1、图2所示,本发明实施例提供的富氢水杯,包括控压增溶杯盖500,杯体300和氢氧分离电解系统,杯体300杯口设置杯盖接口,控压增溶杯盖500 与杯体300通过杯盖接口可拆卸连接,控压增溶杯盖500上设有透气孔,透气孔中设置有隔水透气膜530,氢氧分离电解系统设置在杯体300底部。控压增溶杯盖500与杯体300通过杯盖接口的连接包括螺纹连接、卡扣连接或者采用其他的常见配合安装方式连接,比如采用弹性部件的挤压连接。本发明的技术方案中优选采用螺纹连接。在杯体300的杯口设置外螺纹,在控压增溶杯盖500 内侧设置内螺纹,杯体300和控压增溶杯盖500通过螺纹的匹配连接在一起。杯体300采用专用的富氢水杯杯体,即在杯体300的底部设置安装机构,以便将氢氧分离电解系统安装在杯体300底部。同时提供防水的控制接口连接到杯体300外壁,如控制开关,电源接口等。As shown in Figure 1 and Figure 2, the hydrogen-rich water cup provided by the embodiment of the present invention includes a pressure-controlled solubilization cup cover 500, a cup body 300 and a hydrogen-oxygen separation electrolysis system, the cup body 300 is equipped with a cup lid interface, and the pressure control The solubilizing cup cover 500 is detachably connected to the cup body 300 through the cup cover interface. The pressure-controlled solubilizing cup cover 500 is provided with a vent hole, and a water-proof and breathable membrane 530 is arranged in the vent hole. The hydrogen-oxygen separation electrolysis system is set on the cup body. 300 bottom. The connection between the pressure control solubilization cup cover 500 and the cup body 300 through the cup cover interface includes threaded connection, buckle connection or other common fitting installation methods, such as extrusion connection using elastic components. In the technical solution of the present invention, threaded connection is preferably adopted. An external thread is provided on the mouth of the cup body 300 , and an internal thread is provided on the inner side of the pressure-controlling solubilization cup cover 500 , and the cup body 300 and the pressure-controlling solubilization cup cover 500 are connected together through thread matching. The cup body 300 adopts a special hydrogen-rich water cup cup body, that is, an installation mechanism is provided at the bottom of the cup body 300 so as to install the hydrogen-oxygen separation electrolysis system on the bottom of the cup body 300 . At the same time, a waterproof control interface is provided to connect to the outer wall of the cup body 300, such as a control switch, a power interface, and the like.
本发明实施例提供的富氢水杯,通过提供控压增溶杯盖500,控压增溶杯盖 500中设置通气孔,同时在透气孔中设置隔水透气膜530。隔水透气膜530的特点是只有在压力超过0.1MPa时,气体才会从隔水透气膜530中排出,而且不会漏水。在压力不足0.1MPa时,气体不能排出,从而保证了杯体300内的工作压力始终维持在接近0.1MPa。这既可以通过压力充分增加氢在水中的溶解度,提高单位工作时间内富氢水浓度,又可以稳定维持杯体300内的压力,确保了杯子的使用安全。从而避免了氢氧混合可能发生爆炸、压力过大容器漏水或爆炸的危险,以及压力过低单位时间内富氢水浓度过低的不足。本发明提供的富氢水杯,没有复杂的电子或者控制结构,设备简单,组装实现工艺简单,工作稳定可靠。The hydrogen-rich water cup provided in the embodiment of the present invention provides a pressure-controlled solubilization cup cover 500, and a vent hole is provided in the pressure-controlled solubilization cup cover 500, and a water-proof and breathable film 530 is provided in the vent hole. The characteristic of the water-proof and gas-permeable membrane 530 is that only when the pressure exceeds 0.1 MPa, the gas will be discharged from the water-proof and gas-permeable membrane 530 without water leakage. When the pressure is less than 0.1 MPa, the gas cannot be discharged, thus ensuring that the working pressure in the cup body 300 is always maintained close to 0.1 MPa. This can not only fully increase the solubility of hydrogen in water through pressure, increase the concentration of hydrogen-rich water per unit working time, but also stably maintain the pressure in the cup body 300, ensuring the safety of the cup. This avoids the risk of hydrogen-oxygen mixture explosion, water leakage or explosion in the container with too high pressure, and the problem of too low concentration of hydrogen-rich water per unit time when the pressure is too low. The hydrogen-rich water cup provided by the present invention has no complicated electronic or control structure, simple equipment, simple assembly and realization process, and stable and reliable operation.
其中,控压增溶杯盖500包括上盖510和下盖520,上盖510和下盖520相对应位置均设置有透气孔,隔水透气膜530设置在所述上盖510、下盖520之间,并与透气孔对应设置,下盖520固定在上盖510底面。上盖510包括透气孔外柱511,下盖520包括透气孔内柱521,隔水透气膜530紧密贴合在透气孔内柱 521的气孔上,透气孔内柱521插入透气孔外柱511。Wherein, the pressure control solubilization cup cover 500 includes an upper cover 510 and a lower cover 520, and the corresponding positions of the upper cover 510 and the lower cover 520 are all provided with air holes, and the water-proof and breathable membrane 530 is arranged on the upper cover 510 and the lower cover 520. Between, and corresponding to the ventilation holes, the lower cover 520 is fixed on the bottom surface of the upper cover 510 . The upper cover 510 includes an outer column 511 of the air hole, the lower cover 520 includes an inner column 521 of the air hole, the water-proof and breathable membrane 530 is closely attached to the air hole of the inner column 521 of the air hole, and the inner column 521 of the air hole is inserted into the outer column 511 of the air hole.
控压增溶杯盖500还包括第四密封硅胶圈154,第四密封硅胶圈154中间设置有通孔,第四密封硅胶圈154通过通孔嵌套在下盖520上。通过设置第四密封硅胶圈154,可以增加控压增溶杯盖500的防水性能和保温性能。The pressure control solubilization cup cover 500 also includes a fourth sealing silicone ring 154 , and a through hole is arranged in the middle of the fourth sealing silicone ring 154 , and the fourth sealing silicone ring 154 is nested on the lower cover 520 through the through hole. By arranging the fourth sealing silicone ring 154, the waterproof performance and thermal insulation performance of the pressure control solubilization cup cover 500 can be increased.
氢氧分离电解系统包括氢氧分离电解装置100和氢氧分离电解装置控制系统200;氢氧分离电解装置控制系统200通过固定件固定在氢氧分离电解装置 100的底部并与下固定板121密封连接。氢氧分离电解系统设置在控制底座310 上。在杯体300底部设置安装结构,通过固定控制底座310将氢氧分离电解系统固定在杯体300的杯底。氢氧分离电解系统的氢氧分离电解装置控制系统200 和氢氧分离电解装置100的具体结构请参见实施例2和实施例3。The hydrogen-oxygen separation electrolysis system includes a hydrogen-oxygen separation electrolysis device 100 and a hydrogen-oxygen separation electrolysis device control system 200; the hydrogen-oxygen separation electrolysis device control system 200 is fixed on the bottom of the hydrogen-oxygen separation electrolysis device 100 by a fixture and is sealed with the lower fixing plate 121 connect. The hydrogen-oxygen separation electrolysis system is set on the control base 310 . An installation structure is provided at the bottom of the cup body 300 , and the hydrogen-oxygen separation electrolysis system is fixed on the cup bottom of the cup body 300 by fixing the control base 310 . For the specific structures of the hydrogen-oxygen separation electrolysis device control system 200 and the hydrogen-oxygen separation electrolysis device 100 of the hydrogen-oxygen separation electrolysis system, please refer to Embodiment 2 and Embodiment 3.
实施例2:Example 2:
如图3、图4所示,本发明实施例提供的一种氢氧分离电解装置控制系统200,包括微处理器210、存储器230、自动调压模块220和开关电路240,微处理器210分别连接存储器230、自动调压模块220和开关电路240,自动调压模块220电源输入端外接电源400,自动调压模块220电源输出端正极外接氢氧分离电解装置100的阳极,自动调压模块220电源输出端负极外接氢氧分离电解装置100的阴极;As shown in Fig. 3 and Fig. 4, a hydrogen-oxygen separation electrolysis device control system 200 provided by the embodiment of the present invention includes a microprocessor 210, a memory 230, an automatic voltage regulation module 220 and a switch circuit 240, and the microprocessor 210 is respectively Connect the memory 230, the automatic voltage regulation module 220 and the switch circuit 240, the power input terminal of the automatic voltage regulation module 220 is connected to an external power supply 400, the positive pole of the power output terminal of the automatic voltage regulation module 220 is externally connected to the anode of the hydrogen-oxygen separation electrolysis device 100, and the automatic voltage regulation module 220 The negative pole of the output terminal of the power supply is externally connected to the cathode of the hydrogen-oxygen separation electrolysis device 100;
存储器230存储有根据氢氧分离电解装置100工作电压预设的开机电压检测值,控制电压步进值和计算机可执行程序,微处理器210读取存储器230中的计算机可执行程序并实现以下控制方法:The memory 230 stores the start-up voltage detection value preset according to the working voltage of the hydrogen-oxygen separation electrolysis device 100, the control voltage step value and the computer executable program, and the microprocessor 210 reads the computer executable program in the memory 230 and realizes the following control method:
开机电压检测步骤:检测外接电源400的电源电压,若电源电压低于开机电压检测值,停止工作并提示电压不足,否则,执行下一步骤;Start-up voltage detection step: detect the power supply voltage of the external power supply 400, if the power supply voltage is lower than the start-up voltage detection value, stop working and prompt that the voltage is insufficient, otherwise, go to the next step;
自动升压步骤:控制自动调压模块220以预设的控制电压步进值逐步提高输入至氢氧分离电解装置100阴极和阳极的电压,直到氢氧分离电解装置100 阴极和阳极的实际工作电压达到开机电压检测值。Automatic boosting step: control the automatic voltage regulation module 220 to gradually increase the voltage input to the cathode and anode of the hydrogen-oxygen separation electrolysis device 100 with the preset control voltage step value until the actual working voltage of the cathode and anode of the hydrogen-oxygen separation electrolysis device 100 Reach the power-on voltage detection value.
其中一种优选实施方式中,,存储器230中预设的开机电压检测值设为氢氧分离电解装置的额定工作电压。自动调压模块220在以预设的控制电压步进值逐步提高输入至氢氧分离电解装置100阴极和阳极的电压,如可以设置控制电压步进值为每秒增加0.5V,输出合理电压电流到氢氧分离电解装置100。合理电压指电极加载电压要求缓慢升压。In one preferred implementation manner, the preset start-up voltage detection value in the memory 230 is set as the rated working voltage of the hydrogen-oxygen separation electrolysis device. The automatic voltage regulation module 220 gradually increases the voltage input to the cathode and anode of the hydrogen-oxygen separation electrolysis device 100 with a preset control voltage step value. For example, the control voltage step value can be set to increase by 0.5V per second to output a reasonable voltage and current To hydrogen and oxygen separation electrolysis device 100. Reasonable voltage means that the electrode loading voltage requires a slow boost.
开关电路240控制氢氧分离电解系统的电源通断,在关机时,开关电路240 同时以不同信号给微处理器210,微处理器210处理不同信号运算计时,当计时结束时,微处理器210将关机信号给自动调压模块220,完成停机。The switch circuit 240 controls the power on and off of the hydrogen-oxygen separation electrolysis system. When shutting down, the switch circuit 240 sends different signals to the microprocessor 210 at the same time, and the microprocessor 210 processes different signals to calculate the timing. Send the shutdown signal to the automatic voltage regulation module 220 to complete the shutdown.
本发明实施例提供的一种氢氧分离电解装置控制系统200,通过在开机时检测电源电压,在启动氢氧分离电解装置100时逐步将电压提升到工作电压,避免了氢氧分离电解装置100在电解开始时输入瞬间的高变化电压,从而避免产生臭氧。The control system 200 of the hydrogen-oxygen separation electrolysis device provided by the embodiment of the present invention detects the power supply voltage when starting up, and gradually increases the voltage to the working voltage when starting the hydrogen-oxygen separation electrolysis device 100, avoiding the problem of the hydrogen-oxygen separation electrolysis device 100. Input a momentary high-change voltage at the start of electrolysis to avoid ozone generation.
本实施例提供的氢氧分离电解装置控制系统200可以通过适配器直接连接家用配电。但这样限制了设备的使用。由于氢氧分离电解装置100在工作时不需要很高的电压和电流,一种优选的实施方式中,本发明实施例提供的氢氧分离电解装置控制系统200还包括充放电管理模块260和蓄电池270,自动调压模块220通过充放电管理模块260同时外接电源400和蓄电池270。在使用外接电源400供电时,通过充电器提供稳压的5V电压输出,充放电管理模块260可以根据蓄电池270的电容调节充电电压和充电电流;在不接入外接电源400,并通过蓄电池270供电时,充放电管理模块260提供对蓄电池270进行过流或过载保护。充放电管理模块260通过对蓄电池270充电和放电进行保护,可以快速充电同时不损坏电池,延迟电池的使用寿命。The hydrogen-oxygen separation electrolysis device control system 200 provided in this embodiment can be directly connected to household power distribution through an adapter. But this limits the use of the device. Since the hydrogen-oxygen separation electrolysis device 100 does not require high voltage and current during operation, in a preferred embodiment, the hydrogen-oxygen separation electrolysis device control system 200 provided in the embodiment of the present invention also includes a charging and discharging management module 260 and a storage battery 270 , the automatic voltage regulation module 220 is simultaneously connected to the power source 400 and the storage battery 270 through the charging and discharging management module 260 . When the external power supply 400 is used to supply power, the charger provides a regulated 5V voltage output, and the charging and discharging management module 260 can adjust the charging voltage and charging current according to the capacitance of the storage battery 270; , the charging and discharging management module 260 provides overcurrent or overload protection for the storage battery 270 . The charging and discharging management module 260 protects the charging and discharging of the storage battery 270 , so that the battery can be charged quickly without damaging the battery and prolonging the service life of the battery.
本实施例的一种优选实施方案中,还包括取样比较电路250,取样比较电路 250输入端分别连接自动调压模块220电源输出端正极和负极,取样比较电路 250输出端连接微处理器210,取样比较电路250获取氢氧分离电解装置100的实际工作电压,并输入至微处理器210,微处理器210执行计算机可执行程序实现以下控制方法:In a preferred implementation of this embodiment, it also includes a sampling comparison circuit 250, the input terminals of the sampling comparison circuit 250 are respectively connected to the positive pole and the negative pole of the output terminal of the automatic voltage regulation module 220, and the output terminal of the sampling comparison circuit 250 is connected to the microprocessor 210, The sampling comparison circuit 250 obtains the actual working voltage of the hydrogen-oxygen separation electrolysis device 100, and inputs it to the microprocessor 210, and the microprocessor 210 executes a computer executable program to realize the following control method:
自动调压步骤:比较实际工作电源与开机电压检测值的大小,如果实际工作电压大于开机电压检测值,控制自动调压模块220降低输出至氢氧分离电解装置100的电压,直至实际工作电压等于开机电压检测值,如果实际工作电压小于开机电压检测值,控制自动调压模块220升高输出至氢氧分离电解装置100 的电压,直至实际工作电压等于开机电压检测值。Automatic voltage regulation step: compare the actual working power supply with the detected value of the starting voltage, if the actual working voltage is greater than the detected value of the starting voltage, control the automatic voltage regulating module 220 to reduce the voltage output to the hydrogen-oxygen separation electrolysis device 100 until the actual working voltage is equal to Start-up voltage detection value, if the actual working voltage is lower than the start-up voltage detection value, control the automatic voltage regulation module 220 to increase the voltage output to the hydrogen-oxygen separation electrolysis device 100 until the actual working voltage is equal to the start-up voltage detection value.
通过设置取样比较电路250,实时检测氢氧分离电解装置的工作电压,并及时将其工作电压调节到额定工作电压,可以保持氢氧分离电解装置保持稳定的工作电压和工作电流。特别是在使用蓄电池270供电的时候,由于随着电池的电量变化,容易导致输出到氢氧分离电解装置的工作电压发生变换。通过提供稳定的工作电压和工作电流可以保证生成氢气的稳定性,同时保证水中氢气的溶解量,保证氢水浓度。同时稳定的工作电压和工作电流也有利于延长设备的使用寿命。By setting the sampling comparison circuit 250 to detect the working voltage of the hydrogen-oxygen separation electrolysis device in real time, and adjust the working voltage to the rated working voltage in time, the hydrogen-oxygen separation electrolysis device can maintain a stable working voltage and working current. Especially when the storage battery 270 is used for power supply, the working voltage output to the hydrogen-oxygen separation electrolysis device is easily changed due to the change of the battery power. By providing a stable working voltage and working current, the stability of hydrogen generation can be guaranteed, and at the same time, the amount of hydrogen dissolved in water can be guaranteed, and the concentration of hydrogen water can be guaranteed. At the same time, the stable working voltage and working current are also conducive to prolonging the service life of the equipment.
取样比较电路250可以通过微处理器210执行计算机程序实现,也可以通过电路实现。在取样比较电路250中预设氢氧分离电解装置100额定工作电压。取样比较电路250设置取样电路和比较电路,取样电路获取氢氧分离电解装置 100的实际工作电压,并输入比较电路,比较电路将获取的实际工作电压和额定工作电压值比较并判断大小,并输出比较结果给微处理器210。The sampling comparison circuit 250 can be implemented by the microprocessor 210 executing a computer program, or can be implemented by a circuit. The rated operating voltage of the hydrogen-oxygen separation electrolysis device 100 is preset in the sampling comparison circuit 250 . The sampling comparison circuit 250 is provided with a sampling circuit and a comparison circuit. The sampling circuit obtains the actual working voltage of the hydrogen-oxygen separation electrolysis device 100 and inputs it into the comparison circuit. The comparison result is sent to the microprocessor 210 .
本实施例的一种优选实施方案中,还包括灯光显示装置280,灯光显示装置 280与微处理器210连接。开关电路240以不同信号给微处理器210,微处理器 210处理不同信号,将灯光信号输出给灯光显示装置280,灯光显示装置280用于接收微处理器210的信号,根据不同信号点亮不同灯光。如开机检测、自动升压、自动调压或者电源电压不足,不同定时制氢时间,也可以通过灯光显示装置280进行显示。灯光显示装置280可以通过不同的光显示不同的工作状态,以提醒操作人员采取适当的措施。In a preferred implementation of this embodiment, a light display device 280 is also included, and the light display device 280 is connected with the microprocessor 210. The switch circuit 240 sends different signals to the microprocessor 210, the microprocessor 210 processes different signals, and outputs the light signal to the light display device 280, the light display device 280 is used to receive the signal from the microprocessor 210, and lights up different lights according to different signals. light. Such as power-on detection, automatic voltage boosting, automatic voltage regulation or insufficient power supply voltage, hydrogen production time at different timings can also be displayed through the light display device 280 . The light display device 280 can display different working states through different lights, so as to remind the operator to take appropriate measures.
实施例3:Example 3:
本发明实施例2提供一种氢氧分离电解系统。包括氢氧分离电解装置100 和如实施例1的氢氧分离电解装置控制系统200,氢氧分离电解装置控制系统 200设置在所述氢氧分离电解装置100的下端并密封连接。Embodiment 2 of the present invention provides a hydrogen-oxygen separation electrolysis system. Including the hydrogen-oxygen separation electrolysis device 100 and the hydrogen-oxygen separation electrolysis device control system 200 as in Embodiment 1, the hydrogen-oxygen separation electrolysis device control system 200 is arranged at the lower end of the hydrogen-oxygen separation electrolysis device 100 and is sealed and connected.
如图5、图6所示,氢氧分离电解装置100包括电解发生器、上固定板131 和下固定板121,电解发生器包括阴极片111、阳极片112、选择性质子透过113 膜、上固定板131和下固定板121,阴极片111设置阴极接线端1112,阴极接线端1112外接电源400负极,具体地,阴极接线端1112连接自动调压模块220 电源输出端负极;阳极片112设置阳极接线端1122,阳极接线端1122外接电源 400正极,具体地,阳极接线端1122连接自动调压模块220电源输出端正极极;下固定板121上设置电极孔122,阳极接线端1122和阴极接线端1112穿过电极孔122,可以在上固定板131的底面或者下固定板121的顶面设置与阴极片111、选择性质子透过膜113、阳极片112形状匹配的容置空腔134,也可以同时在上固定板131的底面和下固定板121的顶面设置与阴极片111、选择性质子透过膜 113、阳极片112形状匹配的容置空腔134,下固定板121与上固定板131可拆卸连接,阴极片111、选择性质子透过膜113、阳极片112固定在上固定板131 和下固定板121之间的容置空腔134内,阴极片111与选择性质子透过膜113 之间形成氢气生成区161,阳极片112和选择性质子透过膜113之间形成氧气生成区162,氢气生成区161设置氢气排放口供氢气排出氢气生成区161和水进入氢气生成区161,氧气生成区162设置氧气排放口142供氧气排出氧气生成区 162。As shown in Figure 5 and Figure 6, the hydrogen-oxygen separation electrolysis device 100 includes an electrolytic generator, an upper fixed plate 131 and a lower fixed plate 121, and the electrolytic generator includes a cathode sheet 111, an anode sheet 112, a selective proton permeable 113 membrane, The upper fixing plate 131 and the lower fixing plate 121, the cathode piece 111 is provided with a cathode terminal 1112, the cathode terminal 1112 is connected to the negative pole of the external power supply 400, specifically, the cathode terminal 1112 is connected to the negative pole of the output terminal of the automatic voltage regulating module 220; the anode piece 112 is set Anode terminal 1122, the anode terminal 1122 is connected to the positive pole of the external power supply 400, specifically, the anode terminal 1122 is connected to the positive pole of the power output terminal of the automatic voltage regulation module 220; the lower fixed plate 121 is provided with an electrode hole 122, the anode terminal 1122 and the cathode connection The end 1112 passes through the electrode hole 122, and an accommodating cavity 134 matching the shape of the cathode sheet 111, the selective proton permeable membrane 113, and the anode sheet 112 can be provided on the bottom surface of the upper fixing plate 131 or the top surface of the lower fixing plate 121, The accommodating cavity 134 matching the shape of the cathode sheet 111, the selective proton permeable membrane 113, and the anode sheet 112 can also be set on the bottom surface of the upper fixing plate 131 and the top surface of the lower fixing plate 121 at the same time, and the lower fixing plate 121 and the upper The fixed plate 131 is detachably connected, the cathode sheet 111, the selective proton permeable membrane 113, and the anode sheet 112 are fixed in the accommodation cavity 134 between the upper fixed plate 131 and the lower fixed plate 121, and the cathode sheet 111 and the selective proton A hydrogen generation region 161 is formed between the permeable membranes 113, an oxygen generation region 162 is formed between the anode sheet 112 and the selective proton permeable membrane 113, and a hydrogen discharge port is set in the hydrogen generation region 161 for hydrogen to exit the hydrogen generation region 161 and water enters the hydrogen generation region Zone 161 , oxygen generating zone 162 is provided with an oxygen discharge port 142 for oxygen to exit the oxygen generating zone 162 .
在上固定板131的中部设有通孔,通孔一直延伸到阴极片111以及阴极片和选择性质子透过膜113之间的氢气生成区161。上固定板131中部的通孔形成了氢气排放口。电解需要的水直接从通孔进入阴极片111和选择性质子透过膜 113,并充满整个选择性质子透过膜以上的容置空腔部分。氢气在氢气生成区161 生成后,可以直接溶解到位于氢气生成区161的水中,也可以通过设置在上固定板131中部的通孔排出到杯体中,溶解到其他的水中。多余的氢气将从水中通过杯口排出杯体。A through hole is provided in the middle of the upper fixing plate 131 , and the through hole extends to the cathode sheet 111 and the hydrogen generation region 161 between the cathode sheet and the selective proton permeable membrane 113 . The through hole in the middle part of the upper fixing plate 131 forms a hydrogen discharge port. The water required for electrolysis directly enters the cathode sheet 111 and the selective proton permeable membrane 113 from the through hole, and fills the accommodating cavity above the entire selective proton permeable membrane. After the hydrogen is generated in the hydrogen generating area 161, it can be directly dissolved into the water located in the hydrogen generating area 161, or it can be discharged into the cup through the through hole in the middle of the upper fixing plate 131 and dissolved in other water. Excess hydrogen will exit the cup from the water through the mouth of the cup.
上固定板131的底面边缘设有连通容置空腔134和上固定板侧边外壁的电极卡槽133,在阴极片111和阳极片112的边缘分别设置阴极片凸台1113和阳极片凸台1123,阴极片凸台1113和阳极片凸台1123卡设在电极卡槽133内,以便对阴极片111和阳极片112进行固定。The edge of the bottom surface of the upper fixing plate 131 is provided with an electrode slot 133 communicating with the accommodating cavity 134 and the outer wall of the side of the upper fixing plate, and the cathode plate 111 and the anode plate 112 are provided with a cathode plate boss 1113 and an anode plate boss respectively. 1123 , the cathode tab 1113 and the anode tab 1123 are clamped in the electrode slot 133 , so as to fix the cathode tab 111 and the anode tab 112 .
其中,选择性质子透过膜113为自增湿型质子透过膜。具体地,自增湿型质子透过膜为全氟磺酸离子膜。采用自增湿型质子透过膜,氧气生成区162不需要提前注入水,氢气生成区161中的水可以透过自增湿型质子膜向氧气生成区162渗入少量水以满足电解需要,然后氧气生成区162的少量水通过水合质子(H3O+)的形式传递到氢气生成区161,从而防止氧气生成区162的水随产生的氧气流出,避免产生废液。Wherein, the selective proton permeable membrane 113 is a self-humidifying proton permeable membrane. Specifically, the self-humidifying proton permeable membrane is a perfluorosulfonic acid ion membrane. Adopt self-humidification type proton permeable membrane, oxygen generation region 162 does not need to inject water in advance, the water in hydrogen generation region 161 can permeate self-humidification type proton membrane to oxygen generation region 162 to infiltrate a small amount of water to satisfy electrolysis demand, then A small amount of water in the oxygen generation area 162 is transferred to the hydrogen generation area 161 in the form of hydrated protons (H3O+), thereby preventing the water in the oxygen generation area 162 from flowing out with the generated oxygen and avoiding the generation of waste liquid.
其中,阴极片111和阳极片112上设置多个透气孔。通过设置多个透气孔,使生成的氢气形成小气泡的形式进入水中,可以使得氢气的直径小,比表面积大,气体上升逃逸慢,溶解率更高。Wherein, a plurality of ventilation holes are provided on the cathode sheet 111 and the anode sheet 112 . By setting a plurality of air holes, the generated hydrogen enters the water in the form of small bubbles, which can make the diameter of the hydrogen small, the specific surface area large, the gas rise and escape slowly, and the dissolution rate is higher.
阴极片111和阳极片112均采用钛电极,由三种不同粒径的钛颗粒通过转印法、模压法、电化学沉积法、浸渍还原法或真空溅射法制备而成,呈蜂窝状排列。Both the cathode sheet 111 and the anode sheet 112 are made of titanium electrodes, which are prepared from titanium particles of three different particle sizes by transfer printing, molding, electrochemical deposition, impregnation reduction or vacuum sputtering, arranged in a honeycomb shape .
其中,上固定板131和下固定板121之间的连接可以采用卡扣连接、螺钉连接或者其他的可实现连接方式。本实施例如图1所述采用螺钉连接,在上固定板131上设置螺纹盲孔,下固定板121相应位置设置螺纹通孔,通过螺钉将上固定板131和下固定板121紧密连接在一起。可以在上固定板131底面上设置卡销135,下固定板121相应位置设置卡孔,通过卡销135和卡孔对上固定板 131和下固定板121进行定位。Wherein, the connection between the upper fixing plate 131 and the lower fixing plate 121 may adopt buckle connection, screw connection or other possible connection methods. This embodiment adopts screw connection as described in FIG. 1 , threaded blind holes are set on the upper fixing plate 131 , threaded through holes are set at corresponding positions of the lower fixing plate 121 , and the upper fixing plate 131 and the lower fixing plate 121 are tightly connected together by screws. A detent 135 can be set on the bottom surface of the upper fixed plate 131, and a corresponding position of the lower fixed plate 121 is provided with a clamping hole, and the upper fixed plate 131 and the lower fixed plate 121 are positioned by the detent 135 and the clamped hole.
本发明提供的氢氧分离电解装置100,通过选择性质子透过膜113将阴极片 111和阳极片112隔开,形成氢气生成区161和氧气生成区162。选择性质子透过膜113是允许水合质子(H3O+)通过的膜,水合质子同选择性质子透过膜113 中的基团结合,然后从一个基团传递到另一个基团,最终到达另一边。首先通电后水便立刻在阳极片112失去电子e-生成氢离子和氧气(2H2O-4e-=4H++O2 ↑),氧气从氧气排放口142排出。氢离子以水合质子(H3O+)的形式通过选择性质子透过膜113传递到阴极片111,获得电子生成氢气(4H3O++4e-=4H2O+ H2↑),氢气在氢气生成区161溶解到水中,还有一部分氢气从氢气排放口排出到杯体中,从而达到氢氧安全稳定分离,同时避免氧气或者臭氧溶解到水中。In the hydrogen-oxygen separation electrolysis device 100 provided by the present invention, the cathode sheet 111 and the anode sheet 112 are separated by a selective proton permeable membrane 113 to form a hydrogen generation region 161 and an oxygen generation region 162 . The selective proton permeable membrane 113 is a membrane that allows the passage of hydrated protons (H3O+), and the hydrated protons are combined with groups in the selective proton permeable membrane 113, and then passed from one group to another, and finally reach the other side . After first electrifying, water just loses electron e- at anode sheet 112 immediately and generates hydrogen ion and oxygen (2H2O-4e-=4H++O2 ↑), and oxygen is discharged from oxygen discharge port 142. Hydrogen ions are transferred to the cathode sheet 111 through the selective proton permeable membrane 113 in the form of hydrated protons (H3O+), and electrons are obtained to generate hydrogen gas (4H3O++4e-=4H2O+ H2↑), and the hydrogen gas is dissolved in the water in the hydrogen gas generation area 161, There is also a part of hydrogen discharged from the hydrogen discharge port into the cup, so as to achieve safe and stable separation of hydrogen and oxygen, while preventing oxygen or ozone from dissolving into the water.
本发明提供的一种氢氧分离电解装置100的一种优选实施方式中,阴极片 111、阳极片112、选择性质子透过膜113、上固定板131和下固定板121均设置为大小匹配的圆形,以便更好的用于制作富氢水杯或者富氢饮水机。阴极片111、选择性质子透过膜113、阳极片112可以从上到下的顺序排列,也可以从下到上的顺序排列。本发明实施例优选阴极片111、选择性质子透过膜113、阳极片112 按从上到下的顺序固定在上固定板131和下固定板121之间的容置空腔134内,阳极片112、选择性质子透过膜113和下固定板121之间密封连接。这种设置可以方便氧气排放口142设置在下固定板121上,有利于将氧气通过底部排除装置外,从而在制作富氢水杯时,直接通过杯底将氧气排出杯体外。同时,密封设置可防止水不经过选择性质子透过膜113直接进入氧气生成区162,形成废水。其中,阴极片111和上固定板131之间设置第一密封硅胶圈151、阳极片112和下固定板121之间设置第二密封硅胶圈152。通过设置密封硅胶圈,增加各个部件之间连接的气密性和防水性。In a preferred embodiment of a hydrogen-oxygen separation electrolysis device 100 provided by the present invention, the cathode sheet 111, the anode sheet 112, the selective proton permeable membrane 113, the upper fixing plate 131 and the lower fixing plate 121 are all set to match in size The round shape is better used to make hydrogen-rich water cups or hydrogen-rich water dispensers. The cathode sheet 111, the selective proton permeable membrane 113, and the anode sheet 112 may be arranged in order from top to bottom, or may be arranged in order from bottom to top. In the embodiment of the present invention, the cathode sheet 111, the selective proton permeable membrane 113, and the anode sheet 112 are preferably fixed in the cavity 134 between the upper fixing plate 131 and the lower fixing plate 121 in order from top to bottom, and the anode sheet 112 . A sealed connection between the selective proton permeable membrane 113 and the lower fixing plate 121 . This setting can facilitate the arrangement of the oxygen discharge port 142 on the lower fixing plate 121, which is beneficial to remove oxygen from the device through the bottom, so that when making a hydrogen-rich water cup, the oxygen can be directly discharged out of the cup through the bottom of the cup. At the same time, the sealing arrangement can prevent water from directly entering the oxygen generating region 162 without passing through the selective proton permeable membrane 113 to form waste water. Wherein, a first sealing silicone ring 151 is arranged between the cathode sheet 111 and the upper fixing plate 131 , and a second sealing silicone ring 152 is arranged between the anode sheet 112 and the lower fixing plate 121 . By setting the sealing silicone ring, the airtightness and waterproofness of the connection between the various components are increased.
本发明实施例提供一种进一步改进的氢氧分离电解装置100,还包括电板旋盖141,电板旋盖141的顶部设置为平整平面,下固定板121对应电解发生器区域设置通孔,电板旋盖141设置在通孔内,电板旋盖141可沿通孔上下移动。一种实施方式中,在电板旋盖141上设置外螺纹,通孔内的侧壁上设置与电板旋盖141螺纹匹配的内螺纹,电板旋盖141与下固定板121之间通过螺纹连接。在电解生成器中,阴极片111、选择性质子透过膜113和阳极片112从上至下固定在上固定板131和下固定板121之间,通过电板旋盖141顶部的平整平面,可以调节阳极片112和阴极片111之间的距离,使阳极片112和阴极片111之间的距离更均衡,通过阳极片112和阴极片111之间的电流也更为均衡,从而使电解反应在整个阳极片112和阴极片111上都均衡发生,提高氢气产生的效率。同时,通过调节电板旋盖141压缩阳极片112和阴极片111的距离,使阳极片112 和阴极片111隔着选择性质子透过膜贴合的更紧密,从而使他们之间的电阻更小,电流更高,分解的功率和速度都更快。The embodiment of the present invention provides a further improved hydrogen-oxygen separation electrolysis device 100, which also includes an electric plate screw cover 141. The top of the electric plate screw cover 141 is set as a flat plane, and the lower fixing plate 121 is provided with a through hole corresponding to the area of the electrolytic generator. The electric board screw cover 141 is arranged in the through hole, and the electric board screw cover 141 can move up and down along the through hole. In one embodiment, an external thread is provided on the electric board screw cap 141, and an internal thread matching with the thread of the electric board screw cap 141 is provided on the side wall of the through hole, and the electric board screw cover 141 and the lower fixing plate 121 pass through threaded connection. In the electrolytic generator, the cathode sheet 111, the selective proton permeable membrane 113 and the anode sheet 112 are fixed between the upper fixing plate 131 and the lower fixing plate 121 from top to bottom, passing through the flat plane on the top of the electric plate screw cover 141, The distance between the anode piece 112 and the cathode piece 111 can be adjusted to make the distance between the anode piece 112 and the cathode piece 111 more balanced, and the current passing between the anode piece 112 and the cathode piece 111 is also more balanced, so that the electrolytic reaction Occurs equally across the entire anode sheet 112 and cathode sheet 111, increasing the efficiency of hydrogen generation. At the same time, the distance between the anode sheet 112 and the cathode sheet 111 is compressed by adjusting the electric plate screw cover 141, so that the anode sheet 112 and the cathode sheet 111 are bonded closer through the selective proton permeable membrane, thereby making the resistance between them more compact. Smaller, higher current, faster decomposition power and speed.
本发明实施例提供的氢氧分离电解装置控制系2100的进一步优选实施方式中,还包括倾斜感应装置290,倾斜感应装置290和微处理器210连接,用于检测装置的倾斜角度,并在倾斜角超过预设值时发出警报或者切断输入至所述阴极片111和阳极片112的电压。通过设置倾斜感应装置290来检测氢氧分离电解装置的倾斜程度,在氢氧分离电解装置倾斜,阳极片112和阴极片111未接触到水时,通过关闭电路,防止装置的电解系统受损。In a further preferred implementation of the control system 2100 of the hydrogen-oxygen separation electrolysis device provided in the embodiment of the present invention, it also includes a tilt sensing device 290, which is connected to the microprocessor 210 for detecting the tilt angle of the device, and when tilting When the angle exceeds a preset value, an alarm is issued or the voltage input to the cathode piece 111 and the anode piece 112 is cut off. The inclination of the hydrogen-oxygen separation electrolysis device is detected by setting the tilt sensing device 290. When the hydrogen-oxygen separation electrolysis device is tilted and the anode piece 112 and the cathode piece 111 are not in contact with water, the circuit is closed to prevent damage to the electrolysis system of the device.
本发明实施例提供的氢氧分离电解装置100的进一步优选实施方式中,还包括电解系统卡槽和固定旋盖132,固定旋盖132与上固定板131的上面可拆卸连接,本发明提供的技术方案中,在上固定板131顶面设置外螺纹,固定旋盖 132底面设置内孔,内孔的侧壁上设置与上固定板131螺纹匹配的内螺纹,固定旋盖132与上固定板131之间通过螺纹连接。电解系统卡槽设有卡口,卡口卡接在上固定板131和固定旋盖132之间,通过固定旋盖132将电解发生器固定在电解系统卡槽内,在固定旋盖132与上固定板131之间设置第三密封硅胶圈153,以增加防水性。固定旋盖132的中间对应上固定板131中部的通孔处同时设置通孔,以供上固定板131和固定旋盖132连通形成氢气排放口。在其中一种优选的实施方式中,在固定旋盖132上还可设置保湿硅胶垫170,保湿硅胶垫 170可以通过吸附、卡扣或者其他的连接方式与固定旋盖132连接。在氢氧分离电解装置100需要比较长时间不工作时,可在选择性质子透过膜113和阴极片 111之间的氢气生成区161处倒入一定的水,然后将保湿硅胶垫固定在固定旋盖 132上。保湿硅胶垫可以保持氢气生成区161上的水分不会轻易蒸发掉,保持选择性质子透过膜113的湿润性,从而保证氢氧分离电解装置100的良好功能和使用寿命。In a further preferred embodiment of the hydrogen-oxygen separation electrolysis device 100 provided in the embodiment of the present invention, it also includes an electrolysis system card slot and a fixed screw cover 132, and the fixed screw cover 132 is detachably connected to the top of the upper fixed plate 131. In the technical scheme, an external thread is arranged on the top surface of the upper fixing plate 131, an inner hole is arranged on the bottom surface of the fixing screw cap 132, and an inner thread matching with the thread of the upper fixing plate 131 is arranged on the side wall of the inner hole, and the fixing screw cap 132 and the upper fixing plate 131 are connected by thread. The slot of the electrolysis system is provided with bayonet, and the bayonet is snapped between the upper fixing plate 131 and the fixed screw cover 132, the electrolytic generator is fixed in the slot of the electrolysis system through the fixed screw cover 132, and the A third sealing silicone ring 153 is arranged between the fixing plates 131 to increase waterproofness. A through hole is provided in the middle of the fixed screw cap 132 corresponding to the through hole in the middle of the upper fixed plate 131, so that the upper fixed plate 131 and the fixed screw cap 132 communicate to form a hydrogen discharge port. In one preferred embodiment, a moisturizing silicone pad 170 can also be provided on the fixed screw cap 132, and the moisturizing silicone pad 170 can be connected with the fixed screw cap 132 by adsorption, buckle or other connection methods. When the hydrogen-oxygen separation electrolysis device 100 needs to be out of work for a relatively long time, a certain amount of water can be poured into the hydrogen generation area 161 between the selective proton permeable membrane 113 and the cathode sheet 111, and then the moisturizing silica gel pad is fixed on a fixed surface. Screw cap 132 on. The moisture-retaining silica gel pad can keep the moisture on the hydrogen generating area 161 from evaporating easily, and maintain the wettability of the selective proton permeable membrane 113, thereby ensuring the good function and service life of the hydrogen-oxygen separation electrolysis device 100.
上述实施方式仅为本发明的优选实施方式,不能以此来限定本发明保护的范围,本领域的技术人员在本发明的基础上所做的任何非实质性的变化及替换均属于本发明所要求保护的范围。The above-mentioned embodiment is only a preferred embodiment of the present invention, and cannot be used to limit the protection scope of the present invention. Any insubstantial changes and substitutions made by those skilled in the art on the basis of the present invention belong to the scope of the present invention. Scope of protection claimed.
Claims (14)
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