CN104973570A - Healthy water preparation system and preparation method - Google Patents
Healthy water preparation system and preparation method Download PDFInfo
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- CN104973570A CN104973570A CN201410136008.0A CN201410136008A CN104973570A CN 104973570 A CN104973570 A CN 104973570A CN 201410136008 A CN201410136008 A CN 201410136008A CN 104973570 A CN104973570 A CN 104973570A
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Abstract
The invention discloses a healthy water preparation system and preparation method. The preparation system comprises hydrogen conveying equipment, a membrane separation device, oxygen conveying equipment and water generation equipment, wherein the hydrogen conveying equipment obtains hydrogen through preparation or only conveys the prepared hydrogen; the hydrogen conveying equipment is connected with the membrane separation device, wherein protium in hydrogen is separated out through the membrane separation device while deuterium and tritium in hydrogen cannot be filtered out of the membrane separation device; the oxygen conveying equipment provides oxygen through preparation or only conveys the prepared oxygen; and the water generation equipment receives the hydrogen prepared by hydrogen preparation equipment and the oxygen conveyed by the oxygen conveying equipment to obtain healthy water. The healthy water preparation system disclosed by the invention can be used for preparing light water without radioactive elements deuterium and tritium so as to improve the life quality of people and meet the needs for health. Moreover, the system has portability and is convenient to carry.
Description
Technical field
The invention belongs to healthy drinking water preparing technical field, relate to a kind of water preparation system, particularly relate to a kind of healthy water preparation system; Meanwhile, the invention still further relates to a kind of healthy water preparation method.
Background technology
Protium, deuterium, tritium are hydrogen three kinds of isotropic substances; Have 1 proton in H protium nucleus, without neutron, abundance is 99.98%; Deuterium D(is also known as heavy hydrogen), there is 1 proton in nucleus, 1 neutron, abundance 0.016%; Tritium T(is also known as tritium), there is 1 proton in nucleus, 2 neutrons, abundance 0.004.
But studies have found that, along with the precipitation of time, the energy of solar radiation on earth part is present in water with the form of deuterium, tritium, therefore, nowadays in water, the content of deuterium, tritium, higher than in the past, and is in growing trend.
The radio isotope of a kind of stable form that deuterium (deuterium) is hydrogen, be also referred to as heavy hydrogen, the symbol of element is generally D or 2H.There are a proton and a neutron in nucleus, in hydrogen, have the deuterium of 0.016%.Be about 1/7000th of general hydrogen at the content of the Nature, for thermonuclear reaction, release β during fusion and after ray, form the helium that total mass number is 3; Deuterium is called as " following natural fuel ".
Tritium (tritium) symbol of element is T or 3H.A proton and two neutrons are had in nucleus.And with radioactivity, β decay can occur, and its transformation period is 12.43.β decay due to tritium only can release the electronics of high-speed mobile, can not penetrate human body, and just meeting is harmful therefore to only have a large amount of suction tritium.At the occurring in nature of the earth, compare general hydrogen, the content of tritium is few.The generation of tritium be when Millikan's rays with high-energy neutron bombardment deuteron, its deuteron and neutron are combined into triton.Tritium is the same with deuterium, is all the raw material manufacturing hydrogen bomb.Occurring in nature exists atomic, obtains, be mainly used in thermonuclear reaction from nuclear reaction.
As can be seen here, the deuterium existed in water, tritium have radioactivity, affect the health of people to a certain extent; Heavy water (anomalous water) content is higher, and cell cycle impact is larger, can shorten the life cycle of cell; Heavy water is poisonous, if the content of heavy water exceedes certain value in water, and can be fatal.But nowadays also solution does not dewater the method for middle deuterium, tritium; The water Preparation equipment more do not occur that volume is little, being applicable to family expenses.
In view of this, nowadays in the urgent need to designing a kind of new water Preparation equipment, to overcome the above-mentioned defect of existing water treatment mode.
Summary of the invention
Technical problem to be solved by this invention is: provide a kind of healthy water preparation system, can prepare not containing the light-water of deuterium tritium, promote the quality of the life of people.
In addition, the present invention also provides a kind of healthy water preparation method, can prepare not containing the light-water of deuterium tritium, promote the quality of the life of people.
For solving the problems of the technologies described above, the present invention adopts following technical scheme:
A kind of healthy water preparation system, described preparation system comprises: hydrogen Preparation equipment, oxygen delivery devices, water generation equipment;
Described hydrogen Preparation equipment comprises: liquid container, raw material conveying device, device for rapidly starting, device for producing hydrogen, membrane separation unit, hydrogen delivery tube road;
Described device for producing hydrogen comprises interchanger, vaporizer, reformer chamber; Membrane separation unit is arranged in separate chamber, and separate chamber is arranged at the top of reformer chamber;
Described liquid container is connected with device for producing hydrogen; Liquid first alcohol and water is stored in liquid container;
Described hydrogen Preparation equipment utilizes device for rapidly starting to provide the startup energy to start; Device for rapidly starting comprises heating arrangements, gasification pipe, and the internal diameter of gasification pipe is 1 ~ 2mm, and gasification pipe is closely wound on heating arrangements; One end of described gasification pipe connects liquid container, is sent into by methyl alcohol in gasification pipe; The other end of gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches spontaneous ignition temperature, directly spontaneous combustion after methyl alcohol exports from gasification pipe; Described device for rapidly starting provides the startup energy for device for producing hydrogen; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyzer in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating;
After described device for producing hydrogen starts, device for producing hydrogen provides the energy needed for operation by the hydrogen that device for producing hydrogen obtains;
First alcohol and water in described liquid container is delivered to interchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and water vapour enter reformer chamber, and reformer chamber is provided with catalyzer, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C;
The temperature on described reformer chamber top is 400 DEG C ~ 500 DEG C; Reformer chamber is connected by connecting pipeline with separate chamber, all or part of top being arranged at reformer chamber of connecting pipeline, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting pipeline, as the buffering between reformer chamber and separate chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separate chamber or close;
Temperature in described separate chamber is set as 350 DEG C ~ 500 DEG C; Be provided with membrane separation apparatus in separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus;
Described raw material conveying device provides power, by the feedstock transportation in liquid container to device for producing hydrogen; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that device for producing hydrogen is obtained has enough pressure;
After described device for producing hydrogen starts hydrogen manufacturing, the hydrogen partial that device for producing hydrogen is obtained is or/and residual air is run by burning maintenance device for producing hydrogen;
The hydrogen that described device for producing hydrogen obtains is delivered to membrane separation unit and is separated, and is more than or equal to 0.7M Pa for separating of the difference of pressure inside and outside the membrane separation unit of hydrogen;
Described membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy or palladium yttrium alloys, and coatings is palladium-silver alloy or palladium yttrium alloys, and the mass percent palladium of palladium-silver alloy or palladium yttrium alloys accounts for 75% ~ 78%, and silver or yttrium account for 22% ~ 25%; Protium in hydrogen is isolated by described membrane separation unit, and the deuterium in hydrogen, tritium cannot be separated membrane separation unit, and deuterium, the tritium of failing to be separated are collected in addition; Temperature in membrane separation unit is set as 300 ~ 500 DEG C, and pressure is less than 5Mpa differential pressure and is no more than 15 kilograms;
Described hydrogen delivery tube road is provided with spring safety valve, and spring safety valve comprises valve body, spring device, end of upspringing; Described raw material conveying device comprises transferpump, and the switch-linear hybrid of end near transferpump of upspringing, can disconnect the switch of raw material conveying device when end of upspringing is upspring;
The switch of described transferpump comprises contact segment and three ports, and three ports are respectively the first port, the second port, the 3rd port;
One end of described contact segment is rotatably arranged at the first port, and the first port connects transferpump; The other end of contact segment can contact the second port or the 3rd port;
Described second port connects power supply, when the first port connects the second port, can control transferpump work;
Described 3rd port connects alarm transmitting device, and when the first port connects the 3rd port, can control to carry air pump inoperative, alarm transmitting device sends alarm message to corresponding server or client terminal simultaneously;
Described oxygen delivery devices provides oxygen by preparing, or only delivering oxygen;
Described water generation equipment comprises proton membrane, hydrogen prepared by reception hydrogen Preparation equipment, the oxygen of oxygen delivery devices conveying, obtained healthy water.
A kind of healthy water preparation system, described preparation system comprises: hydrogen handling equipment, membrane separation unit, oxygen delivery devices, water generation equipment;
Described hydrogen handling equipment obtains hydrogen by preparation, or only carries the hydrogen prepared; Hydrogen handling equipment junctional membrane tripping device, is isolated the protium in hydrogen by membrane separation unit, and deuterium in hydrogen, tritium cannot filter out from membrane separation unit;
Described oxygen delivery devices provides oxygen by preparing, or only carries the oxygen prepared;
Hydrogen prepared by described water generation equipment reception hydrogen Preparation equipment, the oxygen of oxygen delivery devices conveying, obtained healthy water.
As a preferred embodiment of the present invention, described membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy or palladium yttrium alloys, coatings is palladium-silver alloy or palladium yttrium alloys, the mass percent palladium of palladium-silver alloy or palladium yttrium alloys accounts for 75% ~ 78%, and silver or yttrium account for 22% ~ 25%.
As a preferred embodiment of the present invention, described hydrogen handling equipment comprises hydrogen Preparation equipment;
Described hydrogen Preparation equipment comprises: liquid container, raw material conveying device, device for rapidly starting, device for producing hydrogen, membrane separation unit, hydrogen delivery tube road;
Described device for producing hydrogen comprises interchanger, vaporizer, reformer chamber; Membrane separation unit is arranged in separate chamber, and separate chamber is arranged at the top of reformer chamber;
Described liquid container is connected with device for producing hydrogen; Liquid first alcohol and water is stored in liquid container;
Described hydrogen Preparation equipment utilizes device for rapidly starting to provide the startup energy to start; Device for rapidly starting comprises heating arrangements, gasification pipe, and the internal diameter of gasification pipe is 1 ~ 2mm, and gasification pipe is closely wound on heating arrangements; One end of described gasification pipe connects liquid container, is sent into by methyl alcohol in gasification pipe; The other end of gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches spontaneous ignition temperature, directly spontaneous combustion after methyl alcohol exports from gasification pipe; Described device for rapidly starting provides the startup energy for device for producing hydrogen; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyzer in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating;
After described device for producing hydrogen starts, device for producing hydrogen provides the energy needed for operation by the hydrogen that device for producing hydrogen obtains;
First alcohol and water in described liquid container is delivered to interchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and water vapour enter reformer chamber, and reformer chamber is provided with catalyzer, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C;
The temperature on described reformer chamber top is 400 DEG C ~ 500 DEG C; Reformer chamber is connected by connecting pipeline with separate chamber, all or part of top being arranged at reformer chamber of connecting pipeline, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting pipeline, as the buffering between reformer chamber and separate chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separate chamber or close;
Temperature in described separate chamber is set as 350 DEG C ~ 500 DEG C; Be provided with membrane separation apparatus in separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus;
Described raw material conveying device provides power, by the feedstock transportation in liquid container to device for producing hydrogen; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that device for producing hydrogen is obtained has enough pressure;
After described device for producing hydrogen starts hydrogen manufacturing, the hydrogen partial that device for producing hydrogen is obtained is or/and residual air is run by burning maintenance device for producing hydrogen;
The hydrogen that described device for producing hydrogen obtains is delivered to membrane separation unit and is separated, and is more than or equal to 0.7M Pa for separating of the difference of pressure inside and outside the membrane separation unit of hydrogen.
As a preferred embodiment of the present invention, described hydrogen delivery tube road is provided with spring safety valve, and spring safety valve comprises valve body, spring device, end of upspringing; Described raw material conveying device comprises transferpump, and the switch-linear hybrid of end near transferpump of upspringing, can disconnect the switch of raw material conveying device when end of upspringing is upspring;
The switch of described transferpump comprises contact segment and three ports, and three ports are respectively the first port, the second port, the 3rd port;
One end of described contact segment is rotatably arranged at the first port, and the first port connects transferpump; The other end of contact segment can contact the second port or the 3rd port;
Described second port connects power supply, when the first port connects the second port, can control transferpump work;
Described 3rd port connects alarm transmitting device, and when the first port connects the 3rd port, can control to carry air pump inoperative, alarm transmitting device sends alarm message to corresponding server or client terminal simultaneously.
A kind of healthy water preparation method, described preparation method comprises:
Hydrogen supplying step, carries out membrane sepn in the process of conveying; In membrane sepn step, by membrane separation unit, the protium in hydrogen is isolated, and deuterium in hydrogen, tritium cannot filter out from membrane separation unit;
Oxygen delivery step, provides oxygen by preparing, or only delivering oxygen;
Water generation step, receives the oxygen of hydrogen, oxygen delivery devices conveying, obtained healthy water.
As a preferred embodiment of the present invention, described membrane separation unit comprises palladium film alloy, membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy or palladium yttrium alloys, coatings is palladium-silver alloy or palladium yttrium alloys, the mass percent palladium of palladium-silver alloy or palladium yttrium alloys accounts for 75% ~ 78%, and silver or yttrium account for 22% ~ 25%.
A preparation method for above-mentioned healthy water preparation system, described preparation method comprises the steps:
Step S1, hydrogen preparation process, prepare hydrogen, specifically comprise:
-step S11, fast setting up procedure; Described hydrogen Preparation equipment utilizes device for rapidly starting to provide the startup energy to start; Specifically comprise:
Heating arrangements energising setting-up time, mechanism to be heated passes into methyl alcohol to gasification pipe after reaching design temperature; Because gasification pipe is closely wound on heating arrangements, methanol temperature progressively raises; Gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches spontaneous ignition temperature, directly spontaneous combustion after methyl alcohol exports from gasification pipe;
The methyl alcohol of gasification passes through combustion heat release, for device for producing hydrogen provides the startup energy; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyzer in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating;
After-step S12, hydrogen Preparation equipment start, hydrogen Preparation equipment provides the energy needed for operation by the hydrogen that device for producing hydrogen obtains; Treat that hydrogen Preparation equipment runs and obtain enough hydrogen, close device for rapidly starting, the hydrogen partial obtained by device for producing hydrogen is or/and residual air maintains device for producing hydrogen operation by burning; Hydrogen production process specifically comprises:
First alcohol and water in described liquid container is delivered to the interchanger heat exchange of device for producing hydrogen by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and water vapour enter reformer chamber, and reformer chamber is provided with catalyzer, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C;
The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting pipeline with separate chamber, all or part of top being arranged at reformer chamber of connecting pipeline, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting pipeline, as the buffering between reformer chamber and separate chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separate chamber or close;
Temperature in described separate chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separation apparatus in separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus; Described raw material conveying device provides power, by the feedstock transportation in liquid container to device for producing hydrogen; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that device for producing hydrogen is obtained has enough pressure; The hydrogen that described device for producing hydrogen obtains is delivered to membrane separation unit and is separated, and is more than or equal to 0.7M Pa for separating of the difference of pressure inside and outside the membrane separation unit of hydrogen; Described membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy, and coatings is palladium-silver alloy, and the mass percent palladium of palladium-silver alloy accounts for 75% ~ 78%, and silver accounts for 22% ~ 25%;
After-step S13, described device for producing hydrogen start hydrogen manufacturing, the hydrogen partial that device for producing hydrogen is obtained is or/and residual air is run by burning maintenance device for producing hydrogen;
Protium in hydrogen is isolated by-step S14, described membrane separation unit, and the deuterium in hydrogen, tritium cannot be separated membrane separation unit, and deuterium, the tritium of failing to be separated are collected in addition; Temperature in membrane separation unit is set as 300 ~ 500 DEG C, and pressure is less than 5Mpa differential pressure and is no more than 15 kilograms;
-step S15, through the isolated hydrogen of membrane separation unit enter hydrogen delivery tube road conveying, hydrogen delivery tube road is provided with spring safety valve; When hydrogen delivery tube road internal pressure is greater than set(ting)value, the end of upspringing of spring safety valve backs down the switch-linear hybrid of transferpump, disconnects the switch of raw material conveying device;
When hydrogen Preparation equipment is started working, the contact segment of switch connects the first port, the second port, raw material conveying device work; When end of upspringing is upspring, can back down being positioned at upspring end top contact segment, the one end due to contact segment is fixed on the first port revolvably, contact segment with the first port for axle center is rotated counterclockwise; Now, the other end of contact segment becomes connection the 3rd port, and raw material conveying device cannot work; Meanwhile, alarm transmitting device work can be driven because the first port connects the 3rd port by contact segment, send alarm message to corresponding server or client terminal, notify corresponding personnel;
Step S2, oxygen delivery step; There is provided oxygen by the mode of preparation, or only carry the oxygen prepared;
Step S3, receive the oxygen of hydrogen prepared by hydrogen Preparation equipment, oxygen delivery devices conveying, obtain healthy water by proton membrane.
Beneficial effect of the present invention is: the healthy water preparation system that the present invention proposes, and can prepare not containing the light-water with radioelement deuterium tritium, promotes the quality of the life of people, meets the demand of people to health.In addition, native system has portability, is convenient for people to carry.
Accompanying drawing explanation
Fig. 1 is the composition schematic diagram of healthy water preparation system of the present invention.
Fig. 2 is the composition schematic diagram of hydrogen Preparation equipment in healthy water preparation system of the present invention.
Fig. 3 is the structural representation of device for rapidly starting in hydrogen Preparation equipment
Fig. 4 is the structural representation of hydrogen Preparation equipment and heating pipe line thereof.
Fig. 5 is the composition schematic diagram of the hydrogen Preparation equipment being provided with safety valve.
Fig. 6 is the schematic diagram under the another kind of state of the hydrogen Preparation equipment being provided with safety valve.
Embodiment
The preferred embodiments of the present invention are described in detail below in conjunction with accompanying drawing.
Embodiment one
Refer to Fig. 1, present invention is disclosed a kind of healthy water preparation system, described preparation system comprises: hydrogen Preparation equipment 1, oxygen delivery devices 2, water generation equipment 3.Wherein, hydrogen Preparation equipment 1 is for the preparation of hydrogen and export, may also be only hydrogen handling equipment, only carry the hydrogen prepared, now hydrogen handling equipment junctional membrane tripping device, by membrane separation unit, the protium in hydrogen is isolated, and deuterium in hydrogen, tritium cannot filter out from membrane separation unit.Oxygen delivery devices provides oxygen by preparing, or only delivering oxygen; Water generation equipment comprises proton membrane, and hydrogen prepared by reception hydrogen Preparation equipment, the oxygen of oxygen delivery devices conveying, obtained healthy water, can also discharge electric energy simultaneously.
In the present embodiment, refer to Fig. 2, described hydrogen Preparation equipment 1 is small portable hydrogen producer, comprising: liquid container 10, raw material conveying device 50, device for rapidly starting 40, device for producing hydrogen 20, membrane separation unit 30, hydrogen delivery tube road 60.
As shown in Figure 3, described device for rapidly starting 40 comprises housing 41, heating arrangements 42, gasification pipe 43, and the internal diameter of gasification pipe 43 is 1 ~ 2mm, and gasification pipe 43 is wound on heating arrangements 42; Described heating arrangements can be electrically heated rod, utilizes alternating-current or store battery, drying battery.
One end of described gasification pipe 43 connects liquid container 10, is sent into by methyl alcohol in gasification pipe 43; The other end of gasification pipe 43 exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of gasification pipe 43 exports vaporized methyl alcohol, and the methanol temperature exported reaches spontaneous ignition temperature, and methyl alcohol exports rear direct spontaneous combustion from gasification pipe 43; Described device for rapidly starting 40 provides the startup energy for device for producing hydrogen (in other words whole hydrogen Preparation equipment).
Referring to Fig. 4, in order to improve the rate of heating of device for producing hydrogen, being provided with heating pipe line 21 at the reformer chamber inwall of described device for producing hydrogen 20, in heating pipe line 21, be placed with catalyzer (as can by heating and temperature control at 380 DEG C ~ 480 DEG C); Described device for rapidly starting 40 is reformer chamber heating by the described heating pipe line 21 of heating, can improve heating efficiency.
As shown in Figure 2, device for producing hydrogen 20 can also arrange the second starter gear 70, described second starter gear 70 comprises the second gasification pipe, and the main body of the second gasification pipe is arranged at reformer chamber, and the second gasification pipe is reformer chamber heating (can also be the heating of other unit of hydrogen Preparation equipment).First gasification pipe is or/and the methyl alcohol that the second gasification pipe exports is heat the second gasification pipe, by the methanol gasifying in the second gasification pipe while reformer chamber heats.Setting-up time after the second starter gear can continue the methyl alcohol of obtained gasification, can close above-mentioned device for rapidly starting, thus reduces the dependence to extra powers such as electric energy further.
In addition, described device for producing hydrogen 20 comprises interchanger, vaporizer, reformer chamber; Membrane separation unit is arranged in separate chamber, and separate chamber is arranged at the top of reformer chamber.Described liquid container is connected with device for producing hydrogen; Liquid first alcohol and water is stored in liquid container.
First alcohol and water in described liquid container is delivered to interchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and water vapour enter reformer chamber, and reformer chamber is provided with catalyzer, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C.The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting pipeline with separate chamber, all or part of top being arranged at reformer chamber of connecting pipeline, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting pipeline, as the buffering between reformer chamber and separate chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separate chamber or close.Temperature in described separate chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separation apparatus in separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus.By above-mentioned improvement, the low temperature requirements of reformer chamber catalyzer can be ensured respectively, and the high temperature requirement of separate chamber, and then improve hydrogen preparation efficiency; Meanwhile, preheating method of the present invention (separate chamber being arranged at the top of reformer chamber) is very convenient.
In addition, described raw material conveying device provides power, by the feedstock transportation in liquid container to device for producing hydrogen; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that device for producing hydrogen is obtained has enough pressure.The hydrogen that described device for producing hydrogen obtains is delivered to membrane separation unit and is separated, and is more than or equal to 0.7M Pa for separating of the difference of pressure inside and outside the membrane separation unit of hydrogen.By this improvement, the hydrogen that device for producing hydrogen is obtained has enough pressure, can improve the purity of hydrogen production efficiency and obtained hydrogen.
After described hydrogen Preparation equipment starts, hydrogen Preparation equipment provides the energy needed for operation by the hydrogen that device for producing hydrogen obtains; Now, device for rapidly starting can be closed.The hydrogen partial obtained due to device for producing hydrogen or/and residual air maintains the operation of hydrogen Preparation equipment by burning, thus can reduce the dependence to extra power, and adaptive ability is strong.
Study discovery through applicant, hydrogen through palldium alloy, can by having radioactive deuterium, tritium is separated with protium.Therefore, in the present invention, described membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy, and coatings is palladium-silver alloy (or palladium yttrium alloys), the mass percent palladium of palladium-silver alloy (or palladium yttrium alloys) accounts for 75% ~ 78%, and silver (or yttrium) accounts for 22% ~ 25%.The present invention utilizes this palladium membrane separation unit, and the purity of hydrogen is higher; And can by having radioactive deuterium in hydrogen, tritium is separated with protium.76%(mass percent is accounted at palladium), silver accounts for 24%(mass percent) time, separating effect is better.
In addition, refer to Fig. 5, Fig. 6, described hydrogen delivery tube road 60 is provided with spring safety valve 61, and spring safety valve 61 comprises valve body, spring device, end of upspringing; Described raw material conveying device 50 comprises transferpump, and the switch-linear hybrid (certain raw material conveying device 50 also can be other power set) of end near transferpump of upspringing, can disconnect the switch of raw material conveying device when end of upspringing is upspring.By arranging mechanical safety valve on hydrogen delivery tube road, when air pressure reaches set(ting)value, mechanical safety valve is opened, and can control raw material conveying device stopping transferring raw material.Thus the security of equipment operation can be improved, prevent hydrogen leak and blast.
Particularly, in the present embodiment, the switch of described transferpump comprises contact segment 62 and three ports, and three ports are respectively the first port 63, second port 64, the 3rd port 65.One end of described contact segment 62 is rotatably arranged at the first port 63, first port 63 and connects transferpump; The other end of contact segment 62 can contact the second port 64 or the 3rd port 65.
Described second port 64 connects power supply, when the first port 63 connects the second port 64, can control transferpump work.Described 3rd port 65 connects alarm transmitting device, when the first port connects the 3rd port 65, can control conveying air pump inoperative, alarm transmitting device sends alarm message (mode as by note) to corresponding server or client terminal simultaneously, can notify corresponding personnel.
It is very little that the volume of hydrogen Preparation equipment of the present invention, oxygen delivery devices all can design, thus can be convenient for people to carry.
The present invention also discloses a kind of preparation method of above-mentioned healthy water preparation system, and described preparation method comprises the steps:
[step S1] hydrogen preparation process, prepare hydrogen, specifically comprise:
-step S11, fast setting up procedure; Described hydrogen Preparation equipment utilizes device for rapidly starting to provide the startup energy to start; Specifically comprise:
Heating arrangements energising setting-up time, mechanism to be heated passes into methyl alcohol to gasification pipe after reaching design temperature; Because gasification pipe is closely wound on heating arrangements, methanol temperature progressively raises; Gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches spontaneous ignition temperature, directly spontaneous combustion after methyl alcohol exports from gasification pipe;
The methyl alcohol of gasification passes through combustion heat release, for device for producing hydrogen provides the startup energy; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyzer in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating;
After-step S12, hydrogen Preparation equipment start, hydrogen Preparation equipment provides the energy needed for operation by the hydrogen that device for producing hydrogen obtains; Treat that hydrogen Preparation equipment runs and obtain enough hydrogen, close device for rapidly starting, the hydrogen partial obtained by device for producing hydrogen is or/and residual air maintains device for producing hydrogen operation by burning; Hydrogen production process specifically comprises:
First alcohol and water in described liquid container is delivered to the interchanger heat exchange of device for producing hydrogen by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and water vapour enter reformer chamber, and reformer chamber is provided with catalyzer, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C;
The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting pipeline with separate chamber, all or part of top being arranged at reformer chamber of connecting pipeline, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting pipeline, as the buffering between reformer chamber and separate chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separate chamber or close;
Temperature in described separate chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separation apparatus in separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus; Described raw material conveying device provides power, by the feedstock transportation in liquid container to device for producing hydrogen; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that device for producing hydrogen is obtained has enough pressure; The hydrogen that described device for producing hydrogen obtains is delivered to membrane separation unit and is separated, and is more than or equal to 0.7M Pa for separating of the difference of pressure inside and outside the membrane separation unit of hydrogen; Described membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy, and coatings is palladium-silver alloy, and the mass percent palladium of palladium-silver alloy accounts for 75% ~ 78%, and silver accounts for 22% ~ 25%;
After-step S13, described device for producing hydrogen start hydrogen manufacturing, the hydrogen partial that device for producing hydrogen is obtained is or/and residual air is run by burning maintenance device for producing hydrogen;
Protium in hydrogen is isolated by-step S14, described membrane separation unit, and the deuterium in hydrogen, tritium cannot be separated membrane separation unit, and deuterium, the tritium of failing to be separated are collected in addition; Temperature in membrane separation unit is set as 300 ~ 500 DEG C, and pressure is less than 5Mpa differential pressure and is no more than 15 kilograms;
-step S15, through the isolated hydrogen of membrane separation unit enter hydrogen delivery tube road conveying, hydrogen delivery tube road is provided with spring safety valve; When hydrogen delivery tube road internal pressure is greater than set(ting)value, the end of upspringing of spring safety valve backs down the switch-linear hybrid of transferpump, disconnects the switch of raw material conveying device;
When hydrogen Preparation equipment is started working, the contact segment of switch connects the first port, the second port, raw material conveying device work; When end of upspringing is upspring, can back down being positioned at upspring end top contact segment, the one end due to contact segment is fixed on the first port revolvably, contact segment with the first port for axle center is rotated counterclockwise; Now, the other end of contact segment becomes connection the 3rd port, and raw material conveying device cannot work; Meanwhile, alarm transmitting device work can be driven because the first port connects the 3rd port by contact segment, send alarm message to corresponding server or client terminal, notify corresponding personnel;
[step S2] oxygen delivery step; There is provided oxygen by the mode of preparation, or only carry the oxygen prepared;
[step S3] receives the oxygen of hydrogen prepared by hydrogen Preparation equipment, oxygen delivery devices conveying, obtains healthy water by proton membrane.
Embodiment two
In the present embodiment, healthy water preparation system does not comprise hydrogen Preparation equipment, and only comprise hydrogen handling equipment, membrane separation unit, only carry the hydrogen prepared, now hydrogen handling equipment junctional membrane tripping device, by membrane separation unit, the protium in hydrogen is isolated, and deuterium in hydrogen, tritium cannot filter out from membrane separation unit.
Certainly, healthy water preparation system can also comprise oxygen Preparation equipment, Preparation of oxygen.Oxygen Preparation equipment is also provided with palladium alloy membrane tripping device (structural similitude that can be a kind of with embodiment), the radio isotope in oxygen can be separated with 16O, make the tap water of people safer.
In sum, the healthy water preparation system that the present invention proposes, can prepare not containing the light-water with radioelement deuterium tritium, promotes the quality of the life of people, meets the demand of people to health.In addition, native system has portability, is convenient for people to carry.
Here description of the invention and application is illustrative, not wants by scope restriction of the present invention in the above-described embodiments.Distortion and the change of embodiment disclosed are here possible, are known for the replacement of embodiment those those of ordinary skill in the art and the various parts of equivalence.Those skilled in the art are noted that when not departing from spirit of the present invention or essential characteristic, the present invention can in other forms, structure, layout, ratio, and to realize with other assembly, material and parts.When not departing from the scope of the invention and spirit, can other distortion be carried out here to disclosed embodiment and change.
Claims (8)
1. a healthy water preparation system, is characterized in that, described preparation system comprises: hydrogen Preparation equipment, oxygen delivery devices, water generation equipment;
Described hydrogen Preparation equipment comprises: liquid container, raw material conveying device, device for rapidly starting, device for producing hydrogen, membrane separation unit, hydrogen delivery tube road;
Described device for producing hydrogen comprises interchanger, vaporizer, reformer chamber; Membrane separation unit is arranged in separate chamber, and separate chamber is arranged at the top of reformer chamber;
Described liquid container is connected with device for producing hydrogen; Liquid first alcohol and water is stored in liquid container;
Described hydrogen Preparation equipment utilizes device for rapidly starting to provide the startup energy to start; Device for rapidly starting comprises heating arrangements, gasification pipe, and the internal diameter of gasification pipe is 1 ~ 2mm, and gasification pipe is closely wound on heating arrangements; One end of described gasification pipe connects liquid container, is sent into by methyl alcohol in gasification pipe; The other end of gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches spontaneous ignition temperature, directly spontaneous combustion after methyl alcohol exports from gasification pipe; Described device for rapidly starting provides the startup energy for device for producing hydrogen; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyzer in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating;
After described device for producing hydrogen starts, device for producing hydrogen provides the energy needed for operation by the hydrogen that device for producing hydrogen obtains;
First alcohol and water in described liquid container is delivered to interchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and water vapour enter reformer chamber, and reformer chamber is provided with catalyzer, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C;
The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting pipeline with separate chamber, all or part of top being arranged at reformer chamber of connecting pipeline, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting pipeline, as the buffering between reformer chamber and separate chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separate chamber or close;
Temperature in described separate chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separation apparatus in separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus;
Described raw material conveying device provides power, by the feedstock transportation in liquid container to device for producing hydrogen; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that device for producing hydrogen is obtained has enough pressure;
After described device for producing hydrogen starts hydrogen manufacturing, the hydrogen partial that device for producing hydrogen is obtained is or/and residual air is run by burning maintenance device for producing hydrogen;
The hydrogen that described device for producing hydrogen obtains is delivered to membrane separation unit and is separated, and is more than or equal to 0.7M Pa for separating of the difference of pressure inside and outside the membrane separation unit of hydrogen;
Described membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy or palladium yttrium alloys, and coatings is palladium-silver alloy or palladium yttrium alloys, and the mass percent palladium of palladium-silver alloy or palladium yttrium alloys accounts for 75% ~ 78%, and silver or yttrium account for 22% ~ 25%; Protium in hydrogen is isolated by described membrane separation unit, and the deuterium in hydrogen, tritium cannot be separated membrane separation unit, and deuterium, the tritium of failing to be separated are collected in addition; Temperature in membrane separation unit is set as 300 ~ 500 DEG C, and pressure is less than 5Mpa differential pressure and is no more than 15 kilograms;
Described hydrogen delivery tube road is provided with spring safety valve, and spring safety valve comprises valve body, spring device, end of upspringing; Described raw material conveying device comprises transferpump, and the switch-linear hybrid of end near transferpump of upspringing, can disconnect the switch of raw material conveying device when end of upspringing is upspring;
The switch of described transferpump comprises contact segment and three ports, and three ports are respectively the first port, the second port, the 3rd port;
One end of described contact segment is rotatably arranged at the first port, and the first port connects transferpump; The other end of contact segment can contact the second port or the 3rd port;
Described second port connects power supply, when the first port connects the second port, can control transferpump work;
Described 3rd port connects alarm transmitting device, and when the first port connects the 3rd port, can control to carry air pump inoperative, alarm transmitting device sends alarm message to corresponding server or client terminal simultaneously;
Described oxygen delivery devices provides oxygen by preparing, or only delivering oxygen;
Described water generation equipment comprises proton membrane, hydrogen prepared by reception hydrogen Preparation equipment, the oxygen of oxygen delivery devices conveying, obtained healthy water.
2. a healthy water preparation system, is characterized in that, described preparation system comprises: hydrogen handling equipment, membrane separation unit, oxygen delivery devices, water generation equipment;
Described hydrogen handling equipment obtains hydrogen by preparation, or only carries the hydrogen prepared; Hydrogen handling equipment junctional membrane tripping device, is isolated the protium in hydrogen by membrane separation unit, and deuterium in hydrogen, tritium cannot filter out from membrane separation unit;
Described oxygen delivery devices provides oxygen by preparing, or only carries the oxygen prepared;
Hydrogen prepared by described water generation equipment reception hydrogen Preparation equipment, the oxygen of oxygen delivery devices conveying, obtained healthy water.
3. healthy water preparation system according to claim 2, is characterized in that:
Described membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy or palladium yttrium alloys, and coatings is palladium-silver alloy or palladium yttrium alloys, and the mass percent palladium of palladium-silver alloy or palladium yttrium alloys accounts for 75% ~ 78%, and silver or yttrium account for 22% ~ 25%.
4. healthy water preparation system according to claim 2, is characterized in that:
Described hydrogen handling equipment comprises hydrogen Preparation equipment;
Described hydrogen Preparation equipment comprises: liquid container, raw material conveying device, device for rapidly starting, device for producing hydrogen, membrane separation unit, hydrogen delivery tube road;
Described device for producing hydrogen comprises interchanger, vaporizer, reformer chamber; Membrane separation unit is arranged in separate chamber, and separate chamber is arranged at the top of reformer chamber;
Described liquid container is connected with device for producing hydrogen; Liquid first alcohol and water is stored in liquid container;
Described hydrogen Preparation equipment utilizes device for rapidly starting to provide the startup energy to start; Device for rapidly starting comprises heating arrangements, gasification pipe, and the internal diameter of gasification pipe is 1 ~ 2mm, and gasification pipe is closely wound on heating arrangements; One end of described gasification pipe connects liquid container, is sent into by methyl alcohol in gasification pipe; The other end of gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches spontaneous ignition temperature, directly spontaneous combustion after methyl alcohol exports from gasification pipe; Described device for rapidly starting provides the startup energy for device for producing hydrogen; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyzer in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating;
After described device for producing hydrogen starts, device for producing hydrogen provides the energy needed for operation by the hydrogen that device for producing hydrogen obtains;
First alcohol and water in described liquid container is delivered to interchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and water vapour enter reformer chamber, and reformer chamber is provided with catalyzer, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C;
The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting pipeline with separate chamber, all or part of top being arranged at reformer chamber of connecting pipeline, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting pipeline, as the buffering between reformer chamber and separate chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separate chamber or close;
Temperature in described separate chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separation apparatus in separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus;
Described raw material conveying device provides power, by the feedstock transportation in liquid container to device for producing hydrogen; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that device for producing hydrogen is obtained has enough pressure;
After described device for producing hydrogen starts hydrogen manufacturing, the hydrogen partial that device for producing hydrogen is obtained is or/and residual air is run by burning maintenance device for producing hydrogen;
The hydrogen that described device for producing hydrogen obtains is delivered to membrane separation unit and is separated, and is more than or equal to 0.7M Pa for separating of the difference of pressure inside and outside the membrane separation unit of hydrogen.
5. healthy water preparation system according to claim 4, is characterized in that:
Described hydrogen delivery tube road is provided with spring safety valve, and spring safety valve comprises valve body, spring device, end of upspringing; Described raw material conveying device comprises transferpump, and the switch-linear hybrid of end near transferpump of upspringing, can disconnect the switch of raw material conveying device when end of upspringing is upspring;
The switch of described transferpump comprises contact segment and three ports, and three ports are respectively the first port, the second port, the 3rd port;
One end of described contact segment is rotatably arranged at the first port, and the first port connects transferpump; The other end of contact segment can contact the second port or the 3rd port;
Described second port connects power supply, when the first port connects the second port, can control transferpump work;
Described 3rd port connects alarm transmitting device, and when the first port connects the 3rd port, can control to carry air pump inoperative, alarm transmitting device sends alarm message to corresponding server or client terminal simultaneously.
6. a healthy water preparation method, is characterized in that, described preparation method comprises:
Hydrogen supplying step, carries out membrane sepn in the process of conveying; In membrane sepn step, by membrane separation unit, the protium in hydrogen is isolated, and deuterium in hydrogen, tritium cannot filter out from membrane separation unit;
Oxygen delivery step, provides oxygen by preparing, or only delivering oxygen;
Water generation step, receives the oxygen of hydrogen, oxygen delivery devices conveying, obtained healthy water.
7. healthy water preparation method according to claim 6, is characterized in that:
Described membrane separation unit comprises palladium film alloy, membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy or palladium yttrium alloys, coatings is palladium-silver alloy or palladium yttrium alloys, and the mass percent palladium of palladium-silver alloy or palladium yttrium alloys accounts for 75% ~ 78%, and silver or yttrium account for 22% ~ 25%.
8. a preparation method for healthy water preparation system described in claim 1, is characterized in that, described preparation method comprises the steps:
Step S1, hydrogen preparation process, prepare hydrogen, specifically comprise:
-step S11, fast setting up procedure; Described hydrogen Preparation equipment utilizes device for rapidly starting to provide the startup energy to start; Specifically comprise:
Heating arrangements energising setting-up time, mechanism to be heated passes into methyl alcohol to gasification pipe after reaching design temperature; Because gasification pipe is closely wound on heating arrangements, methanol temperature progressively raises; Gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches spontaneous ignition temperature, directly spontaneous combustion after methyl alcohol exports from gasification pipe;
The methyl alcohol of gasification passes through combustion heat release, for device for producing hydrogen provides the startup energy; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyzer in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating;
After-step S12, hydrogen Preparation equipment start, hydrogen Preparation equipment provides the energy needed for operation by the hydrogen that device for producing hydrogen obtains; Treat that hydrogen Preparation equipment runs and obtain enough hydrogen, close device for rapidly starting, the hydrogen partial obtained by device for producing hydrogen is or/and residual air maintains device for producing hydrogen operation by burning; Hydrogen production process specifically comprises:
First alcohol and water in described liquid container is delivered to the interchanger heat exchange of device for producing hydrogen by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and water vapour enter reformer chamber, and reformer chamber is provided with catalyzer, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C;
The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting pipeline with separate chamber, all or part of top being arranged at reformer chamber of connecting pipeline, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting pipeline, as the buffering between reformer chamber and separate chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separate chamber or close;
Temperature in described separate chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separation apparatus in separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus; Described raw material conveying device provides power, by the feedstock transportation in liquid container to device for producing hydrogen; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that device for producing hydrogen is obtained has enough pressure; The hydrogen that described device for producing hydrogen obtains is delivered to membrane separation unit and is separated, and is more than or equal to 0.7M Pa for separating of the difference of pressure inside and outside the membrane separation unit of hydrogen; Described membrane separation unit is the membrane separation unit at porous ceramic surface Vacuum Deposition palladium-silver alloy, and coatings is palladium-silver alloy, and the mass percent palladium of palladium-silver alloy accounts for 75% ~ 78%, and silver accounts for 22% ~ 25%;
After-step S13, described device for producing hydrogen start hydrogen manufacturing, the hydrogen partial that device for producing hydrogen is obtained is or/and residual air is run by burning maintenance device for producing hydrogen;
Protium in hydrogen is isolated by-step S14, described membrane separation unit, and the deuterium in hydrogen, tritium cannot be separated membrane separation unit, and deuterium, the tritium of failing to be separated are collected in addition; Temperature in membrane separation unit is set as 300 ~ 500 DEG C, and pressure is less than 5Mpa differential pressure and is no more than 15 kilograms;
-step S15, through the isolated hydrogen of membrane separation unit enter hydrogen delivery tube road conveying, hydrogen delivery tube road is provided with spring safety valve; When hydrogen delivery tube road internal pressure is greater than set(ting)value, the end of upspringing of spring safety valve backs down the switch-linear hybrid of transferpump, disconnects the switch of raw material conveying device;
When hydrogen Preparation equipment is started working, the contact segment of switch connects the first port, the second port, raw material conveying device work; When end of upspringing is upspring, can back down being positioned at upspring end top contact segment, the one end due to contact segment is fixed on the first port revolvably, contact segment with the first port for axle center is rotated counterclockwise; Now, the other end of contact segment becomes connection the 3rd port, and raw material conveying device cannot work; Meanwhile, alarm transmitting device work can be driven because the first port connects the 3rd port by contact segment, send alarm message to corresponding server or client terminal, notify corresponding personnel;
Step S2, oxygen delivery step; There is provided oxygen by the mode of preparation, or only carry the oxygen prepared;
Step S3, receive the oxygen of hydrogen prepared by hydrogen Preparation equipment, oxygen delivery devices conveying, obtain healthy water by proton membrane.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102897712A (en) * | 2012-09-13 | 2013-01-30 | 上海合既得动氢机器有限公司 | High efficiency methanol-water hydrogen production system and hydrogen production method thereof |
| CN103387210A (en) * | 2013-08-06 | 2013-11-13 | 上海合既得动氢机器有限公司 | System and method for producing hydrogen by methanol water |
| CN103613069A (en) * | 2013-11-18 | 2014-03-05 | 上海合既得动氢机器有限公司 | Methanol water hydrogen production system and method capable of rapidly starting |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102897712A (en) * | 2012-09-13 | 2013-01-30 | 上海合既得动氢机器有限公司 | High efficiency methanol-water hydrogen production system and hydrogen production method thereof |
| CN103387210A (en) * | 2013-08-06 | 2013-11-13 | 上海合既得动氢机器有限公司 | System and method for producing hydrogen by methanol water |
| CN103613069A (en) * | 2013-11-18 | 2014-03-05 | 上海合既得动氢机器有限公司 | Methanol water hydrogen production system and method capable of rapidly starting |
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Application publication date: 20151014 |