Hydrolysis hydrogen extractor

Abstract

The invention relates to a water-decomposed hydrogen extractor, which is a tower-shaped body thermal-contact hydrolysis hydrogen extractor which consists of an upper section and a lower section and is provided with an interlayer narrow cavity for containing water-state vaporized gas, a row of water absorption backflow pipes which are transversely and horizontally arranged are arranged in the middle of the lower section of the extractor, and a fuel combustion area is arranged below the through pipes. High-energy solid chemical energy and combustible chemical synthetic carbon replacing fuel are arranged on the through pipe, the through pipe is clamped and wrapped in the fuel for clamping combustion, the middle of the through pipe becomes red and high temperature, vacuum suction force is rapidly generated to permeate and suck water into the two ends of the through pipe, the water is sucked to the limit, heat shock is generated, liquid vaporized gas is rebounded out, and power is formed. And water vapor is pushed to rise and distribute in the whole machine body, circulates and is gradually gasified and upgraded until high-purity hydrogen is formed at the terminal, and the purposes of water inlet and hydrogen outlet are achieved.

Description

TECHNICAL FIELD

[0001] A hydrolysis hydrogen extractor that extracts hydrogen using pure water, in particular, a high-energy solid chemical energy combustible synthetic carbon is used as a fixed alternative heating source. The alternative heating source is started by the existing original fuel combustion to drive the synthesis of carbon red of the solid compound, and the red synthetic carbon continues to burn to produce heat, expand heat, and increase the temperature, forcing the water entering the device to rapidly absorb heat and react to convert into hydrogen. BACKGROUND

[0002] Hydrogen in nature is the cleanest energy source known to man, it comes from water and is colorless, odorless, non-toxic, and has no side effects. It is the first natural resource for the survival of life on earth and the ultimate energy resource for the survival and reproduction of future generations. Its significance lies in the current energy transition process. Using water as a raw material to produce hydrogen energy is the only unique choice. For this reason, the inventor has been researching how to separate or mix the hydrogen and oxygen components in water directly into fuel, and how to use existing human production resources and energy carriers to adapt to a variety of new energy fuel combustion devices by slightly modifying the investment without increasing the investment. Therefore, the inventor focuses on the series of research on energy application and energy conversion system: In 2015, a "steam conversion hydrogen-oxygen premixed clean boiler" was disclosed, with patent number 2015102630236, and in 2019, a "water decomposition hydrogen boiler" was disclosed, with patent number 2019212284144. The above two exploratory creations can both obtain water decomposition and conversion into hydrogen, which can be directly burned as fuel. However, it was found that both have undesirable defects. One of the problems of the "steam conversion hydrogen-oxygen premixed clean boiler" is that the key technical structure of the steam conversion into hydrogen is the steam separation and modification dual-purpose steam reaction modifier, which is set beside the lower part of the furnace and has a distance from the fire point in the center of the furnace. Due to the existence of strong and weak fire during the operation of the boiler, the heat source is naturally unstable, and it does not meet the high-temperature and constant-temperature conditions required for water vapor heat absorption reaction, which makes this scheme impossible to establish.

[0003] The other "water decomposition hydrogen boiler" also has the following shortcomings: one is that a ring cylinder two-stage steam filter dryer is set in the upper part of the furnace of the boiler. Since the two-stage steam filter dryer is connected to all the steam of the boiler, when the steam is full, it forms a whole with the boiler, plays a role in filtering steam and drying, increases the degree of vaporization and atomization, and promotes the limited conversion of steam into hydrogen.

[0004] Second, the structure of the steam decomposition hydrogen generator connected with the steam is buried in the combustion stack at the center of the fire point of the furnace, and because the combustion stack is made of high-temperature material, it will continue to rise in temperature after being red after combustion, so that when the hydrogen generator starts to work to produce hydrogen, the components of the generator will become metal hydrogen, which will be burned and melted to break the circuit, and the hydrogen production will not be sustainable.

[0005] So far, the inventor understands the principle of boiler heating and explores the rule of water heat absorption reaction conversion into hydrogen; in order to further better and more simply make water rapidly absorb heat and react to convert into hydrogen, the inventor takes another path to "let water change into hydrogen at one touch" to realize that hydrogen energy is boiled water, completely opens a new chapter of hydrogen production history, and promotes the green revolution of energy transformation! Contain the increasingly deteriorating atmospheric environment, lead mankind to usher in a hydrogen energy society as soon as possible, and share the welfare of the hydrogen energy society!

[0006] In order to achieve the above purpose, the technical scheme adopted by the present application is as follows. SUMMARY

[0007] The technical scheme of the present application is: according to the principle of water endothermic reaction and molecular increase reaction conversion into hydrogen, the definition of the present scheme is water hot reaction decomposition method: the following is the composition of the technical scheme structure: the body of the water hydrolysis hydrogen extractor is divided into two sections: the lower section is the combustion high temperature water absorption reaction conversion into hydrogen section, and the upper section is the high temperature radiation hydrogen-based fluid drying section; the lower section combustion high temperature water absorption reaction conversion into hydrogen section is composed of: a liquid water vapor mixed interlayer cylindrical shell, a row of transverse horizontal arranged through pipes connected with the liquid water vapor in the interlayer narrow cavity of the cylindrical shell, and a pipe-in-pipe capable of absorbing water and keeping moist which is composed of calcium-based materials and has a strength equivalent to argillaceous ceramic is fitted into the lumen of the through pipes; the upper half of the body of the narrow cavity of the cylindrical shell above the through pipes is filled with combustible chemical synthetic carbon; the lower half of the body of the narrow cavity of the cylindrical shell below the through pipes is the fuel combustion zone, the fuel is combusted in the lower combustion zone, the combustion red through pipes arranged in the middle are combusted at the same time, and the combustion red through pipes above are filled with combustible chemical synthetic carbon to generate intense high temperature radiation; thus, the energy concentrated in the combustible chemical synthetic carbon in the lower section combustion is concentrated upwards to the upper section high temperature radiation hydrogen-based fluid drying section to promote drying and gasification; and the upper section high temperature radiation hydrogen-based fluid drying section is composed of: a tower-shaped body which is also connected with the lower section cylindrical shell and contains liquid vaporized gas in the interlayer narrow cavity, a set of double multi-turn spring rings and pipeline liquid vaporized gas decomposition drying gasification accelerator is arranged around the middle of the body of the tower-shaped body, and the accelerator is composed of the pipeline of the spring ring as the core main part: a shallow surface liquid vaporized gas connecting through honeycomb base is arranged at the lower part of the spring ring pipeline, and a balanced fire blocking thin layer disc top connecting liquid vaporized gas is arranged at the upper part of the spring ring pipeline; a through pipe connecting liquid vaporized gas is arranged between the middle of the lower surface of the thin layer disc top and the middle of the upper surface of the thin layer disc top and the middle space of the inner ring of the spring ring pipeline, and a straight-through pipe-in-pipe pipeline space channel is arranged in the lumen of the through pipe; the two heavy ring heads of the outer heavy and inner heavy of the double multi-turn spring ring pipeline are connected through the two ports of the ring heads, and the two heads of the pipeline penetrating through the thin layer disc top are connected through the two heads of the pipeline penetrating through the thin layer disc top;One end of the tube is connected to the top of the cylindrical interlayer narrow cavity container for liquid gasification gas, and the other end extends to the top of the cylindrical interlayer tower and rotates into the space channel of the pipe-in-pipe pipeline to the lower end. A compression decomposer is arranged at the pipe head port of the space channel lower end. The compression decomposer is composed of a circle tube closely attached to the middle of the bottom surface of the honeycomb-shaped bottom plate. The circle tube is equally divided into left and right halves. Two symmetrical inlets are drilled in the middle of the tube boundary. One of the inlets is connected to the double spring coil pipe of the pipe-in-pipe pipeline. The other inlet is connected to a pipe head with the same diameter as the circle tube. The outlet of the pipe head is connected to a variable small pipe outside the bottom of the cylindrical interlayer narrow cavity container for liquid gasification gas. The compression decomposer (i.e. the circle tube) is arranged with the lower surface of the circle tube closely attached to the bottom surface of the honeycomb-shaped bottom plate. The bottom surface of the circle tube is parallel to the bottom of the cylindrical interlayer narrow cavity container for liquid gasification gas. The body of the water decomposition hydrogen extractor is divided into two sections. The two sections are combined by flexible docking, pipe joint, and corner locking. The water supply scheme of the water decomposition hydrogen extractor is as follows: the upper section is the high-temperature hydrogen-based fluid drying zone. The water is introduced into the lower section through an automatic water inlet. The water is then introduced into the lower part of the liquid water vapor mixing interlayer cylindrical shell. The water is then absorbed by the mud pipe-in-pipe in the middle of the interlayer narrow cavity. The middle of the pipe and the pipe-in-pipe is heated by the fire. The middle of the pipe and the pipe-in-pipe is naturally heated to a high temperature. The high-temperature vacuum in the middle section prevents water vapor circulation. The static suction force formed by the high-temperature vacuum naturally absorbs water into the pipe. The water is heated to a high temperature and then converted into hydrogen. The hydrogen is then pushed out to form a power source. The structure of the interlayer cylindrical shell is a water-scarce, large-thin water package fire heating scene. The hydrogen-oxygen mixture generated by the pipe-in-pipe is expanded and accelerated. The reaction components in the hydrogen-oxygen mixture increase, forming multiple chemical reactions. The liquid gasification gas is rapidly developed and distributed throughout the body to circulate and operate. The gasification is gradually upgraded until the high-purity hydrogen gas is formed at the terminal. The purpose of water entering and hydrogen exiting is achieved. The world's natural energy distribution is uneven. It benefits all mankind.

[0008] Compared with the prior art, the present application has the following obvious advantages: the hydrogen raw material used is water, which is rich in resources and has low cost, and no catalyst is added in the hydrogen production process, reducing the cost burden of catalytic materials; the primary energy consumed in the hydrogen production process is a kind of alternative energy, combustible synthetic carbon, which can replace 70% of the fuel combustion heat value, and can be used for a lifetime without melting, while filtering and intercepting the pollution sources from air and fuel in the combustion process, and has high heat value, low cost, no pollution, high temperature and constant temperature, which ensures the heat required for the hydrogen production process, not only that; the hydrogen production mechanical carrier is simple, small, flexible and low in cost, and the hydrogen production efficiency is high, which can achieve the demand for hydrogen production while water is supplied, and is more convenient for on-demand and local conditions, and has strong mobility, which is not restricted by any objective factors, and can randomly organize the production mode of hydrogen production and supply hydrogen as needed, solving the problems of transportation, storage, safety, convenience and good use of hydrogen in the use process, greatly reducing the cost of hydrogen, greatly reducing the threshold of hydrogen production, stimulating the popularization and development of hydrogen energy industry, and welcoming the early arrival of hydrogen energy society! Let all mankind share the welfare of hydrogen energy society! BRIEF DESCRIPTION OF DRAWINGS

[0009] Further description will be given below in combination with the drawings.

[0010] The drawing is a schematic structural diagram of an embodiment of the present application.

[0011] A preferred embodiment of the present application is shown in the drawing. DETAILED DESCRIPTION

[0012] It is a tower body that contains liquid water vapor and is divided into two sections by a sandwiched cavity. The lower section is a hydrogen extraction device that is heated by water absorption reaction. The upper section is a hydrogen-based fluid drying section. The lower section is composed of a liquid water vapor mixed sandwiched cylindrical shell 9. A row of horizontal transverse pipes 6 is arranged in the middle of the inner space of the cylindrical shell 9. Each pipe 6 has a pipe-in-pipe 4 made of calcium-based material that is equivalent to the strength of mud ceramic. The pipe-in-pipe 4 is embedded in the cavity of the pipe 6. The upper part of the cylindrical shell 9 is filled with combustible chemical synthetic carbon 7. The lower part of the cylindrical shell 9 is a fuel combustion zone. The fuel is burned in the lower combustion zone, which sets the row of horizontal transverse pipes 6 in the middle on fire. This produces intense high-temperature heat radiation, which ignites the combustible chemical synthetic carbon 7 filled above the pipes 6. The energy from the combustion of the combustible chemical synthetic carbon 7 is radiated upward, promoting drying and gasification in the upper hydrogen-based fluid drying section 10. The upper section is composed of a cylindrical sandwiched cavity that contains liquid water vapor and is connected to the lower section cylindrical shell 9. A double multi-turn spring coil pipe gasification accelerator is arranged in the body of the tower 15. The number of turns of the gasification accelerator is determined by the volume of the device. The optimal solution is double thirty turns. The gasification accelerator is composed of spring coil pipes 16 and 17. A shallow surface honeycomb base 24 is arranged at the lower part of the core components spring coil pipes 16 and 17. A thin layer of plate top 22 is arranged at the upper part of the core components spring coil pipes 16 and 17. A vertical tube 18 is arranged between the middle of the lower bottom surface of the thin layer of plate top 22 and the upper bottom surface of the shallow surface honeycomb base 24. A straight tube-in-pipe 19 is arranged in the middle of the inner cavity space of the tube 18. The two ends of the double thirty turns spring coil pipes 16 and 17 are connected to the outer heavy 16 and the inner heavy 17.respectively one pipe head access cylinder type interlayer narrow cavity container liquid gasification gas tower body 15 top and liquid gasification gas connected through, another pipe head extends in the cylinder type interlayer tower body 15 top rotary into the pipe in pipe 19 pipe cavity space channel to the lower end, the pipe head port setting a gasification compression decomposer in the space channel lower end; The composition of gasification compression decomposer is: a circle through pipe 11 is closely attached to the middle of the bottom surface of the through fire honeycomb bottom disc 24, the pipe body of circle through pipe 11 is equally divided into left and right boundary, the middle of the pipe body boundary is symmetrically two-way inboard, each excavates a circle through pipe 11 diameter 1 / 4 through hole, one of the through holes is connected with the port of one end pipe head 21 of double thirty turns spring ring pipe inner ring 17 from the lower pipe in pipe, pipe cavity space channel lower end by corresponding pipe 26 90 degree turn; The other through hole is connected with a pipe head 12 with the same diameter of circle through pipe, the pipe head 12 is connected with a variable small pipe outside the bottom of the cylinder type interlayer narrow cavity container liquid gasification gas tower body 15, so that the whole gasification compression decomposer is closely attached to the pipe surface of circle through pipe 11 on the bottom surface of the through fire honeycomb bottom disc, the downward bottom surface of circle through pipe 11 is parallel to the bottom of cylinder type interlayer narrow cavity container liquid gasification gas tower body 15, and the downward bottom surface of circle through pipe 11 is required to be parallel to the bottom of tower body 15, which is used to match and isolate the upper surface of synthetic carbon 7 in lower section 5, so that it can obtain appropriate constant temperature to realize hydrogen production, avoid the damage of key hydrogen production device of through pipe 11 caused by ultra-high temperature, and affect the establishment of the hydrogen production scheme.The hydrogen-oxygen mixture generated in the pipe-in-pipe 4 is accelerated by incremental expansion, and the increasing reaction components in the hydrogen-oxygen mixture form multiple chemical reactions, which rapidly develop into liquid vaporization gas that rises into the water pipe head 13 connected to the upper section 10, links through the water vapor channel 14 into the honeycomb-shaped bottom plate 24 and the upper thin layer plate top 22, and then enters the channel 23 and the upper section 10, pushing and distributing throughout the machine body to circulate and operate, gradually gasifying and upgrading until high-purity hydrogen gas is formed at the terminal, while the liquid vaporization gas in the machine body forms a circulating operation that opens a small gas separation pipe 8 on either side of the top of the upper section 10, which is the tower body 15, and introduces a small amount of liquid vaporization gas into the lower section 5, which is connected to the pipe 6 in the middle of the cylindrical shell 9, and outputs it to the top of the chemical synthesis carbon 7, which contains a catalyst component, and absorbs the reaction and converts it into hydrogen gas, which is self-combusted and self-heated, thereby reducing the consumption of primary energy, balancing the ultra-high temperature, and intercepting dust and improving fuel quality to eliminate pollution. To further improve thermal efficiency and save energy, a dry high-temperature heat expansion constant temperature insulation layer 2 composed of a semiconductor material is installed on the outer wall of the cylindrical shell 9 in the lower section 5, which promotes the combustion of high-temperature constant temperature and achieves energy saving, improves thermal efficiency, and reduces the cost of hydrogen production.

Claims

1. A water splitting hydrogen extractor, characterized in that: It consists of a tower-shaped body (1) of a hydrothermal hydrogen extractor with a narrow cavity containing liquid vaporized water, divided into upper and lower sections: the lower section is the section (5) where high-temperature combustion and water absorption reaction converts into hydrogen; the upper section is the section (10) where high-temperature radiation and hydrogen-based fluid drying occurs. The lower section (5) is composed of a cylindrical shell (9) containing liquid water vapor. A row of horizontally arranged pipes (6) connected to the liquid water vapor in the middle of the inner space of the cylindrical shell (9) is provided. Each pipe (6) has a tube-in-tube (4) made of calcium-based material with a water-absorbing and moisturizing strength equivalent to that of clay ceramic phases. The upper part of the cylindrical shell (9) above the pipes (6) is equipped with a device. The container is filled with combustible chemical synthetic carbon (7); the lower part of the cylindrical shell (9) below the pipe (6) is the fuel combustion zone. The fuel burns in the lower combustion zone, and the combustible chemical synthetic carbon (7) filled with combustible chemical synthetic carbon (7) in the middle is ignited and generates intense high-temperature heat radiation. In this way, the energy of the combustible chemical synthetic carbon (7) burning up from below is radiated upwards to the upper section of the high-temperature radiant hydrogen-based fluid drying section (10) to promote drying and gasification. The upper section of the high-temperature radiant hydrogen-based fluid drying section (10) is composed of a cylindrical interlayer narrow cavity connected to the lower interlayer cylindrical shell (9) and a tower-shaped body (15) that can pass through liquid vaporized gas. A gasification accelerator for the decomposition, drying, and vaporization of liquid vaporized gas is installed inside the tower-shaped body (15) with a double multi-rotation spring coil pipe: the setting of the double multi-rotation speed of the gasification accelerator is determined according to the volume of the body, and the optimal scheme is double thirty rotations. The gasification accelerator is constructed with spring coil pipes (16) and (17) as the core components: a shallow-surface ignition honeycomb-shaped base (24) for connecting liquid vaporized gas is set at the lower part of the spring coil pipes (16) and (17) of the core components, and a thin-layer plate top (22) for balancing and blocking the flame and connecting liquid vaporized gas is set at the upper part of the spring coil pipes (16) and (17) of the core components. The middle of the lower bottom surface of the thin-layer plate top (22) and the middle of the upper bottom surface of the lower ignition honeycomb-shaped base (24) are located at the middle of the lower bottom surface of the thin-layer plate top (22) and the upper bottom surface of the lower ignition honeycomb-shaped base (24). Between the three of the inner rings of the spring coil pipes (16) and (17), a vertically connected pipe (18) for liquid vaporized gas is set. In the middle of the inner cavity of the pipe (18), between the middle of the upper top surface of the thin-layer plate (22) and the middle of the lower bottom surface of the honeycomb base (24), a straight channel of the inner cavity of the pipe-in-pipe (19) is set. At the same time, the ports of the outer weight (16) and the inner weight (17) of the double thirty-turn spring coil pipes (16) and (17) arranged around the middle are connected to form a single line. The upper ends of the double thirty-turn spring coil pipes (16) and (17) pass through the upper balance fireproof thin-layer plate (22) and the two pipe ends that pass through the top of the thin-layer plate (22).One pipe head is connected to the top of the cylindrical sandwich tower (15) that carries liquid vaporized gas and is connected to the liquid vaporized gas. The other pipe head extends from the top of the cylindrical sandwich tower (15) and rotates into the inner cavity of the pipe-in-pipe (19) to the lower end. A vaporization and compression decomposer is installed at the pipe head port at the lower end of the space channel. The vaporization and compression decomposer is composed of a circular pipe (11) that is closely attached to the middle of the bottom surface of the fire-propelled honeycomb base (24). The pipe body of the circular pipe (11) is divided into two equal halves. In the middle of the pipe body, two openings are symmetrically drilled on the inner sides, each opening being 1 / 4 of the diameter of the circular pipe (11). One of the openings is connected to a corresponding pipe (26). The tube turns 90 degrees and connects to the end of the inner ring (17) of the double 30-turn spring coil pipe (17) that comes out from the lower end of the inner cavity of the pipe. The other opening is connected to a pipe head (12) with the same diameter as the circular tube. The lower end of the pipe head (12) is connected by a variable small tube that passes through the bottom side of the tower-shaped body (15) in the cylindrical interlayer narrow cavity to carry liquid vaporized gas and exits to the outside outlet. The overall arrangement of the vaporization and compression decomposer is that the tube surface of the circular tube (11) is pressed tightly against the bottom surface of the fire-connecting honeycomb base, and the bottom surface of the circular tube (11) is flush with the bottom of the tower-shaped body (15) in the cylindrical interlayer narrow cavity to carry liquid vaporized gas. The bottom surface of the tube (11) is required to be flush with the bottom surface of the tower-shaped body. The purpose of making the bottom of the body (15) flat is to achieve a perfect fit and isolation with the top of the synthetic carbon (7) in the lower section (5), so that it can achieve a suitable constant temperature for hydrogen production, while avoiding damage to the key hydrogen production device of the through pipe (11) due to excessively high temperature, which would affect the establishment of this hydrogen production scheme. At the same time, the method of dividing the body (1) of the above-mentioned water splitting hydrogen extractor into upper and lower sections and then recombining them is to use a flat loading and unloading method for flexible docking; the water pipe joints (13) with two water vapor connections set on the left and right sides of the outer walls of the upper and lower sections of the body (1) and the two corner buckles set at the front and back are used for positioning and shaping; and the water supply scheme of this water splitting hydrogen extractor is: in the lower part of the tower-shaped body (15) of the upper section of the high-temperature radiation hydrogen-based fluid drying section (10), the water supply is supplied through the... While the flow rate is limited by the automatic water inlet device (25), the water is guided by the diversion pipe (3) to the lower part of the jacketed cylindrical shell (9) of the section (5) where the high-temperature water absorption reaction of combustion is converted into hydrogen. The water rises to the two ends of the water-absorbing and moisturizing tube (4) embedded in a row of horizontally arranged through pipes (6) in the middle of the jacketed cylindrical shell (9) of section (5). Because the middle of the through pipe (6) and the embedded water-absorbing and moisturizing tube (4) is encased and burned by the intense fire, the middle of the through pipe (6) and the tube (4) is naturally heated red-hot, forming a high-temperature vacuum in the middle of the tube, which prevents the water vapor from circulating. This generates static suction, which draws water into the tube at both ends. When the water reaches its limit, it is heated and explodes into hydrogen, rebounds and exits, generating the power to do work.Because the structure of the sandwiched cylindrical shell (9) is a thin water-filled fire combustion heating scenario formed by the narrow cavity of the sandwiched shell with little water and a large surface area; then the hydrogen-oxygen mixture generated in the tube-in-tube (4) increases in expansion and accelerates, and the increase in the reactive components in the hydrogen-oxygen mixture forms a variety of chemical reaction effects, and the rapidly developed liquid vaporized gas rises to the water pipe connector (13) connected to the water vapor and enters the lower part of the sandwiched cavity of the upper section (10), and enters the honeycomb chassis (24) and the upper thin-layer disk top (22) through the water vapor channel (14), and then connects with the upper part of the upper section (10) through the channel (23) to promote the circulation of the entire machine body, gradually vaporizing and upgrading until the terminal forms high-purity hydrogen gas, and at the same time forming a circulating liquid in the machine body. A small steam distribution pipe (8) is opened on any side of the top of the upper section (10), i.e., the tower-shaped body (15). A small amount of liquid vaporized gas is introduced into the lower part of the lower section (5) through the small pipe (8) and output to the chemically synthesized carbon (7) above it through the pipe (6) located in the middle of the cylindrical shell (9). The liquid vaporized gas is absorbed and converted into hydrogen by the ultra-high temperature of the chemically synthesized carbon containing catalyst components. It is self-burned and self-heated, thereby reducing the consumption of primary energy. At the same time, it plays a role in balancing the ultra-high temperature and intercepting dust to modify the fuel and eliminate pollution. Secondly, in order to further improve thermal efficiency and save energy, a dry high-temperature heat expansion constant temperature insulation layer (2) made of semiconductor material is set on the outer wall of the lower section (5) cylindrical shell (9).

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