Equipment for producing hydrogen by electrolyzing water vapor and acid mist and control method

Abstract

The invention discloses equipment for producing hydrogen by electrolyzing water vapor and acid mist and a control method. When the U-shaped device for producing hydrogen by electrolyzing water vapor and acid mist is used, water vapor and carbon dioxide enter the U-shaped steel container, and the carbon dioxide is absorbed by the water vapor and becomes carbonic acid mist. When the inverted-T-shaped electrolytic water vapor acid mist hydrogen production device is used, coal powder in the coal cinder circulating fluidized bed furnace burns, generated flue gas heats coal water slurry, and a large amount of water vapor is generated. Direct current with low-voltage high-frequency alternating current harmonic waves is introduced between the anode and the cathode, the carbonic acid mist is separated into carbonate anion liquid drops and hydrogen cation liquid drops, and the carbonate anion liquid drops with negative charges quickly move to the anode to release oxygen and carbon dioxide; and the hydrogen cation liquid drops with positive charges quickly move to the cathode to release hydrogen. In the convex-shaped electrolytic water vapor acid mist hydrogen production device, water vapor reacts with 700 DEG C pulverized coal to generate hydrogen and carbon monoxide, and oxygen reacts with the pulverized coal to generate carbon dioxide.

Description

Technical field:

[0001] The invention relates to a device for producing hydrogen by electrolyzing water vapor and acid mist and a control method thereof. Background technology:

[0002] Purified water is an insulating material. The power supply bureau uses purified water cannons to flush the insulating ceramic bottles on high-voltage power towers. Because purified water is an insulating material, hydrogen cannot be produced by electrolysis. Sodium hydroxide must be added to this process. The efficiency of water electrolysis is very low—only 13%. The remaining 87% of the electrical energy is converted into heat. At normal pressure, water above 100°C absorbs the heat of vaporization and turns into water vapor. As the temperature of the water vapor increases, the pressure increases, necessitating the use of high-strength, high-temperature-resistant sealing materials in water electrolysis equipment. Internet information suggests that the efficiency of hydrogen production by electrolysis of water vapor at 800°C can reach 50%. This is because the proportion of water vapor ionized into ions at this temperature is extremely high. Heating water to 800°C is very inefficient, and the pressure of water vapor at 800°C is also very high, making sealing the 800°C vapor difficult. This method of producing hydrogen by electrolysis is therefore extremely costly.

[0003] Patent No. ZL201110377552.0, "Automobile Waste Heat Power Generation Device," Background Technology: Sourced from Yiyan.com, "New Alloy Can Directly Convert Heat into Electricity," describes a new non-magnetic alloy material. When a copper plate beneath it is slightly heated, the new alloy suddenly becomes strongly magnetic. Researchers at the University of Minnesota have discovered a new alloy with unique properties that can directly convert heat into electricity. Composed of iron, nickel, cobalt, manganese, and tin, the alloy can exhibit either non-magnetic or strong magnetic properties depending on the temperature. According to a University of Minnesota press release, under certain conditions, the new alloy—Ni45C05Mn40Sn10—undergoes a reversible phase transition: when the temperature changes, one type of solid transforms into another. Specifically, the new alloy changes from non-magnetic to strongly magnetic, requiring only a slight increase in temperature. When the heated new alloy is placed near a permanent magnet, such as a rare earth magnet, its magnetic force suddenly and dramatically increases. Current is generated in the surrounding coil. Researchers say this new alloy has low hysteresis, a process that causes heat loss. This allows it to convert significant amounts of waste heat into electricity. This material has obvious potential applications in automobile exhaust pipes. Some automakers are already developing heat exchangers that can convert exhaust into usable electricity. One automaker is using an alloy called skutterudite, which is a mixture of rare earth-doped cobalt and arsenic.

[0004] Patent No. ZL201110377552.0 "Automobile Waste Heat Power Generation Device", the automobile waste heat power generation device (6) consists of a thermomagnetic power generation stator, an excitation coil, a generator coil and a magnetic circuit silicon steel sheet round tube. The thermomagnetic power generation stator core is made of a silicon steel sheet base part and a thermomagnetic alloy sheet magnetic pole part welded together to form an alloy insulation sheet stacked together. The thermomagnetic alloy is a non-magnetic material below 70°C and a magnetic material above 70°C. The thermomagnetic alloy has very small magnetic hysteresis. The magnetic poles of the thermomagnetic power generation stator are on the outside. The slots of the thermomagnetic power generation stator open to the outside. After the thermomagnetic alloy becomes a magnetic material, the magnetic field strength rapidly doubles under the guidance of the guide magnetic field; the excitation coil and the generator coil are installed in the slots of the thermomagnetic power generation stator. The magnetic circuit silicon steel sheet round tube is made of annular insulating silicon steel sheets stacked and then sleeved on a steel pipe. The silicon steel sheet round tube with the shell magnetic circuit is sleeved on the outside of the thermomagnetic power generation stator. Summary of the invention:

[0005] A device for producing hydrogen by electrolyzing water vapor and acid mist. The device consists of a U-shaped steel container with a ceramic lining, a left microporous ceramic plate, an oxygen container, a right microporous ceramic plate, a hydrogen container, an anode, a cathode, a halogen quartz lamp, a ceramic fiber insulation layer, and an outer shell. The left raised portion of the U-shaped steel container houses the left microporous ceramic plate and the oxygen container, while the right raised portion houses the right microporous ceramic plate and the hydrogen container. The U-shaped steel container houses an array of anodes and cathodes. The anode structure is as follows: a flat glass fiber woven bag filled with graphite pellets or graphene powder is mounted vertically below a flat oxygen hood. A glass fiber woven tube covered with a silicone rubber film extends from the top of the flat oxygen hood and is connected below the left microporous ceramic plate on the raised portion of the U-shaped steel container. The cathode structure is as follows: a flat glass fiber woven bag filled with graphite pellets or graphene powder is vertically installed under the flat hydrogen cover, and a glass fiber woven tube covered with a silicone rubber film is connected from the top of the flat hydrogen cover to the bottom of the right microporous ceramic plate on the right convex part of the "concave" shaped steel container; several halogen quartz lamps 3 are installed at the bottom of the "concave" shaped steel container.

[0006] A hydrogen production device using electrolysis of water vapor and acid mist. An oxygen pipe extending from an oxygen container mounted on the raised portion on the left side of a concave-shaped steel container is connected to the inlets of the stator pole heating pipes of the oxygen thermomagnetic generator. Several oxygen pipes extending from the stator pole heating pipes of the oxygen thermomagnetic generator are connected to the inlets of the heat channels of the water cooler of the oxygen thermomagnetic generator. Several oxygen pipes extending from the heat channels of the water cooler of the oxygen thermomagnetic generator are connected to the bottom of the condensate container of the water cooler of the oxygen thermomagnetic generator. A water pipe extending from the bottom of the condensate container of the water cooler of the oxygen thermomagnetic generator is connected to the inlet of the oxygen condensate pump. A water pipe extending from the oxygen condensate pump is connected to the inlet of the oxygen condensate check valve. A water pipe extending from the oxygen condensate check valve is connected to the top inlet of the concave-shaped steel container. The oxygen pipe connected from the top of the condensed water container of the water cooler of the oxygen thermomagnetic power generation device is connected to the inlet of the oxygen compressor, the oxygen pipe connected from the oxygen compressor is connected to the inlet of the hot channel of the oxygen cooling dryer, the oxygen pipe connected from the hot channel of the oxygen cooling dryer is connected to the bottom inlet of the carbon dioxide condensation container of the oxygen cooling dryer, the oxygen pipe connected from the top of the carbon dioxide condensation container of the oxygen cooling dryer is connected to the inlet of the oxygen one-way valve, and the oxygen pipe connected from the oxygen one-way valve is connected to the top inlet of the oxygen tank; the top of the oxygen tank is equipped with an electromagnetic exhaust valve and an oxygen pressure relay. The hydrogen pipe connected from the hydrogen container installed on the raised part on the right side of the "concave" shaped steel container is connected to the inlet of each stator pole heating pipe of the hydrogen thermomagnetic power generation device, several hydrogen pipes connected from the stator pole heating pipes of the hydrogen thermomagnetic power generation device are connected to several hot channel inlets of the water cooler of the hydrogen thermomagnetic power generation device, several hydrogen pipes connected from the several hot channels of the water cooler of the hydrogen thermomagnetic power generation device are connected to the bottom of the condensate water container of the water cooler of the hydrogen thermomagnetic power generation device, the water pipe connected from the bottom of the condensate water container of the water cooler of the hydrogen thermomagnetic power generation device is connected to the inlet of the hydrogen condensate water pump, the water pipe connected from the hydrogen condensate water pump is connected to the inlet of the hydrogen condensate water one-way valve, and the water pipe connected from the hydrogen condensate water one-way valve is connected to the top inlet of the "concave" shaped steel container. The hydrogen pipes exiting from the bottom and top of the condensate container of the water cooler of the hydrogen thermomagnetic power generation device are connected to the inlet of the hydrogen compressor. The hydrogen pipes exiting from the hydrogen compressor are connected to the inlet of the hydrogen cooling dryer. The hydrogen pipes exiting from the hydrogen cooling dryer are connected to the inlet of the hydrogen check valve. The hydrogen pipes exiting from the hydrogen check valve are connected to the inlet of the top of the hydrogen tank. The top of the hydrogen tank is equipped with a solenoid exhaust valve and a pressure relay.

[0007] A device for producing hydrogen by electrolyzing water vapor and acid mist. A water pipe extending from the lower side of a water tank is connected to the inlet of a water pump. Branch water pipes extending from the water pump are connected to the inlet of the cooling water jacket of the oxygen cooling dryer 12, the inlet of the cooling water jacket of the hydrogen cooling dryer, the inlet of the cooling water jacket of the water cooler of the oxygen thermomagnetic generator, and the inlet of the cooling water jacket of the water cooler of the hydrogen thermomagnetic generator. The water pipes extending from the cooling water jackets of the oxygen cooling dryer, hydrogen cooling dryer, oxygen thermomagnetic generator, and hydrogen thermomagnetic generator are connected to the inlet of a one-way water valve. The water pipe extending from the one-way water valve is connected to the top water inlet of the preheating tank of a fuel oil boiler. Inside the fuel oil boiler, from top to bottom, are the preheating tank, the steam generation tank, the steam heating coil, and the fuel oil burner. The water pipe extending from the bottom of the preheating tank of the fuel oil boiler is connected to the bottom water inlet of the steam generation tank of the fuel oil boiler. The oil-fired boiler's steam generator tank is equipped with a liquid level sensor probe, a pressure relay, and a temperature sensor probe. The steam pipe from the top of the oil-fired boiler's steam generator tank is connected to the inlet of the oil-fired boiler's steam heating coil, which in turn is connected to the inlet of the electric steam control valve. A steam pressure sensor probe is installed in the center of the top of the concave-shaped steel container. Several branching steam inlet pipes extend from the bottom of the container, and the steam pipes from the electric steam control valve are connected to the inlets of several branching steam inlet pipes located at the bottom of the concave-shaped steel container.

[0008] A device for producing hydrogen by electrolyzing water vapor and acid mist. A pH sensor probe is installed in the middle section of the top of a concave-shaped steel container. Several branching carbon dioxide inlet pipes are located at the bottom of the container. The air pipe extending from the top of the carbon dioxide storage tank is connected to the inlet of the carbon dioxide solenoid valve. The branching air pipes extending from the carbon dioxide solenoid valve are connected to the inlets of the branching carbon dioxide inlet pipes at the bottom of the container. A liquid carbon dioxide pipe extending from the bottom of the carbon dioxide condensation container of the oxygen cooling dryer is connected to the inlet of the liquid carbon dioxide solenoid valve. The liquid carbon dioxide pipe extending from the liquid carbon dioxide solenoid valve is then connected to the bottom of the carbon dioxide storage tank.

[0009] During summer in northern China and spring to autumn in southern China, temperatures exceed 30°C (112°F). Water vapor in the air vibrates violently and rises rapidly, separating into negatively charged anion droplets and positively charged cation droplets. Under the influence of a strong electric field, the negatively charged anion droplets coalesce to form negatively charged anion clouds, while the positively charged cation droplets coalesce to form positively charged cation clouds. Negatively charged anion clouds discharge to the earth, producing lightning. Positively charged cation clouds discharge to the earth, producing lightning. Lightning is also generated by discharges between positively charged cation clouds and negatively charged anion clouds.

[0010] In foggy and hazy weather, the insulating ceramic bottles on the high-voltage power towers emit electromagnetic radiation and produce sparks.

[0011] Pure water is an insulator, and pure water vapor is an even stronger insulator. The pH of pure water is neutral, and pure water is a weakly polar molecule. Hydrogen is produced by electrolysis of pure water vapor: A window on the right side of the outer surface of a "concave"-shaped glass container is not fitted with a stainless steel mesh. Microwaves generated by a microwave generator enter the container through a metal tube and are stirred by the emitting blades inside the container, causing the water vapor inside to oscillate. A positive DC electrode is installed below the raised portion on the left side of the container, while a negative DC electrode is installed below the raised portion on the right side. A high-voltage DC current is passed between the positive and negative DC electrodes via a computer controller, causing the oscillating water vapor molecules to separate into negatively charged hydroxyl anion droplets and positively charged hydrogen cation droplets. Under the influence of a strong steady electric field and a weak alternating electric field, the oscillating water vapor molecules in the "concave"-shaped glass container separate into negatively charged hydroxyl anion droplets and positively charged hydrogen cation droplets. The negatively charged hydroxyl anion droplets migrate rapidly toward the positive DC electrode, where they lose electrons and release oxygen. The positively charged hydrogen cation droplets migrate rapidly toward the negative DC electrode, where they gain electrons and release hydrogen. Because pure water is a weakly polar molecule, the strong steady electric field and weak alternating electric field result in a very small number of negatively charged hydroxyl anion droplets and positively charged hydrogen cation droplets. Under the influence of a strong steady electric field and a weak alternating electric field, the oscillating water vapor molecules in the "concave"-shaped glass container separate into negatively charged hydroxyl anion droplets and positively charged hydrogen cation droplets. The oscillating water vapor molecules separate into negatively charged hydroxyl anion droplets and positively charged hydrogen cation droplets. The negatively charged hydroxyl anion droplets quickly migrate toward the positive DC electrode, where they lose electrons and release oxygen. The positively charged hydrogen cation droplets quickly migrate toward the negative DC electrode, where they gain electrons and release hydrogen. However, the yield is very low and has no practical value.

[0012] A control method for hydrogen production equipment using electrolytic water vapor and acid mist. A computer controller activates a water pump, which pumps water from the lower side of a water tank into the cooling water jacket of the oxygen cooling dryer, the cooling water jacket of the hydrogen cooling dryer, the cooling water jacket of the water cooler of the oxygen thermomagnetic generator, and the cooling water jacket of the water cooler of the hydrogen thermomagnetic generator. Water exiting the cooling water jackets of the oxygen cooling dryer, the hydrogen cooling dryer, the cooling water jacket of the water cooler of the oxygen thermomagnetic generator, and the cooling water jacket of the water cooler of the hydrogen thermomagnetic generator passes through a one-way water valve and enters the top of the preheating tank of the fuel-fired boiler, and then into the bottom of the water vapor generation tank of the fuel-fired boiler. When a liquid level sensor probe installed in the water vapor generation tank of the fuel-fired boiler detects that the water level inside the water vapor generation tank has reached a set high water level, the computer controller stops powering the water pump. The one-way water valve prevents water in the preheating tank of the fuel-fired boiler from being pushed into the water tank through the cooling water jackets of the oxygen cooling dryer, the hydrogen cooling dryer, the cooling water jacket of the water cooler of the oxygen thermomagnetic generator, the cooling water jacket of the water cooler of the hydrogen thermomagnetic generator, and the water pump. The computer controller ignites the oil-fired boiler's oil burner. The flame from the burner heats the steam inside the boiler's steam heating coil, the steam generator tank, and the water in the preheating tank. The hot oil-fired boiler's steam generator tank produces a large amount of steam. When the pressure relay mounted on top of the steam generator tank detects that the steam pressure inside the tank reaches the set pressure, the computer controller powers the electric steam control valve, causing the motor to rotate forward and the valve to gradually open from closed. Steam from the top of the steam generator tank passes through the steam heating coil and enters the gradually opening electric steam control valve. Steam exiting the gradually opening electric steam control valve enters a concave-shaped steel container. When the pressure relay mounted on top of the steam generator tank detects that the steam pressure inside the tank exceeds the set high pressure, the computer controller reduces the throttle of the oil-fired boiler's burner. When the pressure relay mounted on top of the oil-fired boiler's steam generator detects that the steam pressure inside the tank has dropped below the set low pressure, the computer controller increases the throttle of the oil-fired boiler's oil burner. When the liquid level sensor probe mounted inside the tank detects that the water level inside the tank has dropped below the set low pressure, the computer controller restarts the water pump. When the steam pressure sensor mounted on the top of the middle section of the "concave"-shaped steel container detects that the steam pressure inside the container has exceeded the set high pressure, the computer controller reverses the motor of the electric steam control valve, adjusting the valve from high to low.When the water vapor pressure sensor mounted on the top of the middle section of the "concave"-shaped steel container detects that the water vapor pressure inside the container falls below the set low pressure value, the computer controller controls the electric steam control valve's motor to rotate forward, adjusting the valve from low to high. When the water vapor pressure sensor mounted on the top of the middle section of the "concave"-shaped steel container detects that the water vapor pressure inside the container reaches the set high pressure value, the computer controller energizes the CO2 solenoid valve. CO2 exiting the top of the CO2 storage tank passes through the energized CO2 solenoid valve and enters the "concave"-shaped steel container. It is absorbed by the water vapor inside the container and becomes carbonic acid mist. When the pH sensor probe mounted on the top of the middle section of the "concave"-shaped steel container detects that the pH value of the carbonic acid mist inside the container falls below the set low pressure value, the computer controller stops energizing the CO2 solenoid valve. When the pH sensor probe installed in the center of the top of the "concave"-shaped steel container detects that the pH of the carbonate mist within the container exceeds the set upper limit, the computer controller reenergizes the CO2 solenoid valve. Carbonic acid and sulfurous acid are moderately strong acids, while carbonate and sulfurous acid are moderately polar molecules. Separating the polar carbonate mist droplets within the "concave"-shaped steel container into carbonate anion droplets and hydrogen cation droplets requires only that the computer controller supply a low-voltage, high-frequency AC harmonic (not too high) DC current between the positive and negative DC terminals within the container. The computer controller then supplies a low-voltage, high-frequency AC harmonic DC current between the anode and cathode within the container, powering the halogen quartz lamp. The low-voltage, high-frequency AC current causes the polar carbonate mist droplets within the container to oscillate and generate heat. Under the influence of a strong steady electric field and a weak alternating electric field, the polar droplets of carbonate mist at 130-150°C within the concave-shaped steel container separate into negatively charged carbonate anion droplets and positively charged hydrogen cation droplets. The strong light from the halogen quartz lamp reduces the DC voltage, AC voltage, and frequency required for separation (the ionosphere decreases during the day and increases at night). The negatively charged carbonate anion droplets rapidly migrate toward anode 1, where they lose electrons and release oxygen and carbon dioxide. Most of the carbon dioxide is absorbed by the water vapor droplets, forming carbonate mist. However, the concentration of free carbon dioxide gas near anode 1 within the concave-shaped steel container remains high. The Chinese character for "water vapor" (qi) is composed of three water drops (water) plus one (qi), indicating that water vapor molecules are composed of multiple water molecules. However, the water in air is a single gaseous water molecule, while carbonate mist is composed of droplets composed of multiple water vapor molecules.The computer controller activates the oxygen compressor at a set time. Air, along with a small amount of gaseous water molecules and carbon dioxide molecules, within the concave-shaped steel container passes through the oxygen container mounted on the raised portion of the left side of the concave-shaped container. The oxygen exiting the oxygen container enters the stator pole heating tubes of the oxygen thermomagnetic generator, heating the stator poles and converting them from non-magnetic to magnetic. The computer controller then applies alternating current to the stator excitation coils of the oxygen thermomagnetic generator. The generator converts the thermal energy into magnetic energy. Under the influence of the alternating magnetic field of the stator poles, amplified electrical energy is generated in the stator coils. The oxygen exiting the stator pole heating tubes is further cooled in the hot channel of the water cooler and then enters the bottom of the condensate tank of the water cooler. Water exiting the bottom of the condensate tank of the oxygen-magnetic generator's water cooler enters the oxygen condensate pump. The computer controller activates the oxygen condensate pump at a set time. Water from the oxygen condensate pump passes through the oxygen condensate check valve and is pressed into a concave-shaped steel container. Oxygen exiting the top of the condensate tank of the oxygen-thermomagnetic generator's water cooler is drawn into the oxygen compressor. Oxygen exiting the oxygen compressor enters the hot channel of the oxygen cooling dryer for cooling. Oxygen exiting the hot channel enters the bottom of the oxygen cooling dryer's carbon dioxide condensate tank. Oxygen exiting the top of the oxygen cooling dryer's carbon dioxide condensate tank enters the oxygen check valve, and oxygen exiting the check valve enters the oxygen tank. During initial use, the computer controller energizes the oxygen tank solenoid exhaust valve to vent air from the oxygen compressor, oxygen-thermomagnetic generator, oxygen cooling dryer, and oxygen tank. Then, the oxygen tank solenoid exhaust valve is closed. Liquid carbon dioxide exiting the bottom of the oxygen cooling dryer's carbon dioxide condensate tank enters the liquid carbon dioxide solenoid valve. The liquid carbon dioxide pipe exiting the liquid carbon dioxide solenoid valve enters the bottom of the carbon dioxide storage tank. Under the influence of a strong steady electric field and a weak alternating electric field, the polar droplets of carbonic acid mist within the concave-shaped steel container separate into negatively charged carbonate anion droplets and positively charged hydrogen cation droplets. The positively charged hydrogen cation droplets migrate rapidly toward the cathode, where they gain electrons and release hydrogen gas. Because the negatively charged carbonate anion droplets migrate rapidly toward the anode, the concentration of free carbon dioxide gas near the cathode within the concave-shaped steel container remains low. The Chinese character for "water vapor" (qi) is composed of three water drops (shui) plus one (qi), meaning that water vapor molecules are composed of multiple water molecules. However, the moisture in air is a single gaseous water molecule, whereas carbonic acid mist is composed of droplets composed of multiple water vapor molecules.The computer controller activates the hydrogen compressor. The air and a small amount of gaseous water molecules within the concave-shaped steel container pass through the microporous ceramic plate mounted on the right raised portion of the concave steel container and enter the hydrogen container mounted on the right raised portion of the concave steel container. The hydrogen exiting the hydrogen container enters the stator pole heating tubes of the hydrogen thermomagnetic generator, heating the stator poles and converting them from non-magnetic to magnetic. The computer controller then applies alternating current to the stator excitation coil of the hydrogen thermomagnetic generator. The hydrogen thermomagnetic generator converts the thermal energy into magnetic energy. Under the influence of the alternating magnetic field of the stator poles, amplified electrical energy is generated in the stator generator coil. Hydrogen exiting the stator pole heating tubes of the hydrogen thermomagnetic generator is further cooled in the hot channel of the water cooler. It then enters the bottom of the condenser tank. Water exiting the condenser tank enters the hydrogen condensate pump, which is activated by a computer controller at a set time. Water exiting the pump passes through a condensate check valve and is then pressed into a concave steel container. Hydrogen exiting the top of the condensate tank is drawn into the hydrogen compressor. The hydrogen exiting the compressor enters the hot channel of the hydrogen cooling dryer for cooling. It then enters the hydrogen check valve and enters the hydrogen tank. When using the computer controller for the first time, energize the electromagnetic exhaust valve of the hydrogen tank, discharge the air from the hydrogen compressor, hydrogen thermomagnetic generator, hydrogen cooling dryer and hydrogen tank, and then close the electromagnetic exhaust valve of the hydrogen tank.

[0013] A device for producing hydrogen by electrolyzing water vapor and acid mist. The convex-shaped device consists of an artificial graphite anode tube, a foam ceramic tube, an artificial graphite cathode tube, a microporous ceramic tube, a large cast iron pipe shell, a large cast iron pipe chimney, a small cast iron pipe chimney, and a small cast iron pipe shell. The upper layer of the convex-shaped device, from inside to outside, consists of the large cast iron pipe chimney, the foam ceramic tube, a circle of small cast iron pipe chimneys, and the small cast iron pipe shell. The lower layer of the convex-shaped device, from inside to outside, consists of the artificial graphite anode tube, the foam ceramic tube, a circle of artificial graphite cathode tubes, the microporous ceramic tube, and the large cast iron pipe shell. The large cast iron pipe chimney has the same diameter as the artificial graphite anode tube and is attached to the artificial graphite anode tube via an insulating ceramic connecting tube. The small cast iron chimney has the same diameter as the artificial graphite cathode tube and is mounted on top of it via an insulating ceramic connecting tube. The gap between the large cast iron chimney and the small cast iron tube shell is filled with coal-water slurry, the gap between the artificial graphite anode tube and the microporous ceramic tube is filled with coal powder, and the gap between the microporous ceramic tube and the large cast iron tube shell is filled with calcium hydroxide powder. Several radiation chimneys are installed horizontally between the large cast iron chimney and a circle of small cast iron chimneys. A target is installed in the gap between the lower ends of the artificial graphite anode tube and the microporous ceramic tube. Below the target is a slag chamber. The lower ends of the artificial graphite anode tube and a circle of several artificial graphite cathode tubes pass through the bottom of the slag chamber. An insulating ceramic sleeve is installed between the lower ends of the artificial graphite anode tube and the lower ends of the circle of several artificial graphite cathode tubes and the bottom of the slag chamber. An electric cinder valve is installed at the bottom of the cinder chamber between the lower end of the artificial graphite anode tube and the lower end of a ring of artificial graphite cathode tubes. The electric cinder valve consists of a left half-annular valve disc, a front hinge, a front DC motor, a right half-annular valve disc, a rear hinge, and a rear DC motor. The left and right half-annular valve discs are hinged at a diameter. The front section of the left half-annular valve disc is fixed to the front hinge shaft, which is fixedly connected to the front DC motor shaft. The rear section of the right half-annular valve disc is fixed to the rear hinge shaft, which is fixedly connected to the rear DC motor shaft. An electric calcium hydroxide powder cover is installed at the upper end of the gap between the microporous ceramic tube and the large cast iron tube shell. The electric calcium hydroxide powder cover consists of the left half-annular valve disc, a left output shaft, a left DC motor, the right half-annular valve disc, a right output shaft, and a right DC motor. The top of the outer arc of the left half of the annular cover is fixed to the center of the left output shaft, which is fixedly connected to the left DC motor shaft. The top of the outer arc of the right half of the annular cover is fixed to the center of the right output shaft, which is fixedly connected to the right DC motor shaft. An electric calcium hydroxide powder valve is installed at the lower end of the gap between the microporous ceramic tube and the large cast iron tube shell.The electric calcium hydroxide powder valve is constructed as follows: It consists of a left half annular valve disc, a left output shaft, a left DC motor, a right half annular valve disc, a right output shaft, and a right DC motor. The top of the outer arc of the left half annular valve disc is fixed to the center of the left output shaft, which is fixedly connected to the left DC motor shaft. The top of the outer arc of the right half annular valve disc is fixed to the center of the right output shaft, which is fixedly connected to the right DC motor shaft.

[0014] A device for producing hydrogen by electrolyzing water vapor and acid mist. The water pipe leading from the lower side of the water tank is connected to the water pump inlet, which in turn is connected to the inlet of an electric regulating water valve. Branch water pipes from the electric regulating water valve are connected to the cooling jacket inlets of the mixed gas thermomagnetic generator water cooler and the mixed gas cooling separator, respectively. The water pipes leading from the cooling jackets of the mixed gas thermomagnetic generator water cooler and the mixed gas cooling separator are connected to the top left inlet of the electric coal-water slurry mixing and extrusion kettle. The coal powder hopper is equipped with an electric rotary butterfly valve. The coal powder hopper is located to the upper left of the starting point of the electric belt conveyor, which terminates at the left inlet of the top of the electric coal-water slurry mixing and extrusion kettle. The bottom outlet of the electric coal-water slurry mixing and extrusion kettle and the outlet of the electric coal-water slurry screw extrusion conveyor are connected via a special-shaped elbow to the gap between the large cast iron pipe chimney and the upper end of the small cast iron pipe shell.

[0015] A hydrogen production device based on electrolysis of water vapor and acid mist. A foamed cast iron plate is installed at the gas outlet of a large cast iron pipe housing. A mixed gas pipe extending from the gas outlet of the large cast iron pipe housing is connected to the inlet of the stator pole heating pipes of a mixed gas thermomagnetic generator. Several mixed gas pipes extending from the stator pole heating pipes of the mixed gas thermomagnetic generator are connected to the inlet of several hot channels of the water cooler of the mixed gas thermomagnetic generator. Several mixed gas pipes extending from the hot channels of the water cooler of the mixed gas thermomagnetic generator 41 are connected to the bottom of the condensate container of the water cooler of the mixed gas thermomagnetic generator. A water pipe extending from the bottom of the condensate container of the water cooler of the mixed gas thermomagnetic generator 1 is connected to the inlet of a mixed gas condensate pump. A water pipe extending from the mixed gas condensate pump is connected to the inlet of a mixed gas condensate check valve. A water pipe extending from the mixed gas condensate check valve is connected to the top inlet of a water tank. The mixed gas pipe leading from the top of the condensate water container of the mixed gas thermomagnetic power generation device is connected to the inlet of the mixed gas compressor. The mixed gas pipe leading from the mixed gas compressor is connected to the inlet of the hot channel of the mixed gas cooling separator. The mixed gas pipe leading from the hot channel of the mixed gas cooling separator is connected to the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator. The liquid carbon dioxide pipe leading from the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator is connected to the inlet of the liquid carbon dioxide solenoid valve. The liquid carbon dioxide pipe leading from the liquid carbon dioxide solenoid valve is connected to the bottom of the carbon dioxide storage tank. The hydrogen pipe leading from the top of the condensed liquid carbon dioxide tank of the mixed gas cooling separator is connected to the inlet of the hydrogen check valve. The hydrogen pipe leading from the hydrogen check valve is connected to the inlet at the top of the hydrogen tank. The top of the hydrogen tank is equipped with a solenoid exhaust valve and a pressure relay.

[0016] A hydrogen production device that electrolyzes water vapor and acid mist. A basin-shaped steel mesh is installed below the slag chamber, allowing slag to fall into the slag circulating fluidized bed furnace. An ash pipe is installed below the center hole of the slag circulating fluidized bed furnace's basin-shaped steel mesh. The air duct outlet from the electric blower is located below the slag circulating fluidized bed furnace's basin-shaped steel mesh.

[0017] A control method for a hydrogen production device using electrolysis of water vapor and acid mist. The electric cinder valve installed at the bottom of the cinder chamber between the lower end of an artificial graphite anode tube and the lower end of a ring of artificial graphite cathode tubes is closed. The electric calcium hydroxide powder valve installed at the lower end of the gap between the microporous ceramic tube and the outer shell of a large cast iron pipe is also closed. A computer controller supplies reverse DC power to the left and right DC motors of the electric calcium hydroxide powder cover, causing the left half annular valve disc and the right half annular cover to rotate upward by a set angle, opening the valve. The computer controller then stops supplying reverse DC power to the front and rear DC motors of the electric calcium hydroxide powder valve. The gap between the microporous ceramic tube and the outer shell of the large cast iron pipe is filled with calcium hydroxide powder. The computer controller then supplies forward DC power to the left and right DC motors of the electric calcium hydroxide powder cover, causing the left half annular valve disc and the right half annular cover to rotate downward by a set angle, closing the valve. The computer controller then stops supplying forward DC power to the left and right DC motors of the electric calcium hydroxide powder cover. Some coal powder is placed on the basin-shaped steel wire mesh of the coal slag circulating fluidized bed furnace. Diesel fuel is sprayed onto the coal powder on the mesh, igniting the coal powder on the mesh. A computer controller activates an electric blower, which blows air upward from below the mesh, supporting the combustion of the coal powder on the mesh. The computer controller activates the electric rotary butterfly valve installed at the discharge port of the coal powder hopper 34, causing the coal powder in the hopper to leak to the beginning of an electric belt conveyor. The computer controller then activates the electric belt conveyor, which then delivers the coal powder to an electric water-coal slurry mixing and extrusion kettle. The computer controller starts the water pump and adjusts the electric regulating water valve. The water pump pumps water from the tank through the electric regulating water valve and presses it into the cooling water jacket of the mixed gas thermomagnetic generator water cooler and the cooling water jacket of the mixed gas cooling separator. The water from the cooling water jacket of the mixed gas thermomagnetic generator water cooler and the cooling water jacket of the mixed gas cooling separator enters the electric coal-water slurry mixing and extrusion kettle 37. The computer controller starts the electric coal-water slurry mixing and extrusion kettle, and the coal-water slurry, which initially contains a small amount of water, is pressed into the electric coal-water slurry screw extrusion conveyor. The computer controller starts the electric screw extrusion conveyor, which presses the coal-water slurry, which contains a small amount of water, through the elbow into the gap between the large cast iron pipe chimney and the upper end of the small cast iron pipe shell, and then into the gap between the artificial graphite anode tube and the microporous ceramic tube.The flue gas generated by the combustion of coal powder on the basin-shaped steel wire mesh of the coal slag circulating fluidized bed furnace passes through an artificial graphite anode tube and a ring of several artificial graphite cathode tubes, heating them and the coal-water slurry contained in the gap between the artificial graphite anode tube and the microporous ceramic tube, generating a large amount of water vapor that turns into red-hot coal powder. The flue gas then passes through a large cast iron chimney and a ring of several small cast iron chimneys, heating the coal-water slurry in the gap between the large chimney and the outer shell of the small cast iron tubes, generating a large amount of water vapor. A computer controller supplies a high-voltage direct current (DC) with harmonics of the low-voltage, high-frequency AC current between the artificial graphite anode tube and the artificial graphite cathode tube. This low-voltage, high-frequency AC current causes the water vapor between the artificial graphite anode tube and the artificial graphite cathode tube to oscillate, generating heat. Under the influence of a strong steady electric field and a weak alternating electric field, the water vapor between the artificial graphite anode tube and the artificial graphite cathode tube separates into negatively charged hydroxyl anion droplets and positively charged hydrogen cation droplets. The negatively charged hydroxyl anion droplets rapidly migrate toward the artificial graphite anode tube, where they lose electrons and release oxygen and water vapor. The positively charged hydrogen cation droplets rapidly migrate toward the artificial graphite cathode tube, where they gain electrons and release hydrogen. The oxygen reacts chemically with 400°C coal powder contained in the gap between the artificial graphite anode tube and the microporous ceramic tube to produce carbon dioxide, generating a large amount of heat. The oxygen also reacts chemically with the sulfur in the 400°C coal powder contained in the gap between the artificial graphite anode tube and the microporous ceramic tube to produce sulfur dioxide, generating a large amount of heat. The carbon dioxide is absorbed by the water vapor to form carbonic acid mist droplets, and the sulfur dioxide is absorbed by the water vapor to form sulfite mist droplets. A computer controller reduces the voltage of a direct current (DC) containing harmonics of low-voltage, high-frequency AC current, flowing between the artificial graphite anode tube and the artificial graphite cathode tube. This low-voltage, high-frequency AC current causes the carbonate mist droplets and sulfite mist droplets between the two tubes to oscillate and generate heat. Under the influence of a strong, steady electric field and a weak, alternating electric field, the polar carbonate mist droplets between the two tubes separate into negatively charged carbonate anion droplets and positively charged hydrogen cation droplets, while the polar sulfite mist droplets separate into negatively charged sulfite anion droplets and positively charged hydrogen cation droplets. The negatively charged carbonate anion droplets migrate rapidly toward the artificial graphite anode tube, where they lose electrons and release oxygen and carbon dioxide. The positively charged hydrogen cation droplets migrate rapidly toward the artificial graphite cathode tube, where they gain electrons and release hydrogen. The negatively charged sulfite anion droplets quickly move toward the artificial graphite anode tube, where they lose electrons and release oxygen and sulfur dioxide. The positively charged hydrogen cation droplets quickly move toward the artificial graphite powder cathode tube, where they gain electrons and release hydrogen.Water vapor reacts chemically with 700°C red-hot coal powder contained in the gap between the artificial graphite anode tube and the microporous ceramic tube to produce hydrogen and carbon monoxide, absorbing a significant amount of heat. At this high temperature, the carbon monoxide reacts with oxygen to produce carbon dioxide, also generating significant heat. A computer controller energizes the mixed gas compressor, which draws the mixed gas into the gap between the microporous ceramic tube and the large cast iron pipe shell. The mixed gas, containing gaseous water, passes through the micropores of the outer ceramic tube and enters the annular gap between the two. At this high temperature, sulfur dioxide reacts chemically with calcium hydroxide powder contained in the gap between the microporous ceramic tube and the large cast iron pipe shell to produce calcium sulfite and water. The mixed gas in the gap between the microporous ceramic tube and the large cast iron pipe shell is then drawn into the stator pole heating tubes of the mixed gas thermomagnetic generator, heating the stator poles and converting them from non-magnetic to magnetic. The computer controller supplies alternating current to the stator excitation coils of the mixed gas thermomagnetic generator. The mixed gas thermomagnetic generator converts thermal energy into magnetic energy. Under the influence of the alternating magnetic field of the stator magnetic poles, amplified electrical energy is generated in the stator generator coils. The mixed gas exiting the stator magnetic pole heating tubes of the mixed gas thermomagnetic generator is further cooled in the hot channel of the mixed gas thermomagnetic generator's water cooler. The mixed gas exiting the hot channel of the mixed gas thermomagnetic generator's water cooler enters the bottom of the condensate tank of the mixed gas thermomagnetic generator's water cooler. Water exiting the bottom of the condensate tank of the mixed gas thermomagnetic generator's water cooler enters the mixed gas condensate pump. The computer controller activates the mixed gas condensate pump at a fixed time. Water exiting the mixed gas condensate pump passes through a mixed gas condensate check valve and is pumped into the water tank. The mixed gas exiting the top of the condensate tank of the mixed gas thermomagnetic generator's water cooler enters the mixed gas compressor 44. The mixed gas exiting the mixed gas compressor is then pumped into the hot channel of the mixed gas cooling separator. The mixed gas exiting the hot channel of the mixed gas cooling separator is pressed into the bottom of the mixed gas cooling separator's condensed liquid CO2 tank. The high-pressure CO2 gas is cooled into liquid CO2, which remains at the bottom of the mixed gas cooling separator's condensed liquid CO2 tank. The computer controller periodically energizes and opens the liquid CO2 solenoid valve. The liquid CO2 at the bottom of the mixed gas cooling separator's condensed liquid CO2 tank passes through the open solenoid valve and enters the bottom of the CO2 storage tank. The computer controller then closes the solenoid valve. Hydrogen exiting the top of the mixed gas cooling separator's condensed liquid CO2 tank passes through a hydrogen check valve and is pressed into the hydrogen tank.During the initial stages of hydrogen production from water vapor and acid mist electrolysis, a computer controller energizes and opens the solenoid exhaust valve atop the hydrogen tank, exhausting air from the gap between the microporous ceramic tube and the large cast iron tube shell, the mixed gas thermomagnetic generator, the mixed gas compressor, the mixed gas cooling separator, and the hydrogen tank. The computer controller then closes the solenoid exhaust valve. Oxygen reacts chemically with the 700°C coal powder contained in the gap between the artificial graphite anode tube and the microporous ceramic tube to produce carbon dioxide, generating a significant amount of heat. Water vapor also reacts chemically with the 700°C coal powder contained in the gap between the artificial graphite anode tube and the microporous ceramic tube to produce hydrogen and carbon monoxide, absorbing a significant amount of heat. This consumes the carbon in the 700°C coal powder, resulting in coal slag that leaks through the furnace rake installed at the bottom of the gap between the artificial graphite anode tube and the microporous ceramic tube into the slag chamber. The computer controller stops powering the mixed gas compressor 44 and then supplies forward DC power to the front and rear DC motors of the electric slag valve, causing the left and right half annular valve discs to rotate downward and open. After the left and right half annular valve discs rotate downward by a set angle, the computer controller stops supplying forward DC power to the front and rear DC motors of the electric slag valve. The slag in the slag chamber is discharged onto the basin-shaped steel mesh of the slag circulating fluidized bed furnace, where it is mixed with the coal powder on the basin-shaped steel mesh and burned. After the slag in the slag chamber is discharged, the computer controller supplies reverse DC power to the front and rear DC motors of the electric slag valve, causing the left and right half annular valve discs to rotate upward by a set angle and close. The computer controller stops supplying reverse DC power to the front and rear DC motors of the electric slag valve and resumes powering the mixed gas compressor. At high temperatures, sulfur dioxide reacts chemically with the calcium hydroxide powder contained in the gap between the microporous ceramic tube and the large cast iron pipe shell to produce calcium sulfite and water vapor, consuming the calcium hydroxide powder contained in the gap between the microporous ceramic tube and the large cast iron pipe shell. The computer controller then stops powering the mixed gas compressor and provides positive DC power to the left and right DC motors of the electric calcium hydroxide powder valve, causing the left and right annular valve discs to rotate downward, opening the valve. After the left and right annular valve discs rotate downward to the set angle, the computer controller stops supplying positive DC power to the front and rear DC motors of the electric calcium hydroxide powder valve.The calcium hydroxide powder containing a large amount of calcium sulfite contained in the gap between the microporous ceramic tube and the large cast iron pipe shell is unloaded. After the calcium hydroxide powder containing a large amount of calcium sulfite contained in the gap between the microporous ceramic tube and the large cast iron pipe shell is unloaded, reverse DC power is supplied to the front and rear DC motors of the electric calcium hydroxide powder valve, causing the left half annular valve disc and the right half annular valve disc to rotate upward by a set angle to close. The computer controller stops supplying reverse DC power to the front and rear DC motors of the electric calcium hydroxide powder valve. The computer controller then supplies reverse DC power to the left and right DC motors of the electric calcium hydroxide powder cover, causing the left half annular valve disc and the right half annular cover to rotate upward by a set angle to open. The computer controller stops supplying reverse DC power to the front and rear DC motors of the electric calcium hydroxide powder valve. The gap between the microporous ceramic tube and the large cast iron pipe shell is filled with calcium hydroxide powder. The computer controller then provides positive DC power to the left and right DC motors of the electric calcium hydroxide powder cover, causing the left half of the annular valve disc and the right half of the annular cover to rotate downward to a set angle, closing them. The computer controller then stops supplying positive DC power to the left and right DC motors of the electric calcium hydroxide powder cover and re-energizes the mixed gas compressor. Description of the drawings:

[0018] The present invention will be described in further detail below with reference to the accompanying drawings and specific embodiments.

[0019] Figure 1 This is a schematic diagram of the structural principle of the electrolytic haze hydrogen production device using the "concave"-shaped electrolytic water vapor acid mist hydrogen production device in the present invention.

[0020] Figure 2 This is a schematic diagram of the structural principle of the "convex"-shaped electrolysis water vapor acid mist hydrogen production device used in the present invention to electrolyze haze hydrogen production equipment. Specific implementation method:

[0021] Figure 1The figure shows a hydrogen production device using electrolysis of water vapor and acid mist. The device consists of a U-shaped steel container (0) with a ceramic lining, a left microporous ceramic plate, an oxygen container, a right microporous ceramic plate, a hydrogen container, an anode (1), a cathode (2), a halogen quartz lamp (3), a ceramic fiber insulation layer, and an outer shell. The left raised portion of the U-shaped steel container (0) houses the left microporous ceramic plate and oxygen container, while the right raised portion houses the right microporous ceramic plate and hydrogen container. The U-shaped steel container (0) houses an array of anodes (1) and cathodes (2). The anode (1) is constructed as follows: a flat glass fiber woven bag filled with graphite pellets or graphene powder is mounted vertically below a flat oxygen hood. A glass fiber woven tube covered with a silicone rubber film extends from the top of the flat oxygen hood and is connected to the left raised portion of the U-shaped steel container (0) below the left microporous ceramic plate. The structure of the cathode 2 is as follows: a flat glass fiber woven bag filled with graphite pellets or graphene powder is vertically installed under the flat hydrogen cover, and a glass fiber woven tube covered with a silicone rubber film on the surface is connected from the top of the flat hydrogen cover to the bottom of the right microporous ceramic plate on the right convex part of the "concave" shaped steel container 0; several halogen quartz lamps 3 are installed at the bottom of the "concave" shaped steel container 0.

[0022] Figure 1As shown, a hydrogen production device for electrolyzing water vapor and acid mist is shown. An oxygen pipe extending from an oxygen container mounted on the raised portion on the left side of a concave-shaped steel container (0) is connected to the inlets of the stator magnetic pole heating pipes of an oxygen thermomagnetic generator (20). Several oxygen pipes extending from the stator magnetic pole heating pipes of the oxygen thermomagnetic generator (20) are connected to the inlets of several hot channels of the water cooler of the oxygen thermomagnetic generator (20). Several oxygen pipes extending from the several hot channels of the water cooler of the oxygen thermomagnetic generator (20) are connected to the bottom of the condensate container of the water cooler of the oxygen thermomagnetic generator (20). A water pipe extending from the bottom of the condensate container of the water cooler of the oxygen thermomagnetic generator (20) is connected to the inlet of an oxygen condensate pump (21). A water pipe extending from the oxygen condensate pump (21) is connected to the inlet of an oxygen condensate check valve (22). A water pipe extending from the oxygen condensate check valve (22) is connected to the top inlet of the concave-shaped steel container (0). The oxygen pipe connected from the top of the condensed water container of the water cooler of the oxygen thermomagnetic power generation device 20 is connected to the inlet of the oxygen compressor 11, the oxygen pipe connected from the oxygen compressor 11 is connected to the inlet of the hot channel of the oxygen cooling dryer 12, the oxygen pipe connected from the hot channel of the oxygen cooling dryer 12 is connected to the bottom inlet of the carbon dioxide condensation container connected to the oxygen cooling dryer 12, the oxygen pipe connected from the top of the carbon dioxide condensation container of the oxygen cooling dryer 12 is connected to the inlet of the oxygen one-way valve 14, and the oxygen pipe connected from the oxygen one-way valve 14 is connected to the top inlet of the oxygen tank 15; the top of the oxygen tank 15 is equipped with an electromagnetic exhaust valve and an oxygen pressure relay. The hydrogen pipe connected from the hydrogen container installed on the raised part on the right side of the "concave" shaped steel container 0 is connected to the inlet of each stator pole heating pipe of the hydrogen thermomagnetic power generation device 23, several hydrogen pipes connected from the stator pole heating pipes of the hydrogen thermomagnetic power generation device 23 are connected to several hot channel inlets of the water cooler of the hydrogen thermomagnetic power generation device 23, several hydrogen pipes connected from several hot channels of the water cooler of the hydrogen thermomagnetic power generation device 23 are connected to the bottom of the condensed water container of the water cooler of the hydrogen thermomagnetic power generation device 23, the water pipe connected from the bottom of the condensed water container of the water cooler of the hydrogen thermomagnetic power generation device 23 is connected to the inlet of the hydrogen condensed water pump 24, the water pipe connected from the hydrogen condensed water pump 24 is connected to the inlet of the hydrogen condensed water one-way valve 25, and the water pipe connected from the hydrogen condensed water one-way valve 25 is connected to the top inlet of the "concave" shaped steel container 0. The hydrogen pipes exiting from the bottom and top of the condensate container of the hydrogen thermomagnetic power generation device and the water cooler 23 are connected to the inlet of the hydrogen compressor 16. The hydrogen pipe exiting from the hydrogen compressor 16 is connected to the inlet of the hydrogen cooling dryer 17. The hydrogen pipe exiting from the hydrogen cooling dryer 17 is connected to the inlet of the hydrogen check valve 18. The hydrogen pipe exiting from the hydrogen check valve 18 is connected to the top inlet of the hydrogen tank 19. The top of the hydrogen tank 19 is equipped with an electromagnetic exhaust valve and a pressure relay.

[0023] Figure 1As shown, a hydrogen production device for electrolyzing water vapor and acid mist is shown. A water pipe extending from the lower side of a water tank 4 is connected to the inlet of a water pump 5. Branch water pipes extending from the water pump 5 are connected to the inlet of the cooling jacket of the oxygen cooling dryer 12, the inlet of the cooling jacket of the hydrogen cooling dryer 17, the inlet of the cooling jacket of the water cooler of the oxygen thermomagnetic generator 20, and the inlet of the cooling jacket of the water cooler of the hydrogen thermomagnetic generator 23. The water pipes extending from the cooling jackets of the oxygen cooling dryer 12, the hydrogen cooling dryer 17, the cooling jackets of the water coolers of the oxygen thermomagnetic generator 20, and the cooling jackets of the water coolers of the hydrogen thermomagnetic generator 23 are connected to the inlet of a one-way water valve 6. The water pipe extending from the one-way water valve 6 is connected to the top water inlet of the preheating tank of a fuel oil boiler 7. Inside the fuel oil boiler 7, from top to bottom, are the preheating tank, the steam generator tank, the steam heating coil, and the fuel oil burner. The water pipe extending from the bottom of the preheating tank of the fuel oil boiler 7 is connected to the bottom water inlet of the steam generator tank of the fuel oil boiler 7. The steam generator tank of oil-fired boiler 7 is equipped with a liquid level sensor probe, a pressure relay, and a temperature sensor probe. The steam pipe extending from the top of the steam generator tank is connected to the inlet of the steam heating coil of oil-fired boiler 7, which in turn is connected to the inlet of electric steam control valve 8. A steam pressure sensor probe is installed in the middle of the top of the concave-shaped steel container 0. Several branching steam inlet pipes extend from the bottom of the concave-shaped steel container 0. The steam pipes extending from the electric steam control valve 8 are connected to the inlets of several branching steam inlet pipes located at the bottom of the concave-shaped steel container 0.

[0024] Figure 1 As shown, a hydrogen production device using electrolysis of water vapor and acid mist is shown. A pH sensor probe is installed in the top middle section of a concave-shaped steel container 0. Several branched carbon dioxide inlet pipes are located at the bottom of the container. The air pipe extending from the top of a carbon dioxide storage tank 9 is connected to the inlet of a carbon dioxide solenoid valve 10. Several branched air pipes extending from the carbon dioxide solenoid valve 10 are connected to the inlet of the branched carbon dioxide inlet pipes located at the bottom of the container. A liquid carbon dioxide pipe extending from the bottom of the carbon dioxide condensation container of an oxygen cooling dryer 12 is connected to the inlet of a liquid carbon dioxide solenoid valve 13. The liquid carbon dioxide pipe extending from the liquid carbon dioxide solenoid valve 13 is then connected to the bottom of the carbon dioxide storage tank 9.

[0025] Figure 1As shown, a control method for a hydrogen production device using electrolytic water vapor and acid mist is provided. A computer controller activates a water pump 5, which pumps water from the lower side of a water tank 4 into the cooling water jackets of the oxygen cooling dryer 12, the hydrogen cooling dryer 17, the water cooler of the oxygen thermomagnetic generator 20, and the water cooler of the hydrogen thermomagnetic generator 23. The water exiting the cooling water jackets of the oxygen cooling dryer 12, the hydrogen cooling dryer 17, the water cooler of the oxygen thermomagnetic generator 20, and the water cooler of the hydrogen thermomagnetic generator 23 passes through a one-way water valve 6 and enters the top of the preheating tank of the fuel oil boiler 7, and then enters the bottom of the water vapor generation tank of the fuel oil boiler 7. When the liquid level sensor probe installed inside the water vapor generator tank of fuel oil boiler 7 detects that the water level inside the water vapor generator tank has reached the set high water level, the computer controller stops powering water pump 5. A one-way water valve 6 prevents water from the preheating tank of fuel oil boiler 7 from being pumped into water tank 4 through the cooling water jackets of oxygen cooling dryer 12, hydrogen cooling dryer 17, the cooling water jackets of the water cooler of oxygen thermomagnetic generator 20, and hydrogen thermomagnetic generator 23, as well as pump 5. The computer controller ignites the fuel oil burner of fuel oil boiler 7. The flame generated by the burner heats the water vapor inside the water vapor heating coil of fuel oil boiler 7, the water vapor generator tank, and the water inside the preheating tank. The water vapor generator tank of fuel oil boiler 7 generates a large amount of water vapor. When the pressure relay installed on top of the water vapor generator tank detects that the water vapor pressure inside the water vapor generator tank has reached the set pressure value, the computer controller powers electric water vapor control valve 8, causing the motor to rotate forward and gradually opening electric water vapor control valve 8 from closed. Steam from the top of the steam generator tank of fuel oil boiler 7 passes through the steam heating coil of fuel oil boiler 7 and enters the gradually opened steam electric regulator 8. Steam exiting the gradually opened steam electric regulator 8 enters the "concave"-shaped steel container 0. When the pressure relay installed on the top of the steam generator tank of fuel oil boiler 7 detects that the steam pressure inside the steam generator tank of fuel oil boiler 7 exceeds the set high pressure value, the computer controller decreases the throttle of the oil burner of fuel oil boiler 7. When the pressure relay installed on the top of the steam generator tank of fuel oil boiler 7 detects that the steam pressure inside the steam generator tank of fuel oil boiler 7 drops below the set low pressure value, the computer controller increases the throttle of the oil burner of fuel oil boiler 7. When the liquid level sensor probe installed inside the steam generator tank of fuel oil boiler 7 detects that the water level inside the steam generator tank of fuel oil boiler 7 drops to the set low water level, the computer controller restarts water pump 5. When the water vapor pressure sensor installed on the top of the middle section of the 'concave' shaped steel container 0 detects that the water vapor pressure in the 'concave' shaped steel container 0 exceeds the set high pressure value, the computer controller reverses the motor of the water vapor electric regulating valve 8 and adjusts the water vapor electric regulating valve 8 from large to small.When the water vapor pressure sensor mounted on the top of the middle section of the "concave"-shaped steel container 0 detects that the water vapor pressure within the container 0 is below the set low pressure value, the computer controller controls the forward rotation of the electric water vapor regulating valve motor, adjusting the electric water vapor regulating valve from low to high. When the water vapor pressure sensor mounted on the top of the middle section of the "concave"-shaped steel container 0 detects that the water vapor pressure within the container 0 has reached the set high pressure value, the computer controller energizes the carbon dioxide solenoid valve 10. Carbon dioxide exiting the top of the carbon dioxide storage tank 9 enters the "concave"-shaped steel container 0 through the energized, open carbon dioxide solenoid valve 10, where it is absorbed by the water vapor within the container 0 and becomes carbonic acid mist. When the pH sensor probe mounted on the top of the middle section of the "concave"-shaped steel container 0 detects that the pH of the carbonic acid mist within the container 0 is below the set low pressure value, the computer controller stops energizing the carbon dioxide solenoid valve 10. When the pH sensor probe, mounted in the center of the top of the "concave"-shaped steel container 0, detects that the pH of the carbonate mist within the container exceeds the set upper limit, the computer controller reenergizes the carbon dioxide solenoid valve 10. The computer controller then supplies direct current (DC) with harmonics of low-voltage, high-frequency AC current between the anode 1 and cathode 2 within the container 0, powering the halogen quartz lamp 3. The low-voltage, high-frequency AC current causes the polar droplets of carbonate mist within the container to oscillate and generate heat. Under the influence of a strong steady-state electric field and a weak alternating electric field, the polar droplets of carbonate mist within the container, which are at temperatures between 130°C and 150°C, separate into negatively charged carbonate anion droplets and positively charged hydrogen cation droplets. The strong light from the halogen quartz lamp 3 reduces the DC voltage, AC voltage, and frequency required for separation. Negatively charged carbonate anion droplets rapidly migrate toward anode 1, where they lose electrons and release oxygen and carbon dioxide. Most of the carbon dioxide is absorbed by the water vapor droplets, forming carbonic acid mist. However, the concentration of free carbon dioxide gas near anode 1 within the concave-shaped steel container 0 remains high. The Chinese character for "water vapor" (qi) is composed of three water drops (shui) plus one (qi), meaning that water vapor molecules are composed of multiple water molecules. However, the moisture in the air is a single gaseous water molecule, whereas carbonic acid mist is composed of droplets made up of multiple water vapor molecules. The computer controller starts the oxygen compressor 11 at a fixed time. The air in the concave-shaped steel container 0 and a small amount of gaseous water molecules and a small amount of carbon dioxide molecules pass through the oxygen container installed on the raised part on the left side of the concave-shaped steel container 0. The oxygen flowing out of the oxygen container installed on the raised part on the left side of the concave-shaped steel container 0 enters the stator magnetic pole heating tubes of the oxygen thermomagnetic power generation device 20, heating the stator magnetic poles of the oxygen thermomagnetic power generation device 20, so that the stator magnetic poles of the oxygen thermomagnetic power generation device 20 are converted from non-magnetic materials to magnetic materials.The computer controller supplies alternating current to the stator excitation coils of the oxygen thermomagnetic generator 20. The generator 20 converts thermal energy into magnetic energy. Under the influence of the alternating magnetic field of the stator magnetic poles, amplified electrical energy is generated in the stator generator coils of the generator 20. Oxygen exiting the stator magnetic pole heating tubes of the generator 20 is further cooled in the hot channel of the water cooler. The oxygen exiting the hot channel of the water cooler enters the bottom of the condenser water tank of the water cooler. Water exiting the condenser water tank of the generator 20 enters the oxygen condenser pump 21. The computer controller activates the oxygen condenser pump 21 at a fixed time. The water exiting the oxygen condenser pump 21 passes through the oxygen condenser check valve 22 and is pumped into the "concave"-shaped steel container 0. Oxygen exiting the top of the condenser water tank of the generator 20 is drawn into the oxygen compressor 11. Oxygen exiting the oxygen compressor 11 enters the hot channel of the oxygen cooling dryer 12 for cooling. Oxygen exiting the hot channel of the oxygen cooling dryer 12 then enters the bottom of the carbon dioxide condenser container of the oxygen cooling dryer 12. Oxygen exiting the top of the carbon dioxide condenser container of the oxygen cooling dryer 12 enters the oxygen check valve 14, and then enters the oxygen tank 15. During initial use, the computer controller energizes the solenoid exhaust valve of the oxygen tank 15 to exhaust air from the oxygen compressor 11, the oxygen thermomagnetic generator 20, the oxygen cooling dryer 12, and the oxygen tank 15. The solenoid exhaust valve of the oxygen tank 15 is then closed. Liquid carbon dioxide exiting the bottom of the carbon dioxide condenser container of the oxygen cooling dryer 12 enters the liquid carbon dioxide solenoid valve 13. The liquid carbon dioxide pipe exiting the liquid carbon dioxide solenoid valve 13 enters the bottom of the carbon dioxide storage tank 9. Under the influence of a strong steady electric field and a weak alternating electric field, the polar droplets of carbonate mist within the concave-shaped steel container 0 separate into negatively charged carbonate anion droplets and positively charged hydrogen cation droplets. The positively charged hydrogen cation droplets rapidly migrate toward the cathode 2, where they gain electrons and release hydrogen gas. Because the negatively charged carbonate anion droplets rapidly migrate toward the anode 1, the concentration of free carbon dioxide gas near the cathode 2 within the concave-shaped steel container 0 remains low. The Chinese character for "water vapor" (qi) is composed of three water drops (shui) plus one (qi), meaning that water vapor molecules are composed of multiple water molecules. However, the moisture in the air is gaseous water, consisting of single water molecules, while the carbonate mist is composed of droplets of multiple water vapor molecules. The computer controller activates the hydrogen compressor 16, and the air and a small amount of gaseous water molecules within the concave-shaped steel container 0 pass through the right microporous ceramic plate mounted on the raised right side of the concave-shaped steel container 0 and enter the hydrogen container mounted on the raised right side of the concave-shaped steel container 0.Hydrogen exiting the hydrogen container, housed in the raised portion on the right side of the "concave"-shaped steel container 0, enters the stator pole heating tubes of the hydrogen thermomagnetic generator 23, heating the stator poles and converting them from non-magnetic to magnetic. A computer controller supplies alternating current to the stator excitation coils of the hydrogen thermomagnetic generator 23. The hydrogen thermomagnetic generator 23 converts thermal energy into magnetic energy. Under the influence of the alternating magnetic field of the stator poles, amplified electrical energy is generated in the stator coils of the hydrogen thermomagnetic generator 23. Hydrogen exiting the stator pole heating tubes is further cooled in the hot channel of the hydrogen thermomagnetic generator 23's water cooler. The hydrogen exiting the hot channel enters the bottom of the condenser water container of the hydrogen thermomagnetic generator 23's water cooler. Water exiting the bottom of the condensate container of the water cooler of the hydrogen thermomagnetic generator 23 enters the hydrogen condensate pump 24. The computer controller periodically activates the hydrogen condensate pump 24. The water exiting the pump passes through the hydrogen condensate check valve 25 and is then pressed into the concave-shaped steel container 0. Hydrogen exiting the top of the condensate container of the water cooler of the hydrogen thermomagnetic generator 23 is drawn into the hydrogen compressor 16. The hydrogen exiting the hydrogen compressor 16 enters the hot channel of the hydrogen cooling dryer 17 for cooling. The hydrogen exiting the hot channel of the hydrogen cooling dryer 17 enters the hydrogen check valve 18, and then enters the hydrogen tank 19. During initial use, the computer controller energizes the solenoid exhaust valve of the hydrogen tank 19 to expel air from the hydrogen compressor 16, the hydrogen thermomagnetic generator 23, the hydrogen cooling dryer 17, and the hydrogen tank 19. The solenoid exhaust valve of the hydrogen tank 19 is then closed.

[0026] Figure 2As shown, a hydrogen production device for electrolyzing water vapor and acid mist is shown. The "convex"-shaped device for electrolyzing water vapor and acid mist hydrogen production consists of an artificial graphite anode tube 26, a foam ceramic tube 27, an artificial graphite cathode tube 28, a microporous ceramic tube 29, a large cast iron pipe shell 30, a large cast iron pipe chimney 31, a small cast iron pipe chimney 32, and a small cast iron pipe shell 33. The upper layer of the "convex"-shaped device, from inside to outside, consists of the large cast iron pipe chimney 31, the foam ceramic tube 27, a circle of small cast iron pipe chimneys 32, and the small cast iron pipe shell 33. The lower layer of the "convex"-shaped device, from inside to outside, consists of the artificial graphite anode tube 26, the foam ceramic tube 27, a circle of artificial graphite cathode tubes 28, the microporous ceramic tube 29, and the large cast iron pipe shell 30. The large cast iron chimney 31 has the same diameter as the artificial graphite anode tube 26 and is attached to it via an insulating ceramic connecting tube. The small cast iron chimney 32 has the same diameter as the artificial graphite cathode tube 28 and is attached to it via an insulating ceramic connecting tube. The gap between the large cast iron chimney 31 and the small cast iron tube casing 33 is filled with coal-water slurry, the gap between the artificial graphite anode tube 26 and the microporous ceramic tube 29 is filled with coal powder, and the gap between the microporous ceramic tube 29 and the large cast iron tube casing 30 is filled with calcium hydroxide powder. Several radial chimneys are installed horizontally between the large cast iron chimney 31 and a circle of several small cast iron chimneys 32. A target is installed in the gap between the lower ends of the artificial graphite anode tube 26 and the microporous ceramic tube 29. Below the target is a cinder chamber. The lower end of the artificial graphite anode tube 26 and the lower ends of a circle of artificial graphite cathode tubes 28 pass through the bottom of the cinder chamber. An insulating ceramic sleeve is installed between the lower ends of the artificial graphite anode tube 26 and the lower ends of a circle of artificial graphite cathode tubes 28 and the bottom of the cinder chamber. An electric cinder valve is installed at the bottom of the cinder chamber between the lower ends of the artificial graphite anode tube 26 and the lower ends of the circle of artificial graphite cathode tubes 28. The electric cinder valve is constructed as follows: it consists of a left half annular valve disc, a front hinge, a front DC motor, a right half annular valve disc, a rear hinge, and a rear DC motor. The left half annular valve disc and the right half annular valve disc are hinged at a diameter. The front section of the left half annular valve disc is fixed to the front hinge shaft, which is fixedly connected to the front DC motor shaft. The rear section of the right half annular valve disc is fixed to the rear hinge shaft, which is fixedly connected to the rear DC motor shaft. An electric calcium hydroxide powder cover is installed at the upper end of the gap between the microporous ceramic tube 29 and the large cast iron pipe housing 30. The electric calcium hydroxide powder cover is constructed as follows: the electric calcium hydroxide powder cover consists of the left half annular valve disc, a left output shaft, a left DC motor, the right half annular valve disc, a right output shaft, and a right DC motor.The outer arc top of the left half annular cover is fixed to the middle position of the left output shaft, which is fixedly connected to the left DC motor shaft. The outer arc top of the right half annular cover is fixed to the middle position of the right output shaft, which is fixedly connected to the right DC motor shaft. An electric calcium hydroxide powder valve is installed at the lower end of the gap between the microporous ceramic tube 29 and the large cast iron pipe shell 30. The electric calcium hydroxide powder valve is structured as follows: the electric calcium hydroxide powder valve consists of a left half annular valve disc, a left output shaft, a left DC motor, a right half annular valve disc, a right output shaft, and a right DC motor. The outer arc top of the left half annular valve disc is fixed to the middle position of the left output shaft, which is fixedly connected to the left DC motor shaft. The outer arc top of the right half annular valve disc is fixed to the middle position of the right output shaft, which is fixedly connected to the right DC motor shaft.

[0027] Figure 2 As shown, a hydrogen production device for electrolyzing water vapor and acid mist is shown. The water pipe leading from the lower side of the water tank 4 is connected to the inlet of the water pump 5. The water pipe leading from the water pump 5 is connected to the inlet of the electric regulating water valve 36. Branch water pipes leading from the electric regulating water valve 36 are connected to the cooling water jacket inlet of the water cooler of the mixed gas thermomagnetic generator 41 and the cooling water jacket inlet of the mixed gas cooling separator 45. The water pipes leading from the cooling water jacket of the water cooler of the mixed gas thermomagnetic generator 41 and the cooling water jacket of the mixed gas cooling separator 45 are connected to the top left inlet of the electric mixing and extrusion kettle 37 for water-coal slurry. The discharge port of the coal powder hopper 34 is equipped with an electric rotary butterfly valve. The coal powder hopper 34 is located to the upper left of the starting point of the electric belt conveyor 35. The terminal end of the electric belt conveyor 35 extends into the top left inlet of the electric mixing and extrusion kettle 37 for water-coal slurry. The bottom outlet of the water-coal slurry electric stirring and extruding kettle 37 and the outlet of the water-coal slurry electric screw extruding conveyor 38 are connected to the gap between the large cast iron pipe chimney 31 and the upper end of the small cast iron pipe shell 33 through a special-shaped elbow.

[0028] Figure 2As shown, a hydrogen production device for electrolyzing water vapor and acid mist is shown. A foamed cast iron plate is installed at the gas outlet of a large cast iron pipe housing 30. A mixed gas pipe extending from the gas outlet of the large cast iron pipe housing 30 is connected to the inlet of the stator magnetic pole heating pipes of a mixed gas thermomagnetic generator 41. Several mixed gas pipes extending from the stator magnetic pole heating pipes of the mixed gas thermomagnetic generator 41 are connected to the inlet of several hot channels of the water cooler of the mixed gas thermomagnetic generator 41. Several mixed gas pipes extending from the hot channels of the water cooler of the mixed gas thermomagnetic generator 41 are connected to the bottom of the condensate container of the water cooler of the mixed gas thermomagnetic generator 41. A water pipe extending from the bottom of the condensate container of the water cooler of the mixed gas thermomagnetic generator 41 is connected to the inlet of a mixed gas condensate pump 42. The water pipe extending from the mixed gas condensate pump 42 is connected to the inlet of a mixed gas condensate check valve 43. The water pipe extending from the mixed gas condensate check valve 43 is connected to the top inlet of the water tank 4. The mixed gas pipe leading from the top of the condensed water container of the water cooler of the mixed gas thermomagnetic power generation device 41 is connected to the inlet of the mixed gas compressor 44. The mixed gas pipe leading from the mixed gas compressor 44 is connected to the inlet of the hot channel of the mixed gas cooling separator 45. The mixed gas pipe leading from the hot channel of the mixed gas cooling separator 45 is connected to the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator 45. The liquid carbon dioxide pipe leading from the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator 45 is connected to the inlet of the liquid carbon dioxide solenoid valve 13. The liquid carbon dioxide pipe leading from the liquid carbon dioxide solenoid valve 13 is connected to the bottom of the carbon dioxide storage tank 9. The hydrogen pipe leading from the top of the condensed liquid carbon dioxide tank of the mixed gas cooling separator 45 is connected to the inlet of the hydrogen check valve 18. The hydrogen pipe leading from the hydrogen check valve 18 is connected to the top inlet of the hydrogen tank 19. The top of the hydrogen tank 19 is equipped with an electromagnetic exhaust valve and a pressure relay.

[0029] Figure 2 Figure 1 shows a hydrogen production system using electrolysis of water vapor and acid mist. A basin-shaped steel mesh is installed below the slag chamber, allowing slag to fall into a slag circulating fluidized bed furnace 39. An ash pipe is installed below the center hole of the basin-shaped steel mesh in the slag circulating fluidized bed furnace 39. The air duct outlet from the electric blower 40 is located below the basin-shaped steel mesh in the slag circulating fluidized bed furnace 39.

[0030] Figure 2A control method for a hydrogen production device using electrolysis of water vapor and acid mist is shown. The electric cinder valve installed at the bottom of the cinder chamber between the lower end of the artificial graphite anode tube 26 and the lower end of a ring of artificial graphite cathode tubes 28 is closed. The electric calcium hydroxide powder valve installed at the lower end of the gap between the microporous ceramic tube 29 and the large cast iron pipe housing 30 is also closed. A computer controller supplies reverse DC power to the left and right DC motors of the electric calcium hydroxide powder cover, causing the left half of the annular valve disc and the right half of the annular cover to rotate upward by a set angle, opening them. The computer controller then stops supplying reverse DC power to the front and rear DC motors of the electric calcium hydroxide powder valve. The gap between the microporous ceramic tube 29 and the large cast iron pipe housing 30 is filled with calcium hydroxide powder. The computer controller then supplies positive DC power to the left and right DC motors of the electric calcium hydroxide powder cover, causing the left half annular valve disc and the right half annular cover to rotate downward by a set angle, closing the cover. The computer controller then stops supplying positive DC power to the left and right DC motors of the electric calcium hydroxide powder cover. Coal powder is placed on the basin-shaped steel wire mesh of the slag circulating fluidized bed furnace 39. Diesel fuel is sprayed onto the coal powder on the basin-shaped steel wire mesh, igniting the coal powder on the basin-shaped steel wire mesh. The computer controller then activates the electric blower 40, causing air from the electric blower 40 to blow upward from below the basin-shaped steel wire mesh of the slag circulating fluidized bed furnace 39, supporting the combustion of the coal powder on the basin-shaped steel wire mesh. The computer controller activates the electric rotary butterfly valve installed at the discharge port of the coal powder hopper 34, causing the coal powder in the hopper 34 to leak into the starting end of the electric belt conveyor 35. The computer controller then activates the electric belt conveyor 35, which then feeds the coal powder into the electric coal-water slurry mixing and extrusion kettle 37. The computer controller then activates the water pump 5 and adjusts the electric regulating water valve 36. The water pump 5 pumps water from the water tank 4 through the electric regulating water valve 36 and into the cooling water jacket of the water cooler of the mixed gas thermomagnetic generator 41 and the cooling water jacket of the mixed gas cooling separator 45. The water from the cooling water jackets of the water cooler of the mixed gas thermomagnetic generator 41 and the cooling water jacket of the mixed gas cooling separator 45 enters the electric coal-water slurry mixing and extrusion kettle 37. The computer controller then activates the electric coal-water slurry mixing and extrusion kettle 37, and the coal-water slurry, initially containing a small amount of water, is pressed into the electric coal-water slurry screw extrusion conveyor 38. The computer controller starts the water-coal slurry electric screw extrusion conveyor 38, which presses the water-coal slurry containing a small amount of water into the gap between the large cast iron pipe chimney 31 and the upper end of the small cast iron pipe shell 33 through the elbow, and then enters the gap between the artificial graphite anode tube 26 and the microporous ceramic tube 29.The flue gas generated by the combustion of coal powder on the basin-shaped steel wire mesh of the slag circulating fluidized bed furnace 39 passes through the artificial graphite anode tube 26 and a ring of several artificial graphite cathode tubes 28, heating them and the coal-water slurry contained in the gap between the artificial graphite anode tube 26 and the microporous ceramic tube 29, generating a large amount of water vapor that turns into red-hot coal powder. The flue gas then passes through the large cast iron chimney 31 and a ring of several small cast iron chimneys 32, heating the coal-water slurry contained in the gap between the large cast iron chimney 31 and the small cast iron shell 33, generating a large amount of water vapor. A computer controller supplies a high-voltage direct current (DC) with harmonics of the low-voltage, high-frequency AC current between the artificial graphite anode tube 26 and the artificial graphite cathode tube 28. The low-voltage, high-frequency AC current causes the water vapor between the artificial graphite anode tube 26 and the artificial graphite cathode tube 28 to oscillate and generate heat. Under the influence of a strong steady electric field and a weak alternating electric field, the water vapor between the artificial graphite anode tube 26 and the artificial graphite cathode tube 28 separates into negatively charged hydroxyl anion droplets and positively charged hydrogen cation droplets. The negatively charged hydroxyl anion droplets rapidly migrate toward the artificial graphite anode tube 26, where they lose electrons and release oxygen and water vapor. The positively charged hydrogen cation droplets rapidly migrate toward the artificial graphite cathode tube 28, where they gain electrons and release hydrogen. The oxygen reacts chemically with the 400°C coal powder contained in the gap between the artificial graphite anode tube 26 and the microporous ceramic tube 29 to produce carbon dioxide, generating a large amount of heat. The oxygen also reacts chemically with the sulfur in the 400°C coal powder contained in the gap between the artificial graphite anode tube 26 and the microporous ceramic tube 29 to produce sulfur dioxide, generating a large amount of heat. The carbon dioxide is absorbed by the water vapor to form carbonic acid mist droplets, while the sulfur dioxide is absorbed by the water vapor to form sulfite mist droplets. The computer controller reduces the voltage of the direct current (DC) with harmonics of the low-voltage, high-frequency AC current flowing between the artificial graphite anode tube 26 and the artificial graphite cathode tube 28. This low-voltage, high-frequency AC current causes the carbonate and sulfite mist droplets between the two tubes to oscillate and generate heat. Under the influence of the strong, stable electric field and the weak, alternating electric field, the polar carbonate droplets between the two tubes separate into negatively charged carbonate anion droplets and positively charged hydrogen cation droplets, while the polar sulfite droplets separate into negatively charged sulfite anion droplets and positively charged hydrogen cation droplets. The negatively charged carbonate anion droplets rapidly migrate toward the artificial graphite anode tube 26, where they lose electrons and release oxygen and carbon dioxide. The positively charged hydrogen cation droplets quickly move toward the artificial graphite cathode tube 28 , and obtain electrons in the artificial graphite cathode tube 28 and release hydrogen gas.The negatively charged sulfite anion droplets quickly move toward the artificial graphite anode tube 26, where they lose electrons and release oxygen and sulfur dioxide. The positively charged hydrogen cation droplets quickly move toward the artificial graphite powder cathode tube (78), where they gain electrons and release hydrogen. Water vapor reacts chemically with the 700°C red-hot coal powder contained in the gap between the artificial graphite anode tube 26 and the microporous ceramic tube 29 to produce hydrogen and carbon monoxide, and absorbs a large amount of heat. Carbon monoxide reacts chemically with oxygen at high temperature to produce carbon dioxide, and generates a large amount of heat. The computer controller energizes the mixed gas compressor 44, which draws the mixed gas into the gap between the microporous ceramic (2) and the large cast iron pipe shell 30. The mixed gas containing gaseous water passes through the micropores of the outer ceramic tube 29 and enters the microporous ceramic tube 29. In the annular gap between the microporous ceramic tube 29 and the large cast iron pipe shell 30, sulfur dioxide reacts chemically with the calcium hydroxide powder contained in the gap between the microporous ceramic tube 29 and the large cast iron pipe shell 30 at high temperature to produce calcium sulfite and water. The mixed gas compressor 44 draws the mixed gas in the gap between the microporous ceramic tube 29 and the large cast iron pipe shell 30 into the stator magnetic pole heating tubes of the mixed gas thermomagnetic generator 41, heating the stator magnetic poles of the mixed gas thermomagnetic generator 41, and transforming the stator magnetic poles of the mixed gas thermomagnetic generator 41 from non-magnetic materials to magnetic materials. The computer controller passes alternating current to the stator excitation coil of the mixed gas thermomagnetic generator 41, and the mixed gas heats up. The magnetic power generation device 41 converts thermal energy into magnetic energy, and under the action of the alternating magnetic field of the stator magnetic poles of the mixed gas thermomagnetic power generation device 41, amplified electrical energy is generated in the stator generating coil of the mixed gas thermomagnetic power generation device 41. The mixed gas discharged from the stator magnetic pole heating tubes of the mixed gas thermomagnetic power generation device 41 is further cooled in the hot channel of the water cooler of the mixed gas thermomagnetic power generation device 41. The mixed gas discharged from the hot channel of the water cooler of the mixed gas thermomagnetic power generation device 41 enters the bottom of the condensate container of the water cooler of the mixed gas thermomagnetic power generation device 41. The water discharged from the bottom of the condensate container of the water cooler of the mixed gas thermomagnetic power generation device 41 enters the mixed gas condensate pump 4 2. The computer controller regularly activates the mixed gas condensate pump 42. The water discharged from the mixed gas condensate pump 42 passes through the mixed gas condensate check valve 43 and is pressed into the water tank 4. The mixed gas discharged from the top of the condensate container of the water cooler of the mixed gas thermomagnetic power generation device 41 enters the mixed gas compressor 44. The mixed gas discharged from the mixed gas compressor 44 is pressed into the hot channel of the mixed gas cooling separator 45. The mixed gas discharged from the hot channel of the mixed gas cooling separator 45 is pressed into the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator 45. The high-pressure carbon dioxide gas is cooled into liquid carbon dioxide and retained at the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator 45.The computer controller periodically energizes and opens the liquid CO2 solenoid valve 13. The liquid CO2 condensed from the bottom of the mixed gas cooling separator 45 flows through the open liquid CO2 solenoid valve 13 into the bottom of the CO2 storage tank 9. The computer controller then closes the liquid CO2 solenoid valve 13. Hydrogen exiting the top of the mixed gas cooling separator 45's liquid CO2 condensation tank passes through the hydrogen check valve 18 and is compressed into the hydrogen tank 19. During the initial stages of hydrogen production from the electrolysis of water vapor and acid mist, the computer controller energizes and opens the solenoid exhaust valve installed at the top of the hydrogen tank 19, exhausting air from the gap between the microporous ceramic tube 29 and the large cast iron pipe housing 30, the mixed gas thermomagnetic generator 41, the mixed gas compressor 44, the mixed gas cooling separator 45, and the hydrogen tank 19. The computer controller then closes the solenoid exhaust valve installed at the top of the hydrogen tank 19. Oxygen reacts chemically with the 700°C coal powder contained in the gap between the artificial graphite anode tube 26 and the microporous ceramic tube 29 to produce carbon dioxide, generating a large amount of heat. Water vapor also reacts chemically with the 700°C coal powder contained in the gap between the artificial graphite anode tube 26 and the microporous ceramic tube 29 to produce hydrogen and carbon monoxide, absorbing a large amount of heat and consuming the carbon in the 700°C coal powder. This reacts as coal slag, which leaks into the slag chamber through the furnace rake installed at the lower end of the gap between the artificial graphite anode tube 26 and the microporous ceramic tube 29. The computer controller stops powering the mixed gas compressor 44 and then supplies positive DC power to the front and rear DC motors of the electric slag valve, causing the left and right half annular valve discs to rotate downward, opening them. After the left and right annular valve discs rotate downward by a set angle, the computer controller stops supplying forward DC power to the front and rear DC motors of the electric slag valve. The slag in the slag chamber is unloaded onto the basin-shaped steel wire mesh of the slag circulating fluidized bed furnace 39, where it is mixed with the coal powder on the basin-shaped steel wire mesh and burned. After the slag in the slag chamber is unloaded, the computer controller supplies reverse DC power to the front and rear DC motors of the electric slag valve, causing the left and right annular valve discs to rotate upward by a set angle, closing the valve. The computer controller stops supplying reverse DC power to the front and rear DC motors of the electric slag valve and resumes supplying power to the mixed gas compressor 44. At high temperatures, sulfur dioxide chemically reacts with the calcium hydroxide powder contained in the gap between microporous ceramic tube 29 and large cast iron pipe shell 30 to produce calcium sulfite and water vapor, consuming the calcium hydroxide powder contained in the gap between microporous ceramic tube 29 and large cast iron pipe shell 30. The computer controller stops powering mixed gas compressor 44 and then provides positive DC power to the left and right DC motors of the electric calcium hydroxide powder valve, causing the left and right annular valve discs to rotate downward, opening the valve.After the left and right half annular valve discs rotate downward by a set angle, the computer controller stops supplying forward DC power to the front and rear DC motors of the electric calcium hydroxide powder valve. The calcium hydroxide powder, which contains a large amount of calcium sulfite, contained in the gap between the microporous ceramic tube 29 and the large cast iron pipe housing 30 is discharged. After the calcium hydroxide powder, which contains a large amount of calcium sulfite, is discharged from the gap between the microporous ceramic tube 29 and the large cast iron pipe housing 30, reverse DC power is supplied to the front and rear DC motors of the electric calcium hydroxide powder valve, causing the left and right half annular valve discs to rotate upward by a set angle, closing the valve. The computer controller then stops supplying reverse DC power to the front and rear DC motors of the electric calcium hydroxide powder valve. The computer controller then supplies reverse DC power to the left and right DC motors of the electric calcium hydroxide powder cover, causing the left and right half annular valve discs to rotate upward by a set angle, opening the valve. The computer controller then stops supplying reverse DC power to the front and rear DC motors of the electric calcium hydroxide powder valve. The gap between the microporous ceramic tube 29 and the large cast iron pipe housing 30 is filled with calcium hydroxide powder. The computer controller then supplies positive DC power to the left and right DC motors of the electric calcium hydroxide powder cover, causing the left half annular valve disc and the right half annular cover to rotate downward by a set angle, closing them. The computer controller then stops supplying positive DC power to the left and right DC motors of the electric calcium hydroxide powder cover. The computer controller then re-energizes the mixed gas compressor 44.

Claims

1. A hydrogen production device by electrolyzing water vapor and acid mist, characterized by: The 'concave' shaped electrolytic water vapor acid mist hydrogen production device comprises a 'concave' shaped steel container (0) with a ceramic lining inside, a left microporous ceramic plate, an oxygen container, a right microporous ceramic plate, a hydrogen container, an anode (1), a cathode (2), a halogen quartz lamp (3), a ceramic fiber insulation layer and an outer shell. The left raised portion of the 'concave' shaped steel container (0) is equipped with the left microporous ceramic plate and the oxygen container, and the right raised portion of the 'concave' shaped steel container (0) is equipped with the right microporous ceramic plate and the hydrogen container; the 'concave' shaped steel container (0) is equipped with an array of anodes (1) and cathodes (2), and the structure of the anode (1) is as follows: a flat plate filled with graphite spherical particles or graphene powder; A flat glass fiber woven bag is vertically installed under a flat oxygen hood, and a glass fiber woven tube covered with a silicone rubber film is connected from the top of the flat oxygen hood to the bottom of the left microporous ceramic plate on the left convex part of the "concave" shaped steel container (0); the cathode (2) has the following structure: a flat glass fiber woven bag filled with graphite spheres or graphene powder is vertically installed under a flat hydrogen hood, and a glass fiber woven tube covered with a silicone rubber film is connected from the top of the flat hydrogen hood to the bottom of the right microporous ceramic plate on the right convex part of the "concave" shaped steel container (0); a plurality of halogen quartz lamps (3) are installed at the bottom of the "concave" shaped steel container (0).

2. The hydrogen production equipment by electrolyzing water vapor and acid mist according to claim 1, characterized in that: The oxygen pipe connected from the oxygen container installed on the convex part on the left side of the "concave" shaped steel container (0) is connected to the inlet of each magnetic pole heating pipe of the stator of the oxygen thermomagnetic power generation device (20), and the several oxygen pipes connected from the magnetic pole heating pipe of the stator of the oxygen thermomagnetic power generation device (20) are connected to the inlet of several hot channels of the water cooler of the oxygen thermomagnetic power generation device (20). The several oxygen pipes connected from the several hot channels of the water cooler of the oxygen thermomagnetic power generation device (20) are connected to the bottom of the condensed water container of the water cooler of the oxygen thermomagnetic power generation device (20). The water pipe connected from the bottom of the condensed water container of the water cooler of the oxygen thermomagnetic power generation device (20) is connected to the inlet of the hot channel of the water cooler of the oxygen thermomagnetic power generation device (20). The oxygen condensate pump (21) inlet, the water pipe connected to the oxygen condensate pump (21) is connected to the oxygen condensate one-way valve (22) inlet, the water pipe connected to the oxygen condensate one-way valve (22) is connected to the top inlet of the "concave" shaped steel container (0); the oxygen pipe connected to the top of the condensate container of the water cooler of the oxygen thermomagnetic power generation device (20) is connected to the oxygen compressor (11) inlet, the oxygen pipe connected to the oxygen compressor (11) is connected to the hot channel inlet of the oxygen cooling dryer (12), the oxygen pipe connected to the hot channel of the oxygen cooling dryer (12) is connected to the oxygen pipe connected to the oxygen cooling dryer (12) The bottom inlet of the carbon dioxide condensation container of the oxygen cooling dryer (12), the oxygen pipe connected from the top of the carbon dioxide condensation container of the oxygen cooling dryer (12) is connected to the inlet of the oxygen one-way valve (14), and the oxygen pipe connected from the oxygen one-way valve (14) is connected to the top inlet of the oxygen tank (15); the top of the oxygen tank (15) is equipped with an electromagnetic exhaust valve, and the top of the oxygen tank (15) is equipped with an oxygen pressure relay; the hydrogen pipe connected from the hydrogen container equipped with the raised part on the right side of the "concave" shaped steel container (0) is connected to the inlet of each magnetic pole heating pipe of the stator of the hydrogen thermomagnetic power generation device (23), and the hydrogen pipe connected from each magnetic pole heating pipe of the stator of the hydrogen thermomagnetic power generation device (23) is connected to the inlet of the hydrogen thermomagnetic power generation device (23). Several hydrogen pipes are connected to several hot channel inlets of the water cooler of the hydrogen thermomagnetic power generation device (23); several hydrogen pipes connected from the several hot channels of the water cooler of the hydrogen thermomagnetic power generation device (23) are connected to the bottom of the condensed water container of the water cooler of the hydrogen thermomagnetic power generation device (23); water pipes connected from the bottom of the condensed water container of the water cooler of the hydrogen thermomagnetic power generation device (23) are connected to the inlet of the hydrogen condensed water pump (24); water pipes connected from the hydrogen condensed water pump (24) are connected to the inlet of the hydrogen condensed water check valve (25); and water pipes connected from the hydrogen condensed water check valve (25) are connected to the top inlet of the "concave" shaped steel container (0);The hydrogen pipe exiting from the bottom and top of the condensed water container of the water cooler of the hydrogen thermomagnetic power generation device (23) is connected to the inlet of the hydrogen compressor (16), the hydrogen pipe exiting from the hydrogen compressor (16) is connected to the inlet of the hydrogen cooling dryer (17), the hydrogen pipe exiting from the hydrogen cooling dryer (17) is connected to the inlet of the hydrogen check valve (18), and the hydrogen pipe exiting from the hydrogen check valve (18) is connected to the top inlet of the hydrogen tank (19); the top of the hydrogen tank (19) is equipped with an electromagnetic exhaust valve and a pressure relay.

3. The hydrogen production equipment according to claim 1 or claim 2, characterized in that: The water pipe connected from the lower side of the water tank (4) is connected to the inlet of the water pump (5), and the branch water pipes connected from the water pump (5) are respectively connected to the inlet of the cooling water jacket of the oxygen cooling dryer (12), the inlet of the cooling water jacket of the hydrogen cooling dryer (17), the inlet of the cooling water jacket of the water cooler of the oxygen thermomagnetic power generation device (20), and the cooling water jacket and inlet of the water cooler of the hydrogen thermomagnetic power generation device (23). The water pipes connected from the cooling water jacket of the oxygen cooling dryer (12), the cooling water jacket of the hydrogen cooling dryer (17), the cooling water jacket of the water cooler of the oxygen thermomagnetic power generation device (20), and the cooling water jacket of the water cooler of the hydrogen thermomagnetic power generation device (23) are connected to the inlet of the one-way water valve (6), and the water pipe connected from the one-way water valve (6) is connected to the water inlet at the top of the preheating box of the fuel oil boiler (7); the fuel oil boiler (7) is provided with a preheating box, a steam generating tank, a steam heating coil, and a fuel oil burner from top to bottom. The water pipe connected from the bottom of the preheating box of the fuel oil boiler (7) is connected to the water inlet at the bottom of the water vapor generating tank of the fuel oil boiler (7), a liquid level sensor probe is installed inside the water vapor generating tank of the fuel oil boiler (7), a pressure relay is installed on the top of the water vapor generating tank of the fuel oil boiler (7), and a temperature sensor probe is installed on the top of the water vapor generating tank of the fuel oil boiler (7); the water vapor pipe connected from the top of the water vapor generating tank of the fuel oil boiler (7) is connected to the inlet of the water vapor heating coil of the fuel oil boiler (7), the water vapor pipe connected from the water vapor heating coil of the fuel oil boiler (7) is connected to the inlet of the water vapor electric regulating valve (8), the water vapor pressure sensor probe is installed in the middle section of the top of the "concave" shaped steel container (0), the bottom of the "concave" shaped steel container (0) is provided with several branch water vapor inlet pipes, and the water vapor pipe connected from the water vapor electric regulating valve (8) is connected to the inlet of several branch water vapor inlet pipes provided at the bottom of the "concave" shaped steel container (0).

4. The hydrogen production equipment according to claim 1 or claim 2, characterized in that: A pH sensor probe is installed in the middle section of the top of the concave steel container (0); a plurality of branch carbon dioxide inlet pipes are provided at the bottom of the concave steel container (0); the air pipe connected from the top of the carbon dioxide storage tank (9) is connected to the inlet of the carbon dioxide solenoid valve (10); the plurality of branch air pipes connected from the carbon dioxide solenoid valve (10) are connected to the inlet of the plurality of branch carbon dioxide inlet pipes provided at the bottom of the concave steel container (0); the liquid carbon dioxide pipe connected from the bottom of the carbon dioxide condensation container of the oxygen cooling dryer (12) is connected to the inlet of the liquid carbon dioxide solenoid valve (13); and the liquid carbon dioxide pipe connected from the liquid carbon dioxide solenoid valve (13) is connected to the bottom of the carbon dioxide storage tank (9).

5. The control method of a hydrogen production equipment by electrolyzing water vapor and acid mist according to claim 1, or claim 2, or claim 3, or claim 4, characterized in that: The computer controller starts the water pump (5), and the water pumped out from the lower side of the water tank (4) by the water pump (5) enters the cooling water jacket of the oxygen cooling dryer (12), the cooling water jacket of the hydrogen cooling dryer (17), the cooling water jacket of the water cooler of the oxygen thermomagnetic power generation device (20), and the cooling water jacket of the water cooler of the hydrogen thermomagnetic power generation device (23). The water coming out of the cooling water jacket of the oxygen cooling dryer (12), the cooling water jacket of the hydrogen cooling dryer (17), the cooling water jacket of the water cooler of the oxygen thermomagnetic power generation device (20), and the cooling water jacket of the water cooler of the hydrogen thermomagnetic power generation device (23) passes through the one-way water valve (6) and enters the top of the preheating tank of the fuel oil boiler (7), and then enters the bottom of the water vapor generating tank of the fuel oil boiler (7). When the liquid level sensor probe installed inside the water vapor generating tank of the furnace (7) detects that the water level inside the water vapor generating tank of the oil-fired boiler (7) reaches the set high water level, the computer controller stops supplying power to the water pump (5), and the one-way water valve (6) can prevent the water in the preheating tank of the oil-fired boiler (7) from passing through the cooling water jacket of the oxygen cooling dryer (12), the cooling water jacket of the hydrogen cooling dryer (17), the cooling water jacket of the water cooler of the oxygen thermomagnetic generator (20), the cooling water jacket of the water cooler of the hydrogen thermomagnetic generator (23), and the water pump (5) and being pressed into the water tank (4), the computer controller ignites the oil burner of the oil-fired boiler (7), and the flame generated by the oil burner of the oil-fired boiler (7) heats the water vapor of the oil-fired boiler (7). The water vapor in the heating coil, the water vapor generating tank and the water in the preheating box, the water vapor generating tank of the hot oil boiler (7) generates a large amount of water vapor. When the pressure relay installed on the top of the water vapor generating tank of the oil boiler (7) detects that the pressure of the water vapor in the water vapor generating tank of the oil boiler (7) reaches the set pressure value, the computer controller supplies power to the water vapor electric regulating valve (8), the motor rotates forward, and the water vapor electric regulating valve (8) is gradually opened from closed. The water vapor on the top of the water vapor generating tank of the oil boiler (7) passes through the water vapor heating coil of the oil boiler (7) and enters the gradually opened water vapor electric regulating valve (8). The water vapor discharged from the gradually opened water vapor electric regulating valve (8) enters the 'concave' shaped steel container (0 ); when the pressure relay installed on the top of the water vapor generating tank of the oil-fired boiler (7) detects that the pressure of the water vapor in the water vapor generating tank of the oil-fired boiler (7) exceeds the set high pressure value, the computer controller adjusts the throttle of the oil burner of the oil-fired boiler (7) down; when the pressure relay installed on the top of the water vapor generating tank of the oil-fired boiler (7) detects that the pressure of the water vapor in the water vapor generating tank of the oil-fired boiler (7) drops below the set low pressure value, the computer controller adjusts the throttle of the oil burner of the oil-fired boiler (7) up; when the liquid level sensor probe installed inside the water vapor generating tank of the oil-fired boiler (7) detects that the water level inside the water vapor generating tank of the oil-fired boiler (7) drops to the set low water level, the computer controller restarts the water pump (5);When the water vapor pressure sensor installed at the top of the middle section of the 'concave' shaped steel container (0) detects that the water vapor pressure in the 'concave' shaped steel container (0) exceeds the set high pressure value, the computer controller allows the motor of the water vapor electric regulating valve (8) to reverse and the water vapor electric regulating valve (8) to be adjusted from large to small. When the water vapor pressure sensor installed at the top of the middle section of the 'concave' shaped steel container (0) detects that the water vapor pressure in the 'concave' shaped steel container (0) is lower than the set low pressure value, the computer controller allows the motor of the water vapor electric regulating valve to rotate forward and the water vapor electric regulating valve to be adjusted from small to large. When the water vapor pressure sensor installed at the top of the middle section of the 'concave' shaped steel container (0) detects that the water vapor pressure in the 'concave' shaped steel container (0) reaches the set high pressure value, the computer controller supplies power to the carbon dioxide solenoid valve (10), and the carbon dioxide discharged from the top of the carbon dioxide gas storage tank (9) passes through the carbon dioxide solenoid valve opened by power. (10) enters the "concave" shaped steel container (0), is absorbed by the water vapor in the "concave" shaped steel container (0), and becomes carbonic acid mist. When the pH value sensor probe installed in the middle section of the top of the "concave" shaped steel container (0) detects that the pH value of the carbonic acid mist in the "concave" shaped steel container (0) is lower than the set low value, the computer controller stops supplying power to the carbon dioxide solenoid valve (10). When the pH value sensor probe installed in the middle section of the top of the "concave" shaped steel container (0) detects that the pH value of the carbonic acid mist in the "concave" shaped steel container (0) exceeds the set high value, the computer controller restarts supplying power to the carbon dioxide solenoid valve (10); the computer controller passes direct current with low-voltage and high-frequency alternating current harmonics between the anode (1) and the cathode (2) in the "concave" shaped steel container (0), and the computer controller supplies power to the halogen quartz lamp (3). The low-voltage and high-frequency alternating current causes the polar droplets of the carbonic acid mist in the "concave" shaped steel container (0) to oscillate and generate heat;Under the action of a strong stable electric field and a weak alternating electric field, the polar droplets of carbonate mist at 130°C to 150°C in the "concave" shaped steel container (0) are separated into negatively charged carbonate anion droplets and positively charged hydrogen cation droplets. The strong light of the halogen quartz lamp (3) can reduce the DC voltage, AC voltage and frequency required for the separation of carbonate mist. The negatively charged carbonate anion droplets quickly move to the anode (1) and lose electrons at the anode (1), releasing oxygen and carbon dioxide. Most of the carbon dioxide is absorbed by the water vapor droplets to become carbonate mist, but the carbon dioxide in the "concave" shaped steel container (0) The concentration of free carbon dioxide gas near the anode (1) is still very high. The word "qi" in water vapor is composed of three water drops and one "qi", which means that water vapor molecules are composed of multiple water molecules, but the moisture in the air is gaseous water of a single water molecule. Carbonic acid mist is a droplet composed of multiple water vapor molecules. The computer controller starts the oxygen compressor (11) at a fixed time. The air in the "concave" shaped steel container (0) and a small amount of gaseous water molecules and a small amount of carbon dioxide molecules pass through the oxygen container installed on the raised part on the left side of the "concave" shaped steel container (0). The oxygen discharged from the oxygen container enters the stator magnetic pole heating tubes of the oxygen thermomagnetic power generation device (20), heats the stator magnetic poles of the oxygen thermomagnetic power generation device (20), and converts the stator magnetic poles of the oxygen thermomagnetic power generation device (20) from non-magnetic materials to magnetic materials. The computer controller passes alternating current to the stator excitation coil of the oxygen thermomagnetic power generation device (20), and the oxygen thermomagnetic power generation device (20) converts thermal energy into magnetic energy. Under the action of the alternating magnetic field of the stator magnetic poles of the oxygen thermomagnetic power generation device (20), amplified electric energy is generated in the stator generating coil of the oxygen thermomagnetic power generation device (20), and the oxygen thermomagnetic power generation device (20) generates a magnetic energy. 0) is further cooled in the hot channel of the water cooler of the oxygen thermomagnetic power generation device (20), and the oxygen discharged from the hot channel of the water cooler of the oxygen thermomagnetic power generation device (20) enters the bottom of the condensation water container of the water cooler of the oxygen thermomagnetic power generation device (20), and the water discharged from the bottom of the condensation water container of the water cooler of the oxygen thermomagnetic power generation device (20) enters the oxygen condensation water pump (21). The computer controller starts the oxygen condensation water pump (21) at a fixed time, and the water discharged from the oxygen condensation water pump (21) passes through the oxygen condensation water one-way valve (22) and is pressed into the "concave" shaped steel container (0);Oxygen discharged from the top of the condensed water container of the water cooler of the oxygen thermomagnetic power generation device (20) is sucked into the oxygen compressor (11), the oxygen discharged from the oxygen compressor (11) enters the hot channel of the oxygen cooling dryer (12) to be cooled, the oxygen discharged from the hot channel of the oxygen cooling dryer (12) enters the bottom of the carbon dioxide condensation container of the oxygen cooling dryer (12), the oxygen discharged from the top of the carbon dioxide condensation container of the oxygen cooling dryer (12) enters the oxygen one-way valve (14), and the oxygen discharged from the oxygen one-way valve (14) enters the oxygen tank (15); the computer controller is used for the first time to energize the electromagnetic exhaust valve of the oxygen tank (15), discharge the air in the oxygen compressor (11), the oxygen thermomagnetic power generation device (20), the oxygen cooling dryer (12) and the oxygen tank (15), and then close the electromagnetic exhaust valve of the oxygen tank (15); the liquid carbon dioxide discharged from the bottom of the carbon dioxide condensation container of the oxygen cooling dryer (12) enters the liquid carbon dioxide electromagnetic valve (13), and the liquid carbon dioxide discharged from the liquid carbon dioxide electromagnetic valve (13) enters the carbon dioxide pipe The bottom of the gas storage tank (9); under the action of a strong stable electric field and a weak alternating electric field, the polar droplets of carbonate mist in the 'concave' shaped steel container (0) are separated into negatively charged carbonate anion droplets and positively charged hydrogen cation droplets, and the positively charged hydrogen cation droplets quickly move toward the cathode (2), and obtain electrons at the cathode (2) and release hydrogen gas; because the negatively charged carbonate anion droplets quickly move toward the anode (1), the concentration of free carbon dioxide gas near the cathode (2) in the 'concave' shaped steel container (0) remains The temperature is very low. The word "qi" in water vapor is composed of three water drops and one "qi", which means that water vapor molecules are composed of multiple water molecules, but the moisture in the air is gaseous water of a single water molecule. Carbonic acid mist is a droplet composed of multiple water vapor molecules. The computer controller starts the hydrogen compressor (16). The air and a small amount of gaseous water molecules in the "concave" shaped steel container (0) pass through the right microporous ceramic plate installed on the right raised part of the "concave" shaped steel container (0) and enter the hydrogen container installed on the right raised part of the "concave" shaped steel container (0);The hydrogen gas discharged from the hydrogen container installed in the raised part on the right side of the "concave" shaped steel container (0) enters the stator magnetic pole heating tubes of the hydrogen thermomagnetic power generation device (23), heating the stator magnetic poles of the hydrogen thermomagnetic power generation device (23), so that the stator magnetic poles of the hydrogen thermomagnetic power generation device (23) are transformed from non-magnetic materials into magnetic materials. The computer controller passes AC power to the stator excitation coil of the hydrogen thermomagnetic power generation device (23), and the hydrogen thermomagnetic power generation device (23) transforms heat energy into magnetic energy. Under the action of the alternating magnetic field of the stator magnetic poles of the magnetic power generation device (23), amplified electric energy is generated in the stator power generation coil of the hydrogen thermomagnetic power generation device (23), and the hydrogen discharged from the stator magnetic pole heating tubes of the hydrogen thermomagnetic power generation device (23) is further cooled in the hot channel of the water cooler of the hydrogen thermomagnetic power generation device (23). The hydrogen discharged from the hot channel of the water cooler of the hydrogen thermomagnetic power generation device (23) enters the bottom of the condensed water container of the water cooler of the hydrogen thermomagnetic power generation device (23) The water discharged from the bottom of the condensate container of the water cooler of the hydrogen thermomagnetic power generation device (23) enters the hydrogen condensate pump (24), and the computer controller starts the hydrogen condensate pump (24) at a fixed time. The water discharged from the hydrogen condensate pump (24) passes through the hydrogen condensate check valve (25) and is pressed into the "concave" shaped steel container (0); the hydrogen discharged from the top of the condensate container of the water cooler of the hydrogen thermomagnetic power generation device (23) is sucked into the hydrogen compressor (16), and the hydrogen discharged from the hydrogen compressor (16) enters The hydrogen entering the hot channel of the hydrogen cooling dryer (17) is cooled, and the hydrogen exiting the hot channel of the hydrogen cooling dryer (17) enters the hydrogen check valve (18), and the hydrogen exiting the hydrogen check valve (18) enters the hydrogen tank (19); the computer controller is used for the first time to energize the electromagnetic exhaust valve of the hydrogen tank (19), exhaust the air in the hydrogen compressor (16), the hydrogen thermomagnetic generator (23), the hydrogen cooling dryer (17) and the hydrogen tank (19), and then the electromagnetic exhaust valve of the hydrogen tank (19) is closed.

6. A hydrogen production device by electrolyzing water vapor and acid mist, characterized by: The convex-shaped electrolytic water vapor acid mist hydrogen production device is composed of an artificial graphite anode tube (26), a foam ceramic tube (27), an artificial graphite cathode tube (28), a microporous ceramic tube (29), a large cast iron pipe shell (30), a large cast iron pipe chimney (31), a small cast iron pipe chimney (32) and a small cast iron pipe shell (33). The upper layer of the convex-shaped electrolytic water vapor acid mist hydrogen production device is composed of the large cast iron pipe chimney (31), the foam ceramic tube (27), a circle of small cast iron pipe chimneys (32) and the small cast iron pipe shell (33) from the inside to the outside. The lower layer of the convex-shaped electrolytic water vapor acid mist hydrogen production device is composed of the artificial graphite anode tube (26) from the inside to the outside. , a foam ceramic tube (27), a circle of artificial graphite cathode tubes (28), a microporous ceramic tube (29), a large cast iron tube shell (30), the large cast iron tube chimney (31) has the same diameter as the artificial graphite anode tube (26), the large cast iron tube chimney (31) is mounted on the artificial graphite anode tube (26) through an insulating ceramic connecting tube, the small cast iron tube chimney (32) has the same diameter as the artificial graphite cathode tube (28), the small cast iron tube chimney (32) is mounted on the artificial graphite cathode tube (28) through an insulating ceramic connecting tube, the gap between the large cast iron tube chimney (31) and the small cast iron tube shell (33) is filled with water-coal slurry, the artificial graphite anode tube (26) and the microporous ceramic tube are connected. Coal powder is filled in the gap between the porcelain tubes (29), calcium hydroxide powder is filled in the gap between the microporous ceramic tube (29) and the large cast iron tube shell (30), several radiation chimneys are horizontally installed between the large cast iron tube chimney (31) and a circle of several small cast iron tube chimneys (32), a furnace target is installed in the gap between the lower end of the artificial graphite anode tube (26) and the lower end of the microporous ceramic tube (29), a slag chamber is arranged below the furnace target, the lower end of the artificial graphite anode tube (26) and the lower end of a circle of several artificial graphite cathode tubes (28) pass through the bottom of the slag chamber, and an insulating layer is installed between the lower end of the artificial graphite anode tube (26) and the lower end of a circle of several artificial graphite cathode tubes (28) and the bottom of the slag chamber. An electric cinder valve is installed at the bottom of the cinder chamber between the ceramic tube sleeve, the lower end of the artificial graphite anode tube (26) and the lower end of a circle of artificial graphite cathode tubes (28). The electric cinder valve has the following structure: the electric cinder valve consists of a left half annular valve disc, a front hinge, a front DC motor, a right half annular valve disc, a rear hinge and a rear DC motor. The left half annular valve disc and the right half annular valve disc are hinged at a diameter position. The front section of the left half annular valve disc is fixed on the front hinge rotating shaft, which is fixedly connected to the front DC motor rotating shaft. The rear section of the right half annular valve disc is fixed on the rear hinge rotating shaft, which is fixedly connected to the rear DC motor rotating shaft.An electric calcium hydroxide powder cover is installed at the upper end of the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30). The electric calcium hydroxide powder cover has the following structure: the electric calcium hydroxide powder cover consists of a left half annular valve plate, a left output shaft, a left DC motor, a right half annular valve plate, a right output shaft and a right DC motor. The outer arc top of the left half annular cover is fixed at the middle position of the left output shaft, and the left output shaft is fixedly connected to the left DC motor shaft. The outer arc top of the right half annular cover is fixed at the middle position of the right output shaft, and the right output shaft is fixedly connected to the right DC motor shaft. An electric calcium hydroxide powder valve is installed at the lower end of the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30). The electric calcium hydroxide powder valve has the following structure: the electric calcium hydroxide powder valve consists of a left half annular valve disc, a left output shaft, a left DC motor, a right half annular valve disc, a right output shaft and a right DC motor. The outer arc top of the left half annular valve disc is fixed at the middle position of the left output shaft, and the left output shaft is fixedly connected to the left DC motor shaft. The outer arc top of the right half annular valve disc is fixed at the middle position of the right output shaft, and the right output shaft is fixedly connected to the right DC motor shaft.

7. The hydrogen production equipment by electrolyzing water vapor and acid mist according to claim 6, characterized in that: The water pipe connected from the lower side of the water tank (4) is connected to the inlet of the water pump (5), the water pipe connected from the water pump (5) is connected to the inlet of the electric regulating water valve (36), the branch water pipes connected from the electric regulating water valve (36) are respectively connected to the cooling water jacket inlet of the water cooler of the mixed gas thermomagnetic power generation device (41) and the cooling water jacket inlet of the mixed gas cooling separator (45), the water pipes connected from the cooling water jacket of the water cooler of the mixed gas thermomagnetic power generation device (41) and the cooling water jacket of the mixed gas cooling separator (45) are connected to the water-coal slurry power generation device (41). The left inlet of the top of the dynamic stirring and extruding kettle (37) and the discharge port of the coal powder hopper (34) are equipped with an electric rotary butterfly valve. The coal powder hopper (34) is at the upper left of the starting end of the electric belt conveyor (35). The terminal of the electric belt conveyor (35) extends into the left inlet of the top of the water-coal slurry electric stirring and extruding kettle (37). The bottom outlet of the water-coal slurry electric stirring and extruding kettle (37) and the outlet of the water-coal slurry electric spiral extruding conveyor (38) are connected to the gap between the large cast iron pipe chimney (31) and the upper end of the small cast iron pipe shell (33) through a special-shaped elbow.

8. The hydrogen production equipment by electrolyzing water vapor and acid mist according to claim 6, characterized in that: The gas outlet of the large cast iron pipe shell (30) is equipped with a foam cast iron plate, the mixed gas pipe connected to the gas outlet of the large cast iron pipe shell (30) is connected to the inlet of each magnetic pole heating pipe of the stator of the mixed gas thermomagnetic power generation device (41), and several mixed gas pipes connected to the inlet of several hot channels of the water cooler of the mixed gas thermomagnetic power generation device (41) are connected to the inlet of several hot channels of the water cooler of the mixed gas thermomagnetic power generation device (41). The mixed gas pipes are connected to the bottom of the condensed water container of the water cooler of the mixed gas thermomagnetic power generation device (41), the water pipes connected from the bottom of the condensed water container of the water cooler of the mixed gas thermomagnetic power generation device (41) are connected to the inlet of the mixed gas condensed water pump (42), the water pipes connected from the mixed gas condensed water pump (42) are connected to the inlet of the mixed gas condensed water check valve (43), and the water pipes connected from the mixed gas condensed water check valve (43) are connected to the top inlet of the water tank (4); the water pipes connected from the mixed gas thermomagnetic power generation device (41) are connected to the inlet of the mixed gas condensed water check valve (43). The mixed gas pipe connected to the top of the condensed water container of the water cooler (41) is connected to the inlet of the mixed gas compressor (44), the mixed gas pipe connected to the mixed gas compressor (44) is connected to the inlet of the hot channel of the mixed gas cooling separator (45), the mixed gas pipe connected to the hot channel of the mixed gas cooling separator (45) is connected to the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator (45), the liquid carbon dioxide pipe connected to the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator (45) is connected to the inlet of the liquid carbon dioxide electromagnetic valve (13), and the liquid carbon dioxide pipe connected to the liquid carbon dioxide electromagnetic valve (13) is connected to the bottom of the carbon dioxide storage tank (9); the hydrogen pipe connected to the top of the condensed liquid carbon dioxide tank of the mixed gas cooling separator (45) is connected to the inlet of the hydrogen check valve (18), and the hydrogen pipe connected to the hydrogen check valve (18) is connected to the top inlet of the hydrogen tank (19); the top of the hydrogen tank (19) is equipped with an electromagnetic exhaust valve, and the top of the hydrogen tank (19) is equipped with a pressure relay.

9. The hydrogen production equipment according to claim 6, characterized in that: A basin-shaped steel wire mesh is installed below the slag chamber to prevent slag from falling into the slag circulating fluidized bed furnace (39). A slag pipe is installed below the center hole of the basin-shaped steel wire mesh of the slag circulating fluidized bed furnace (39). The air outlet of the air duct connected to the electric blower (40) is below the basin-shaped steel wire mesh of the slag circulating fluidized bed furnace (39).

10. The control method of the hydrogen production equipment by electrolyzing water vapor and acid mist according to claim 6, or claim 7, or claim 8, or claim 9, characterized in that: The electric slag valve installed at the bottom of the slag chamber between the lower end of the artificial graphite anode tube (26) and the lower end of a circle of data root artificial graphite cathode tubes (28) is in a closed state, and the electric calcium hydroxide powder valve installed at the lower end of the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30) is in a closed state. The computer controller provides reverse DC power to the left DC motor and the right DC motor of the electric calcium hydroxide powder cover, so that the left half of the annular valve plate and the right half of the annular cover are rotated upward to a set angle to open. The computer controller stops supplying reverse DC power to the front DC motor and the rear DC motor of the electric calcium hydroxide powder valve, and fills the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30) with calcium hydroxide powder. Then the computer controller provides positive direct current to the left DC motor and the right DC motor of the electric calcium hydroxide powder cover, so that the left half annular valve plate and the right half annular cover rotate downward to a set angle and close, and the computer controller stops supplying positive direct current to the left DC motor and the right DC motor of the electric calcium hydroxide powder cover; put some coal powder on the basin-shaped steel wire mesh of the coal slag circulating fluidized bed furnace (39), spray diesel on the coal powder on the basin-shaped steel wire mesh of the coal slag circulating fluidized bed furnace (39), ignite the coal powder on the basin-shaped steel wire mesh of the coal slag circulating fluidized bed furnace (39), and the computer controller starts the electric blower (40), and the wind blown out from the electric blower (40) is blown out from the basin-shaped steel wire mesh of the coal slag circulating fluidized bed furnace (39) The net is blown upward to support the combustion of coal powder on the basin-shaped steel wire mesh of the coal slag circulating fluidized bed furnace (39); the computer controller starts the electric rotary butterfly valve installed at the discharge port of the coal powder hopper (34), and the coal powder in the coal powder hopper (34) leaks to the starting end of the electric belt conveyor (35). The computer controller starts the electric belt conveyor (35), and the electric belt conveyor (35) puts the coal powder into the water-coal slurry electric stirring extrusion kettle (37); the computer controller starts the water pump (5) and adjusts the electric regulating water valve (36). The water pump (5) draws out the water from the water tank (4) through the electric regulating water valve (36) and presses it into the cooling water jacket of the water cooler of the mixed gas thermomagnetic power generation device (41) and the cooling water of the mixed gas cooling separator (45). Water jacket, water from the cooling water jacket of the water cooler of the mixed gas body thermomagnetic power generation device (41) and the cooling water jacket of the mixed gas cooling separator (45) enters the water-coal slurry electric stirring extrusion kettle (37), the computer controller starts the water-coal slurry electric stirring extrusion kettle (37), and the water-coal slurry containing a small amount of water in the initial stage is pressed into the water-coal slurry electric screw extrusion conveyor (38), the computer controller starts the water-coal slurry electric screw extrusion conveyor (38), and the water-coal slurry electric screw extrusion conveyor (38) presses the water-coal slurry containing a small amount of water into the gap between the large cast iron pipe chimney (31) and the upper end of the small cast iron pipe shell (33) through the elbow, and then enters the gap between the artificial graphite anode tube (26) and the microporous ceramic tube (29);The flue gas generated by the combustion of coal powder on the basin-shaped steel wire mesh of the coal slag circulating fluidized bed furnace (39) passes through the artificial graphite anode tube (26) and a circle of several artificial graphite cathode tubes (28), heats the artificial graphite anode tube (26) and a circle of several artificial graphite cathode tubes (28), heats the water-coal slurry contained in the gap between the artificial graphite anode tube (26) and the microporous ceramic tube (29), generates a large amount of water vapor and turns into red-hot coal powder; then passes through the large cast iron pipe chimney (31) and a circle of several small cast iron pipe chimneys (32), heats the large cast iron pipe chimney (31) and the small cast iron pipe shell (33) The gap between the two tubes is filled with water-coal slurry, which generates a large amount of water vapor. The computer controller passes a high-voltage direct current with low-voltage high-frequency alternating current harmonics between the artificial graphite anode tube (26) and the artificial graphite cathode tube (28). The low-voltage high-frequency alternating current causes the water vapor between the artificial graphite anode tube (26) and the artificial graphite cathode tube (28) to oscillate and generate heat. Under the action of a strong stable electric field and a weak alternating electric field, the water vapor between the artificial graphite anode tube (26) and the artificial graphite cathode tube (28) is separated into negatively charged hydroxyl anion droplets and positively charged hydrogen cation droplets. The negatively charged hydroxyl anion droplets quickly move toward the artificial graphite anode tube (26), and lose electrons in the artificial graphite anode tube (26), releasing oxygen and water vapor. The positively charged hydrogen cation droplets quickly move toward the artificial graphite cathode tube (28), and gain electrons in the artificial graphite cathode tube (28), releasing hydrogen. The oxygen reacts chemically with the 400°C coal powder in the gap between the artificial graphite anode tube (26) and the microporous ceramic tube (29) to generate carbon dioxide and generate a large amount of heat. The oxygen reacts with the artificial graphite anode tube (26) and the microporous ceramic tube (29). The sulfur in the 400°C coal powder contained in the gap undergoes a chemical reaction to generate sulfur dioxide and generate a large amount of heat. The carbon dioxide is absorbed by water vapor to generate carbonic acid mist droplets, and the sulfur dioxide is absorbed by water vapor to generate sulfite mist droplets. The computer controller reduces the voltage of the direct current with low-voltage high-frequency alternating current harmonics passed between the artificial graphite anode tube (26) and the artificial graphite cathode tube (28). The low-voltage high-frequency alternating current causes the carbonic acid mist droplets and the sulfite mist droplets between the artificial graphite anode tube (26) and the artificial graphite cathode tube (28) to vibrate and generate heat.Under the action of a strong stable electric field and a weak alternating electric field, the polar droplets of carbonate mist between the artificial graphite anode tube (26) and the artificial graphite cathode tube (28) are separated into negatively charged carbonate anion droplets and positively charged hydrogen cation droplets, and the polar droplets of sulfite mist are separated into negatively charged sulfite anion droplets and positively charged hydrogen cation droplets. The negatively charged carbonate anion droplets quickly move toward the artificial graphite anode tube (26) and lose electrons in the artificial graphite anode tube (26), releasing oxygen and carbon dioxide. The positively charged hydrogen cation droplets quickly move toward the artificial graphite powder cathode tube (28) and release electrons in the artificial graphite cathode tube (28). The water vapor obtains electrons and releases hydrogen, and the negatively charged sulfite anion droplets quickly move to the artificial graphite anode tube (26), and lose electrons in the artificial graphite anode tube (26), releasing oxygen and sulfur dioxide. The positively charged hydrogen cation droplets quickly move to the artificial graphite cathode tube (28), and obtain electrons in the artificial graphite powder cathode tube (28), releasing hydrogen. The water vapor reacts chemically with the 700°C red-hot coal powder contained in the gap between the artificial graphite anode tube (26) and the microporous ceramic tube (29) to generate hydrogen and carbon monoxide, and absorbs a large amount of heat. The carbon monoxide reacts chemically with oxygen at high temperature to generate carbon dioxide, and generates a large amount of heat. The computer controller energizes the mixed gas compressor (44), and the mixed gas compressor (44) sucks the mixed gas into the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30). The mixed gas containing gaseous water passes through the micropores of the outer ceramic tube (29) and enters the annular gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30). At high temperature, sulfur dioxide reacts with calcium hydroxide powder contained in the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30) to generate calcium sulfite and water. The mixed gas compressor (44) sucks the mixed gas in the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30) into the stator of the mixed gas thermomagnetic power generation device (41). The stator magnetic poles of the mixed gas thermomagnetic power generation device (41) are heated by the stator magnetic poles heating tubes, so that the stator magnetic poles of the mixed gas thermomagnetic power generation device (41) are converted from non-magnetic materials into magnetic materials. The computer controller supplies alternating current to the stator excitation coil of the mixed gas thermomagnetic power generation device (41). The mixed gas thermomagnetic power generation device (41) converts thermal energy into magnetic energy. Under the action of the alternating magnetic field of the stator magnetic poles of the mixed gas thermomagnetic power generation device (41), amplified electric energy is generated in the stator power generation coil of the mixed gas thermomagnetic power generation device (41). The mixed gas discharged from the stator magnetic pole heating tubes of the mixed gas thermomagnetic power generation device (41) is cooled in the hot channel of the water cooler of the mixed gas thermomagnetic power generation device (41). One-step cooling: the mixed gas discharged from the hot channel of the water cooler of the mixed gas thermomagnetic power generation device (41) enters the bottom of the condensed water container of the water cooler of the mixed gas thermomagnetic power generation device (41); the water discharged from the bottom of the condensed water container of the water cooler of the mixed gas thermomagnetic power generation device (41) enters the mixed gas condensed water pump (42); the computer controller starts the mixed gas condensed water pump (42) at a fixed time; the water discharged from the mixed gas condensed water pump (42) passes through the mixed gas condensed water one-way valve (43) and is pressed into the water tank (4); the mixed gas discharged from the top of the condensed water container of the water cooler of the mixed gas thermomagnetic power generation device (41) enters the mixed gas compressor (44); the mixed gas compressor (44) The mixed gas discharged is pressed into the hot channel of the mixed gas cooling separator (45), and the mixed gas discharged from the hot channel of the mixed gas cooling separator (45) is pressed into the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator (45). The high-pressure carbon dioxide gas is cooled into liquid carbon dioxide and retained at the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator (45). The computer controller energizes and opens the liquid carbon dioxide solenoid valve (13) at a fixed time. The liquid carbon dioxide at the bottom of the condensed liquid carbon dioxide tank of the mixed gas cooling separator (45) passes through the opened liquid carbon dioxide solenoid valve (13) and enters the bottom of the carbon dioxide storage tank (9). Then the computer controller closes the liquid carbon dioxide solenoid valve (13);The hydrogen gas discharged from the top of the condensed liquid carbon dioxide tank of the mixed gas cooling separator (45) is pressed into the hydrogen tank (19) through the hydrogen one-way valve (18); in the early stage of hydrogen production by electrolyzing water vapor acid mist, the computer controller energizes and opens the electromagnetic exhaust valve installed on the top of the hydrogen tank (19), and discharges the air in the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30), the mixed gas thermomagnetic power generation device (41), the mixed gas compressor (44), the mixed gas cooling separator (45), and the hydrogen tank (19), and then the computer controller closes the electromagnetic exhaust valve installed on the top of the hydrogen tank (19); oxygen and artificial graphite anode are discharged. The 700℃ coal powder contained in the gap between the artificial graphite anode tube (26) and the microporous ceramic tube (29) reacts chemically to generate carbon dioxide and generates a large amount of heat. The water vapor reacts chemically with the 700℃ coal powder contained in the gap between the artificial graphite anode tube (26) and the microporous ceramic tube (29) to generate hydrogen and carbon monoxide, and absorbs a large amount of heat, consuming the carbon in the 700℃ coal powder contained in the gap between the artificial graphite anode tube (26) and the microporous ceramic tube (29) and turning into coal slag, which leaks from the furnace rake installed at the lower end of the gap between the artificial graphite anode tube (26) and the microporous ceramic tube (29) into the coal slag chamber, and the computer controller stops feeding the mixed gas. The gas compressor (44) is powered, and then the computer controller provides positive DC power to the front DC motor and the rear DC motor of the electric slag valve, so that the left half annular valve disc and the right half annular valve disc rotate downward and open. After the left half annular valve disc and the right half annular valve disc rotate downward to a set angle, the computer controller stops providing positive DC power to the front DC motor and the rear DC motor of the electric slag valve, and unloads the slag in the slag chamber onto the basin-shaped steel wire mesh of the slag circulating fluidized bed furnace (39), and mixes with the coal powder on the basin-shaped steel wire mesh of the slag circulating fluidized bed furnace (39) to burn. After the slag in the slag chamber is unloaded, the computer controller stops providing positive DC power to the front DC motor and the rear DC motor of the electric slag valve. The controller provides reverse DC power to the front DC motor and the rear DC motor of the electric cinder valve, so that the left half annular valve disc and the right half annular valve disc rotate upward to a set angle and close. The computer controller stops supplying reverse DC power to the front DC motor and the rear DC motor of the electric cinder valve, and the computer controller restarts supplying power to the mixed gas compressor (44); sulfur dioxide reacts chemically with calcium hydroxide powder contained in the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30) at high temperature to generate calcium sulfite and water vapor, consuming the calcium hydroxide powder contained in the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30);The computer controller stops supplying power to the mixed gas compressor (44), and then the computer controller provides positive direct current to the left DC motor and the right DC motor of the electric calcium hydroxide powder valve, so that the left half annular valve disc and the right half annular valve disc rotate downward and open. After the left half annular valve disc and the right half annular valve disc rotate downward by a set angle, the computer controller stops providing positive direct current to the front DC motor and the rear DC motor of the electric calcium hydroxide powder valve, and unloads the calcium hydroxide powder containing a large amount of calcium sulfite in the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30). After the calcium hydroxide powder containing a large amount of calcium sulfite in the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30) is unloaded, reverse direct current is provided to the front DC motor and the rear DC motor of the electric calcium hydroxide powder valve, so that the left half annular valve disc and the right half annular valve disc rotate upward by a set angle. The electric calcium hydroxide powder valve is closed, and the computer controller stops supplying reverse DC power to the front DC motor and the rear DC motor of the electric calcium hydroxide powder valve; the computer controller supplies reverse DC power to the left DC motor and the right DC motor of the electric calcium hydroxide powder cover, so that the left half annular valve disc and the right half annular cover rotate upwards to a set angle to open; the computer controller stops supplying reverse DC power to the front DC motor and the rear DC motor of the electric calcium hydroxide powder valve, and fills the gap between the microporous ceramic tube (29) and the large cast iron pipe shell (30) with calcium hydroxide powder; then the computer controller supplies forward DC power to the left DC motor and the right DC motor of the electric calcium hydroxide powder cover, so that the left half annular valve disc and the right half annular cover rotate downwards to a set angle to close; the computer controller stops supplying forward DC power to the left DC motor and the right DC motor of the electric calcium hydroxide powder cover; the computer controller re-powers the mixed gas compressor (44).

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