Full-intelligent oxyhydrogen production system equipment

The fully intelligent hydrogen and oxygen production system uses electrolysis of pure water to generate hydrogen and oxygen, solving the safety, environmental protection, and efficiency problems of traditional gaseous fuels in boiler soot blowing and dust removal, and providing an efficient and inexpensive energy solution.

CN121759967APending Publication Date: 2026-03-31HENAN NORTH LONGYUAN ELECTRIC POWER DEV CO LTD
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-12-31
Publication Date
2026-03-31

AI Technical Summary

Technical Problem

Traditional gaseous fuels pose safety hazards, pollute the environment, consume high energy, are inefficient, require frequent equipment maintenance, and are complex to operate in boiler soot blowing and dust removal, making it difficult to meet the high-quality development needs of modern industry.

Method used

The system employs a fully intelligent hydrogen and oxygen production system, including a control and management system, an electrolysis reaction device, a separation and purification device, a material storage device, and a circulating cooling device. It generates hydrogen and oxygen by electrolyzing pure water, achieving intelligent control and unattended operation. Hydrogen and oxygen are used as high-energy fuels to replace traditional gases for combustion.

Benefits of technology

It achieves a highly safe, environmentally friendly, low-energy-consumption, and highly efficient energy supply, eliminates safety hazards in gas storage, reduces equipment maintenance costs, and adapts to various working conditions.

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Abstract

The invention relates to the technical field of clean energy preparation, and discloses full-intelligent oxyhydrogen production system equipment which comprises a control management system, an electrolytic reaction device, a separation and purification device, a material storage device, a circulating and cooling device and a structure supporting assembly. The control management system is electrically connected with the electrolytic reaction device, the separation and purification device, the material storage device and the circulation and cooling device and used for achieving full-process intelligent regulation and control, and the structure supporting assembly is used for achieving positioning installation of all the devices and structural stability of the whole equipment. According to the full-intelligent oxyhydrogen gas production system equipment, electricity serves as power, pure water and independent property electrolyte serve as raw materials, oxyhydrogen gas generated through electrolysis serves as high-energy fuel gas, and energy can be saved by 80% or above; a ready-to-use and ready-to-produce mode is adopted, a gas source does not need to be stored, and potential safety hazards of gas storage are eliminated from the source; and in the soot blowing operation process, carbon emission is zero, no harmful gas is generated, and cleanliness and environmental protection are achieved.
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Description

Technical Field

[0001] This invention relates to the field of clean energy production technology, and in particular to a fully intelligent system for producing hydrogen and oxygen. Background Technology

[0002] In boiler soot blowing and dust removal and related combustion operations in industries such as metal smelting, power generation, and heat production and supply, liquefied petroleum gas (LPG), acetylene, and natural gas are currently the most widely used energy carriers on the market. However, in practical applications, these traditional gases have gradually revealed a series of unavoidable technical defects and application pain points, which not only restrict the improvement of industry production efficiency but also bring significant safety hazards and environmental pressures, becoming a prominent bottleneck for the high-quality development of the industry.

[0003] From a safety perspective, liquefied petroleum gas (LPG), acetylene, and other gases are flammable and explosive substances. Their use requires specialized gas source storage, a process that inherently poses a high safety risk. Leaks or improper operation can easily lead to combustion and explosion accidents, severely threatening the lives and property of personnel and property on the production site. Regarding operational reliability and ash removal capabilities, traditional gas combustion exhibits poor stability, and flame temperature and intensity are difficult to control precisely, resulting in inconsistent ash removal effects. Often, it fails to completely remove ash accumulation from boiler heating surfaces, thus affecting boiler thermal efficiency. Furthermore, the combustion of these gases easily produces carbon deposits and other residues, potentially exacerbating equipment contamination and further reducing operational reliability.

[0004] Traditional gas combustion emits large amounts of harmful gases such as carbon dioxide and sulfides, resulting in high carbon emissions. This not only violates the current development concept of low-carbon and environmental protection but also pollutes the atmosphere. Furthermore, its energy utilization efficiency is extremely low, with a large amount of energy being lost as heat during combustion, leading to serious energy waste and high energy costs for enterprises.

[0005] In terms of equipment operation and maintenance, traditional gas combustion systems rely on large auxiliary equipment, which occupies a large area and has high initial investment costs. The operation process is complicated and requires professional personnel to monitor and control it in real time, which increases labor costs. In addition, the equipment is prone to failure, with frequent and expensive repairs. At the same time, the high-temperature flame and corrosive products generated by combustion can also damage the furnace body, shorten the service life of the equipment, and further increase the operational burden of enterprises.

[0006] Faced with the multiple problems mentioned above, such as significant safety hazards, poor ash removal capacity, environmental pollution, excessive energy consumption, low efficiency, poor reliability, high maintenance costs, damage to the furnace body, and complex operation, the industry urgently needs a new type of energy supply system equipment that can break through the limitations of traditional technology and has the characteristics of being inexpensive, energy-saving, efficient, safe, and environmentally friendly. This is to meet the high-quality energy utilization requirements of modern industrial production and promote the green, safe, and efficient development of related industries.

[0007] Therefore, those skilled in the art urgently need to develop a fully intelligent system for producing hydrogen and oxygen. Summary of the Invention

[0008] The purpose of this invention is to overcome the shortcomings of existing technologies and to propose a fully intelligent system for producing hydrogen and oxygen.

[0009] To achieve the above objectives, the present invention adopts the following technical solution: a fully intelligent system for producing hydrogen and oxygen, comprising a control and management system, an electrolysis reaction device, a separation and purification device, a material storage device, a circulation and cooling device, and a structural support component. The control and management system is electrically connected to the electrolysis reaction device, the separation and purification device, the material storage device, and the circulation and cooling device to achieve intelligent control of the entire process. The structural support component is used to achieve the positioning and installation of each device and the structural stability of the entire equipment. The electrolysis reaction device includes a left electrolytic cell and a right electrolytic cell; the separation and purification device includes a primary left separation tank, a primary right separation tank, a filter residue tank, and a secondary separation tank, wherein the primary left separation tank and the primary right separation tank are interconnected; the material storage device includes a left liquid storage tank and a right liquid storage tank, wherein the left liquid storage tank and the right liquid storage tank are interconnected. The left electrolytic cell is connected to the primary left separation tank, the right electrolytic cell is connected to the primary right separation tank, the left storage tank is connected to both the primary left and primary right separation tanks, the right storage tank is connected to the secondary separation tank, the right storage tank is connected to the filter residue tank via a circulation and cooling device, and the filter residue tank is connected to both the left and right electrolytic cells.

[0010] Preferably, the circulation and cooling device includes a cooler and a circulation pump. The inlet end of the circulation pump is in fluid communication with the right storage tank, and the outlet end is in fluid communication with the inlet end of the cooler. The cooler is equipped with a cooling pump, and the outlet end of the cooler is connected to the filter residue tank.

[0011] Preferably, a replenishing pump is connected to the left liquid storage tank, the inlet of which is connected to an external electrolyte storage tank, and the outlet is connected to the inside of the left liquid storage tank.

[0012] Preferably, the control and management system includes an automatic control system and a sub-control system. The automatic control system and the sub-control system are bidirectionally electrically connected. The automatic control system provides electrolysis parameter regulation and safety control for the left and right electrolytic cells. The sub-control system is used to collect operating parameters such as pressure, temperature, and liquid level, and feed the parameters back to the automatic control system.

[0013] Preferably, the control and management system further includes temperature sensors, liquid level sensors, and pressure sensors. There are three temperature sensors, used to monitor the real-time temperature of the electrolyte in the pipeline, the electrolyte in the left electrolytic cell, and the electrolyte in the right electrolytic cell, respectively. There are two liquid level sensors, used to monitor the liquid levels in the left and right storage tanks, respectively. The pressure sensor is used to monitor the pressure of the produced hydrogen and oxygen in real time. All sensors are connected to the sub-control system signal.

[0014] Preferably, the structural support assembly includes an electrolytic cell frame and a main equipment frame, with both the left and right electrolytic cells mounted on the electrolytic cell frame, and the main equipment frame providing overall structural support for the entire system.

[0015] Preferably, both the left and right electrolytic cells are equipped with arrayed electrode groups and ion exchange membranes. The top of the left and right electrolytic cells is equipped with gas-liquid outlet pipes, which are respectively connected to the primary left separation tank and the primary right separation tank.

[0016] Preferably, the top of the secondary separation tank is provided with a hydrogen outlet pipe and an oxygen outlet pipe, and each outlet pipe is equipped with a one-way valve and a flow sensor.

[0017] Compared with the prior art, the beneficial effects of the present invention are: The fully intelligent hydrogen and oxygen production system equipment involved in this invention uses electricity as power and pure water plus proprietary electrolyte as raw materials. The hydrogen and oxygen produced by electrolysis are high-energy fuels, which can achieve energy saving of more than 80%. It adopts an on-demand production mode, eliminating the need to store gas sources and eliminating the safety hazards of gas storage from the source. After combustion, it is reduced to water only. The carbon emissions during the soot blowing operation are zero and no harmful gases are generated, achieving clean and environmentally friendly operation.

[0018] By monitoring the electrolyte temperature, level, and gas pressure in real time through a sub-control system, intelligent control and unattended operation of hydrogen and oxygen production can be achieved, adapting to various working conditions and providing inexpensive and efficient energy solutions for related industries. Attached Figure Description

[0019] Figure 1 This is a front view structural diagram of the present invention; Figure 2 This is a top view of the structure of the present invention; Figure 3 This is a diagram showing the connection relationships of the various components of the present invention; Figure 4 This is a circuit diagram of the control system described in this invention.

[0020] In the diagram: 1. Automatic control system; 2. Sub-control system; 3. Left electrolytic cell; 4. Right electrolytic cell; 5. Primary left separator; 6. Primary right separator; 7. Left storage tank; 8. Right storage tank; 9. Filter residue tank; 10. Secondary separator; 11. Cooler; 12. Cooling pump; 13. Make-up pump; 14. Circulation pump; 15. Electrolytic cell frame; 16. Main frame of the equipment. Detailed Implementation

[0021] The present invention will now be clearly described with reference to the accompanying drawings and specific embodiments. This description is merely illustrative and is not intended to limit the scope of the invention. Any modifications, equivalent substitutions, or improvements made by those skilled in the art based on the embodiments of the present invention without inventive effort to obtain all other embodiments should be included within the scope of protection of the present invention.

[0022] In the description of this invention, it should be noted that the terms "center," "upper," "lower," "left," "right," "vertical," "horizontal," "inner," and "outer," etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are used only for the convenience of describing the invention and for simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on the invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and should not be construed as indicating or implying relative importance.

[0023] In the description of this invention, it should be noted that, unless otherwise explicitly specified and limited, the terms "installation," "connection," and "linking" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; and they can refer to the internal connection of two components. Those skilled in the art can understand the specific meaning of the above terms in this invention based on the specific circumstances.

[0024] Please see Figures 1-4 The present invention provides an embodiment of a fully intelligent system for producing hydrogen and oxygen, comprising a control and management system, an electrolysis reaction device, a separation and purification device, a material storage device, a circulation and cooling device, and a structural support component. The control and management system is electrically connected to the electrolysis reaction device, the separation and purification device, the material storage device, and the circulation and cooling device to achieve intelligent control of the entire process. The structural support component is used to achieve the positioning and installation of each device and the structural stability of the entire equipment.

[0025] The electrolysis reaction device includes a left electrolytic cell 3 and a right electrolytic cell 4; the separation and purification device includes a primary left separation tank 5, a primary right separation tank 6, a filter residue tank 9, and a secondary separation tank 10, with the primary left separation tank 5 and the primary right separation tank 6 interconnected; the material storage device includes a left liquid storage tank 7 and a right liquid storage tank 8, with the left liquid storage tank 7 and the right liquid storage tank 8 interconnected.

[0026] The left electrolytic cell 3 is connected to the primary left separation tank 5, the right electrolytic cell 4 is connected to the primary right separation tank 6, the left storage tank 7 is connected to the primary left separation tank 5 and the primary right separation tank 6 respectively, the right storage tank 8 is connected to the secondary separation tank 10, the right storage tank 8 is connected to the filter residue tank 9 through a circulation and cooling device, and the filter residue tank 9 is connected to the left electrolytic cell 3 and the right electrolytic cell 4 respectively.

[0027] The primary left separator 5 and the primary right separator 6 separate the gas and liquid flowing out of the electrolytic cell; the left and right storage tanks 7 and 8, under the monitoring of the sub-control system 2, replenish pure water in a timely manner to ultimately provide the electrolysis system with a stable concentration of electrolyte; the filter tank 9 filters impurities in the electrolyte to ensure that the electrolyte entering the electrolytic cell is free of impurities, thus ensuring the safe and stable operation of the electrolytic cell; the secondary separator 10 further separates the hydrogen and oxygen from the storage tank into gas and liquid, ensuring the dryness of the gas.

[0028] Furthermore, the circulation and cooling device includes a cooler 11 and a circulation pump 14. The inlet end of the circulation pump 14 is in fluid communication with the right liquid storage tank, and the outlet end is in fluid communication with the liquid inlet end of the cooler 11. The cooler 11 is equipped with a cooling pump 12, and the liquid outlet end of the cooler 11 is connected to the filter residue tank 9. The left liquid storage tank 7 is connected to a replenishment pump 13. The inlet end of the replenishment pump 13 is connected to an external electrolyte storage tank, and the outlet end is in communication with the inside of the left liquid storage tank 7.

[0029] The cooler 11 uses water cooling to control the temperature of the electrolyte within the design range; the cooling pump 12 provides circulating cooling water to the cooler 11; the initial electrolyte injection and the replenishment of pure water during equipment operation are both achieved through the replenishment pump 13; the circulation pump 14 provides power to the electrolyte circulation system.

[0030] Furthermore, the control and management system includes an automatic control system 1 and a sub-control system 2. The automatic control system 1 and the sub-control system 2 are bidirectionally electrically connected. The automatic control system 1 provides electrolysis parameter regulation and safety control for the left electrolytic cell 3 and the right electrolytic cell 4. The sub-control system 2 is used to collect operating parameters such as pressure, temperature, and liquid level, and feed the parameters back to the automatic control system 1 for real-time monitoring to achieve precise control of the equipment and realize intelligent control and unattended operation of hydrogen and oxygen production.

[0031] Furthermore, the control and management system also includes temperature sensors, liquid level sensors, and pressure sensors. There are three temperature sensors used to protect and control the start and stop of the electrolysis power supply and cooling water supply, as well as the equipment.

[0032] Three temperature sensors ( Figure 4 Temperature sensors 1, 2, and 3 are used to monitor the temperature of the electrolyte in the pipeline in real time. Figure 4 Temperature sensor 1 in the middle), electrolyte temperature in the left electrolytic cell 3 ( Figure 4 Temperature sensor 2), electrolyte temperature in right electrolytic cell 4 ( Figure 4 Medium temperature sensor 3); Figure 4 Temperature sensor 1 monitors the solution temperature. When the solution temperature rises to 75°C, cooling pump 12 is started to draw cooling water to cooler 11 to cool the electrolyte. When the temperature drops to 55°C, cooling pump 12 is stopped.

[0033] Figure 4 Temperature sensors 2 and 3 monitor the solution temperature in electrolytic cells 1 and 2. When the solution temperature exceeds 80 degrees Celsius, the electrolysis power supply is turned off, and cooling pump 12 is turned on to cool the solution. Once the temperature drops, the electrolysis power supply automatically restarts. Figure 4 Temperature sensor 2 and temperature sensor 3 are used to protect the electrolysis process and control it to prevent power consumption and gas production (energy saving).

[0034] Figure 4 The liquid level sensor has one pair to monitor the liquid level of the left liquid tank 7 and the right liquid tank 8 in real time. When the liquid level of the left liquid tank 7 and the right liquid tank 8 reaches the set lower limit value of the solution, the replenishment pump 13 is automatically started to replenish the liquid in the storage tank. When the set upper limit of the liquid level is reached, the replenishment pump 13 is automatically turned off.

[0035] Figure 4 The medium pressure sensor is used to monitor the pressure of the produced hydrogen and oxygen in real time. Each sensor is connected to the host RS485 communication signal. When the equipment pressure reaches the set pressure limit, the electrolysis power supply is turned off to stop electrolysis and gas production. When the pressure drops after the gas is used, the electrolysis power supply is automatically turned on to start electrolysis and gas production again.

[0036] The main intelligent control of the host includes: all data is collected by the host and communicated with the Siemens Smart 200 PLC and the rectifier power supply via RS485 to monitor the equipment temperature, liquid level and pressure in real time. The start and stop control of the rectifier is displayed on the MGCS touch screen, which can intuitively monitor the real-time temperature, real-time liquid level and real-time pressure of the equipment, and can control the start and stop of the DC current rectifier of the electrolytic cell according to the real-time pressure.

[0037] Once the pressure is reached, the DC rectifier is shut off. After the hydrogen and oxygen are used (for on-site blasting and ash removal), the pressure drops, and the rectifier power supply starts to regenerate oxygen to ensure the lower pressure limit for the next blast. A flow sensor detects whether there is water in the pipeline to prevent the water pump from running dry and burning out the motor in the absence of water, thus enabling unattended operation of the equipment.

[0038] Furthermore, the structural support components include an electrolytic cell frame 15 and an equipment body frame 16. The left electrolytic cell 3 and the right electrolytic cell 4 are both mounted on the electrolytic cell frame 15, and the equipment body frame 16 provides overall structural support for the entire system.

[0039] Furthermore, both the left electrolytic cell 3 and the right electrolytic cell 4 are equipped with arrayed electrode groups and ion exchange membranes. The top of the left electrolytic cell 3 and the right electrolytic cell 4 are equipped with gas-liquid outlet pipes, which are respectively connected to the primary left separation tank 5 and the primary right separation tank 6.

[0040] Furthermore, the top of the secondary separation tank 10 is equipped with a hydrogen outlet pipe and an oxygen outlet pipe, and each outlet pipe is equipped with a one-way valve and a flow sensor.

[0041] The working principle of this invention is as follows: using ordinary pure water as the basic raw material, adding alkaline electrolyte, and using electricity as power, water is electrolyzed into hydrogen and oxygen; hydrogen and oxygen are used as high-energy fuel gas to replace gases such as acetylene and natural gas for combustion and explosion; the fully intelligent hydrogen and oxygen production system of this invention includes an electrolytic cell, a separation tank, a storage tank, and a filter tank. Under the control of the electrical control system, continuous electrolysis is achieved. The electrolytic cell continuously electrolyzes pure water to produce hydrogen and oxygen, providing zero-pollution hydrogen and oxygen for boiler explosion ash removal.

[0042] The above description is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any equivalent substitutions or modifications made by those skilled in the art within the scope of the technology disclosed in the present invention, based on the technical solution and inventive concept of the present invention, should be covered within the scope of protection of the present invention.

Claims

1. A fully intelligent system for producing hydrogen and oxygen, characterized in that: It includes a control and management system, an electrolysis reaction device, a separation and purification device, a material storage device, a circulation and cooling device, and a structural support component. The control and management system is electrically connected to the electrolysis reaction device, the separation and purification device, the material storage device, and the circulation and cooling device to achieve intelligent control of the entire process. The structural support component is used to achieve the positioning and installation of each device and the structural stability of the entire set of equipment. The electrolysis reaction device includes a left electrolytic cell and a right electrolytic cell; the separation and purification device includes a primary left separation tank, a primary right separation tank, a filter residue tank, and a secondary separation tank, wherein the primary left separation tank and the primary right separation tank are interconnected; the material storage device includes a left liquid storage tank and a right liquid storage tank, wherein the left liquid storage tank and the right liquid storage tank are interconnected. The left electrolytic cell is connected to the primary left separation tank, the right electrolytic cell is connected to the primary right separation tank, the left storage tank is connected to both the primary left and primary right separation tanks, the right storage tank is connected to the secondary separation tank, the right storage tank is connected to the filter residue tank via a circulation and cooling device, and the filter residue tank is connected to both the left and right electrolytic cells.

2. The fully intelligent system equipment for producing hydrogen and oxygen according to claim 1, characterized in that: The circulation and cooling device includes a cooler and a circulation pump. The inlet of the circulation pump is in fluid communication with the right liquid storage tank, and the outlet is in fluid communication with the liquid inlet of the cooler. The cooler is equipped with a cooling pump, and the liquid outlet of the cooler is connected to the filter residue tank.

3. The fully intelligent system equipment for producing hydrogen and oxygen according to claim 2, characterized in that: A replenishment pump is connected to the left liquid storage tank. The inlet of the replenishment pump is connected to an external electrolyte storage tank, and the outlet is connected to the inside of the left liquid storage tank.

4. The fully intelligent system equipment for producing hydrogen and oxygen according to claim 1, characterized in that: The control and management system includes an automatic control system and a sub-control system. The automatic control system and the sub-control system are bidirectionally electrically connected. The automatic control system provides electrolysis parameter regulation and safety control for the left and right electrolytic cells. The sub-control system is used to collect operating parameters such as pressure, temperature, and liquid level, and feed the parameters back to the automatic control system.

5. The fully intelligent system equipment for producing hydrogen and oxygen according to claim 4, characterized in that: The control and management system also includes temperature sensors, liquid level sensors, and pressure sensors. There are three temperature sensors, which are used to monitor the electrolyte temperature in the pipeline, the electrolyte temperature in the left electrolytic cell, and the electrolyte temperature in the right electrolytic cell in real time. There are two liquid level sensors, which are used to monitor the liquid level in the left and right storage tanks in real time. The pressure sensor is used to monitor the pressure of the produced hydrogen and oxygen in real time. All sensors are connected to the sub-control system signal.

6. The fully intelligent system equipment for producing hydrogen and oxygen according to claim 1, characterized in that: The structural support components include an electrolytic cell frame and a main equipment frame. The left and right electrolytic cells are both mounted on the electrolytic cell frame, and the main equipment frame provides overall structural support for the entire system.

7. The fully intelligent system equipment for producing hydrogen and oxygen according to claim 1, characterized in that: Both the left and right electrolytic cells are equipped with arrayed electrode groups and ion exchange membranes. The top of the left and right electrolytic cells is equipped with gas-liquid outlet pipes, which are connected to the primary left and primary right separation tanks respectively.

8. The fully intelligent system equipment for producing hydrogen and oxygen according to claim 1, characterized in that: The top of the secondary separation tank is equipped with a hydrogen outlet pipe and an oxygen outlet pipe, and each outlet pipe is equipped with a one-way valve and a flow sensor.