CN114774953A - Hydrogen production reaction equipment with programmable control of hydrogen production rate - Google Patents
Hydrogen production reaction equipment with programmable control of hydrogen production rate Download PDFInfo
- Publication number
- CN114774953A CN114774953A CN202210406495.2A CN202210406495A CN114774953A CN 114774953 A CN114774953 A CN 114774953A CN 202210406495 A CN202210406495 A CN 202210406495A CN 114774953 A CN114774953 A CN 114774953A
- Authority
- CN
- China
- Prior art keywords
- pin
- hydrogen production
- chip
- capacitor
- electrode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/60—Constructional parts of cells
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/02—Process control or regulation
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/02—Process control or regulation
- C25B15/023—Measuring, analysing or testing during electrolytic production
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Automation & Control Theory (AREA)
- Analytical Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The invention discloses hydrogen production reaction equipment with a programmable control hydrogen production rate, which comprises an electrolytic bath, a first electrode and a second electrode which are arranged on the electrolytic bath, a hydrogen outlet pipe and an oxygen outlet pipe which are arranged on the upper part of the electrolytic bath, a gas flow monitor which is arranged on the hydrogen outlet pipe, a liquid inlet pipe and a liquid outlet pipe which are arranged on the side part of the electrolytic bath, a current regulating circuit which is connected with the first electrode and the second electrode, a DC-DC (direct current) -DC conversion device and a rectifying circuit which are connected with the current regulating circuit, an ammeter which is arranged on a connecting line of the first electrode and the current regulating circuit, and a PLC (programmable logic controller) which is connected with the ammeter and the gas flow monitor, wherein the liquid inlet pipe is positioned above the liquid outlet pipe, and the PLC is connected with the current regulating circuit. The PLC controller of the hydrogen production reaction equipment can automatically control the current of the hydrogen production electrode in a programmable mode by acquiring and analyzing the data of the gas flow monitor and the ammeter, so that the high-precision adjustment of the hydrogen production rate is realized.
Description
Technical Field
The invention belongs to the technical field of hydrogen production equipment, and particularly relates to hydrogen production reaction equipment with a programmable hydrogen production rate control function.
Background
The hydrogen energy industry is a strategic industry system for constructing a low-carbon clean energy system, responding to environmental challenges and ensuring energy safety, and hydrogen has the dual property of communicating energy and substances and is an important link for extending electric energy to various industry fields and deeply replacing fossil energy for utilization. The hydrogen has the dual properties of energy and substance communication, is an important link for extending electric energy to various industry fields to replace fossil fuels, and does not discharge atmospheric pollutants and greenhouse gases in the using process. Therefore, the development of the hydrogen energy industry has great strategic significance.
In the hydrogen energy industry, hydrogen is produced by using a water electrolysis method, hydrogen is separated out by electrolyzing water and then is input into a hydrogen storage tank through a hydrogen outlet pipe to be stored, in the actual hydrogen production process, if the hydrogen production rate is too slow, the production efficiency is very low and cannot meet the use requirement, but if the hydrogen production rate is too fast, the gas flow and the pressure can be increased and even exceed the bearing capacity of a matched conveying pipeline and the storage tank, so that potential safety hazards are caused.
Disclosure of Invention
In order to overcome the defects in the prior art, the invention provides hydrogen production reaction equipment which adopts a programmable PLC to automatically control the current of a hydrogen production electrode so as to adjust the hydrogen production rate and has high control precision.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
a hydrogen production reaction device with a programmable control hydrogen production rate comprises an electrolytic bath, a first electrode and a second electrode which are arranged on the electrolytic bath, a hydrogen outlet pipe and an oxygen outlet pipe which are arranged on the upper part of the electrolytic bath, a gas flow monitor which is arranged on the hydrogen outlet pipe, a liquid inlet pipe and a liquid outlet pipe which are arranged on the side part of the electrolytic bath, a current regulating circuit connected to both the first electrode and the second electrode, a DC-DC direct current conversion device connected to the current regulating circuit, a rectifying circuit connected with the DC-DC conversion device, an ammeter arranged on a connecting line of the first electrode and the current regulating circuit, and a PLC controller connected with the ammeter and the gas flow monitor, the liquid inlet pipe is positioned above the liquid outlet pipe, and the PLC is connected with the current regulating circuit.
Further, the current regulation circuit comprises a digital potentiometer chip U1 with the model of MAX5435, a power amplifier chip U2 with the model of LM1875 connected with the W pin of the digital potentiometer chip U1, a resistor R1 with one end connected with the VIN-pin of the power amplifier chip U2 and the other end grounded, and a resistor R2 with one end connected with the VOUT pin of the power amplifier chip U2 and the other end connected with the VIN-pin of the power amplifier chip U2, wherein the H pin of the digital potentiometer chip U1 is connected with the DC-DC conversion device, the SDA pin, the SCL pin and the A0 pin of the digital potentiometer chip U1 are all connected with the PLC controller, the GND pin and the L pin of the digital potentiometer chip U1 are both grounded, the VDD pin of the digital potentiometer chip U1 is connected with a power supply VIN, and the + pin of the power amplifier chip U2 is connected with the W pin of the digital potentiometer chip U1, the V + pin of the digital potentiometer chip U1 is connected with a power supply Vs, the V-pin of the digital potentiometer chip U1 is grounded, the VOUT pin of the power amplifier chip U2 is connected with the first electrode, and the second electrode is grounded.
Further, the rectification circuit comprises a transformer T1 with one end connected with an external 220V alternating current power supply, and a bridge stack QL1 connected with the other end of the transformer T1, wherein an AC + pin and an AC-pin of the bridge stack QL1 are both connected with the transformer T1, and a DC + pin and a DC-pin of the bridge stack QL1 are both connected with the DC-DC conversion device.
Further, the DC-DC conversion device includes a first DC-DC conversion circuit and a second DC-DC conversion circuit, wherein the first DC-DC conversion circuit is connected to the current regulation circuit and the PLC controller, respectively, and the second DC-DC conversion circuit is connected to the current regulation circuit and the PLC controller, respectively.
Further, the first DC-DC conversion circuit includes a power conversion chip U3 of type LM7805, a capacitor C1 and a capacitor C2, one end of which is connected to the VIN pin of the power conversion chip U3 and the other end of which is grounded, and a capacitor C3 and a capacitor C4, one end of which is connected to the VOUT pin of the power conversion chip U3 and the other end of which is grounded.
Further, the second DC-DC conversion circuit includes a power conversion chip U4 of model LM7824, a capacitor C5 and a capacitor C6, one end of which is connected to the VIN pin of the power conversion chip U4 and the other end of which is grounded, and a capacitor C7 and a capacitor C8, one end of which is connected to the VOUT pin of the power conversion chip U4 and the other end of which is grounded.
Furthermore, a barometer connected with the PLC controller is arranged on the hydrogen outlet pipe.
Furthermore, a first valve is arranged on the liquid inlet pipe, and a second valve is arranged on the liquid outlet pipe.
Further, the first valve and the second valve are both connected with the PLC.
Compared with the prior art, the invention has the following beneficial effects:
(1) the invention relates to a hydrogen production reaction device, which is characterized in that a current regulating circuit is connected with a first electrode and a second electrode to form a circuit loop, then a PLC controller is used for collecting data on a gas flow monitor and an ammeter and calculating the current hydrogen production rate, the PLC controller is used for regulating and controlling the current of the current regulating circuit, so that the hydrogen production rate of the first electrode and the second electrode is changed, in the current regulating circuit, the high-precision regulation of the current is realized by adopting a digital potentiometer chip, meanwhile, a 220V external alternating current power supply is converted into a direct current power supply by arranging a rectifying circuit, and the stable voltage which is suitable for the current regulating circuit and the PLC controller is output by a DC-DC conversion device.
(2) The current regulating circuit realizes high-precision control of current by adopting a digital potentiometer chip with the model of MAX5435, the rectifying circuit converts alternating current into direct current power by adopting a bridge rectifier QL1, the first DC-DC conversion circuit outputs stable 5V voltage by adopting a power conversion chip with the model of LM7805, and the second DC-DC conversion circuit outputs stable 24V voltage by adopting a power conversion chip with the model of LM7824, so that stable power input is provided for the current regulating circuit and a PLC (programmable logic controller).
(3) The PLC controller of the invention improves the measurement precision of the current hydrogen production rate by acquiring and analyzing the data of the barometer arranged on the hydrogen outlet pipe, and in addition, the automatic input of the electrolyte and the automatic discharge of the waste liquid are realized by the arrangement of the first valve and the second valve and the control of the PLC controller, thereby enhancing the degree of automatic control.
Drawings
FIG. 1 is a schematic diagram of the overall control of a hydrogen production reaction apparatus according to the present invention.
Fig. 2 is a schematic diagram of a current regulating circuit of the present invention.
Fig. 3 is a schematic diagram of a rectifier circuit of the present invention.
Fig. 4 is a schematic diagram of the DC-DC converter according to the present invention.
Fig. 5 is a schematic diagram of a first DC-DC conversion circuit of the present invention.
Fig. 6 is a schematic diagram of a second DC-DC conversion circuit of the present invention.
In the drawings, the names of the parts corresponding to the reference numerals are as follows:
the device comprises an electrolytic cell 1, a first electrode 2, a second electrode 3, an ammeter 4, a hydrogen outlet pipe 5, an oxygen outlet pipe 6, a liquid inlet pipe 7, a liquid outlet pipe 8, a barometer 9, a gas flow monitor 10, a first valve 11, a second valve 12, an electrolyte tank 13, a waste liquid tank 14, a PLC 15, a current regulating circuit 16, a direct current conversion device 17-DC-DC, a rectification circuit 18, a hydrogen storage tank 19, a first DC-DC conversion circuit 1701, and a second DC-DC conversion circuit 1702.
Detailed Description
The present invention is further illustrated by the following figures and examples, which include, but are not limited to, the following examples.
Examples
As shown in fig. 1 and fig. 6, the present embodiment provides a hydrogen production reaction apparatus with a programmable hydrogen production rate control, comprising an electrolytic tank 1, a first electrode 2, a second electrode 3, a hydrogen outlet pipe 5, an oxygen outlet pipe 6, a gas flow monitor 10, a liquid inlet pipe 7, a liquid outlet pipe 8, a current regulating circuit 16, a DC-DC direct current conversion device 17, a rectification circuit 18, an ammeter 4, and a PLC controller 15, wherein the electrolytic tank 1 is a basic apparatus for producing hydrogen, and provides a hydrogen production reaction space for an electrolyte and the first electrode 2 and the second electrode 3, the first electrode 2 is used as a hydrogen production positive electrode, the second electrode 3 is used as a hydrogen production negative electrode, the hydrogen outlet pipe 5 is used for outputting produced hydrogen, a hydrogen storage tank 19 is provided on the hydrogen outlet pipe 5 for storing hydrogen, the oxygen outlet pipe 6 is used for outputting produced oxygen, and according to actual production conditions, the oxygen is discharged to the air or collected and stored, the gas flow monitor 10 is used for monitoring the flow of hydrogen, the rate of hydrogen generation is calculated through flow data, the liquid inlet pipe 7 is an input pipe of electrolyte, the liquid inlet pipe 7 is connected with an electrolyte tank 13, the liquid outlet pipe 8 is a waste liquid discharge pipe generated by electrolytic reaction, the liquid outlet pipe 8 is provided with a waste liquid tank 14, the current regulating circuit 16 is used for regulating electrode current, the DC-DC conversion device 17 is used for converting DC voltage to obtain the voltage required by the current regulating circuit 16 and the PLC 15, the rectifying circuit 18 is used for converting 220V AC into DC power, and the ammeter 4 is used for measuring the current of a loop formed by the electrode and the current regulating circuit 16.
In this embodiment, the PLC controller 15 is used as a control core of the whole hydrogen production reaction apparatus, and the PLC is an acronym of Programmable logic controller in english, and is called a Programmable logic controller in chinese, and the PLC controller 15 of this embodiment performs corresponding regulation control by being programmed in advance and combining data collected from the ammeter 4 and the gas flow rate monitor 10.
In this embodiment, the current adjusting circuit 16 includes a digital potentiometer chip U1 with a model of MAX5435, a power amplifier chip U2 with a model of LM1875 connected to a W pin of the digital potentiometer chip U1, a resistor R1 with one end connected to a VIN-pin of the power amplifier chip U2 and the other end grounded, and a resistor R2 with one end connected to a VOUT pin of the power amplifier chip U2 and the other end connected to a VIN-pin of the power amplifier chip U2, wherein a H pin of the digital potentiometer chip U1 is connected to the DC-DC converter 17, an SDA pin, an SCL pin and an a0 of the digital potentiometer chip U1 are connected to the PLC controller 15, a GND pin and an L pin of the digital potentiometer chip U1 are grounded, a VDD pin of the digital potentiometer chip U1 is connected to a power source VCC, a VIN + pin of the power amplifier chip U2 is connected to a W pin of the digital potentiometer chip U1, and a V + pin of the digital potentiometer chip U1 is connected to a power source Vs, the V-pin of the digital potentiometer chip U1 is grounded, the VOUT pin of the power amplifier chip U2 is connected with the first electrode 2, and the second electrode 3 is grounded. In this embodiment, a power source VCC and a power source Vs are both connected to the DC-DC conversion device 17, where the power source VCC is a +5V power input, and the power source Vs is a +24V power input.
Current regulation circuit 16 is through adopting the digital potentiometer chip that the model is MAX5435 in this embodiment, the high accuracy control to the electric current has been realized, MAX5435 is a high sensitivity's digital resistance adjustment chip of a section, compare in traditional adjustable resistance, automatic control not only can be realized to the digital potentiometer chip, and it is higher to adjust the precision, and simultaneously, the power signal of output is carried out the operational amplification to the digital potentiometer chip through setting up the power amplifier chip that the model is LM1875, the current regulation ability has been strengthened.
In the present embodiment, the rectifying circuit 18 converts the ac power into the dc power by using a transformer T1 and a bridge q l1, wherein the transformer T1 is a 220V ac transformer commonly used in the industry, and the bridge QL1 is a power device whose interior is mainly a bridge circuit composed of four diodes to convert the input ac voltage into the output dc voltage.
In the present embodiment, the DC-DC conversion device 17 includes a first DC-DC conversion circuit 1701 and a second DC-DC conversion circuit 1702, wherein the first DC-DC conversion circuit 1701 outputs a stable 5V voltage by using a power conversion chip of a model LM7805, and the second DC-DC conversion circuit 1702 outputs a stable 24V voltage by using a power conversion chip of a model LM7824, thereby providing a stable power input to the current regulation circuit 16 and the PLC controller 15.
In this embodiment, the barometer 9 is arranged on the hydrogen outlet pipe 5, the PLC controller 15 collects and analyzes the air pressure measured by the barometer 9, and on the basis of the gas flow monitor 10, reference data is added, and the measurement accuracy of the current hydrogen production rate is improved through the operation and analysis of the PLC controller 15.
In this embodiment, be provided with first valve 11 on the feed liquor pipe 7, be provided with second valve 12 on the drain pipe 8, the switching and the regulation of first valve 11 and second valve 12, the accessible manual regulation is realized, also can be connected first valve 11 and second valve 12 with PLC controller 15, carry out the regulation and control to first valve 11 and second valve 12 through actual need, thereby realized the automatic input to electrolyte and the automatic discharge of waste liquid, strengthened the degree of automated control.
When the invention is used, the current regulating circuit 16 is connected with the first electrode 2 and the second electrode 3 to form a circuit loop, then the PLC 15 collects the data of the gas flow monitor 10 and the ammeter 4 and calculates the current hydrogen production rate, the current of the current regulating circuit 16 is regulated and controlled by the PLC 15, thereby changing the hydrogen production rate of the first electrode 2 and the second electrode 3, in the current regulating circuit 16, high-precision regulation of the current is realized by adopting a digital potentiometer chip, meanwhile, a rectifying circuit 18 is arranged to convert a 220V external alternating current power supply into a direct current power supply, and a DC-DC conversion device 17 outputs a stable voltage suitable for the current regulation circuit 16 and the PLC 15. In this embodiment, the connection between the PLC controller 15 and the current adjusting circuit 16, the DC-DC converter 17, the gas flow monitor 10, the ammeter 4, the barometer 9, the first valve 11, and the second valve 12 belongs to the prior art, and may be implemented by conventional hardware design, and the specific circuit configuration thereof is not described in this embodiment again.
The above-described embodiments are only preferred embodiments of the present invention, and are not intended to limit the scope of the present invention, but all changes that can be made by applying the principles of the present invention and performing non-inventive work on the basis of the principles shall fall within the scope of the present invention.
Claims (9)
1. A hydrogen production reaction device with a programmable hydrogen production rate control, which is characterized in that: including electrolysis trough (1), set up in first electrode (2) and second electrode (3) on electrolysis trough (1), set up in hydrogen outlet duct (5) and oxygen outlet duct (6) on electrolysis trough (1) upper portion, set up in gas flow monitor (10) on hydrogen outlet duct (5), set up in feed liquor pipe (7) and drain pipe (8) of electrolysis trough (1) lateral part, with first electrode (2) with current regulation circuit (16) that second electrode (3) homogeneous phase is connected, with DC-DC direct current conversion device (17) that current regulation circuit (16) are connected, with rectifier circuit (18) that DC-DC direct current conversion device (17) are connected, first electrode (2) with ammeter (4) that set up on the connecting line of current regulation circuit (16), and with ammeter (4) with PLC controller (15) that gas flow monitor (10) homogeneous phase is connected ) The liquid inlet pipe (7) is positioned above the liquid outlet pipe (8), and the PLC controller (15) is connected with the current regulating circuit (16).
2. A hydrogen production reaction apparatus with programmable control of hydrogen production rate according to claim 1, characterized in that: the current regulating circuit (16) comprises a digital potentiometer chip U1 with the model of MAX5435, a power amplifier chip U2 with the model of LM1875 connected with a W pin of the digital potentiometer chip U1, a resistor R1 with one end connected with a VIN-pin of the power amplifier chip U2 and the other end grounded, and a resistor R2 with one end connected with a VOUT pin of the power amplifier chip U2 and the other end connected with a VIN-pin of the power amplifier chip U2, wherein an H pin of the digital potentiometer chip U1 is connected with the DC-DC conversion device (17), an SDA pin, an SCL pin and an A0 pin of the digital potentiometer chip U1 are all connected with the PLC (15), a GND pin and an L pin of the digital potentiometer chip U1 are both grounded, a VIN pin of the digital potentiometer chip U1 is connected with a VCC, a + pin of the power amplifier chip U2 is connected with a W pin of the digital potentiometer chip U1, the V + pin of the digital potentiometer chip U1 is connected with a power supply Vs, the V-pin of the digital potentiometer chip U1 is grounded, the VOUT pin of the power amplifier chip U2 is connected with the first electrode (2), and the second electrode (3) is grounded.
3. A hydrogen production reaction apparatus with programmable control of hydrogen production rate according to claim 2, characterized in that: the rectifying circuit (18) comprises a transformer T1 with one end connected with an external 220V alternating current power supply and a bridge stack QL1 connected with the other end of the transformer T1, wherein an AC + pin and an AC-pin of the bridge stack QL1 are both connected with the transformer T1, and a DC + pin and a DC-pin of the bridge stack QL1 are both connected with the DC-DC conversion device (17).
4. A hydrogen production reaction apparatus with a programmable hydrogen production rate control as claimed in claim 3, characterized in that: the DC-DC direct current conversion device (17) includes a first DC-DC conversion circuit (1701) and a second DC-DC conversion circuit (1702), wherein the first DC-DC conversion circuit (1701) is connected to the current regulation circuit (16) and the PLC controller (15), respectively, and the second DC-DC conversion circuit (1702) is connected to the current regulation circuit (16) and the PLC controller (15), respectively.
5. A hydrogen production reaction apparatus with a programmable hydrogen production rate control as claimed in claim 4, characterized in that: the first DC-DC conversion circuit (1701) comprises a power conversion chip U3 with the model number LM7805, a capacitor C1 and a capacitor C2, wherein one end of the capacitor C1 is connected with the VIN pin of the power conversion chip U3, the other end of the capacitor C2 is grounded, one end of the capacitor C3 and the other end of the capacitor C4 are connected with the VOUT pin of the power conversion chip U3, and the other end of the capacitor C4 is grounded.
6. A hydrogen production reaction apparatus with a programmable hydrogen production rate control as claimed in claim 4, characterized in that: the second DC-DC conversion circuit (1702) comprises a power conversion chip U4 with the model of LM7824, a capacitor C5 and a capacitor C6, wherein one end of the capacitor C5 is connected with the VIN pin of the power conversion chip U4, the other end of the capacitor C6 is grounded, one end of the capacitor C7 and one end of the capacitor C8 are connected with the VOUT pin of the power conversion chip U4, and the other end of the capacitor C7 and the other end of the capacitor C8 are grounded.
7. A hydrogen production reaction apparatus with programmable control of hydrogen production rate according to claim 1, characterized in that: and the hydrogen outlet pipe (5) is provided with a barometer (9) connected with the PLC (15).
8. A hydrogen production reaction apparatus with a programmable control of hydrogen production rate according to claim 1, characterized in that: the liquid inlet pipe (7) is provided with a first valve (11), and the liquid outlet pipe (8) is provided with a second valve (12).
9. A hydrogen production reaction apparatus with programmable control of hydrogen production rate according to claim 8, characterized in that: the first valve (11) and the second valve (12) are both connected with the PLC (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210406495.2A CN114774953B (en) | 2022-04-18 | 2022-04-18 | Hydrogen production reaction equipment with programmable control of hydrogen production rate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210406495.2A CN114774953B (en) | 2022-04-18 | 2022-04-18 | Hydrogen production reaction equipment with programmable control of hydrogen production rate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN114774953A true CN114774953A (en) | 2022-07-22 |
| CN114774953B CN114774953B (en) | 2023-08-22 |
Family
ID=82431758
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210406495.2A Active CN114774953B (en) | 2022-04-18 | 2022-04-18 | Hydrogen production reaction equipment with programmable control of hydrogen production rate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114774953B (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1403630A (en) * | 2002-09-26 | 2003-03-19 | 上海交通大学 | Aniline-synthesizing and electric energy-generating process utilizing proton exchange film fuel cell |
| CN101372313A (en) * | 2007-02-14 | 2009-02-25 | 三星电机株式会社 | Hydrogen generating apparatus and fuel cell power generation system |
| CN102656742A (en) * | 2009-12-24 | 2012-09-05 | 丰田自动车株式会社 | Air battery system |
| CN110570893A (en) * | 2018-06-05 | 2019-12-13 | 记忆科技(深圳)有限公司 | Flash automatic screening system and screening method for realizing voltage bias |
| CN113215593A (en) * | 2021-03-16 | 2021-08-06 | 宝武清洁能源有限公司 | Green hydrogen preparation system of hybrid electrolysis water |
| WO2021196564A1 (en) * | 2020-04-03 | 2021-10-07 | 中国华能集团清洁能源技术研究院有限公司 | Wide-power hydrogen production system and method by electrolysis of water |
| CN113897618A (en) * | 2020-06-22 | 2022-01-07 | 现代自动车株式会社 | Water electrolysis system |
-
2022
- 2022-04-18 CN CN202210406495.2A patent/CN114774953B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1403630A (en) * | 2002-09-26 | 2003-03-19 | 上海交通大学 | Aniline-synthesizing and electric energy-generating process utilizing proton exchange film fuel cell |
| CN101372313A (en) * | 2007-02-14 | 2009-02-25 | 三星电机株式会社 | Hydrogen generating apparatus and fuel cell power generation system |
| CN102656742A (en) * | 2009-12-24 | 2012-09-05 | 丰田自动车株式会社 | Air battery system |
| CN110570893A (en) * | 2018-06-05 | 2019-12-13 | 记忆科技(深圳)有限公司 | Flash automatic screening system and screening method for realizing voltage bias |
| WO2021196564A1 (en) * | 2020-04-03 | 2021-10-07 | 中国华能集团清洁能源技术研究院有限公司 | Wide-power hydrogen production system and method by electrolysis of water |
| CN113897618A (en) * | 2020-06-22 | 2022-01-07 | 现代自动车株式会社 | Water electrolysis system |
| CN113215593A (en) * | 2021-03-16 | 2021-08-06 | 宝武清洁能源有限公司 | Green hydrogen preparation system of hybrid electrolysis water |
Also Published As
| Publication number | Publication date |
|---|---|
| CN114774953B (en) | 2023-08-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106119883B (en) | A kind of coupled hydrogen making system and its control method | |
| CN208748209U (en) | Device for preparing hydrogen under a kind of wide power of wind energy | |
| CN109683103A (en) | A kind of multi-channel fuel battery impedance test system of hardware in loop formula | |
| CN100447693C (en) | Programmable power supply system dedicated for nano processing | |
| CN114774953A (en) | Hydrogen production reaction equipment with programmable control of hydrogen production rate | |
| CN111291958A (en) | Power grid and industrial user power supply and demand interaction device and implementation method | |
| CN113481526A (en) | Intelligent test system and method for multi-channel electrolytic cell | |
| CN210457661U (en) | Accurate aeration control system of magnetic suspension centrifugal blower | |
| CN111693679A (en) | Wind turbine generator system lubricating oil on-line monitoring management system | |
| CN116497369A (en) | Electrolytic tank testing device and testing method thereof | |
| CN214894655U (en) | Measuring equipment for measuring anti-embolism degree of plant xylem by using pneumatic method | |
| CN207096321U (en) | New power supply sample circuit and its low-voltage circuit breaker | |
| CN2859552Y (en) | Resistance tester for accumulator separator | |
| CN203896297U (en) | Low voltage photovoltaic power generation meter box | |
| CN109444704A (en) | LEDbulb lamp photoelectric properties on-line detecting system | |
| CN210958189U (en) | Special power supply for high-voltage corrosion foil small sample formation test | |
| CN209606536U (en) | A kind of DC charging motor logging | |
| CN203645593U (en) | Numerical control alternating current power supply used for sensor test | |
| CN207050767U (en) | A kind of urban drainage pipe network monitoring terminal | |
| CN104331090B (en) | Corona discharge ozone frequency generator automatic following control system | |
| CN109915352A (en) | A kind of tracking regulator control system of variable-flow hydrogen gas compressor operating condition | |
| CN220105225U (en) | Test system for monitoring vanadium battery | |
| CN114817841A (en) | Carbon emission measuring and calculating method of low-carbon sewage treatment process | |
| CN219951237U (en) | Water inlet control device for hydrogen production | |
| CN220887709U (en) | Visual experiment frock of monitoring electrolysis water performance |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |