CN110550706A - Electrolytic water tank device for electrolytic hydrogen-rich water machine - Google Patents
Electrolytic water tank device for electrolytic hydrogen-rich water machine Download PDFInfo
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- CN110550706A CN110550706A CN201910891039.XA CN201910891039A CN110550706A CN 110550706 A CN110550706 A CN 110550706A CN 201910891039 A CN201910891039 A CN 201910891039A CN 110550706 A CN110550706 A CN 110550706A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
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- Hydrology & Water Resources (AREA)
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- Water Supply & Treatment (AREA)
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The invention relates to an electrolytic water tank device for an electrolytic hydrogen-rich water machine, which comprises a water storage tank, a sintered electrolytic anode, a sintered electrolytic cathode, an SPE membrane recovery tank, a drainage pump, a diversion pipe, a temperature sensor and a controller, wherein the water storage tank is of a closed cavity structure with a rectangular cross section, the SPE membrane recovery tank is embedded in a tank body to divide the tank body into a hydrogen chamber and an oxygen chamber, the sintered electrolytic anode and the sintered electrolytic cathode are symmetrically distributed on two sides of the SPE membrane recovery tank, the drainage pump is connected with the upper end face of a sealing cover, the temperature sensor is respectively connected with the corresponding side wall of the tank body of the hydrogen chamber and the oxygen chamber, and the controller is connected with the upper. The invention can effectively improve the working efficiency of water electrolysis operation, effectively improve and prolong the service life of the electrode plate, has stable electrochemical reaction, is not easy to separate out harmful substances, effectively realizes the formation of hydrogen-ion-rich water body by the hydrogen ions after electrolysis in the form of water molecules and hydrated protons, and improves the product quality of the electrolysis type hydrogen-enriched water machine.
Description
Technical Field
The invention relates to an electrolysis device, in particular to an electrolytic water tank device for an electrolytic hydrogen-rich water machine.
background
The electrolytic hydrogen-rich water machine is an important device for preparing electrolytic water rich in hydrogen ions and can be used for carrying out adjuvant therapy on certain diseases, wherein the electrolytic cell plays a crucial role in the running quality and stability of the electrolytic hydrogen-rich water machine. The current practical use discovers that the ion membrane used by the current water ionizer is a semipermeable membrane, and positive and negative ions can penetrate through each other, so that the water treated by the water ionizer is alkaline because more ions with positive charges, such as potassium, sodium, calcium, magnesium and the like, are accumulated in the water from the cathode; the water from the anode is acidic because more negatively charged acid radical ions are accumulated. Because the water-resisting performance of the semipermeable membrane is poor, the alkaline tank and the acidic tank can discharge water together, so that the ion content in the electrolyzed water is complex, a large amount of heavy metal ions and other ions harmful to human bodies are easily discharged along with water bodies, and the quality of the electrolytic hydrogen-rich water machine product is seriously influenced.
how to solve the technical problems becomes a technical difficulty to be solved urgently. .
Disclosure of Invention
The invention provides an electrolytic water tank device for an electrolytic hydrogen-rich water machine, which can effectively improve the working efficiency of water electrolysis operation, effectively prolong the service life of an electrode plate, reduce overhigh water temperature and corrosion loss of the electrode plate caused by continuous electrolysis, and effectively realize formation of a water body rich in hydrogen ions by water molecules in the form of hydrated protons after electrolysis, thereby improving the product quality of the electrolytic hydrogen-rich water machine.
In order to realize the purpose, the invention is realized by the following technical scheme:
An electrolytic water tank device for an electrolytic hydrogen-rich water machine comprises a water storage tank, a sintered electrolytic anode, a sintered electrolytic cathode, an SPE membrane recovery tank, a drainage pump, a diversion pipe, a temperature sensor and a controller, wherein the water storage tank is of a closed cavity structure with a rectangular cross section and comprises a tank body and a sealing cover, the sealing cover covers the upper end face of the tank body, the SPE membrane recovery tank is embedded in the tank body and is vertically distributed at the bottom of the tank body and coaxially distributed with the tank body, the side surface of the SPE membrane recovery tank is in sliding connection with the inner surface of the side wall of the tank body, the tank body is equally divided into a hydrogen chamber and an oxygen chamber, at least two diversion ports are arranged at the bottom of the SPE membrane recovery tank, the hydrogen chamber and the oxygen chamber are communicated through the diversion ports, a water filling port is arranged on the upper end face of a sealing cover corresponding to the hydrogen chamber, an air exhaust port is arranged on the sealing cover corresponding to the, and the outlet passes through honeycomb duct and SPE membrane accumulator intercommunication, and the equal at least one of sintering electrolysis positive pole, sintering electrolysis negative pole, and symmetric distribution is in SPE membrane accumulator both sides, and sintering electrolysis positive pole is located the oxygen chamber, sintering electrolysis negative pole is located the hydrogen chamber, and sintering electrolysis positive pole, sintering electrolysis negative pole up end all lie in sealed covering outside, the drain pump sets up at sealed covering up end and through honeycomb duct and outlet intercommunication, the cell body lateral wall that hydrogen chamber and oxygen chamber correspond is established respectively to at least two of temperature sensor, the controller sets up at sealed covering up end and respectively with sintering electrolysis positive pole, sintering electrolysis negative pole, drain pump, temperature sensor electrical connection.
Further, SPE membrane accumulator upper end and sealed lid down the terminal surface offset, SPE membrane accumulator is including bearing fossil fragments, SPE membrane, water conservancy diversion branch pipe, wherein bear fossil fragments for the cross-section be the airtight cavity structure of rectangle, wherein bear the side surface that fossil fragments and hydrogen room correspond and set for the constant head tank, the constant head tank area is for bearing 60% -80% of fossil fragments side surface area, the SPE membrane inlays in the constant head tank and with the coaxial distribution of constant head tank, the water conservancy diversion branch pipe inlays in bearing fossil fragments, its lower terminal surface and bear the keel bottom interval be 4-13 millimeters, the up end passes through honeycomb duct and outlet intercommunication.
Further, SPE membrane accumulator bear fossil fragments side and cell body lateral wall and bottom between pass through spout sliding connection, and the spout is connected through the elastic sealing strip with SPE membrane accumulator's bearing fossil fragments surface between.
Furthermore, the sintered electrolytic anode and the sintered electrolytic cathode are both distributed in parallel with the lateral surface of the SPE film recovery tank, and the distance between the lateral surface of the SPE film recovery tank and the sintered electrolytic anode and the sintered electrolytic cathode is 5-30 mm.
Furthermore, the sintered electrolytic anode and the sintered electrolytic cathode are respectively positioned between the water feeding port, the exhaust port and the SPE membrane recycling tank, the axes of the water feeding port and the exhaust port are distributed in parallel with the sintered electrolytic anode and the sintered electrolytic cathode, and the distance between the sintered electrolytic anode and the sintered electrolytic cathode is 1/3-3/4 of the width of the hydrogen chamber and the oxygen chamber.
According to the invention, on one hand, the working efficiency of water electrolysis operation can be effectively improved, the service life of the electrode plate can be effectively improved and prolonged, the overhigh water temperature and the corrosion loss of the electrode plate caused by continuous electrolysis can be reduced, on the other hand, the electrochemical reaction is stable, harmful substances are not easy to separate out, and on the other hand, the hydrogen ions after electrolysis can be effectively formed into the water body rich in hydrogen ions in the form of water molecules and hydrated protons, so that the hydrogen-enriched water can be prepared, and the quality of the electrolytic hydrogen-enriched water machine product can be improved.
Drawings
The invention is described in detail below with reference to the drawings and the detailed description;
FIG. 1 is a schematic structural view of the present invention;
Fig. 2 is a block diagram of the circuit of the present invention.
Detailed Description
In order to make the technical features, the creation characteristics, the achievement purposes and the effects of the invention easy to understand, the invention is further described with reference to the specific embodiments.
As shown in fig. 1 to 2, the electrolytic water tank device for an electrolytic hydrogen-rich water machine comprises a water storage tank 1, a sintered electrolytic anode 2, a sintered electrolytic cathode 3, an SPE membrane recovery tank 4, a drainage pump 5, a drainage tube 6, a temperature sensor 7 and a controller 8, wherein the water storage tank 1 is a closed cavity structure with a rectangular cross section and comprises a tank body 101 and a sealing cover 102, the sealing cover 102 covers the upper end surface of the tank body 101, the SPE membrane recovery tank 4 is embedded in the tank body 101 and vertically distributed with the bottom of the tank body 101 and coaxially distributed with the tank body 101, the side surface of the SPE membrane recovery tank 4 is slidably connected with the inner surface of the side wall of the tank body 101, the tank body 101 is equally divided into a hydrogen chamber 103 and an oxygen chamber 104, the bottom of the SPE membrane recovery tank 4 is provided with at least two flow guide ports 105, the hydrogen chamber 103 is communicated with the oxygen chamber 104 through the flow guide ports 105, the upper end surface of the sealing, an air outlet 107 is arranged on a sealing cover corresponding to the oxygen chamber 104, a drain 108 is arranged at the bottom of the tank body 101 on the corresponding side, a water outlet 109 is arranged on the upper end surface of the sealing cover 102 corresponding to the SPE membrane recycling tank 4, the water outlet 109 is communicated with the SPE membrane recycling tank 4 through a guide pipe 6, at least one of the sintered electrolytic anode 2 and the sintered electrolytic cathode 3 is symmetrically distributed on two sides of the SPE membrane recycling tank 4, the sintered electrolytic anode 2 is positioned in the oxygen chamber 104, the sintered electrolytic cathode 3 is positioned in the hydrogen chamber 103, the upper end surfaces of the sintered electrolytic anode 2 and the sintered electrolytic cathode 3 are positioned outside the sealing cover 102 and are higher than the upper end surface of the sealing cover 102, a drainage pump 5 is arranged on the upper end surface of the sealing cover 102 and is communicated with the water outlet 109 through the guide pipe 6, at least two temperature sensors 7 are arranged on the side walls of the tank body 101 corresponding to the hydrogen chamber 103 and the oxygen chamber 104, a, The sintered electrolytic negative electrode 3, the drain pump 5, and the temperature sensor 7 are electrically connected.
It is emphasized that, the upper end of the SPE membrane recycling tank 4 abuts against the lower end face of the sealing cover 102, the SPE membrane recycling tank 4 includes a bearing keel 41, a SPE membrane 42 and a diversion branch pipe 43, wherein the bearing keel 41 is a closed cavity structure with a rectangular cross section, a positioning groove 44 is set on the side surface of the bearing keel 41 corresponding to the hydrogen chamber 103, the area of the positioning groove 44 is 60% -80% of the area of the side surface of the bearing keel 41, the SPE membrane 42 is embedded in the positioning groove 44 and coaxially distributed with the positioning groove 44, the diversion branch pipe 43 is embedded in the bearing keel 41, the distance between the lower end face and the bottom of the bearing keel 41 is 4-13 mm, and the upper end face is communicated with the water outlet 109 through the diversion pipe 6.
In addition, bearing keel 41 side and cell body 101 lateral wall and bottom of SPE membrane accumulator 4 between pass through spout 9 sliding connection, and spout 9 is connected through elastic sealing strip 10 with bearing keel 101 surface of SPE membrane accumulator 4 between.
Preferably, the sintered electrolytic anode 2 and the sintered electrolytic cathode 3 are both distributed in parallel with the lateral surface of the SPE membrane recovery tank 4, the distance between the lateral surface of the SPE membrane recovery tank 4 and the sintered electrolytic anode 2 and the sintered electrolytic cathode 3 is 5-30 mm, the sintered electrolytic anode 2 and the sintered electrolytic cathode 3 are respectively located between the water feeding port 106 and the exhaust port 107 and the SPE membrane recovery tank 4, the axial lines of the water feeding port 106 and the exhaust port 107 are distributed in parallel with the sintered electrolytic anode 2 and the sintered electrolytic cathode 3, and the distance between the sintered electrolytic anode 2 and the sintered electrolytic cathode 3 is 1/3-3/4 of the width of the hydrogen chamber 103 and the oxygen chamber 104.
In this embodiment, the sintered electrolytic anode 2 and the sintered electrolytic cathode 3 are both platinum alloy plates, and the thickness is not more than 5 mm.
When the electrolytic water machine is used for electrolysis, firstly, a water storage tank, a sintered electrolysis positive electrode, a sintered electrolysis negative electrode, an SPE membrane recovery tank, a drainage pump, a flow guide pipe, a temperature sensor and a controller which form the electrolytic water machine are assembled, then, the water storage tank is installed in the electrolytic hydrogen-rich water machine, the drainage pump is communicated with a water outlet pipe of the electrolytic hydrogen-rich water machine, and the controller is electrically connected with an electric control system of the electrolytic hydrogen-rich water machine, so that the assembly of the electrolytic water machine is completed.
When the electrolysis operation is carried out, purified deionized water is added into the water storage tank 1 through the water filling port, when water enters the water storage tank, the purified deionized water firstly enters the hydrogen chamber and the SPE membrane recycling tank of the water storage tank, then flows into the oxygen chamber through the flow guide port of the SPE membrane recycling tank, is kept to be continuously added, and achieves the purposes of ensuring the water quality of the water storage tank and reducing the temperature of the water body, the sintered electrolysis anode and the sintered electrolysis cathode in the water storage tank through continuously adding the water body.
Meanwhile, after at least 1/3 parts of the effective heights of the sintered electrolytic anode and the sintered electrolytic cathode enter the water body, the controller drives the sintering electrolysis anode and the sintering electrolysis cathode to operate to carry out electrolysis operation, hydrogen ions and hydroxyl ions are generated in the hydrogen chamber, oxygen ions and hydroxyl ions are generated in the oxygen chamber, then the generated hydrogen ions are directly combined with water molecules in the form of hydrated protons and enter the SPE membrane recycling tank through the SPE membrane of the SPE membrane recycling tank, then the water is discharged under the drive of a drainage pump, so that the finished product hydrogen-rich water body is obtained, and the residual oxygen is directly discharged into the air, sodium ions, calcium ions and the like remained in the water body are remained in the water body and discharged from a sewage discharge outlet of the oxygen chamber, the water quality is ensured, and the purpose of reducing the temperature of the water body in the water storage tank and the temperature of the sintered electrolytic anode and the sintered electrolytic cathode is achieved through water drainage.
It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are described in the specification and illustrated only to illustrate the principle of the present invention, but that various changes and modifications may be made therein without departing from the spirit and scope of the present invention, which fall within the scope of the invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (5)
1. The utility model provides an electrolysis water tank device for electrolysis hydrogen-rich water machine, electrolysis water tank device for electrolysis hydrogen-rich water machine includes catch basin, sintering electrolysis anodal, sintering electrolysis negative pole, SPE membrane accumulator, drain pump, honeycomb duct, temperature sensor and controller, its characterized in that: the water storage tank is of a closed cavity structure with a rectangular cross section and comprises a tank body and a sealing cover, the sealing cover covers the upper end face of the tank body, the SPE film recovery tank is embedded in the tank body and is vertically distributed at the bottom of the tank body and coaxially distributed with the tank body, the side surface of the SPE film recovery tank is in sliding connection with the inner surface of the side wall of the tank body, the tank body is equally divided into a hydrogen chamber and an oxygen chamber, at least two flow guide ports are arranged at the bottom of the SPE film recovery tank, the hydrogen chamber is communicated with the oxygen chamber through the flow guide ports, a water filling port is arranged at the upper end face of the sealing cover corresponding to the hydrogen chamber, an exhaust port is arranged at the sealing cover corresponding to the oxygen chamber, a drain outlet is arranged at the bottom of the tank body corresponding to the side, a drain outlet is arranged at the upper end face of the sealing cover corresponding to the SPE, symmetric distribution is in SPE membrane accumulator both sides, and sintering electrolysis is anodal to be located the oxygen chamber, sintering electrolysis negative pole is located the hydrogen chamber, just sintering electrolysis is anodal, sintering electrolysis negative pole up end all is located sealed covering outside, the drain pump sets up at sealed covering up end and through honeycomb duct and outlet intercommunication, the cell body lateral wall that hydrogen chamber and oxygen chamber correspond is established respectively to two at least temperature sensor, the controller sets up at sealed covering up end and respectively with sintering electrolysis is anodal, sintering electrolysis negative pole, drain pump, temperature sensor electrical connection.
2. The electrolytic water tank device for the hydrogen-rich water machine of claim 1, wherein the upper end of the SPE membrane recovery tank abuts against the lower end surface of the sealing cover, the SPE membrane recovery tank comprises a bearing keel, a SPE membrane and a diversion branch pipe, wherein the bearing keel is a sealed cavity structure with a rectangular cross section, a positioning groove is defined on the side surface of the bearing keel corresponding to the hydrogen chamber, the area of the positioning groove is 60% -80% of the area of the side surface of the bearing keel, the SPE membrane is embedded in the positioning groove and coaxially distributed with the positioning groove, the diversion branch pipe is embedded in the bearing keel, the distance between the lower end surface of the diversion branch pipe and the bottom of the bearing keel is 4-13 mm, and the upper end surface of the diversion branch pipe is communicated with the water outlet through a diversion.
3. The electrolytic water tank device for the electrolytic hydrogen-rich water machine as claimed in claim 1 or 2, wherein the SPE membrane recovery tank is connected with the side wall and the bottom of the tank body through a sliding chute, and the sliding chute is connected with the outer surface of the bearing keel of the SPE membrane recovery tank through an elastic sealing strip.
4. The electrolytic water tank device for an electrolytic hydrogen-rich water machine as claimed in claim 1, wherein the sintered electrolytic positive electrode and the sintered electrolytic negative electrode are both distributed in parallel with the lateral surface of the SPE membrane recovery tank, and the distance between the lateral surface of the SPE membrane recovery tank and the sintered electrolytic positive electrode and the sintered electrolytic negative electrode is 5-30 mm.
5. The electrolytic water tank device for an electrolytic hydrogen-rich water machine as claimed in claim 1, wherein the sintered electrolytic anode and the sintered electrolytic cathode are respectively located between the water inlet, the air outlet and the SPE membrane recovery tank, and the axes of the water inlet and the air outlet are parallel to the sintered electrolytic anode and the sintered electrolytic cathode, and the distance between the sintered electrolytic anode and the sintered electrolytic cathode is 1/3-3/4 of the width of the hydrogen chamber and the oxygen chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910891039.XA CN110550706A (en) | 2019-09-20 | 2019-09-20 | Electrolytic water tank device for electrolytic hydrogen-rich water machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910891039.XA CN110550706A (en) | 2019-09-20 | 2019-09-20 | Electrolytic water tank device for electrolytic hydrogen-rich water machine |
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| CN110550706A true CN110550706A (en) | 2019-12-10 |
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| CN201910891039.XA Pending CN110550706A (en) | 2019-09-20 | 2019-09-20 | Electrolytic water tank device for electrolytic hydrogen-rich water machine |
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Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106108658A (en) * | 2016-08-29 | 2016-11-16 | 福州品行科技发展有限公司 | A kind of antibacterial mineralising hydrogen-rich water dispenser and method of work thereof |
| CN106868531A (en) * | 2017-03-06 | 2017-06-20 | 许昌学院 | Solid polymer dielectric film electrode hydrogen water generating device and preparation method and application |
| CN106904720A (en) * | 2017-03-27 | 2017-06-30 | 大连东方舟工业装备有限公司 | A kind of device for generating water element water |
| CN206371791U (en) * | 2016-05-25 | 2017-08-04 | 广州弘皓电子科技有限公司 | Portable hydrogen hydrogen water integrated cup |
| CN107032454A (en) * | 2017-05-26 | 2017-08-11 | 中建水务（深圳）有限公司 | The current control method of proton water generator, water container and proton water generator |
| CN207091067U (en) * | 2017-05-26 | 2018-03-13 | 中建水务（深圳）有限公司 | proton water generator, water container |
| CN207158866U (en) * | 2017-07-31 | 2018-03-30 | 张慧明 | A kind of integrated form online production device of hydrogen beverage |
| CN108025931A (en) * | 2015-12-04 | 2018-05-11 | 日本多宁股份有限公司 | Electrolytic water generating device and electrolysis water generation system |
| CN108467090A (en) * | 2018-02-26 | 2018-08-31 | 深圳市量子氢生物技术有限公司 | A kind of hydrogen-oxygen separation electrolysis unit and hydrogen-rich cup, hydrogen-rich water dispenser |
| CN207958518U (en) * | 2017-11-08 | 2018-10-12 | 广州弘皓电子科技有限公司 | hydrogen cabin |
| CN109179592A (en) * | 2018-09-26 | 2019-01-11 | 傲自然成都生物科技有限公司 | A kind of reproducible electrochemistry water purification system of anode |
-
2019
- 2019-09-20 CN CN201910891039.XA patent/CN110550706A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108025931A (en) * | 2015-12-04 | 2018-05-11 | 日本多宁股份有限公司 | Electrolytic water generating device and electrolysis water generation system |
| CN206371791U (en) * | 2016-05-25 | 2017-08-04 | 广州弘皓电子科技有限公司 | Portable hydrogen hydrogen water integrated cup |
| CN106108658A (en) * | 2016-08-29 | 2016-11-16 | 福州品行科技发展有限公司 | A kind of antibacterial mineralising hydrogen-rich water dispenser and method of work thereof |
| CN106868531A (en) * | 2017-03-06 | 2017-06-20 | 许昌学院 | Solid polymer dielectric film electrode hydrogen water generating device and preparation method and application |
| CN106904720A (en) * | 2017-03-27 | 2017-06-30 | 大连东方舟工业装备有限公司 | A kind of device for generating water element water |
| CN107032454A (en) * | 2017-05-26 | 2017-08-11 | 中建水务（深圳）有限公司 | The current control method of proton water generator, water container and proton water generator |
| CN207091067U (en) * | 2017-05-26 | 2018-03-13 | 中建水务（深圳）有限公司 | proton water generator, water container |
| CN207158866U (en) * | 2017-07-31 | 2018-03-30 | 张慧明 | A kind of integrated form online production device of hydrogen beverage |
| CN207958518U (en) * | 2017-11-08 | 2018-10-12 | 广州弘皓电子科技有限公司 | hydrogen cabin |
| CN108467090A (en) * | 2018-02-26 | 2018-08-31 | 深圳市量子氢生物技术有限公司 | A kind of hydrogen-oxygen separation electrolysis unit and hydrogen-rich cup, hydrogen-rich water dispenser |
| CN109179592A (en) * | 2018-09-26 | 2019-01-11 | 傲自然成都生物科技有限公司 | A kind of reproducible electrochemistry water purification system of anode |
Non-Patent Citations (1)
| Title |
|---|
| 张招贤等: "《钛电极反应工程学》", 30 April 2009, 北京：冶金工业出版社 * |
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Application publication date: 20191210 |