WO2019154781A1 - Electrolytic cell and universal oxyhydrogen generator - Google Patents
Electrolytic cell and universal oxyhydrogen generator Download PDFInfo
- Publication number
- WO2019154781A1 WO2019154781A1 PCT/EP2019/052716 EP2019052716W WO2019154781A1 WO 2019154781 A1 WO2019154781 A1 WO 2019154781A1 EP 2019052716 W EP2019052716 W EP 2019052716W WO 2019154781 A1 WO2019154781 A1 WO 2019154781A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- electrolyte
- oxyhydrogen
- electrolytic cell
- useful
- cathode
- Prior art date
Links
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
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/02—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
-
- 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
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
-
- 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
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
-
- 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
- C25B9/70—Assemblies comprising two or more cells
-
- 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
Definitions
- electrolytic cell indicates a particular electrochemical cell that allows converting electrical energy into chemical energy. This process is called electrolysis.
- an electrolytic cell is a device that is capable of converting electric energy into chemical energy or chemical energy into electrical energy.
- the electrolytic cell is composed of two half-elements, also called half-cells.
- a half-element is generally composed of a metal electrode immersed in an electrolytic solution, sometimes constituted by the ions of the same metal and other times from the ions of another metal; there are also half elements in which the solution contains oxidized and reduced forms of ions different from the material which constitutes the electrode.
- anode The electrode where the half-reaction of oxidation takes place is called "anode", the one where reduction occurs "cathode”.
- electrolytic cells or electrolysers or electrochemical reactors : electric power is supplied in order to develop a chemical reaction (this process is called electrolysis), as already explained before.
- the electrolytic cells may be wet or dry.
- a dry cell uses a fluid electrolyte, with only enough moisture to allow current to flow. Unlike a wet cell, a dry cell can work in any orientation without spilling, as it contains no free liquid, making it suitable for portable equipment.
- WO 2013/097423 refers to a group of electrodes of an oxygen -hydrogen generator.
- a "multi-hole" (multi-slot) electrode sheet and a flat electrode sheet are arranged in parallel and the positive electrode or negative electrode can respectively be electrically connected to achieve an optimal electrolysis effect.
- This electrode group efficiently and rapidly electrolytes the aqueous liquid and the electrolyte to generate a large quantity of hydrogen -oxygen gas and increases the specific gravity and the hydrogen purity. This is a system of immersion cells.
- the oxyhydrogen generator of the present invention is aimed at:
- booster of hydrogen in accordance with the present invention means an additional electrolytic cell, which has the sole task of producing pure hydrogen; said supplementary electrolytic cell being coupled to an additional oxyhydrogen electrolytic cell, with the purpose of increasing the amount of hydrogen obtained from the native mixture, which usually is of 12% per litre of produced gas) for gaseous or liquid generators or combustion burners also through the intake system or dedicated injection system (coupling to a boiler of any size for heating in both household and industrial application );
- the present invention therefore relates also to a generator with electrolytic cells (dry oxyhydrogen multiple cells) and with multiple feeders, which uses a hydrogen booster producing an adjustable amount of hydrogen gas and, in the case of a kit for the automotive industry, with ionizing systems for liquid and gaseous fuels.
- thermometer (8) At least a thermometer (8) ;
- an electrolytic cell (23) comprising:
- cathode (31) and an anode (31) of triangular shape in which said cathode and said anode (31) report a U-cutting (38), useful to speed up/facilitate mounting and/or removing the supply rod (37).
- said grip plate (29) shows a U-shaped cut (38), in the case in which the grip plate (29) retraces the perimeter of the cathode (31) and of the anode (31);
- the term "unbalanced configuration" is intended to refer to the fact that, according to such configuration, the number of elements for each category (cathodes, anodes, full neutral plates and perforated neutral plates) is not the same.
- the electrolytic cells is composed of a total of 2 anodes, 3 cathodes, 32 full neutral plates and 16 perforated neutral plates placed in the following sequence: anode - 8 full neutral plates - anode - 8 full neutral plates - cathode - 16 perforated neutral plates - cathode - 16 full neutral plates.
- triangular electrolytic cell (23) having an unbalanced or different configuration, are also possible, by arranging and/or by changing the number of the elements (29, 30, 31, 32 and 33) according to a different order; wherein said triangular electrolytic cell (23) is characterised in that:
- the elements (29, 30, 31, 32 and 33) preferably have:
- a triangular electrolytic cell in accordance with the present invention has all three sides measuring from 100 to 600 mm; preferably from 200 to 400 mm; more preferably 300 mm; or
- a triangular electrolytic cell in accordance with the present invention has a base measuring from 50 to 800 mm; preferably from 200 to 600 mm; more preferably 396 mm; and a height measuring of 25 to 400 mm; preferably from 100 to 300 mm; more preferably 198 mm;
- perimeter holes with a diameter from 5 to 10 mm;
- the number and/or the size of the holes can vary, as the dimensions of the elements (29, 30, 31, 32 and 33).
- the expression "full" plate (which is for example referred to element (32) of Figures 3a and 3b) is intended to refer to a plate, which does not have holes over the whole surface (or it is not perforated over the whole su rface), but that presents holes only along its perimeter and/or angles and in the centre.
- This expression is used in contrast with the expression "perforated” plate (which is for example referred to element (33) of Figures 3a and 3b), which according to the present invention is intended to refer to a plate, which has holes over the whole surface (or it is perforated over the whole surface). Therefore, a perforated plate according to the invention is intended to refer to a plate, which presents holes not only along its perimeter and/or angles and its centre, but also in its entire surface.
- a further object of the present invention is a hydrogen booster (20) comprising:
- ionizing filters (41) are external to the oxyhydrogen generator and are installed on the fuel inlet tube;
- bubbler (2) preferably of square section having lamellar system useful to prevent leakage of electrolyte into the oxyhydrogen flow tube in case of strong gurgling.
- kit useful in the automotive field to optimize the combustion processes of the engine comprising :
- At least one bubbler (2) optionally with a square cross-section, having a lamellar system specially designed to prevent leakage of electrolyte into the oxyhydrogen flow tube in the event of a strong gurgling;
- a further object of the present invention is an ionizing filter (41), comprising:
- the plastic body 51a has an inlet tube (52);
- the plastic body 51b has an outlet tube (53);
- the two bodies made of plastic material (51a and 51b) are coupled/connected to each other through a classic screw closure system, or through a classical pressure closing system or welded;
- a bubbler (2) at least a bubbler (2) , optionally with a square cross section having a lamellar system specifically designed to prevent leakage of electrolyte into the oxyhydrogen flow tube in case of strong gurgling;
- the hydrogen and the oxygen are obtained/produced by the triangular electrolytic cells according to the invention in gaseous form. These two gases (hydrogen and oxygen) are generated/produced on-demand (and not stored) in stoichiometric gaseous form with the 88% of oxygen and 12% of hydrogen, at a pressure of 1.5 bar. Moreover, said hydrogen and oxygen gases both pass inside the bubbler, which also acts as a mixing chamber when the electrolytic hydrogen cell is activated, which enriches the mixture of oxyhydrogen, by increasing the amount of hydrogen of at least 12 %. The maximum operating pressures of the gases do not exceed 5 bar, maintaining the generator in safety.
- the cell and the oxyhydrogen generator of the present invention will now be described by way of illustration and not by way of limitation, according to a preferred embodiment, with particular reference to the figures of the accompanying drawings.
- Figure 1 shows a block diagram of the oxyhydrogen generator, comprising:
- thermometer (8)
- FIG. 3a are shown individually and disassembled, the elements that make up the triangular electrolytic cell (23) according to the invention:
- the electrolytic cell (23) can have different types of configurations, by arranging one or more elements (29, 30, 31, 32 and 33) according to a different order.
- An example of a possible configuration is described in Example 1.
- Figure 3c shows the triangular electrolytic cell (23), assembled in front view, comprising:
- FIG. 3d shows a further version/variant of the cathode/anode (31) having triangular shape.
- Said cathode/anode (31) has a U-shaped cutting (38), useful to speed up/facilitate the setting up/extraction of the supply rod (37).
- a U-shaped cutting (38) useful to speed up/facilitate the setting up/extraction of the supply rod (37).
- an identical U-shaped cut (38) is made on said grip plate (29).
- Said U-cutting (38) is closed by a stud (39), black or red depending on the polarity of the supply rod (37).
- the membrane (61) for the separation of gases with electrolyte is in single-filament polyester mesh "Mesh T165", indicated for the electrolyte NaOH, which forms a thin wall, which allows the water to pass through, but not the gas bubbles.
- the ions H + and 0 2 pass through the water, pass through the membrane and form the gas on the plate of the electrode from which they are attracted (positive or negative).
- the hydrogen remains on the negative side of the wall of the membrane and the oxygen remains on the positive side.
- the network functions as a "dividing wall” which separates the two chambers. The gases rise to the top of their respective side of the chamber, collect at the top and exit through the hole in the electrode plate.
- the ionizing filter (41) is shown - viewed from above (a), viewed laterally (b) and viewed from below (c)- comprising: - an outer shell composed of two bodies made of plastic (51a and 51b).
- the plastic body (51a) has an inlet tube (52) and the plastic body (51b) has an outlet tube (53).
- the two bodies made of plastic material (51a and 51b) are coupled/connected to each other through a classic screw closure system or through a classic pressure closing system or a bayonet coupling or welded;
- FIG. 7 shows a block diagram of the boiler energy saving system, comprising:
- bubbler (2) optionally having square section, having a lamellar system to prevent leakage of electrolyte into the oxyhydrogen flow tube in case of strong gurgling;
- New trianqular cells fed with unbalanced (and not) electrical system New trianqular cells fed with unbalanced (and not) electrical system.
- the triangular electrolytic cell (dry cells) object of the present invention has a new unbalanced configuration system of the type: Anode - 8 full neutral plates - Anode - 8 full neutral plates - Cathode - 16 perforated neutral plates - Cathode - 16 full neutral plates - Cathode
- the oxyhydrogen generator obtained with the new triangular cells object of the invention, yielded, with the same weight, more than twice the amount of oxyhydrogen (up to 17 litres / minute of oxyhydrogen gas) with respect to the generator described in patent n. IT0001402836 (up to 7 litres/minute of gas oxyhydrogen), thus bringing the production of oxyhydrogen from 480 litres / hour to 1,000 litres / hour.
- the new triangular cells object of the present invention being less bulky thanks to their triangular shape, allowed the application of multiple cooling systems by means of extractor fans placed on the sides.
- the new triangular cells object of the present invention created a forced air flow, which also allowed the simultaneous cooling of the two sides of the same and of the electric tie rods/connectors, which fed the triangular cells from the base, thus avoiding electric dispersions.
- the triangular space that was formed between the two triangular cells could accommodate a tank or bubbler with an inverted triangular section, optimizing the installation spaces.
- the inverted funnel shape increased the velocity of the outgoing gas upwards.
- a small generator capable of producing up to 4 l/min of oxyhydrogen was connected to a 30 kW LPG boiler (normal wall boiler in residential buildings and also applicable to condensing boilers).
- connection of the oxyhydrogen generator was carried out by means of a tube connected to the main gas supply pipe (LPG) with a hydraulic coupling Y-shaped.
- the regulation of the quantity of the gas mixture to be introduced into the boiler burner was carried out by a technician skilled in the sector (for example a technician who tests the new boilers at the first ignition).
- Modular kits were made for the automotive industry using two electrolytic triangular cells for the production of oxyhydrogen.
- the production of hydrogen was made adjustable and was managed through one or more PWM modulators ( ulse-width modulation ).
- the feeding of the dry cells occurred through a buffer battery or the alternator of the medium (if oversized).
- the results reported in Tables 2 and 3 show a saving of fuel (and therefore also a cost saving, as well as a lower environmental pollution due to a lower emission of C0 2 ), both for vans up to 3,000 cm 3 and for heavy vehicles up to 12,000 cm 3 .
- a generator of oxyhydrogen was used according to the present invention to optimize the combustion processes of an engine.
- a modular kit of oxyhydrogen composed of: two electrolytic cells, a tank, a bubbler, a PWM modulator, a control unit connected to the CPU (central processing unit) of the car, a protection fuse, a relay under key, an external ionizing filter (optimized for liquid fuels) which was placed on the fuel flow tube.
- the ionizing filter that was used consisted of a cylindrical body with two connectors placed at the ends to allow installation on the fuel flow tube of the engine.
- metal beads of the same size in the following quantities: copper: aluminium: zinc or stainless steel in ratio 1:1: 1; a small neodymium magnet with an approximate diameter of 1 cm; and two filtering synthetic membranes (10 micron, made of nylon or stainless steel) to prevent the exit of metal beads from about 0.4 mm.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT102018000002441 | 2018-02-06 | ||
IT201800002441A IT201800002441A1 (en) | 2018-02-06 | 2018-02-06 | ELECTROLYTIC CELL AND UNIVERSAL OXYDROGEN GENERATOR |
Publications (1)
Publication Number | Publication Date |
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WO2019154781A1 true WO2019154781A1 (en) | 2019-08-15 |
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ID=62143459
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/EP2019/052716 WO2019154781A1 (en) | 2018-02-06 | 2019-02-05 | Electrolytic cell and universal oxyhydrogen generator |
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IT (1) | IT201800002441A1 (en) |
WO (1) | WO2019154781A1 (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100276279A1 (en) | 2008-11-17 | 2010-11-04 | Etorus, Inc. | Electrolytic hydrogen generating system |
WO2013097423A1 (en) | 2011-12-31 | 2013-07-04 | 瑞劲绿能科技股份有限公司 | Electrode group for oxyhydrogen generator |
IT1402836B1 (en) | 2010-12-01 | 2013-09-27 | Soriano | ELECTROLYTIC CELL AND DEVICE FOR THE GENERATION OF OXIDROGEN IN PRESSURE. |
US20150068889A1 (en) | 2013-11-17 | 2015-03-12 | Don Lee Hansen | System and method for generating hydrogen and oxygen gases |
WO2015080684A1 (en) | 2013-11-27 | 2015-06-04 | Ayys Muhendislik Insaat Ve Tic. Ltd. Sti. | Pure hydroxy (hydrogen - oxygen) energy system |
-
2018
- 2018-02-06 IT IT201800002441A patent/IT201800002441A1/en unknown
-
2019
- 2019-02-05 WO PCT/EP2019/052716 patent/WO2019154781A1/en active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100276279A1 (en) | 2008-11-17 | 2010-11-04 | Etorus, Inc. | Electrolytic hydrogen generating system |
IT1402836B1 (en) | 2010-12-01 | 2013-09-27 | Soriano | ELECTROLYTIC CELL AND DEVICE FOR THE GENERATION OF OXIDROGEN IN PRESSURE. |
WO2013097423A1 (en) | 2011-12-31 | 2013-07-04 | 瑞劲绿能科技股份有限公司 | Electrode group for oxyhydrogen generator |
US20150068889A1 (en) | 2013-11-17 | 2015-03-12 | Don Lee Hansen | System and method for generating hydrogen and oxygen gases |
WO2015080684A1 (en) | 2013-11-27 | 2015-06-04 | Ayys Muhendislik Insaat Ve Tic. Ltd. Sti. | Pure hydroxy (hydrogen - oxygen) energy system |
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IT201800002441A1 (en) | 2019-08-06 |
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