WO2003054252A1 - Apparatus and method for the production of pure oxygen and hydrogen - Google Patents
Apparatus and method for the production of pure oxygen and hydrogen Download PDFInfo
- Publication number
- WO2003054252A1 WO2003054252A1 PCT/GB2001/005411 GB0105411W WO03054252A1 WO 2003054252 A1 WO2003054252 A1 WO 2003054252A1 GB 0105411 W GB0105411 W GB 0105411W WO 03054252 A1 WO03054252 A1 WO 03054252A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- oxygen
- hydrogen
- water
- environmental
- mixture
- 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
- 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
-
- 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
- the Environmental Regenerator is a system and a method for the production of an oxygen and hydrogen mixture for the regeneration of the environment.
- the efficacity of the system is based on a new process of water electrolysis. It results from the fact that the analysis electrodes are extremely close to each other, which reduces drastically the distance to be covered by the electrons going from an electrode to the other.
- the layout of the electrodes allows a more intensive production thanks to the extreme closeness of the electrodes, the absence of separating membrane and the great freedom of movement.
- the Environmental Regenerator is very self-sufficient as it contains water still for its distilled water supply. One must point out that, to be sure that the water will only produce oxygen and hydrogen, any other molecule that the water may contain must be eliminated.
- each species has a life cycle, which is related to its specific characteristics.
- the life cycle of each species is therefore commensurate with its size or sometimes with other distinctive properties.
- the tortoise which is a small animal shows outstanding longevity. This is certainly attributable to the slow formation of its shell.
- a large size means a large consumption of the nutrients, which is necessary for the development and maintenance of the body.
- the quantity of food required by, for example, an elephant is proportional to its size.
- the same principle applies to its oxygen consumption. Every time it breathes, the elephant must absorb an average quantity of oxygen to maintain its internal activities and the work of its muscles. If the air it breathes has low oxygen content, the elephant will get weaker and lose weight as a consequence of the reduction of its internal activities. Therefore, it is clear that the reduction of oxygen in nature is one of the main permanent causes of loss of species, whether they belong to fauna or to flora.
- the ozone cycle is constant and goes from the transformation of oxygen into ozone in the upward direction to the destruction of ozone by sunlight in the downward direction, from the sky to the ground. This cycle insures the protection of the earth from the full intensity of sunrays. Its temperature and density are its operational characteristics. Both these main characteristics are totally and absolutely complementary. This means that a loss of ozone density results automatically in a loss of ozone temperature.
- Oxygen is one of the coldest gases of the atmosphere. It is also a fuel, which is absolutely necessary for any combustion. A lack of oxygen reduces the combustion rate at the individual level as well as at the collective level. But, unlike hydrogen, oxygen is a gas produced by synthesis, a chemical reaction. Forests constitute its main source of production through photosynthesis. But oxygen is stocked as composites and the largest reserve on earth is stocked as water, which is made up of a third (1/3) oxygen and two thirds (2/3) hydrogen. The liquid form of this water constitute the oceans and its solid form makes up the south and north poles. Because of global warming, water reserves are larger and larger for a simple reason: the main reserve of oxygen, which could be used for the restoration of natural conditions, is in hibernation in the oceans.
- This invention through the production of oxygen released in the atmosphere, creates a whole series of reactions and transformations:
- oxygen is very heavy and cold.
- the cohesive force of the oxygen produced by the Environmental Regenerator is higher than that of the other molecules which compose the air; therefore it goes downwards and automatically pushes upwards other gas, including toxic gases such as fumes emitted by cars and industrial processes.
- toxic gases such as fumes emitted by cars and industrial processes.
- men and animals breathe a purer atmosphere.
- the still is made up of a heating resistance 21fitted inside a kettle 20.
- a thermostat 22 is fitted at the central point of the base of the kettle 20. Its function is to stop the electric supply if there is overheating. The thermostat directly supplies the heating resistance 21.
- the ordinary water comes into the kettle through a chilling coil 23, which is fitted in a tube situated above the kettle. Before reaching the kettle, the incoming water goes through the coil 23 to cool the steam coming out of the kettle 20. Consequently, the water is pre-heated when it reaches the kettle.
- a water level regulator 24 is fitted between the chilling coil 23 and the kettle 20. This water level regulator 24 maintains in permanence a constant level of water in the kettle 20, allowing the spillage of water into the electrolyser 40.
- a header is provided on top of the kettle 20. It's a tube containing the chilling coil 23. It receives the steam from the kettle 20 and that steam cool as gets into contact with the coil 23 and turns into water drops. All these water drops fall at the bottom of the header and go directly to the distilled water discharge duct 32. 2.
- a distilled water tank 30 is provided next to the still. Its function is to recover all the distilled water produced by the still and to control the operation of the still in accordance with the supply cycle of the electrolyser 40. a.
- a discharge duct 32 links the still to the distilled water tank 30. That duct 32 supplies distilled water to the tank 30.
- the distilled water tank 30 is a box of a size proportional to its supply and to the electrolysis rate of the Environmental Regenerator. It is fed by the still and, in its turns, feeds the electrolyser 40 while controlling the volume of distilled water through the electrolyser 40.
- a water level detector (not shown in Fig.3) fitted inside the tank 30 turns controls the operation (on/off) of the still.
- a low capacity pump 34 for the power supply of the distilled water electrolyser 40, a low capacity pump 34, with a non-return valve (not shown) is fitted above the tank 30, This pump 34 is operated and regulated according to the demand, at the rate of consumption of the electrolyser 40.
- the electrolyser 40 provides the ultimate production of the two components which are the object of the invention, i.e. oxygen and hydrogen.
- the electrolyser 40 is housed in a metal box which is divided in three parts: the inlet tank 42, the electrode housing and the gas header 43.
- the electrodes 46,47 are fitted one against the other, separated and isolated by a plastic material 48. Their shape is square and they have a communication opening to allow the water to circulate and the gases to be discharged.
- the anodes 46 are made of stainless steel and the cathodes 47 of nickel. The difference in potential allows the maximum water separation. However, the electrodes anodes 46 and cathodes 47 can both be made of stainless steel to reduce production costs. d.
- Isolating plastic 48 placed between anodes 46 and cathodes 47 has the same shape as the electrodes 46,47 but a larger inside opening to allow for a large surface of contact created by distilled water between two electrodes.
- the electrolyser 40 receives electricity at both ends.
- Each anode 46 is connected to the positive termmal of electricity supply 60 on the side opposite the cathodes 47 and each cathode 47 is connected to the negative terminal of the electricity supply 60 on the side opposite the anodes 46.
- the space between two electrodes constitutes a cell 45 and each cell 45 is the active area of water separation. The rate of consumption of electrical energy of a cell 45 varies with the distance which separates its two electrodes 46,47 which means that the larger the separating distance, the higher the consumption.
- the apparatus has a very low consumption because its cells 45 are very narrow as the anodes are very near the cathodes. g. As distilled water does not conduct electricity, a solution of saturation of KOH is diluted in the distilled water, inside the electrolyser cells 45. This establishes conductivity in the water to allow the passage of current in the water and the process of separation..
- the purifier Fig.5 is a box for the separation of the gases from any steam which may be present in the gas flow released from the electrolyser 40.
- a. It's a stainless steel or plastic box. It includes a separation 54 in its centre with a communication path at the bottom of the box which allow the liquids and gases to enter at one end and come out at the other end.
- b. It always contains an electrolyte saturation h which the gases are flushed. Gases cross through this liquid; the water steam remain in the liquid and the gas which escapes is purified.
- the entrance of gases 51 in the purification box 50 is situated above its first side and the exit 53 is situated above its second side. The only way of communication of both side is at the bottom of the box 50; therefore, all gases have to cross the liquid to go from one side to the other side.
- An universal type electric supply card 60 for the system is mounted above the electrolyser 40. Its components provide for the filtering of the electric current and the control of the direction of the current. a. A bridge of rectifying diodes is fitted at the entrance of the current to define the direction of the energy so that a pole is always negative and the other pole always positive. b. An electric current transformer of the alternative to direct current type is fitted on the supply card 60. The direct current increases the speed of separation of the water as it facilitates the movement of the electrons. c. A visual control circuit is fitted on the card 60 to show the rate of production of the apparatus and to detect any operating failure.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2002222136A AU2002222136A1 (en) | 2001-12-04 | 2001-12-04 | Apparatus and method for the production of pure oxygen and hydrogen |
PCT/GB2001/005411 WO2003054252A1 (en) | 2001-12-04 | 2001-12-04 | Apparatus and method for the production of pure oxygen and hydrogen |
EP01275064A EP1461473A1 (en) | 2001-12-04 | 2001-12-04 | Apparatus and method for the production of pure oxygen and hydrogen |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/GB2001/005411 WO2003054252A1 (en) | 2001-12-04 | 2001-12-04 | Apparatus and method for the production of pure oxygen and hydrogen |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2003054252A1 true WO2003054252A1 (en) | 2003-07-03 |
Family
ID=9910004
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB2001/005411 WO2003054252A1 (en) | 2001-12-04 | 2001-12-04 | Apparatus and method for the production of pure oxygen and hydrogen |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP1461473A1 (en) |
AU (1) | AU2002222136A1 (en) |
WO (1) | WO2003054252A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106757125A (en) * | 2017-01-13 | 2017-05-31 | 武汉大学 | A kind of plateau air water-intaking oxygen integrated device and its control method |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9833769B2 (en) | 2011-02-07 | 2017-12-05 | Basf Se | Process for producing water-absorbing polymer particles with high free swell rate |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4107008A (en) * | 1975-06-16 | 1978-08-15 | Beeston Company Limited | Electrolysis method for producing hydrogen and oxygen |
EP0111573A1 (en) * | 1982-12-14 | 1984-06-27 | Stanley A. Meyer | Hydrogen generator system |
EP0417647A1 (en) * | 1989-09-08 | 1991-03-20 | Packard Instrument Company, Inc. | Apparatus and method for generating hydrogen and oxygen by electrolytic dissociation of water |
US5231954A (en) * | 1992-08-05 | 1993-08-03 | J. C. Conner | Hydrogen/oxygen fuel cell |
-
2001
- 2001-12-04 WO PCT/GB2001/005411 patent/WO2003054252A1/en not_active Application Discontinuation
- 2001-12-04 AU AU2002222136A patent/AU2002222136A1/en not_active Abandoned
- 2001-12-04 EP EP01275064A patent/EP1461473A1/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4107008A (en) * | 1975-06-16 | 1978-08-15 | Beeston Company Limited | Electrolysis method for producing hydrogen and oxygen |
EP0111573A1 (en) * | 1982-12-14 | 1984-06-27 | Stanley A. Meyer | Hydrogen generator system |
EP0417647A1 (en) * | 1989-09-08 | 1991-03-20 | Packard Instrument Company, Inc. | Apparatus and method for generating hydrogen and oxygen by electrolytic dissociation of water |
US5231954A (en) * | 1992-08-05 | 1993-08-03 | J. C. Conner | Hydrogen/oxygen fuel cell |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106757125A (en) * | 2017-01-13 | 2017-05-31 | 武汉大学 | A kind of plateau air water-intaking oxygen integrated device and its control method |
Also Published As
Publication number | Publication date |
---|---|
EP1461473A1 (en) | 2004-09-29 |
AU2002222136A1 (en) | 2003-07-09 |
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