US1913429A - Apparatus for producing gases by electrolysis - Google Patents
Apparatus for producing gases by electrolysis Download PDFInfo
- Publication number
- US1913429A US1913429A US492898A US49289830A US1913429A US 1913429 A US1913429 A US 1913429A US 492898 A US492898 A US 492898A US 49289830 A US49289830 A US 49289830A US 1913429 A US1913429 A US 1913429A
- Authority
- US
- United States
- Prior art keywords
- steam
- electrolyte
- electrolysis
- water
- hydrogen
- 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.)
- Expired - Lifetime
Links
- 239000007789 gas Substances 0.000 title description 12
- 238000005868 electrolysis reaction Methods 0.000 title description 4
- 239000003792 electrolyte Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 8
- 239000001257 hydrogen Substances 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 239000011244 liquid electrolyte Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
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
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
Definitions
- This invention relates to an apparatus for producing gases by electrolysis, and has to do particularly with a novel method of producing hydrogen gas from water.
- the present invention makes use of the fact that water in the form of live steam is as close to being decomposed into its elements as it is physically possible and working on this principle I have discovered that if the water is introduced into the electrolyte bath in the form of live steam and is maintained in this substantially decomposed form during the electrolytic action, that the breaking up of the water intohydrogen and oxygen is accomplished with great rapidity.
- Any suitable means may be used for producing steam and I have shown a suitable steam generator which may be generally designated 1.
- This generator may consist of a storage container 2, flash coils 3 and a suitable burner 4.
- a valve 5 controls the flow of steam to a I superheater 6.
- the superheater coil 6 is designed to discharge the steam through the jet 7 and against the deflector member 8.
- the jet 7 discharges into a tank 9 which may be called the electrolyte tank and is designed to hold a supply of electrolyte 10. Circulation within the tank 9 is maintained b means of a suitable convection tube 11 and c eck valves 12 and 13 insure the isolation of the electrolyte or acid in the correct part of the system.
- An inverted gas container 14 is posltioned within the tank 9 and may be more or less standard in that it contains a negative electrode plate 15, a positive electrode plate 16 and oxygen and hydrogen outlets l7 and 18, respectively.
- a suitable baflle plate 19 may be positioned as shown whereby to positively separate the inverted container 1 4: into two separate gas chambers.
- thermometer may be located as at 21 so as to enable the electrolyte to be maintained at a constant temperature through the medium of a burner 22.
- eature of the present invention resides in the material decrease of elec- In operation the container '9 is filled to a predetermined level with electrol and the container 14 is inserted in the mam tank to a depth-that will submerge both electrodes and form an electrical connection with the electrolyte, direct current being fed into the electrodes as indicated in the drawin Superheated steam is then forced into t e electro lyte through the ipe 6 and jet 7 which electrolyte is prefera 1y maintained at a tem rature suflicient to prevent condensation o the steam before the gases have separated.
- a device of the bharacter described comprising a tank for holding a quantity of liquid electrolyte, an inverted gas container 40 divided into a' plurality of chambers, electrodes in said chambers, means for maintaining said electrolyte'at a predetermined temperature, means for introducing steam into said electrolyte, and means for bafliing said steam whereby to initially distribute the same throughout the electiglyte.
- a device of the character described comprising a tank for holding a quantity of liquid electrolyte, an inverted gas container divided into a plurality of chambers, electrodes in each of said chamber, means for maintaining said electrolyte at a predetermined temperature, means for introducing steam into said electrolyte, and means for lcausing a positive circulation of the electro- In testimony whereof I ailix my signature.
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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)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
June 13, 1933.
E. M. CRAWFORD APPARATUS FOR PRODUCING GASES BY ELECTROLYS IS Filed NOV. 3, 1950 "llll i ll fwsurwv \"5 III H H1 :i
A TTORNEYJ Patented June 13, 1933 UNITED STATES PATENT OFFICE EARL MILES CRAWFORD, OF FLINT, MICHIGAN, ASSIGNOR OF ONE-FOURTH TO EDWIN W. ATWOOD, ONE-FOURTH 1'0 EARL L. PIIMON, AND ONE-FOURTH TO HUBER! E.
PIERCE, ALL OF FLINT, MICHIGAN APPARATUS FOR PRODUCING GASES BY ELECTROLYSIS Application filed November 3, 1930. Serial No. 492,898.
This invention relates to an apparatus for producing gases by electrolysis, and has to do particularly with a novel method of producing hydrogen gas from water. 1
Heretofore in the production of hydrogen as a commercial gas, it has been the general practice to obtain the same by subJecting water to an electrolytic action. Various methods and apparatus have been provided in attemptingto accelerate the decomposition of water by means of electrolysis, but so far as I am aware the majority of these methods have beendirected towards improvements in connection with the electrolytic action. However, with the fastest method now in use, the production of hydrogen from water is considered a relative expensive process and requires the expenditure of a large amount of electrical units in transforming the liquid to a stable gas that may be collected.
' It is the object of the present invention to greatly accelerate the production of hydrogen from water and with a minimum expenditure of electrical units. More specifically, the present invention makes use of the fact that water in the form of live steam is as close to being decomposed into its elements as it is physically possible and working on this principle I have discovered that if the water is introduced into the electrolyte bath in the form of live steam and is maintained in this substantially decomposed form during the electrolytic action, that the breaking up of the water intohydrogen and oxygen is accomplished with great rapidity.
An additional that various forms of apparatus may be utilized in carrying out the steps of the method.
Any suitable means may be used for producing steam and I have shown a suitable steam generator which may be generally designated 1. This generator may consist of a storage container 2, flash coils 3 and a suitable burner 4.
A valve 5 controls the flow of steam to a I superheater 6. The superheater coil 6 is designed to discharge the steam through the jet 7 and against the deflector member 8. The jet 7 discharges into a tank 9 which may be called the electrolyte tank and is designed to hold a supply of electrolyte 10. Circulation within the tank 9 is maintained b means of a suitable convection tube 11 and c eck valves 12 and 13 insure the isolation of the electrolyte or acid in the correct part of the system. An inverted gas container 14 is posltioned within the tank 9 and may be more or less standard in that it contains a negative electrode plate 15, a positive electrode plate 16 and oxygen and hydrogen outlets l7 and 18, respectively. A suitable baflle plate 19 may be positioned as shown whereby to positively separate the inverted container 1 4: into two separate gas chambers.
In case of an A. C. current supply, any suitable rectifying equipment, such as generally indicated at 20, may be utilized as will be well understood by those skilled in the art. A thermometer may be located as at 21 so as to enable the electrolyte to be maintained at a constant temperature through the medium of a burner 22. eature of the present invention resides in the material decrease of elec- In operation the container '9 is filled to a predetermined level with electrol and the container 14 is inserted in the mam tank to a depth-that will submerge both electrodes and form an electrical connection with the electrolyte, direct current being fed into the electrodes as indicated in the drawin Superheated steam is then forced into t e electro lyte through the ipe 6 and jet 7 which electrolyte is prefera 1y maintained at a tem rature suflicient to prevent condensation o the steam before the gases have separated. This steam passes through the electric field created by the current traveling between the electrodes and as the hydrogen and oxygen ele-' ments are as near their separation point as possible when in the form of steam, it will be obvious that very little more energy is required to completely separate the hydrogen 5 and oxygen. Therefore, as the steam passes into the electric field decom osition of the same will take place, the hy rogen positives .being drawn to the negative electrode and the oxygen negatives being drawn to the positive electrode 16. Due to the bafile 19, it will be obvious that the separated oxygen and hydrogen gases will be collected in their respective chambers and drawn off through the pipes 17 and 18 to be stored. or used as 15 desired.
It will thus be seen that I'have provided means for greatly accelerating decomposition of water into hydrogen and oxygen as a greater part of the work is accomplished in 20 changing the water to steam before the electrolytic action. Further, the amount of current required is considerably reduced, as it will be obvious that very little current is required to complete the breaking up which is substantially accomplished by changing the water to steam. I obtain the best results by maintaining the electrolyte at a temperature suflicient to prevent any condensing of the steam, but it will be understood that I do not wish to be limited to any specific temperature as it may be possible to obtain eflicient results at a substantially lower temperature; and it may be possible to obtain eflicient results by applying the heat at difl'erent points than at the bottom of the tank 9.
What I claim is:
1. A device of the bharacter described, comprising a tank for holding a quantity of liquid electrolyte, an inverted gas container 40 divided into a' plurality of chambers, electrodes in said chambers, means for maintaining said electrolyte'at a predetermined temperature, means for introducing steam into said electrolyte, and means for bafliing said steam whereby to initially distribute the same throughout the electiglyte. 2." A device of the character described, comprising a tank for holding a quantity of liquid electrolyte, an inverted gas container divided into a plurality of chambers, electrodes in each of said chamber, means for maintaining said electrolyte at a predetermined temperature, means for introducing steam into said electrolyte, and means for lcausing a positive circulation of the electro- In testimony whereof I ailix my signature.
EARL MILES CRAWFORD. I
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US492898A US1913429A (en) | 1930-11-03 | 1930-11-03 | Apparatus for producing gases by electrolysis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US492898A US1913429A (en) | 1930-11-03 | 1930-11-03 | Apparatus for producing gases by electrolysis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1913429A true US1913429A (en) | 1933-06-13 |
Family
ID=23958059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US492898A Expired - Lifetime US1913429A (en) | 1930-11-03 | 1930-11-03 | Apparatus for producing gases by electrolysis |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1913429A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2471912A (en) * | 1942-12-08 | 1949-05-31 | Westinghouse Electric Corp | Control of electrolytic processes |
| US3471391A (en) * | 1965-11-30 | 1969-10-07 | Fischer & Porter Co | Chlorine gas leak detector |
| US3917524A (en) * | 1974-05-10 | 1975-11-04 | Leeds & Northrup Co | Electrochemical cell assembly |
| US4361471A (en) * | 1980-06-23 | 1982-11-30 | Kosarek Louis J | Electrolytic swimming pool chlorination |
| US4493760A (en) * | 1982-12-23 | 1985-01-15 | Industrie Zanussi S.P.A. | Electrolytic cell having nonporous partition |
| US20090011297A1 (en) * | 2007-07-03 | 2009-01-08 | Samsung Electro-Mechanics Co., Ltd. | Metal composite electrode for a hydrogen generating apparatus |
| US20100005809A1 (en) * | 2008-07-10 | 2010-01-14 | Michael Anderson | Generating electricity through water pressure |
| WO2019190729A1 (en) * | 2018-03-29 | 2019-10-03 | Battelle Energy Alliance, Llc | Electrochemical cells comprising three-dimensional (3d) electrodes |
-
1930
- 1930-11-03 US US492898A patent/US1913429A/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2471912A (en) * | 1942-12-08 | 1949-05-31 | Westinghouse Electric Corp | Control of electrolytic processes |
| US3471391A (en) * | 1965-11-30 | 1969-10-07 | Fischer & Porter Co | Chlorine gas leak detector |
| US3917524A (en) * | 1974-05-10 | 1975-11-04 | Leeds & Northrup Co | Electrochemical cell assembly |
| US4361471A (en) * | 1980-06-23 | 1982-11-30 | Kosarek Louis J | Electrolytic swimming pool chlorination |
| US4493760A (en) * | 1982-12-23 | 1985-01-15 | Industrie Zanussi S.P.A. | Electrolytic cell having nonporous partition |
| US20090011297A1 (en) * | 2007-07-03 | 2009-01-08 | Samsung Electro-Mechanics Co., Ltd. | Metal composite electrode for a hydrogen generating apparatus |
| US20100005809A1 (en) * | 2008-07-10 | 2010-01-14 | Michael Anderson | Generating electricity through water pressure |
| WO2019190729A1 (en) * | 2018-03-29 | 2019-10-03 | Battelle Energy Alliance, Llc | Electrochemical cells comprising three-dimensional (3d) electrodes |
| US12308483B2 (en) | 2018-03-29 | 2025-05-20 | Battelle Energy Alliance, Llc | Electrochemical cells comprising three-dimensional (3D) electrodes including a 3D architectured material, related systems, and related methods of forming hydrogen |
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