US1461661A - Electrolyzing apparatus for the manufacture of oxygen and hydrogen - Google Patents
Electrolyzing apparatus for the manufacture of oxygen and hydrogen Download PDFInfo
- Publication number
- US1461661A US1461661A US549602A US54960222A US1461661A US 1461661 A US1461661 A US 1461661A US 549602 A US549602 A US 549602A US 54960222 A US54960222 A US 54960222A US 1461661 A US1461661 A US 1461661A
- Authority
- US
- United States
- Prior art keywords
- electrodes
- hydrogen
- oxygen
- manufacture
- nickel
- 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
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title description 6
- 239000001257 hydrogen Substances 0.000 title description 6
- 229910052739 hydrogen Inorganic materials 0.000 title description 6
- 238000004519 manufacturing process Methods 0.000 title description 6
- 239000001301 oxygen Substances 0.000 title description 6
- 229910052760 oxygen Inorganic materials 0.000 title description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 18
- 229910052759 nickel Inorganic materials 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 239000002184 metal Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000003792 electrolyte Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 229910001018 Cast iron Inorganic materials 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 239000003518 caustics Substances 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 229920001875 Ebonite Polymers 0.000 description 1
- 239000000899 Gutta-Percha Substances 0.000 description 1
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 1
- 229910000576 Laminated steel Inorganic materials 0.000 description 1
- 240000000342 Palaquium gutta Species 0.000 description 1
- 244000273618 Sphenoclea zeylanica Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 101150012763 endA gene Proteins 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229920000588 gutta-percha Polymers 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 229920000136 polysorbate Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 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
- C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
Definitions
- Figure 1 is a sectional view of a portion of the apparatus
- Figure 2 is a sectional view at right angles w to Figure 1;
- Figure 3 is a plan view partly in section and broken away.
- A is a tank having double walls with a iillin of sand a be- 7o tween them and B the electrofte.
- B the electrofte.
- Supported in the tank above the bottom thereof is a frame C preferably of insulating material and having perforations c in its bottom and carrying the diaphragms D.
- E are the elec- @0 trodes of pure nickel on laminated steel heavily covered with nickel, supported on the bottom of the frame.
- the electrodes have hollow stems e which pass through the top of the frame and strips e2 to which the @it electric wires are attached.
- the use of iron does not offer any drawback. It is of course possible to give any shape to the electrolyzer.
- the distance between two electrodes is the same as the space between the member 02 of the frame (15 to 30 mm), the diaphragm 95 which is moulded or otherwise secured in and transversely of the frame being at a distane e substance of which the frame is formed may be for instance gutta-percha, ebonite, cement which may be either pure or mixed with silicious sand, etc.
- the gases which escape from the cells and which are alternately oxygen and hydrogen are gathered at the external part of the apl paratus, tor instance by means of hollow electrode-stems (such for instance as described in my French patent application filed February 8, 1917) or by any other means.
- the electrolyte it arrives no through the holes in the bottom of the treme end is formed for instance by caustic sode at 15%.
- This apparatus offers the following edventages: y
- the foreminous metallic diaphrigm which perfectly Withstands the hi h temperatures (70*85" C.) renders possible the use of e very high strength oi current, so that it is possible-to make the epperctus with a very little Volume.
- the use of electrodes and electrode stems of nickel4 or of metal covered with nickelpreserves the purity of the electrolyte end enables the use of a diephregm with very line apertures so that the gases produced nre very pure, the said purity 'easily attaining more than 99%.
- the diaphragm is preferably of pure nickel (wire-gauze or perforated laminated sheets) or of another metal strongly covered with nickel, though the saidcondition is notV absolutely necessary.
- An apparatus for manufacturing oxygen and hydrogen by electrolysis having nickel electrodes, endA nickel diaphragme perforated to form alfine mesh and separating the electrodes.
- An electrolyzer for manufacturing 0Xygen and hydrogen comprising a tank containing an electrolyte7 nickel electrodes heving tubular stems of the same materiel, a frame supported in the tnnknnd supporting the electrodes and foraminous dinphragms of line mesh and mounted in the frame and separating the electrodes.
Landscapes
- 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
'my w, w22
Q F. .LAMBERT ELECTROLY Filed Avril 4. 1922 m1 5 u2. A T/NG /f//z Tamm armen/5x5 Patented may io, ieee.
I naar' arras GEORGE FRANQOS TAUBEBT, OF PARIS, FRANCE.
EILECTROLYZING APPARATUS FOR THE MANUFACTURE 0F OXYGEN HYDEOGHU.
Application filed April 4, 1922. Serial Ho. 549,602.
To aZZ whom it may concern: v
Be it known that I, GEORGE FRANoIs JAUBERT, a citizen of the Swiss Republic, and residing in Paris, France, 155 Boulevard Malesherbes, have invented certain new and useful Improvements in and Relating to Electrolyzing Apparatus for the Manufacture of Oxygen and Hydrogen, of which the following is a complete specification.
In the electrolyzing apparatus which are to be used for vthe manufacture of oxygen and hydrogen with an alkaline electrolyte and electrodes of cast-iron, iron or steel, it has been proposed, very long ago, to separate the anodic and cathodic compartments by means of a metallic diaphragm such as wire-gauze, or perforated sheets of metal. The said apparatus has given no industrial result.
I have found that the bad results hereto obtained are due to the fact that with the electrodes of cast-iron, iron or steel, a formation of soluble compounds takes places which are decomposed in the course of -the electrolysis and deposit upon the electrodes and stop the apertures of the wire-gauze.
It is consequently absolutely necessary, because of the said stopping, to use a. gauze or a net with rather coarse lmesh and then the pureness of the gas is questionable in such a degree that the said gas cannot be used for industrial purposes.
I have found that when using for all metallic arts which are dipping in the electrolyte Faqueous solution of alkalies either caustic or carbonated) and directly submitted to the action of the electric current, that is to say for the electrodes and electrode stems, an acid proof metal which cannot be bitten or acted upon in the said conditions, it ,is then possible to use as a diaphragm, a wire-gauze or a metallic plate finely perforated without the perforations of said diaphragm becomingobstructed.
If this said metallic diaphragm is constantly maintained immersed in the liquid, (which is necessary) and if the diameter of each aperture in the diaphragm (wire-gauze, perforated plate) is small enough so that the superficial pressure at the surface of separation of both fluids (liquid, gas or emulsion), which are inv the anodic compartment as well as the cathodic one, is stronger than the pressure existing in the said two compartments and constantly tending to provoke .of 7.5 to 15 mm. from the electrodes.
the mining of both gases, then a complete separating is obtained, and both gases 0btamed are at a very high degree of pureness.
In the construction of electrodes, and elece0 trode-stems, it is possible to use for instance either sheets or stems of pure nickel or castiron or laminated sheets of iron or of steel, which are strongly covered with nickel, preferably with a hot process.
ln the drawing is illustratedva practical embodiment of the invention and lin which.:
Figure 1 is a sectional view of a portion of the apparatus;
Figure 2 is a sectional view at right angles w to Figure 1; and,
Figure 3 is a plan view partly in section and broken away.
Referring to the drawing A is a tank having double walls with a iillin of sand a be- 7o tween them and B the electrofte. Supported in the tank above the bottom thereof is a frame C preferably of insulating material and having perforations c in its bottom and carrying the diaphragms D. E are the elec- @0 trodes of pure nickel on laminated steel heavily covered with nickel, supported on the bottom of the frame. The electrodes have hollow stems e which pass through the top of the frame and strips e2 to which the @it electric wires are attached.
For the tank and the other parts of the apparatus which are not-under tension, that is to say which are not submitted tothe ao tion of the electric current, the use of iron does not offer any drawback. It is of course possible to give any shape to the electrolyzer. The distance between two electrodes is the same as the space between the member 02 of the frame (15 to 30 mm), the diaphragm 95 which is moulded or otherwise secured in and transversely of the frame being at a distane e substance of which the frame is formed may be for instance gutta-percha, ebonite, cement which may be either pure or mixed with silicious sand, etc.
The gases which escape from the cells and which are alternately oxygen and hydrogen are gathered at the external part of the apl paratus, tor instance by means of hollow electrode-stems (such for instance as described in my French patent application filed February 8, 1917) or by any other means. As to the electrolyte, it arrives no through the holes in the bottom of the treme end is formed for instance by caustic sode at 15%.
This apparatus offers the following edventages: y
The foreminous metallic diaphrigm which perfectly Withstands the hi h temperatures (70*85" C.) renders possible the use of e very high strength oi current, so that it is possible-to make the epperctus with a very little Volume.
@n the other hand, the use of electrodes and electrode stems of nickel4 or of metal covered with nickelpreserves the purity of the electrolyte end enables the use of a diephregm with very line apertures so that the gases produced nre very pure, the said purity 'easily attaining more than 99%.
The diaphragm is preferably of pure nickel (wire-gauze or perforated laminated sheets) or of another metal strongly covered with nickel, though the saidcondition is notV absolutely necessary.
The neness ofthe mesh of the 'wire gauze Menem sheets or the size of the diameters. of the perforations in the foraminous metal sheets 1. An apparatus for manufacturing oxygen and hydrogen by electrolysis, having nickel electrodes, endA nickel diaphragme perforated to form alfine mesh and separating the electrodes.
2. An electrolyzer for manufacturing 0Xygen and hydrogen comprising a tank containing an electrolyte7 nickel electrodes heving tubular stems of the same materiel, a frame supported in the tnnknnd supporting the electrodes and foraminous dinphragms of line mesh and mounted in the frame and separating the electrodes.
' ln testimony l have hereunto set my hand.
et Peris,l France., this 24th day of March, 1922. d
Geenen rRANois JAUBEirr.`v
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US549602A US1461661A (en) | 1922-04-04 | 1922-04-04 | Electrolyzing apparatus for the manufacture of oxygen and hydrogen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US549602A US1461661A (en) | 1922-04-04 | 1922-04-04 | Electrolyzing apparatus for the manufacture of oxygen and hydrogen |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1461661A true US1461661A (en) | 1923-07-10 |
Family
ID=24193675
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US549602A Expired - Lifetime US1461661A (en) | 1922-04-04 | 1922-04-04 | Electrolyzing apparatus for the manufacture of oxygen and hydrogen |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1461661A (en) |
-
1922
- 1922-04-04 US US549602A patent/US1461661A/en not_active Expired - Lifetime
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