US1837050A - Colloidal diaphragm adapted for use in electrolytic apparatus for the manufacture ofhydrogen and oxygen - Google Patents
Colloidal diaphragm adapted for use in electrolytic apparatus for the manufacture ofhydrogen and oxygen Download PDFInfo
- Publication number
- US1837050A US1837050A US235118A US23511827A US1837050A US 1837050 A US1837050 A US 1837050A US 235118 A US235118 A US 235118A US 23511827 A US23511827 A US 23511827A US 1837050 A US1837050 A US 1837050A
- Authority
- US
- United States
- Prior art keywords
- diaphragm
- electrolyte
- colloidal
- oxygen
- manufacture
- 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 8
- 239000001301 oxygen Substances 0.000 title description 8
- 229910052760 oxygen Inorganic materials 0.000 title description 8
- 238000004519 manufacturing process Methods 0.000 title description 7
- 239000003792 electrolyte Substances 0.000 description 18
- 239000000017 hydrogel Substances 0.000 description 13
- 239000000084 colloidal system Substances 0.000 description 10
- 239000007789 gas Substances 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 8
- 239000002184 metal Substances 0.000 description 8
- 239000001257 hydrogen Substances 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical class [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 6
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 238000005868 electrolysis reaction Methods 0.000 description 4
- 239000008151 electrolyte solution Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000012670 alkaline solution Substances 0.000 description 3
- 239000010425 asbestos Substances 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 239000000395 magnesium oxide Substances 0.000 description 3
- 229910052895 riebeckite Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 150000004677 hydrates Chemical class 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 244000286663 Ficus elastica Species 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 230000003190 augmentative effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- -1 copper and nickel Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- YOBAEOGBNPPUQV-UHFFFAOYSA-N iron;trihydrate Chemical compound O.O.O.[Fe].[Fe] YOBAEOGBNPPUQV-UHFFFAOYSA-N 0.000 description 1
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L magnesium chloride Substances [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 1
- 239000000391 magnesium silicate Substances 0.000 description 1
- 229910052919 magnesium silicate Inorganic materials 0.000 description 1
- 235000019792 magnesium silicate Nutrition 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229920001195 polyisoprene Polymers 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 235000011181 potassium carbonates Nutrition 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
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
- C25B13/00—Diaphragms; Spacing elements
- C25B13/04—Diaphragms; Spacing elements characterised by the material
- C25B13/05—Diaphragms; Spacing elements characterised by the material based on inorganic materials
- C25B13/06—Diaphragms; Spacing elements characterised by the material based on inorganic materials based on asbestos
Definitions
- hydrogel refers. to all organic or inorganic bodies in a state of fine suspension in water or in an electrolyte or other solvent, the size of its parti les being between 1/ 1,000 and 1/ 1,000,000 millimeters diameter, which suspended particlw have the property of being transportable in the electric field by the action of the current.
- the said colloidal diaphragm according to my invention can be variously manufactured as follows.
- the imperfect diaphragm such as steef wire gauze N o. 30 to 50, is coated by a spatula with a hydrogel paste already prepared, for instance according to the list given below.
- hydrogel is formed'in the holes of the diaphragm, i. e. the preparation is carried out in situ. Considering for example the wire gauze above mentioned, this is immer'sed in a soluble salt which is dissolved to the proper strength, and then without drying the diaphragm thus'moistened (each l mersed in a solution of another substance,
- 3.'-I may proceed in the following manner, making use of the fact that the colloidal substances will serve as electrolytes, taking part in the phenomenon of electrolysis and moving in the electric field.
- hydrogels whether or nic or inorganic these being given sole y by way of example and without limitation-silicates of magnesia, silicates of iron, the kaolins, the ferric hydrates, yellow ochre natural or artificial, the limonites, the clays, hosphates of magnesia and of alumina car on in the form of raphite, carbon from blood, india rubber, t e hydrates ofthe alkaline earths or those ofthe series of rare earths, the flocculent metals such as copper and nickel, and the like.
- colloid impervious to an attack by alkaline solution or alkali is made in the specification andclaims, it is intended to include any of the above substances.
- the electrolyte consists of a solution of sodium or potassium carbonate
- My said diaphragm according to the invention may be employed equally well with electrolytic apparatus of the tank type utilizing a diaphragm, or with electrolytic apparatus of the plate type represented by filter presses.
- My said method is advantageous for these latter, as I may employ if necessary a very inferior grade of asbestos cloth, with a consequent reduction in cost, whereas such material could not be used in the absence of the said layer of colloidal hydrogel.
- a process for the manufacture of diaphragms for electrolytic cells which comprises passing a current through an electrolyte containing a colloid impervious to an alkaline solution and depositing the colloid on a metal diaphragm during the electrolysis of the electrolyte while fixing the colloid on said metal diaphragm and maintaining the fiow of the current through the electrolyte.
- a process for the manufacture of diaphragms for electrolytic cells which are permeable to the electrolyte but impermeable to the gaseous products evolved by the electrolysis which comprises forming a metal diaphragm, surrounding the diaphragm with an electrolyte solution containing a colloid impervious to attack by the electrolyte solution, passing an electric current through the electrolyte and causing disassociation of the elements of the electrolyte while causing the colloid to be deposited on the diaphragm so that hydrogen and oxygen which are bein evolved from the electrolyte will be separate from each other when the colloid has completelX covered the diaphragm.
- process for the manufacture of diaphragms for electrolytic cells which are permeable to the electrolyte but impermeable to the gaseous products evolved by the electrolysis which comprises forming a metal diaphragm, surrounding the diaphragm with an electrolyte solution containing a colloid impervious to attack by the electrolyte solution, passing an electric current through the electrolyte and causing disassociation of the elements of the electrolyte while causing the.
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)
Description
Patented Dec. 15, 1931 UNITED STATES- PATENT OFFICE- GEORGE FRANCOIS J'AUBEBT, OF PARIS, FRANCE COLLOIDAL DIAPHRAGM ADAPTED FOR USE IN ELECTROLYTIC APPARATUS FOR THE IANUEACTURE OF HYDROGEN .AND OXYGEN No Drawing. Application filed November 22,1927, Serial No. 235,118, and in France December 1, 1926 I have already shown that it was feasible to employ as a diaphragm for the perfect separation of oxygen and hydro en gas at the time of their formation in tie electrolytic tank, a wire gauze member, a woven fabric, for instance of asbestos, or perforated sheet metal, but on the express condition that the cross-section of each of the innumerable orifices in this diaphragm shall be so small that the surface tension of the liquid contained in each of the minute orifices and formingthesurface of separation between the two fluids (such as liquid, gas or emulsion), contained in the anode and the cathode chambers, shall exceed the counter-pressure prevailing respectively in these two chambers, Which counter-pressure tends constantly to cause the mixing of the oxygen and hydrogen gases, thus forming a dangerous explosive 2o mixture.
If the above-mentioned conditions are strictly observed, a complete separation will be effected, and the oxygen and hydrogen.
gases will each be obtained in a very pure state. i
However, the manufacture of wire gauze, fabrics, or erforated sheet metal, having the necessary egree of fineness to comply with the said conditions, becomes a most expensive matter. In fact, when the holes are of a small size, their number will increase for a given surface, and the cost of manufacture is thus augmented.
A great advantage, and a considerable progress in manufacture, would be obtained by the use of sheet steel having larger holes, or of wire gauze sheets of the current sizes which are found in the market and inwhich the holes are much lar er than what theory prescribes. This would offer a great saving in cost, and would represent a considerable improvement in my said above process. It was however necessary to means for revent-ing the anode and the'cathode gases rom passing through these larger holes.
I have obtained this result by means of a colloidal diaphragm, the sub ect matter of the present invention, which diaphragm is so to speak superposed upon the diaphragm mentioned hereabove.
- I have observed that by the use of a diaphragm' consisting of perforated sheet metal or wire gauze, or even of a strong textile fabric, whose holes are too large to assure a sufficient separation between the anode and the cathode gases in the nascent state, it is simply necessary to coat this diaphragm with the hydrogel of a colloidal substance'which is unafi'ected by the electrolyte in the conditions of the operation, in order to-obtain at once a perfect separation of the gases, and without any appreciable reduction of the electric efficiency of the apparatus.
The term hydrogel refers. to all organic or inorganic bodies in a state of fine suspension in water or in an electrolyte or other solvent, the size of its parti les being between 1/ 1,000 and 1/ 1,000,000 millimeters diameter, which suspended particlw have the property of being transportable in the electric field by the action of the current.
The said colloidal diaphragm according to my invention can be variously manufactured as follows.
L The imperfect diaphragm, such as steef wire gauze N o. 30 to 50, is coated by a spatula with a hydrogel paste already prepared, for instance according to the list given below.
2.-The hydrogel is formed'in the holes of the diaphragm, i. e. the preparation is carried out in situ. Considering for example the wire gauze above mentioned, this is immer'sed in a soluble salt which is dissolved to the proper strength, and then without drying the diaphragm thus'moistened (each l mersed in a solution of another substance,
thus forming the hydrogel by double decomposition or coagulation, or the like.
As an example, I immerse a wire gauze sheet in an aqueous solution of magnesium sulphate or chloride, and then in an aqueuos solution of silicate of soda. There is at once formed in the holes of the wire gauze a hydrogel of magnesium silicate, otherwise known as colloidal asbestos, which is ex tremely porous and forms an excellent diaphra m, thus assuring the perfect separation etween the hydrogen and oxygen.
3.'-I may proceed in the following manner, making use of the fact that the colloidal substances will serve as electrolytes, taking part in the phenomenon of electrolysis and moving in the electric field.
For this purpose I place in an electrolytic tank of any type, the two electrodes, positive and negative, which are separated by an imperfect diaphragm, such as a No. 3050 steel wire gauze sheet. I then add the electrolytic bath (an aqueous solution of caustic soda or potash of 15 to 20 percent strength) holding in suspension the suitable hydrogel which ma be organic or inorganic, all that is require being thatit will be transported by the current, which gradually fixes it upon the diaphragm by an action of adsorption. It is obvious that this hydrogen must not be attacked by the electrolyteto any great degree, in the conditions of temperature and concentration in which the operation is performed with the said electrolyte consisting of water represented by the alkaline solution.
The best results are furnished by the following hydrogels whether or nic or inorganic, these being given sole y by way of example and without limitation-silicates of magnesia, silicates of iron, the kaolins, the ferric hydrates, yellow ochre natural or artificial, the limonites, the clays, hosphates of magnesia and of alumina car on in the form of raphite, carbon from blood, india rubber, t e hydrates ofthe alkaline earths or those ofthe series of rare earths, the flocculent metals such as copper and nickel, and the like. Wherever the use of the phrase colloid impervious to an attack by alkaline solution or alkali, is made in the specification andclaims, it is intended to include any of the above substances.
If the electrolyte consists of a solution of sodium or potassium carbonate, I obtain a good dia hragm b the use of a hydrogel of hydrocar onate of magnesia.
'The quantities of the said hydrogels to be added to the electrolyte are small, as a general rule. When the apparatus is put in operation, I add a quantity which is about 5 to 10 per cent-estimated as dry substancefor each liter of electrolyte.
. As soon as the hydrogel is fixed by electric transportation into the holes of the wire gauze in which it forms a gelatinous spongy substance pierced with extremely fine holes, the bath becomes clearer, due to the absence of the amount of the said substance which has been fixed upon the diaphragm, and-the gases are then perfectly pure.
I add at intervals a certain quantity of hydrogel, in case the portion fixed on the wire gauze should be accidentally detached, and shrogld fall to the bottom of the electrolytic ta' Should the electrolytic apparatus be taken apart, or its use discontinued for a long time, the diaphragm should not be dried, since it would lose its effectiveness; it should be simply washed with water to remove the eyectrolyte, and is then dipped in a 50 per cent glycerine solution and allowed to drain.
Obviously, the three methods of preparation herein specified by way of example may be combined together, or like methods may be devised with equal facility.
My said diaphragm according to the invention may be employed equally well with electrolytic apparatus of the tank type utilizing a diaphragm, or with electrolytic apparatus of the plate type represented by filter presses. My said method is advantageous for these latter, as I may employ if necessary a very inferior grade of asbestos cloth, with a consequent reduction in cost, whereas such material could not be used in the absence of the said layer of colloidal hydrogel. I
What I claim is 1. A process for the manufacture of diaphragms for electrolytic cells which comprises passing a current through an electrolyte containing a colloid impervious to an alkaline solution and depositing the colloid on a metal diaphragm during the electrolysis of the electrolyte while fixing the colloid on said metal diaphragm and maintaining the fiow of the current through the electrolyte.
2. A process for the manufacture of diaphragms for electrolytic cells which are permeable to the electrolyte but impermeable to the gaseous products evolved by the electrolysis which comprises forming a metal diaphragm, surrounding the diaphragm with an electrolyte solution containing a colloid impervious to attack by the electrolyte solution, passing an electric current through the electrolyte and causing disassociation of the elements of the electrolyte while causing the colloid to be deposited on the diaphragm so that hydrogen and oxygen which are bein evolved from the electrolyte will be separate from each other when the colloid has completelX covered the diaphragm.
3. process for the manufacture of diaphragms for electrolytic cells which are permeable to the electrolyte but impermeable to the gaseous products evolved by the electrolysis which comprises forming a metal diaphragm, surrounding the diaphragm with an electrolyte solution containing a colloid impervious to attack by the electrolyte solution, passing an electric current through the electrolyte and causing disassociation of the elements of the electrolyte while causing the.
colloid to be deposited on the diaphra so that hydrogen and oxygen which are a ing evolved from the electrolyte will beseparated from each other when the colloid has completely covered the diaphragm,
In testimony whereof I have hereunto set my hand.
GEORGE FRANCOIS JAUBERT.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR638346T | 1926-12-01 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1837050A true US1837050A (en) | 1931-12-15 |
Family
ID=8995928
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US235118A Expired - Lifetime US1837050A (en) | 1926-12-01 | 1927-11-22 | Colloidal diaphragm adapted for use in electrolytic apparatus for the manufacture ofhydrogen and oxygen |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US1837050A (en) |
| FR (1) | FR638346A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2872388A (en) * | 1954-07-30 | 1959-02-03 | Fahnoe Frederick | Nuclear fuel elements and methods for making same |
| US2938839A (en) * | 1954-07-30 | 1960-05-31 | Vitro Corp Of America | Uranium dioxide impregnated compacts and method for making same |
-
1926
- 1926-12-01 FR FR638346D patent/FR638346A/en not_active Expired
-
1927
- 1927-11-22 US US235118A patent/US1837050A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2872388A (en) * | 1954-07-30 | 1959-02-03 | Fahnoe Frederick | Nuclear fuel elements and methods for making same |
| US2938839A (en) * | 1954-07-30 | 1960-05-31 | Vitro Corp Of America | Uranium dioxide impregnated compacts and method for making same |
Also Published As
| Publication number | Publication date |
|---|---|
| FR638346A (en) | 1928-05-22 |
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