US568231A - Henry blackmaist - Google Patents
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- US568231A US568231A US568231DA US568231A US 568231 A US568231 A US 568231A US 568231D A US568231D A US 568231DA US 568231 A US568231 A US 568231A
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- anode
- electrolytic
- electrolyte
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- oxid
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- 239000003792 electrolyte Substances 0.000 description 28
- SZVJSHCCFOBDDC-UHFFFAOYSA-N Iron(II,III) oxide Chemical compound O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 22
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 16
- 229910052799 carbon Inorganic materials 0.000 description 16
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 14
- 238000005868 electrolysis reaction Methods 0.000 description 12
- YDZQQRWRVYGNER-UHFFFAOYSA-N iron;titanium;trihydrate Chemical compound O.O.O.[Ti].[Fe] YDZQQRWRVYGNER-UHFFFAOYSA-N 0.000 description 12
- 239000000243 solution Substances 0.000 description 12
- 238000004061 bleaching Methods 0.000 description 10
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 10
- 239000007864 aqueous solution Substances 0.000 description 8
- 238000000354 decomposition reaction Methods 0.000 description 8
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical compound [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 8
- 239000004020 conductor Substances 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- WGSLWEXCQQBACX-UHFFFAOYSA-N Chlorin Chemical compound C=1C(C=C2)=NC2=CC(C=C2)=NC2=CC(C=C2)=NC2=CC2=NC=1CC2 WGSLWEXCQQBACX-UHFFFAOYSA-N 0.000 description 4
- SUKJFIGYRHOWBL-UHFFFAOYSA-N Sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 4
- 125000004429 atoms Chemical group 0.000 description 4
- 239000012267 brine Substances 0.000 description 4
- 235000012970 cakes Nutrition 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 230000004907 flux Effects 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 235000010755 mineral Nutrition 0.000 description 4
- 229910052697 platinum Inorganic materials 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- 239000011780 sodium chloride Substances 0.000 description 4
- 235000011121 sodium hydroxide Nutrition 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 229910005438 FeTi Inorganic materials 0.000 description 2
- 229910005451 FeTiO3 Inorganic materials 0.000 description 2
- 229920001131 Pulp (paper) Polymers 0.000 description 2
- 239000005708 Sodium hypochlorite Substances 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 239000007844 bleaching agent Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 150000004035 chlorins Chemical class 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000002845 discoloration Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- KEHCHOCBAJSEKS-UHFFFAOYSA-N iron(2+);oxygen(2-);titanium(4+) Chemical compound [O-2].[O-2].[O-2].[Ti+4].[Fe+2] KEHCHOCBAJSEKS-UHFFFAOYSA-N 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000615 nonconductor Substances 0.000 description 2
- 230000001590 oxidative Effects 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
Images
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/1021—Electrochemical processes
-
- 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
- C25B1/34—Simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine, e.g. by chlor-alkali electrolysis
-
- 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
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/12—Bleaching ; Apparatus therefor with halogens or halogen-containing compounds
Definitions
- This invention relates to anodes for electrolytic decompositions, of which the electrolysis of sodium chlorid is a type.
- Sodium chlorid may be electrolyzed inthe form of an aqueous solution or brine or when liquefied by fusion. ⁇
- chlorin is liberated at the anode and sodium at the cathode.
- an aqueous solution the sodium decomposes water and unites with the oxygen and one atom of hydrogen to form sodium hydroxid or caustic soda, and the other atom of hydrogen is set free.
- chlorin and caustic soda these two products are kept separated after their fformation in the electrolytic cell.
- Plates of prepared peroxid of lead have also been used, but are very expensive of preparation, are very imperfect conductors, and are excessively heavy.
- the desirable properties for an electrolytic anode for such uses are, first, that it shall be unacted upon by the electrolyte or the products of electrolysis; second, that it shall be a good electric conductor; third, that it shall be reasonably cheap, and, fourth, that it shall not be so heavy as to render the necessary handling of the plates burdensome.
- the object of my present invention is to provide means for effecting such electrolytic iron.
- the requireddecomposition is effected by passing a ⁇ liberated at the anode, that is, the electronegative products of such electrolysis.
- Mag- .n'etic iron oxid or magnetite (Fe304) and iron titanium oxid or ilmenite, the formula for which is given by Vatts as FeTiO3 and by Roscoe and Schorlemmer as (FeTi)2O3, are examples of mag- .n'etic iron oxid or magnetite (Fe304) and iron titanium oxid or ilmenite, the formula for which is given by Vatts as FeTiO3 and by Roscoe and Schorlemmer as (FeTi)2O3, are
- electrolytic bleaching as ordinarily practiced, that is, by electrolyzing brine, using carbon as the anode, it is found that even with the most refractory carbon there is a continual disintegration of the carbon, disengaging in the resulting bleaching solution fine particles or specks of carbon, which it has been found almost impossible to remove by filtration or otherwise, so that when the solution is employed for bleaching paperpulp, for example, the pulp is found to be slightly discolored by the minute specks of carbon which are deposited upon it. Vith an anode of magnetite or ilmenite instead of carbon the specking or discoloration of the solution is reduced to such an extent as to be practically insignificant.
- Figure 1 is a vertical section of an electrolytic cell B, with an anode A, of magnetite,
- Fig. 2 is a seetion of an electrolytic cell B, of metal, and connected in the circuit, so that its inner surface C serves as the cathode and an anode A of ilmenite.
- My invention may be used with an electrolyte consisting of an aqueous solution of a chlorid or other salt or compound to be decomposed.
- Fig. l may be understood as showing such a solution.
- My invention is also applicable with molten or fused electrolytes, such as fused sodium chlorid.
- the electrolyte maybe fused by heat externally applied to the cell or receptacle, this being shown in Fig. 2, where a Bunsen burner CZ is arranged beneath the cell to direct its iiame e against it; or the electrolyte may be fused or kept fused by electric heat in case it oifers sufficient resistance to the passage of the current through it to generate sufficient heat to keep it fu sed. In this Acase the burner d may be omitted from Fig. 2.
- the iron or analogous oXids may be used in the form in which they occur as minerals by sawing, chipping, or otherwise shaping the mineral into a slab, cylinder, or other desired shape; or it is within myinvention to east the oxid into the desired shape for the electrode by adding to it a sufficient proportion of suitable fluxing agents, such as silica, liine,.and magnesia, to enable it to be fused and caused to flow, but such fluxes, being non-conductors, should not be in such large proportion as to materially impair the electric conductivity of the electrode.
- suitable fluxing agents such as silica, liine,.and magnesia
- My invention may be modified by mixing or fusing together the magnetite and ilmenite, either with or without other materials or substances, such as fluxing agents.
- My invention may be further modified by pulverizing the oxid and eompacting it into a cake, slab, or other form by heavy pressure or by the use of any binding material, such,
- the binding agent in any such case being preferably so insignificant in pro portion that if subject to disintegration it cannot seriously discolor the electrolyte.
- My invention is not limited to the anode being homogeneous throughout, as the portions of the anode which are not in contact with the electrolyte might be of other materials than those essential to my invention if found advantageous.
- the anode an iron plate heavily covered or coated with a dense impermeable layer of such an electroconductive oXid as is essential to my invention wherever the anode comes in contact with the electrolyte.
- An anode for use in electrolytie decomposition consisting of eleetroconduetive oXid of iron in a dense impermeable mass, substantially as set forth.
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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)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
PATENT A@GFF.F.ICE
HENRY B LAOKMAN, pr NunT YORK, N. Y.
ELECTROLYTIC ANODE AND APPARATUS.
SPECIFICATION forming part of Letters Patent No. 568,231, dated. September 22, 189e Application fueainy 21,1895. sentano. 550,104. (Nomad.)
T all whom, it may concern,.-
Be it known that I, HENRY BLACKMAN, a citizen of the United States, residing in the city, county, and State of New York, have invented certain new and useful Improvements in Electrolytic Anodes and Apparatus, of which the following is a specification.
This invention relates to anodes for electrolytic decompositions, of which the electrolysis of sodium chlorid is a type. Sodium chlorid may be electrolyzed inthe form of an aqueous solution or brine or when liquefied by fusion.` In either case chlorin is liberated at the anode and sodium at the cathode. In the case of an aqueous solution the sodium decomposes water and unites with the oxygen and one atom of hydrogen to form sodium hydroxid or caustic soda, and the other atom of hydrogen is set free. For the manufacture of chlorin and caustic soda these two products are kept separated after their fformation in the electrolytic cell. For the manufacture of electric bleach, so called, no separation is effected, and a reaction occurs whereby sodium hypochlorite (NaClO) is formed, which has important bleaching properties. In such electrolytic decompositions much difficulty has been experienced by reason of the rapid destruction of the anode during the electrolytic action. The substances with which most success has been attained are refractory-retort carbon and platinum. The carbon, however, has the disadvantage of disintegrating and disengaging particles or specks in the electrolyte, which greatly impairs it, particularly in the case of bleaching solutions. Platinum plates are excessively expensive and in course of time become corroded or dissolved by the electrolytic action. Plates of prepared peroxid of lead have also been used, but are very expensive of preparation, are very imperfect conductors, and are excessively heavy. The desirable properties for an electrolytic anode for such uses are, first, that it shall be unacted upon by the electrolyte or the products of electrolysis; second, that it shall be a good electric conductor; third, that it shall be reasonably cheap, and, fourth, that it shall not be so heavy as to render the necessary handling of the plates burdensome.
The object of my present invention is to provide means for effecting such electrolytic iron.
'the less they are affected.
decompositions without encountering the disadvantages heretofore experienced.
In accordance with my invention the requireddecomposition is effected by passing a `liberated at the anode, that is, the electronegative products of such electrolysis. Mag- .n'etic iron oxid or magnetite (Fe304) and iron titanium oxid or ilmenite, the formula for which is given by Vatts as FeTiO3 and by Roscoe and Schorlemmer as (FeTi)2O3, are
examples of such electroconductive oxids of These oxids are almost wholly unacted upon during the 'electrolysis of an aqueous solution of sodium chloride. They have the advantage of being good conductors and when used as the anodedo not speck or discolor the electrolyte and have great durability against corrosion or disintegration by the electrolytic action. In this respect my experiencewith them indicates that the longer they are used They also have the advantage that their specific gravity is not great, so that electrodes made from them .are not inconveniently heavy to handle. They are also very cheap.
In electrolytic bleaching as ordinarily practiced, that is, by electrolyzing brine, using carbon as the anode, it is found that even with the most refractory carbon there is a continual disintegration of the carbon, disengaging in the resulting bleaching solution fine particles or specks of carbon, which it has been found almost impossible to remove by filtration or otherwise, so that when the solution is employed for bleaching paperpulp, for example, the pulp is found to be slightly discolored by the minute specks of carbon which are deposited upon it. Vith an anode of magnetite or ilmenite instead of carbon the specking or discoloration of the solution is reduced to such an extent as to be practically insignificant.
The accompanying drawings illustrate two forms of electrolytic apparatus embodying my invention.
Figure 1 is a vertical section of an electrolytic cell B, with an anode A, of magnetite,
IOO
l i l.
and a cathode C, of any suitable material, adapted to withstand the action of the electrolyte during electrolysis. Fig. 2 is a seetion of an electrolytic cell B, of metal, and connected in the circuit, so that its inner surface C serves as the cathode and an anode A of ilmenite.
My invention may be used with an electrolyte consisting of an aqueous solution of a chlorid or other salt or compound to be decomposed. Fig. l may be understood as showing such a solution.
My invention is also applicable with molten or fused electrolytes, such as fused sodium chlorid. The electrolyte maybe fused by heat externally applied to the cell or receptacle, this being shown in Fig. 2, where a Bunsen burner CZ is arranged beneath the cell to direct its iiame e against it; or the electrolyte may be fused or kept fused by electric heat in case it oifers sufficient resistance to the passage of the current through it to generate sufficient heat to keep it fu sed. In this Acase the burner d may be omitted from Fig. 2.
The iron or analogous oXids (as magnetite or ilmenite) may be used in the form in which they occur as minerals by sawing, chipping, or otherwise shaping the mineral into a slab, cylinder, or other desired shape; or it is within myinvention to east the oxid into the desired shape for the electrode by adding to it a sufficient proportion of suitable fluxing agents, such as silica, liine,.and magnesia, to enable it to be fused and caused to flow, but such fluxes, being non-conductors, should not be in such large proportion as to materially impair the electric conductivity of the electrode. An electrode of such composition of magnetic iron oXid and a flux is claimed in my application, Serial No. 537,805, filed February 9, 1895. An electrode of ilmenite is claimed in my application, Serial No. 5lS,722, filed May 9, 1895.
My invention may be modified by mixing or fusing together the magnetite and ilmenite, either with or without other materials or substances, such as fluxing agents.
My invention may be further modified by pulverizing the oxid and eompacting it into a cake, slab, or other form by heavy pressure or by the use of any binding material, such,
for example, as tar or sugar, and then pressing it into the desired form by heavy pressure and afterward drying or baking the resulting cake, the binding agent in any such case being preferably so insignificant in pro portion that if subject to disintegration it cannot seriously discolor the electrolyte.
I do not wish to be understood as limiting my invention in its application solely to the electrolysis of'chlorin compounds, as it may be equally applicable with other compounds or solutions as the electrolyte, being especially advantageous in any case where the eleetrolytic process develops a powerful oxidizing action at the anode.
My invention is not limited to the anode being homogeneous throughout, as the portions of the anode which are not in contact with the electrolyte might be of other materials than those essential to my invention if found advantageous. For example, it might be found practicable to employ as the anode an iron plate heavily covered or coated with a dense impermeable layer of such an electroconductive oXid as is essential to my invention wherever the anode comes in contact with the electrolyte.
I claim as my invention the following-de fined novel features, substantially as hereinbefore specified, namely: v
1. An anode for use in electrolytie decomposition consisting of eleetroconduetive oXid of iron in a dense impermeable mass, substantially as set forth.
2. The combination in an electrolytic apparatus, with an extraneous source of electric current, of a receptacle for the electrolyte, a cathode, and an anode the exposed surface of which is 'a dense impermeable electroconduetive iron oxid, substantially as specified.
The combination in an electrolytic apparatus, with a receptacle for the electrolyte and a cathode, of an anode consisting of dense impermeable magnetic iron oXid.
In witness whereof I have hereunto signed my name in the presence of two subscribing witnesses.
HENRY BLACKMAN. lVitnesses:
vARTHUR C. FRAsnR,
Lucius PITKIN.
Publications (1)
Publication Number | Publication Date |
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US568231A true US568231A (en) | 1896-09-22 |
Family
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Family Applications (1)
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US568231D Expired - Lifetime US568231A (en) | Henry blackmaist |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3071532A (en) * | 1959-12-07 | 1963-01-01 | Ciba Ltd | Cells for the electrolysis of fused salts |
US3203881A (en) * | 1952-07-16 | 1965-08-31 | British Titan Products | Production of metallic halides |
US6712952B1 (en) * | 1998-06-05 | 2004-03-30 | Cambridge Univ. Technical Services, Ltd. | Removal of substances from metal and semi-metal compounds |
-
0
- US US568231D patent/US568231A/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3203881A (en) * | 1952-07-16 | 1965-08-31 | British Titan Products | Production of metallic halides |
US3203880A (en) * | 1952-07-16 | 1965-08-31 | British Titan Products | Electrolytic production of titanium tetrahalides |
US3071532A (en) * | 1959-12-07 | 1963-01-01 | Ciba Ltd | Cells for the electrolysis of fused salts |
US6712952B1 (en) * | 1998-06-05 | 2004-03-30 | Cambridge Univ. Technical Services, Ltd. | Removal of substances from metal and semi-metal compounds |
US20040159559A1 (en) * | 1998-06-05 | 2004-08-19 | Fray Derek John | Removal of oxygen from metal oxides and solid solutions by electrolysis in a fused salt |
US7790014B2 (en) | 1998-06-05 | 2010-09-07 | Metalysis Limited | Removal of substances from metal and semi-metal compounds |
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