US1897308A - Apparatus for electrolysis of a fused bath - Google Patents
Apparatus for electrolysis of a fused bath Download PDFInfo
- Publication number
- US1897308A US1897308A US367494A US36749429A US1897308A US 1897308 A US1897308 A US 1897308A US 367494 A US367494 A US 367494A US 36749429 A US36749429 A US 36749429A US 1897308 A US1897308 A US 1897308A
- Authority
- US
- United States
- Prior art keywords
- curtain
- bath
- anode
- electrolysis
- cell
- 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
- 238000005868 electrolysis reaction Methods 0.000 title description 8
- 229910052751 metal Inorganic materials 0.000 description 15
- 239000002184 metal Substances 0.000 description 15
- 229910010293 ceramic material Inorganic materials 0.000 description 5
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- 229910001208 Crucible steel Inorganic materials 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
- C25C7/005—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells of cells for the electrolysis of melts
Definitions
- the present invention relates to means for separating anodic and cathodic products produced by electrolysis and has particular reference to the separation of such roducts derived from the electrolysis of used baths. It relates specifically to means for separating metallic magnesium floating upon the fused, bath from which it has been liberated and the chlorine constituting the anode product.
- FIG. 1 is a partial vertical cross-section through a typical fused bath cell employing my curtain.
- Fig. 2 is a similar cross-section at right angles to that in Fig. 1.
- Fig. 3 is a top plan
- Fig. 4 a vertical longitudinal crosssection of one form of curtain
- Fig. 5 is a vertical section at right angles to that of Fig. 4.
- I Fig. 6 is a plan similar to Fig. 3 of 1929. Serial No. 367,494.
- the curtain proper consists essentially of a suitable tubular sleeve which may be slipped over the anode or through which the anode may be assed when it is lowered into the cell bath.
- a suitable tubular sleeve which may be slipped over the anode or through which the anode may be assed when it is lowered into the cell bath.
- a sleeve which in Figs. 3, 4 and 5 is is somewhat rectangular in cross-section as shown in the plan, Fig. 3.
- the sleeve has rounded corners and is preferably provided with a flange 2 suited to engage with fixed members in the cell for the purpose of supporting the curtain in position.
- the curtain has a round or tubular form.
- Other forms may be employed in which the sleeve may have a corrugated or other contour and themanner of support may be varied.
- FIGs. 1 and 2 represent the cathode cell pot which may be of cast steel or other suitable metal.
- a single anode or a plurality thereof, 4 depend into the bath from above.
- Such anodes will preferably be carried .by adjust-. able hangers enablng their easy removal in a vertical direction and relowering into the cell for the purpose of adjusting the submergence and for incidentally permitting the removal and replacement of the curtains.
- the pot 3 is provided with an inverted trough 5 adapted to form a trap for the liberated metal 6 risin from the cathbde pot.
- the pot 3 will pre erably be supported, as indicated, in a furnace for supplying initial heat or controlling the temperature during operation. Suitable electrical connections indcated at 7 and 8 will be provided to supply current for the electrolysis.
- the light metal caughtin the traps 5 will preferably be led by said traps to a suitable collecting well or zone, not shown, enabling the later removal of the metal with case.
- Fig. 2 three anodes of a series, which may contain any convenient number, are shown depending in the bath from above, each being surrounded by a curtain 1. These curtains are shown in Fig.
- the curtain will preferably be made of a suitable quality of fire clay or other ceramic material adapted to withstand the conditions of exposure to bath and metallic magnesium in the molten state, some of which latter may beliberated upon the inner face of the trap 5 facing the curtain. I find it best that there be a substantial clearance between such curtain and metal parts 10f the cell to avoid unnecessar contact of liberated metal, there entangle with the curtain.
- Another object of the curtain is to cover the exposed surface of the trap 5 or other cathodic surface from which metal liberated thereon would not directly enter the trap. Such covering restricts the liberation of metal on the protected surface and to an equal extent prevents losses there- It will be seen that the curtain afi'ords a partition between that part of thebath occupied by the anode through which the chlorine or other anodic product rises and that part of the bath in which the cathodic metal is produced and collected. Cover slabs 9 may be provided and a duct 12 connected therewith for drawing ofi' the gaseous anodic products, such as chlorine gas and the like.
- suflicient suction will preferably have been provided at the outlet 12 to prevent issue of gas into the room, there being preferably a draft of air drawn into the compartment 11 to wash out the gas therein.
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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 Metals (AREA)
Description
Feb. 14, 1933. R M HUNTER 1,897,308
APPARATUS FOR ELECTROLYSIS OF A FUSED BATH Filed May 51, 1929 [NVENTOR BY W m. A um/$4,
Patented Feb. 14, 1933 UNITED STATES PATENT OFFICE RALPH I. HUNTER, 0F MIDLAND, MICHIGAN, ASSIGNOR TO THE DOW CHEMICAL COMPANY, OF MIDLAND, MICHIGAN, A CORPOFATION OFMIGHIGAN APPARATUS FOR ELECTROLYSIS OF A FUSED BATE Application filed May 31,-
The present invention relates to means for separating anodic and cathodic products produced by electrolysis and has particular reference to the separation of such roducts derived from the electrolysis of used baths. It relates specifically to means for separating metallic magnesium floating upon the fused, bath from which it has been liberated and the chlorine constituting the anode product.
When operating an electrolytic cell employing a fused bath upon which the liberated metal will float, both cathodic metal and anodic gas rise to the surface of the bath and the separation and separate disposal thereof becomes a problem. Due to the high temperature, the requirement for non-conductivity of electric current and the chemical activity to which a curtain or other means of separation must be subjected, the choice of material therefor and form thereof has required much study and experiment. The difiiculties, moreover, incident to cells ofsmall capacity are greatly magnified when it is attempted to operate large cells.
I have invented a form of curtain applicable to any and all sizes of cells employing one or more anodes, which said curtain may be withdrawn and a new one inserted without interrupting operations when a plurality of anodes are used. Other advantages will appear as the description proceeds.
To the accomplishment of the foregoing and related ends, the invention, then, consists of the means hereinafter fully described and particularly pointed out in the claims, the annexed drawing and the following description setting forth in detail certain means for carrying out the invention, such disclosed means illustrating, however, but two of various ways in which the principle ofthe invention may be used.
In said annexed drawing Fig. 1 is a partial vertical cross-section through a typical fused bath cell employing my curtain. Fig. 2 is a similar cross-section at right angles to that in Fig. 1. Fig. 3 is a top plan, Fig. 4 a vertical longitudinal crosssection of one form of curtain, and Fig. 5 is a vertical section at right angles to that of Fig. 4. I Fig. 6 is a plan similar to Fig. 3 of 1929. Serial No. 367,494.
an alternative form of curtain, the other views of which would be similar to Figs. 4 and 5.
The curtain proper consists essentially of a suitable tubular sleeve which may be slipped over the anode or through which the anode may be assed when it is lowered into the cell bath. eferring to Figs. 3, 4, 5 and 6,1 is a sleeve, which in Figs. 3, 4 and 5 is is somewhat rectangular in cross-section as shown in the plan, Fig. 3. The sleeve has rounded corners and is preferably provided with a flange 2 suited to engage with fixed members in the cell for the purpose of supporting the curtain in position. In Fig. 6 the curtain has a round or tubular form. Other forms may be employed in which the sleeve may have a corrugated or other contour and themanner of support may be varied. v
The application of my curtain to a cell will be explained by referring to Figs. 1 and 2, in which 3 represents the cathode cell pot which may be of cast steel or other suitable metal. A single anode or a plurality thereof, 4, depend into the bath from above. Such anodes will preferably be carried .by adjust-. able hangers enablng their easy removal in a vertical direction and relowering into the cell for the purpose of adjusting the submergence and for incidentally permitting the removal and replacement of the curtains. The pot 3 is provided with an inverted trough 5 adapted to form a trap for the liberated metal 6 risin from the cathbde pot. The pot 3 will pre erably be supported, as indicated, in a furnace for supplying initial heat or controlling the temperature during operation. Suitable electrical connections indcated at 7 and 8 will be provided to supply current for the electrolysis. The light metal caughtin the traps 5 will preferably be led by said traps to a suitable collecting well or zone, not shown, enabling the later removal of the metal with case. In Fig. 2, three anodes of a series, which may contain any convenient number, are shown depending in the bath from above, each being surrounded by a curtain 1. These curtains are shown in Fig. 1 as supported by They may be carried in that manner or in any other convenient manner adapted to the particular form of the cell, but they will have the sleeve-like construction, one such sleeve for a single anode or a group thereof, and, preferably, in large scale practice one such for each individual anode. The curtain will preferably be made of a suitable quality of fire clay or other ceramic material adapted to withstand the conditions of exposure to bath and metallic magnesium in the molten state, some of which latter may beliberated upon the inner face of the trap 5 facing the curtain. I find it best that there be a substantial clearance between such curtain and metal parts 10f the cell to avoid unnecessar contact of liberated metal, there entangle with the curtain. Another object of the curtain is to cover the exposed surface of the trap 5 or other cathodic surface from which metal liberated thereon would not directly enter the trap. Such covering restricts the liberation of metal on the protected surface and to an equal extent prevents losses there- It will be seen that the curtain afi'ords a partition between that part of thebath occupied by the anode through which the chlorine or other anodic product rises and that part of the bath in which the cathodic metal is produced and collected. Cover slabs 9 may be provided and a duct 12 connected therewith for drawing ofi' the gaseous anodic products, such as chlorine gas and the like.
When, in the course of cell operation, the
- curtain or one of a plurality of curtains in a cell employing a plurality of anodes, becomes damaged by cracking or erosion or the like, I provide in a handy location a separate curtain preferably gradually preheated to the temperature of the bath. I then remove such portions of the cover 9 and the sealing salt 1 0 thereon as will expose the damaged curtain, raise the anode therein, insert a suitable tool, such as a hook or special tongs, to engage the curtain, remove it and then immediately replace it with the fresh curtain referred to. The anode may then be again lowered into the bath and the cover replaced. During such operations the other anodes of a plurality, when used, will be in service, the metal will continue to be produced as well as the gaseous anodic products, but suflicient suction will preferably have been provided at the outlet 12 to prevent issue of gas into the room, there being preferably a draft of air drawn into the compartment 11 to wash out the gas therein.
Small pieces of ceramic material are relatively cheaper than large ones, are more easily handled without breakage and are less liable to break due to temperature changes. By employing relatively small individual curtains for each anode, or a number of such each for a group of anodes, the limitations 0 ceramic material are given proper regard, and the otherwise advantageous properties made available.
a large share of heretofore very onerous and diflicult procedures in the electrolysis of a fused bath, such as one containing magnesium chloride employed forthe production of metallic magnesium. I find that the use of my curtain greatly simplifies procedure and contributes markedly to the reduction in cost of cell maintenance. This is particularly true in large scale operation in which it is convenient to employ a cathode pot of large size and a plurality of anodes depending therein. By supplying each individual anode with its own individual curtain, breakage or erosion losses are easily, cheaply and quicklytaken care of and that without interruption of the operation of the cell or cessation of the production of valuable product. The cutting in and out of such large units is a difiicult and onerous proceeding, both as to cell operation and to power control. The elimination of the necessity to so cut out va cell to remove a curtain and the application of an individual small'curtain to each of a plurality of anodes constitute distinct and valuable advances in the art of electrolyzing fused baths.
Other modes of applying the principle of my invention may be employed instead of the one explained, change being made as regards the means and the steps herein disclosed, provided those stated by any of the following claims or their equivalentbe employed. I therefore particularly point out and distinctlyclaim as my invent1on:
1. In an apparatus for the electrolysis of a fused bath to produce a metal lighter than the electrolyte, the combination of a metallic vessel to contain such bath and constitutin the cathode, an inwardly directed inverted metallic trough member connected to the upper part of the sidewall of said vessel in electrical contact therewith and adapted to entrap molten metal rising from the active cathode surface, a plurality of vertically adjustable anodes depending in said bath, and a removable one-piece sleeve-like curtain member of ceramic material circumscribing each anode in spaced relation therefrom, said curtain member being immersed in said bath to a depth suflicient to cover the surface of said trough member facing the anode and thereby to restrict the flow of I find that the use of my curtain removes I menace of the sidewall of said vessel adapted to entrap molten metal rising from the active cathode surface, a plurality of vertically adjustable anodes depending in said bath,
9 and a removable one-piece sleeve-like curtain member of ceramic material circumscribing each anode in spaced relation therefrom, said curtain member having lateral extensions adapted to support the same upon the super- 19 structure of said apparatus and being immersed in said bath to a depth sufiicient to cover the surface ofsaid trough'member facing the anode and thereby to restrict the flow of current therebetween. Signed by me this 28th da of May, 1929.
RALPH HUNTER.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US367494A US1897308A (en) | 1929-05-31 | 1929-05-31 | Apparatus for electrolysis of a fused bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US367494A US1897308A (en) | 1929-05-31 | 1929-05-31 | Apparatus for electrolysis of a fused bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1897308A true US1897308A (en) | 1933-02-14 |
Family
ID=23447397
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US367494A Expired - Lifetime US1897308A (en) | 1929-05-31 | 1929-05-31 | Apparatus for electrolysis of a fused bath |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1897308A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2539092A (en) * | 1940-11-12 | 1951-01-23 | Gen Motors Corp | Electrolytic apparatus for reduction of aluminum bromide |
-
1929
- 1929-05-31 US US367494A patent/US1897308A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2539092A (en) * | 1940-11-12 | 1951-01-23 | Gen Motors Corp | Electrolytic apparatus for reduction of aluminum bromide |
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