US531235A - Peooebs of and apparatus foe the production of caustic alkali - Google Patents
Peooebs of and apparatus foe the production of caustic alkali Download PDFInfo
- Publication number
- US531235A US531235A US531235DA US531235A US 531235 A US531235 A US 531235A US 531235D A US531235D A US 531235DA US 531235 A US531235 A US 531235A
- Authority
- US
- United States
- Prior art keywords
- potassium
- sodium
- caustic alkali
- production
- furnace
- 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
- 239000003513 alkali Substances 0.000 title description 13
- 239000003518 caustics Substances 0.000 title description 12
- 238000004519 manufacturing process Methods 0.000 title description 6
- 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 21
- 239000011734 sodium Substances 0.000 description 20
- 229910052708 sodium Inorganic materials 0.000 description 20
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 18
- 239000011591 potassium Substances 0.000 description 18
- 229910052700 potassium Inorganic materials 0.000 description 18
- 229910052751 metal Inorganic materials 0.000 description 9
- 239000002184 metal Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 6
- 239000003792 electrolyte Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 150000001805 chlorine compounds Chemical class 0.000 description 4
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 3
- 239000000920 calcium hydroxide Substances 0.000 description 3
- 235000011116 calcium hydroxide Nutrition 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- ZKQDCIXGCQPQNV-UHFFFAOYSA-N Calcium hypochlorite Chemical compound [Ca+2].Cl[O-].Cl[O-] ZKQDCIXGCQPQNV-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000007844 bleaching agent Substances 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- 229910000978 Pb alloy Inorganic materials 0.000 description 1
- 150000001447 alkali salts Chemical class 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- -1 chlorides Chemical class 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 150000004677 hydrates Chemical class 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005580 one pot reaction Methods 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Inorganic materials [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 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
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/06—Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
Definitions
- caustic alkali such as the hydrates of sodium and potassium
- salts of sodium and potassium such as chlorides
- Figure 1 is a longitudinal section of a furnace, showing auxiliary pot or vessel for the production of caustic alkali, and means for the collection of chlorine.
- Fig. 2 is a trans verse section of the said furnace, showing means for the continual supply of the alkali salt.
- Fig. 3 is a sectional elevation of two pots combined.
- metal A which will alloy with sodium or potassium and which will not be affected by a fused caustic alkali when in a molten condition, such as metallic lead, in the bottom df the furnace or vessel,in which the operation is to be carried out, and this charge of metal or metallic lead constitutes the cathode A of an electric circuitD F.
- a sodium or potassium salt such as a carbonate of sodium or potassium but preferably sodium or potassium chloride, as an electrolyte and I may mix with the said chloride other salts, such as chloride of calcium or strontium to reduce the temperature at which the electrolyte melts.
- One or more anodes F of carbon or other suitable material are inserted into the sodium or potassium salt, and they are surrounded by a case G of refractory and impervious material, such as fire-clay, to protect them from the products of combustion of the fuel used in the furnace, and also serve to collect the chlorine gas, which is liberated and rises at the said anodes where chlorides are used, and
- the charge of alloyed metal, or lead and sodium or potassium (the cathode) is thus in free communication with the auxiliary pot or vessel N, and it is found that as the sodium or potassium is removed from the alloy in the pot N, in the form of a hydrate, it will be continually replaced by fresh sodium or potassium in consequence of the difiusion of further sodium or potassium from the hearth of the furnace through the metal in the conduit P to the metal in the pot N.
- the conversion of thesodium or potassium into the hydrate,-that is into caustic alkali may be effected by'a jet of steam admitted by the pipe K to the surface of the charge in the auxiliary pot or vessel N, without chill-
- the charge of sodium or potassium salts in the furnace may be maintained through a suitable hopper or hoppers S; the metal or lead bath remaining as a collector and carrier of the sodium or potassium, and the chlorine (where chlorides are used as the electrolyte) being collected simultaneously for the production of bleaching powder, or otherwise.
- a continuous process forthe production of a caustic alkali consisting of the treatment in a fused condition by electrolysis of a salt of sodium or potassium forming the electrolyte, upon a molten bath of lead alloying with sodium and potassium, and not affected by fused caustic alkali, the said metal forming the cathode of the electric circuit; the conversion into acaustic alkali of the sodium or potassium from its alloy with the molten cathode, by the treatment of a part of said cathode, t'n situ, by water in any form; and the removal of the caustic alkali from the surface of the molten bath for collection and utilization, substantially as described.
- a process consisting of the treatment by electrolysis of the chlorides of potassium or sodium in a fused condition over a cathode of molten lead; the treatment by water in any form, of part of the cathode in situ,without removal or diminution of the lead, to convert the potassium or sodium into caustic alkali; the collection of the chlorine evolved at the anodes of the electric circuit; and the conversion of the chlorine into the chloride of lime, substantially as described.
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
(NozModeL) 2 Sheets-Sheet 1.
I G. T. J. VAUTIN.
PROCESS- OF AND APPARATUS FOR THE PRODUCTION OF GAUSTIG ALKALI.
Patented Dec. 18,1894.
a a Q/Aw A ABA,
THE NORRIS PErzns c0. vnorau'mq. wAsamcYom n. c.
2 SheetsShe et 2.
' (NoMod eL) 0. T...J. V'AUTIN; A PROCESS OF AND APPARATUS FOR THE PRODUCTION OF GAUSTIC ALKALI.
Patented Dee. 18', 1894 FIG-3'.
fivemr azaaalazw jg 6) QYiZy Z TH: "cums PETERS co. vncrruumu. wnsnmeron, u. c
f TED S AT PATENT iFFc' CLAUDE THEODORE JAMES VAUTIN, OF LONDON, ENGLAND.-
PROCESS OF AND APPARATUS FOR THE PRODUCTION OF CAUSTIC ALKALI.
SPECIFICATION forming part of Letters IEatent No. 531,235, dated December 18, 1894. Application filed January 11, 1894. Serial No. 496 459. (N0 specimens.)
cess, and means used therein, for the produc-- t1on of caustic alkali, such as the hydrates of sodium and potassium, from'salts of sodium and potassium, such as chlorides, by electrolf ysis.
In order that my invention may be the better understood, I now proceed to describe the same in relation to the means illustrated" herewith, reference being had to the letters marked thereon.
Figure 1 is a longitudinal section of a furnace, showing auxiliary pot or vessel for the production of caustic alkali, and means for the collection of chlorine. Fig. 2, is a trans verse section of the said furnace, showing means for the continual supply of the alkali salt. Fig. 3, is a sectional elevation of two pots combined.
To carry my improved process into effect, I place a charge of metal A which will alloy with sodium or potassium and which will not be affected by a fused caustic alkali when in a molten condition, such as metallic lead, in the bottom df the furnace or vessel,in which the operation is to be carried out, and this charge of metal or metallic lead constitutes the cathode A of an electric circuitD F. Above this charge of metal or lead A, is added a sodium or potassium salt, such asa carbonate of sodium or potassium but preferably sodium or potassium chloride, as an electrolyte and I may mix with the said chloride other salts, such as chloride of calcium or strontium to reduce the temperature at which the electrolyte melts. I
One or more anodes F of carbon or other suitable material,are inserted into the sodium or potassium salt, and they are surrounded by a case G of refractory and impervious material, such as fire-clay, to protect them from the products of combustion of the fuel used in the furnace, and also serve to collect the chlorine gas, which is liberated and rises at the said anodes where chlorides are used, and
ner. surface of the molten bath of metal or lead X containing calcic hydrate, or powdered .slaked lime, for the purpose of producing bleaching powder. The whole charge of the furnace is exposed to gentle heat until the metallic or lead charge A is melted, and the taining calcium hydrate, or powdered slaked lime, to be converted into chloride of lime,or to be utilized in any other convenient man- .The sodium or potassium freed at the L L for heating the same, is connected by a conduit P, communicating with the lower part of the metallic bath in the hearth. The charge of alloyed metal, or lead and sodium or potassium (the cathode) is thus in free communication with the auxiliary pot or vessel N, and it is found that as the sodium or potassium is removed from the alloy in the pot N, in the form of a hydrate, it will be continually replaced by fresh sodium or potassium in consequence of the difiusion of further sodium or potassium from the hearth of the furnace through the metal in the conduit P to the metal in the pot N.
The conversion of thesodium or potassium into the hydrate,-that is into caustic alkalimay be effected by'a jet of steam admitted by the pipe K to the surface of the charge in the auxiliary pot or vessel N, without chill- The charge of sodium or potassium salts in the furnace may be maintained through a suitable hopper or hoppers S; the metal or lead bath remaining as a collector and carrier of the sodium or potassium, and the chlorine (where chlorides are used as the electrolyte) being collected simultaneously for the production of bleaching powder, or otherwise.
It is obvious that instead of an open hearth furnace, the process as above described could be conducted in a pair or series of conjoined crucibles N N, Fig. 3, one provided with a suitable lining .1, containing the electrolyte for electrolysis and the cathode, and the preparation of the caustic alkali being effected in the other, which is provided with a draw-off cock y in its bottom and the lateral draw olf cock Z.
Having now described my invention, what I claim, and desire to secure by Letters Patent, is
1. A continuous process forthe production of a caustic alkali, consisting of the treatment in a fused condition by electrolysis of a salt of sodium or potassium forming the electrolyte, upon a molten bath of lead alloying with sodium and potassium, and not affected by fused caustic alkali, the said metal forming the cathode of the electric circuit; the conversion into acaustic alkali of the sodium or potassium from its alloy with the molten cathode, by the treatment of a part of said cathode, t'n situ, by water in any form; and the removal of the caustic alkali from the surface of the molten bath for collection and utilization, substantially as described.
2. A process, consisting of the treatment by electrolysis of the chlorides of potassium or sodium in a fused condition over a cathode of molten lead; the treatment by water in any form, of part of the cathode in situ,without removal or diminution of the lead, to convert the potassium or sodium into caustic alkali; the collection of the chlorine evolved at the anodes of the electric circuit; and the conversion of the chlorine into the chloride of lime, substantially as described.
3. The treatment of a part of a cathode of an electrolytical furnace, consisting of a molten alloy of lead with sodium and potassium, by heating the said part to be treated, while still in fluid communication with the said cathode, and by introducing a jet of steam upon the surface of the said separated part, to convert the sodium or potassium as it collects by transfusion through the molten cathode, into a caustic alkali, for collection and utilization, substantially as described.
4. The combination of two covered furnaces or equivalent furnace pots, connected at the bottom by an open conduit; grates and flues adapted thereto to externally heat the same; anodes in one pot or furnace, protected by surrounding refractory tubes having connecting pipes; a fluid cathode common to both furnaces or pots; and a steam admission pipe, and exit pipe passed through the cover of the other pot or furnace, to carry the herein described process into effect, substantially as described.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
CLAUDE THEODORE JAMES VAUTIN.
Witnesses:
RICHARD A. HOFFMANN, CHARLES H. CARTER.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US531235A true US531235A (en) | 1894-12-18 |
Family
ID=2600011
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US531235D Expired - Lifetime US531235A (en) | Peooebs of and apparatus foe the production of caustic alkali |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US531235A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3622491A (en) * | 1969-04-23 | 1971-11-23 | Us Interior | Electrolytic apparatus for molten salt electrolysis |
-
0
- US US531235D patent/US531235A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3622491A (en) * | 1969-04-23 | 1971-11-23 | Us Interior | Electrolytic apparatus for molten salt electrolysis |
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