GB194638A - Electrolytic iron - Google Patents
Electrolytic ironInfo
- Publication number
- GB194638A GB194638A GB3193522A GB3193522A GB194638A GB 194638 A GB194638 A GB 194638A GB 3193522 A GB3193522 A GB 3193522A GB 3193522 A GB3193522 A GB 3193522A GB 194638 A GB194638 A GB 194638A
- Authority
- GB
- United Kingdom
- Prior art keywords
- solution
- tank
- ferric
- vat
- reduction
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/06—Electrolytic production, recovery or refining of metals by electrolysis of solutions or iron group metals, refractory metals or manganese
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Treating Waste Gases (AREA)
Abstract
194,638. Eustis, F. A. Dec. 22, 1921. Iron chlorides and sulphates.-A solution of ferric salts is electrolytically reduced in a tank G to the ferrous condition, and is then led to a lixiviating tank B containing iron oxide ore. The lixiviator may be kept at a temperature of 70‹ C. or above, and preferably works on the countercurrent principle. After filtration, most of the solution, which has taken up ferric salts from the ore, returns to the reducing tank G. The remainder is treated with scrap iron in a vat F and with limestone in a tank D to remove ferric salts and acid. It is then filtered, if necessary, and electrolyzed in a depositing vat A, the ferric solution obtained then returning to the electrolytic reduction tank G. Any acid lost during operations with a sulphate solution may be restored by treating the solution with sulphur dioxide, say in the reduction vat G. Sulphide ores may be treated, if of such character that reduction of a ferric solution does not readily take place in the lixiviator. Specifications 194,639 and 196,334 are referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3193522A GB194638A (en) | 1921-12-22 | 1921-12-22 | Electrolytic iron |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3193522A GB194638A (en) | 1921-12-22 | 1921-12-22 | Electrolytic iron |
Publications (1)
Publication Number | Publication Date |
---|---|
GB194638A true GB194638A (en) | 1923-03-15 |
Family
ID=10330582
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3193522A Expired GB194638A (en) | 1921-12-22 | 1921-12-22 | Electrolytic iron |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB194638A (en) |
-
1921
- 1921-12-22 GB GB3193522A patent/GB194638A/en not_active Expired
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