US1752348A - Electrolysis of ferrous chloride - Google Patents
Electrolysis of ferrous chloride Download PDFInfo
- Publication number
- US1752348A US1752348A US257096A US25709628A US1752348A US 1752348 A US1752348 A US 1752348A US 257096 A US257096 A US 257096A US 25709628 A US25709628 A US 25709628A US 1752348 A US1752348 A US 1752348A
- Authority
- US
- United States
- Prior art keywords
- ferrous chloride
- anode
- electrolysis
- chlorine
- chloride
- 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
- 229960002089 ferrous chloride Drugs 0.000 title description 9
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 title description 9
- 238000005868 electrolysis reaction Methods 0.000 title description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 15
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 9
- 239000000460 chlorine Substances 0.000 description 9
- 229910052801 chlorine Inorganic materials 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- 229910052742 iron Inorganic materials 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000011084 recovery Methods 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
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 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
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 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
- 230000001427 coherent effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 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
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/24—Halogens or compounds thereof
- C25B1/26—Chlorine; Compounds thereof
Definitions
- This invention has for its object the electrolysis of ferrous chloride in aqueous solution, in order to recover therefrom pure electrolytic iron and pure chlorine in one operation without excessive consumption of power.
- I employ a concentrated solution of ferrous chloride, which I maintain at a temperature of 90100 C. and I allow this solution to flow 10 throu h the electrolytic cell at such a rate that t e issuing spent liquor contains about 20 parts of ferrous chloride as F6012 per 100 parts by weight of liquor.
- the cathode a thin plate, mandrel or other suitable object, which may be stationary or may be rotated.
- the anode I use a rod, plate or cylinder of carbon or other inert material, which I support in a concentrated solution of a suita le chloride,such
- the partition between the anode and cathode solutions may be a cylinder or wall across the cell, and may be formed from poi-ousclay, preferabl unglazed, or other suitable porous materia WhlCh whilst opposing only a low resistance to the electric current, serves to prevent diffusion between the two solu- 3 tions.
- Such partitions may be formed by moulding from a good china clay paste, without addition of any soluble, fiuxl'ng or glazing material, drying slowly in known manner, and firing at a temperature of GOO-900 C.
- the spent liquor is used to dissolve further quantities of ferrous chloride to form a concentrated solution, so that a continuous circulation is maintained.
- the cell and circulating pipes are preferably enclosed to prevent atmospheric oxidation.
- I claim 1 A process for the recovery of electrolytic iron and chlorine from ferrous chloride, consisting in electrolyzing a concentrated solution of the ferrous chloride in an electrolytic cell having a cathode, on which the iron is deposited, and an anode of inert material, said anode surrounded by a concentrated solution of a chloride of a metal more electropositive than iron and collectingthe chlorine evolved at the anode.
- a process for the recovery of electrolytic iron and chlorine from ferrous chloride consisting in electrolyzing a concentrated solution of the ferrous chloride in an electrolytic cell using a current of 10 to 25 amperes per square foot and a pressure of 2.3 to 3.0 volts, a cathode adapted to receive a deposit of the iron, and an anode of inert material, said anode surrounded by a concentrated solution of a chloride of a met-a1 more electropositive than iron and collecting the chlorine evolved at the anode.
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 Apr. 1, 1930 UNITED STATES STANLEY ISAAd LEVY, 01' LONDON, ENGLAND ELEC'IBOLYSIB OF IEBBOUS CHLORIDE R Drawing. Application filed February 25, 1928, Serial No. 257,096, and in Great Britain February 10, 1928.
This invention has for its object the electrolysis of ferrous chloride in aqueous solution, in order to recover therefrom pure electrolytic iron and pure chlorine in one operation without excessive consumption of power.
In accordance with the present invention I employ a concentrated solution of ferrous chloride, which I maintain at a temperature of 90100 C. and I allow this solution to flow 10 throu h the electrolytic cell at such a rate that t e issuing spent liquor contains about 20 parts of ferrous chloride as F6012 per 100 parts by weight of liquor.
I use as the cathode a thin plate, mandrel or other suitable object, which may be stationary or may be rotated. As the anode I use a rod, plate or cylinder of carbon or other inert material, which I support in a concentrated solution of a suita le chloride,such
as sodium, calcium, magnesium or other similar chloride, contained in an anode compartment or chamber. 1
The partition between the anode and cathode solutions may be a cylinder or wall across the cell, and may be formed from poi-ousclay, preferabl unglazed, or other suitable porous materia WhlCh whilst opposing only a low resistance to the electric current, serves to prevent diffusion between the two solu- 3 tions. Such partitions may be formed by moulding from a good china clay paste, without addition of any soluble, fiuxl'ng or glazing material, drying slowly in known manner, and firing at a temperature of GOO-900 C.
For the electrolysis I employ a current of 10-25 amperes per square foot, at a ressure .of 2.3-3.0 volts. Under these conditions a uniform coherent de osit of iron'is obtained on the cathode wiiilst pure chlorine is 40 evolved at the anode. The anode compartment is enclosed in known manner, and provided with an exit pipe for chlorine at the top; the chlorine gas is passed through a condenser, so that water va our carried off with the chlorine is deposite The water so condensed may be returned to the anode compartment or chamber. The current efiiciency is 90100% estimated on both the chlorine and the iron deposited. Y
The spent liquor is used to dissolve further quantities of ferrous chloride to form a concentrated solution, so that a continuous circulation is maintained. The cell and circulating pipes are preferably enclosed to prevent atmospheric oxidation. I
I claim 1. A process for the recovery of electrolytic iron and chlorine from ferrous chloride, consisting in electrolyzing a concentrated solution of the ferrous chloride in an electrolytic cell having a cathode, on which the iron is deposited, and an anode of inert material, said anode surrounded by a concentrated solution of a chloride of a metal more electropositive than iron and collectingthe chlorine evolved at the anode.
2. A process for the recovery of electrolytic iron and chlorine from ferrous chloride, consisting in electrolyzing a concentrated solution of the ferrous chloride in an electrolytic cell using a current of 10 to 25 amperes per square foot and a pressure of 2.3 to 3.0 volts, a cathode adapted to receive a deposit of the iron, and an anode of inert material, said anode surrounded by a concentrated solution of a chloride of a met-a1 more electropositive than iron and collecting the chlorine evolved at the anode.
In testimony whereof I have signed my name to this specification.
,s ANLEY ISAAC LEVY.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB1752348X | 1928-02-10 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1752348A true US1752348A (en) | 1930-04-01 |
Family
ID=10889871
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US257096A Expired - Lifetime US1752348A (en) | 1928-02-10 | 1928-02-25 | Electrolysis of ferrous chloride |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1752348A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2470073A (en) * | 1944-08-16 | 1949-05-10 | Fmc Corp | Electrolytic cell and method of operating same |
| US4130627A (en) * | 1977-06-20 | 1978-12-19 | Russ James J | Process for recovering mineral values from fly ash |
| US20100044243A1 (en) * | 2006-09-21 | 2010-02-25 | Qit-Fer & Titane Inc. | Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes |
| US20110114500A1 (en) * | 2008-03-20 | 2011-05-19 | Cardarelli Francois | Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes |
-
1928
- 1928-02-25 US US257096A patent/US1752348A/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2470073A (en) * | 1944-08-16 | 1949-05-10 | Fmc Corp | Electrolytic cell and method of operating same |
| US4130627A (en) * | 1977-06-20 | 1978-12-19 | Russ James J | Process for recovering mineral values from fly ash |
| US20100044243A1 (en) * | 2006-09-21 | 2010-02-25 | Qit-Fer & Titane Inc. | Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes |
| US20110114500A1 (en) * | 2008-03-20 | 2011-05-19 | Cardarelli Francois | Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes |
| US8784639B2 (en) | 2008-03-20 | 2014-07-22 | Rio Tinto Fer Et Titane Inc. | Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2273795A (en) | Electrolytic process | |
| GB814031A (en) | Improvements in or relating to the electrolytic production of aluminium | |
| CS218296B1 (en) | Method of continuous regeneration of the iron trichloride solution | |
| US2865823A (en) | Method of reclaiming waste pickle liquor | |
| US1752348A (en) | Electrolysis of ferrous chloride | |
| GB823531A (en) | A process for protecting a metal structure in contact with a stream of sea water | |
| US3804739A (en) | Electrolytic cell including arrays of tubular anode and diaphragm covered tubular cathode members | |
| NO128335B (en) | ||
| GB1155927A (en) | Electrolytic manufacture of alkali metals. | |
| GB1365150A (en) | Continuous electrolytic treatment for cleaning and conditioning aluminium surfaces | |
| US3779876A (en) | Process for the preparation of glyoxylic acid | |
| ES441433A1 (en) | Method for electrolysis of non-ferrous metal | |
| DE709742C (en) | Process for the production of metallic chromium by fusible electrolysis | |
| US1990582A (en) | Process of reducing sugars to alcohols | |
| GB655098A (en) | Improvements in or relating to electrolysis of fluorine salts | |
| PT86003B (en) | PROCESS OF ELECTROCHEMICAL REMOVAL OF HYPOCHLORITE FROM LICORS OF CELLS CONTAINING CHLORIDE | |
| US2756201A (en) | Electrolysis of chloride solutions and cell therefor | |
| JPS5477284A (en) | Ion exchange membrane electrolyzer | |
| US1098338A (en) | Cleaning metal surfaces. | |
| JPS5591989A (en) | Electrolysis method | |
| GB1080119A (en) | Improvements in or relating to methods of manufacturing pure nickel hydroxide | |
| GB1051597A (en) | ||
| US2285858A (en) | Electrolytic process for the production of quinone and hydroquinone | |
| DE526777C (en) | Process for the production of electrolytic iron and chlorine by electrolysis | |
| GB304053A (en) | Electrolysis of ferrous chloride |