US1111977A - Electrolytic cell. - Google Patents
Electrolytic cell. Download PDFInfo
- Publication number
- US1111977A US1111977A US59722310A US1910597223A US1111977A US 1111977 A US1111977 A US 1111977A US 59722310 A US59722310 A US 59722310A US 1910597223 A US1910597223 A US 1910597223A US 1111977 A US1111977 A US 1111977A
- Authority
- US
- United States
- Prior art keywords
- brine
- diaphragm
- compartment
- electrolytic cell
- 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
- 239000012267 brine Substances 0.000 description 9
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000010425 asbestos Substances 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- SURLGNKAQXKNSP-DBLYXWCISA-N chlorin Chemical compound C\1=C/2\N/C(=C\C3=N/C(=C\C=4NC(/C=C\5/C=CC/1=N/5)=CC=4)/C=C3)/CC\2 SURLGNKAQXKNSP-DBLYXWCISA-N 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 238000005325 percolation Methods 0.000 description 2
- 229910052895 riebeckite Inorganic materials 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000010454 slate Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
Images
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
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
- C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
Definitions
- This cell is especially designed for the electrolysis of sodium chlorid and production of chlorin and caustic soda.
- the cell has two compartments separated by a diaphragm and a foraminous sheet-metal cathode, and an overflow pipe for brine leading from the upper end of the anode compartment into the outer compartment.
- FIG. 1 is a transverse vertical section of the cell on the line 11 of Fig. 2; and Fig. 2 is a plan view of the cell.
- the cell illustrated comprises a rectangular sheet steel vessel 1, withinand spaced away from which is a rectangular sheet steel vessel 2 having perforated sides and serving as the cathode.
- a rectangular sheet steel vessel 2 having perforated sides and serving as the cathode.
- the diaphragm 3 of asbestos cloth.
- Supported on the flanged upper ends of the cathode vesscl are plates 4 of slate or silicated asbestos, forming a chamber 5 which is closed at the top by a graphite cover 6.
- a series of depending graphite bar anodes 7 are carr ed by this cover, their upper ends being screwed into holes therein.
- a brine-supply pipe 8 and a chlorin-discharge pipe 9 extend through the cover.
- a dischargepipe 10 for the causticized brine extends from the upper end of the vessel 1.
- such basic deposit is allowed to remain and ac cumulate on the diaphragm, and the cell is provided With a special-overflow pipe 11 leading from the upper end of the chamber 5 and thence extendin downward into and being sealed by the bum in the outer compartment.
- brine is supplied to the anode compartment through the pipe 8, sealed by the brine therein, and the chlorin is withdrawn through the pipe 9 by means of an exhaust'gpump, creating a partial vacuum in the chamber 5 and raising the level of the anolyte until it reaches the pipe 11, whereupon the brine continuously overfiows into the outer compartment.
- the pipe 11 is fixed at such height that there is a' pressure of about two inches of brine against the inner surface of the diaphragm, notwithstanding the partial vacuum, to. prevent diffusion and leakage of the catholyte into the anode chamber.
- the rates of supply of fresh brine to the anode compartment and removal of causticized brine from the outer compartment are correlated and predetermined to give the desired percentage of caustic in the product.
- an overflbw passage extending from the upper end ofthe anode compartment into the other compartment.
- an overflow pipe extending from the upper end of the anode compartment downward into the other compartment.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Description
C. C. TITUS.
ELECTROLYTIC CELL. APPLIQAT'IQN FILED DEO.14, 1910.
Patented Sept. 29, 1914.
Illliiiii! J-----l-- -----L----- 1 sonar 0. runs, OEHELEITA, MONTANA, ABSIGNOR r0 norr mHA METALLURGIQAL comranr, 01 Karma, MONTANA. A CORPORATION OF MONTANA.
ELECTROLYTIC Specification of Letters Patent.
Patented Sept. 29, 1914."
Application filed December 14, 1910. Serial No. 597,223.
To all whom it may concern:
Be it known that I, COURT C. Tr'rUs, a citizen of the United States, residing at Helena, in the county of Lewis and'Clarke and State of Montana, have invented certain new and useful Improvements in Electrolytic Cells, of which the following 'is a specification.
This cell is especially designed for the electrolysis of sodium chlorid and production of chlorin and caustic soda. The cell has two compartments separated by a diaphragm and a foraminous sheet-metal cathode, and an overflow pipe for brine leading from the upper end of the anode compartment into the outer compartment.
Referring to the accompanying drawingFigure 1 is a transverse vertical section of the cell on the line 11 of Fig. 2; and Fig. 2 is a plan view of the cell.
The cell illustrated comprises a rectangular sheet steel vessel 1, withinand spaced away from which is a rectangular sheet steel vessel 2 having perforated sides and serving as the cathode. Within the cathode vessel, and lining its sides is the diaphragm 3 of asbestos cloth. Supported on the flanged upper ends of the cathode vesscl are plates 4 of slate or silicated asbestos, forming a chamber 5 which is closed at the top by a graphite cover 6. A series of depending graphite bar anodes 7 are carr ed by this cover, their upper ends being screwed into holes therein. A brine-supply pipe 8 and a chlorin-discharge pipe 9 extend through the cover. A dischargepipe 10 for the causticized brine extends from the upper end of the vessel 1.
In cells of this type, it is customary to maintain a higherlevel in the anode compartment than in the outer compartment, in order to cause percolation of the bum out- Ward through the diaphragm at such a rate, .as to continuously dissolve and carry off the caustic produced. In using these cells to electrolyze impure natural salt 'or brine, however, the diaphragm is clogged by the insoluble basic products of electrolysis, e. g., hydroxids of magnesium and calcium, so
that the rate of brine-percolation rapidly decreases, necessitating cleaning or replacement of the diaphragm. Yet the deposit on the diaphragm does not materially raise the internal resistance ofthe cell or require an increased potential difference at its terminals, but does increase the resistance to diffusion and current-efficiency.
According to the present invention, such basic deposit is allowed to remain and ac cumulate on the diaphragm, and the cell is provided With a special-overflow pipe 11 leading from the upper end of the chamber 5 and thence extendin downward into and being sealed by the bum in the outer compartment. In use, brine is supplied to the anode compartment through the pipe 8, sealed by the brine therein, and the chlorin is withdrawn through the pipe 9 by means of an exhaust'gpump, creating a partial vacuum in the chamber 5 and raising the level of the anolyte until it reaches the pipe 11, whereupon the brine continuously overfiows into the outer compartment. The pipe 11 is fixed at such height that there is a' pressure of about two inches of brine against the inner surface of the diaphragm, notwithstanding the partial vacuum, to. prevent diffusion and leakage of the catholyte into the anode chamber. The rates of supply of fresh brine to the anode compartment and removal of causticized brine from the outer compartment are correlated and predetermined to give the desired percentage of caustic in the product.
1. In an electrolytic cell having two compartments separated by a diahragm and foraminous cathode, an overflbw passage extending from the upper end ofthe anode compartment into the other compartment.
2. In an electrolytic cell having two compartments separated by a diaphragm and foraminous cathode, an overflow pipe extending from the upper end of the anode compartment downward into the other compartment.
3. In an. electrolytic cell having two compartments separated by a diaphragm and In testimony whereof, I aflix my signature in presence of two witnesses,
COURT C. TITUS.
foraminous cathode, a gas-tight chamber at the upper end of the anode compartment, means for maintaining a partial vacuum therein, and an overflow pipe extending 5 from said chamber downward into the outer l Witnesses: V
compartment and sealed by the liquid IRA T. HIGHT, therein. 7 i CHARLES E. PEw.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US59722310A US1111977A (en) | 1910-12-14 | 1910-12-14 | Electrolytic cell. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US59722310A US1111977A (en) | 1910-12-14 | 1910-12-14 | Electrolytic cell. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1111977A true US1111977A (en) | 1914-09-29 |
Family
ID=3180164
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US59722310A Expired - Lifetime US1111977A (en) | 1910-12-14 | 1910-12-14 | Electrolytic cell. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1111977A (en) |
-
1910
- 1910-12-14 US US59722310A patent/US1111977A/en not_active Expired - Lifetime
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