GB362579A - Process and apparatus for carrying out electrolyte processes, more particularly those with decomposable end products, such as for instance the manufacture of persulphuric acid or of its salts by electrolysis - Google Patents
Process and apparatus for carrying out electrolyte processes, more particularly those with decomposable end products, such as for instance the manufacture of persulphuric acid or of its salts by electrolysisInfo
- Publication number
- GB362579A GB362579A GB29733/30A GB2973330A GB362579A GB 362579 A GB362579 A GB 362579A GB 29733/30 A GB29733/30 A GB 29733/30A GB 2973330 A GB2973330 A GB 2973330A GB 362579 A GB362579 A GB 362579A
- Authority
- GB
- United Kingdom
- Prior art keywords
- cell
- anolyte
- vessel
- catholyte
- anode
- 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
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
- D06N3/16—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with oil varnishes, i.e. drying oil varnishes, preferably linseed-oil-based; factice (sulfurised oils), Turkish birdlime, resinates reacted with drying oils; naphthenic metal salts
-
- 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
- C25B1/28—Per-compounds
- C25B1/29—Persulfates
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Textile Engineering (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
362,579. Electrolysis. OESTERREICHISCHE CHEMISCHE WERKE GES., 5, Technikerstrasse, Vienna. Oct. 4, 1930, No. 29733. Convention date, Feb. 20. [Class 41.] In a two - compartment cell for the manufacture of persulphuric acid and its salts and like easily decomposable products by an anodic oxidation process, the anolyte passes through the cell at high speed in a thin layer, while the catholyte on the opposite side of the diaphragm passes slowly through the cell as a cooled column. In the apparatus shown the anolvte enters the anode chamber at the bottom of a glass tube 6 around which is mounted a closed glass vessel 5 which nearly fills the anode chamber. The anolyte then flows upwards in a thin stream between the vessel 5 and the diaphragm vessel 3 which it leaves at 4. The vessel 5 is supported on a plate 21 having a central opening and a radial slot to allow egress of the anolyte from the tube 6. The catholyte moves slowly through the outer chamber which is cooled by a lead pipe 14 which constitutes the cathode. The cooling fluid on leaving the pipe 14 is led by a tube 20 to cool the vessel 5, which it leaves by an overflow, not shown. The anode may consist of thin strips of platinum reinforced by strips of tantulum secured to a lead ring 9 ; the ring is provided with an ebonite covering which may extend partly over the strips. The diaphragm may be of unglazed porcelain, clay, gurocel, fabric or an artificial resin. The container may be of lead or a lead alloy or may be composed of or impregnated with a natural or artificial resin. Several cells may be connected in cascade, the anolyte and catholyte passing in succession through their various compartments ; a number of such series may be connected in parallel. In a modification several anode compartments are mounted in a single cell and surrounded by a common coil-shaped cathode; several of such cells may be arranged with all the anodes connected to the common cathode of the preceding cell, the anolyte flowing from each compartment to the corresponding compartment of the next cell, and the catholyte from each outer compartment to that of the next cell. Liquid containing persulphuric acid or its salts obtained by this method may be treated by hydrolytic decomposition for the manufacture of hydrogen peroxide, after removal of which it is passed through the cathode chambers before return to the anode chambers. Detailed examples of dimensions and current densities are given.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT362579X | 1930-02-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB362579A true GB362579A (en) | 1931-12-10 |
Family
ID=3672793
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB29733/30A Expired GB362579A (en) | 1930-02-20 | 1930-10-04 | Process and apparatus for carrying out electrolyte processes, more particularly those with decomposable end products, such as for instance the manufacture of persulphuric acid or of its salts by electrolysis |
Country Status (5)
Country | Link |
---|---|
BE (1) | BE373771A (en) |
DE (1) | DE567542C (en) |
FR (1) | FR702760A (en) |
GB (1) | GB362579A (en) |
NL (1) | NL30269C (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE753434C (en) * | 1937-02-13 | 1951-10-31 | Henkel & Cie Gmbh | Process for the purification of solutions used to generate per compounds |
NL92567C (en) * | 1951-12-22 |
-
0
- BE BE373771D patent/BE373771A/xx unknown
- NL NL30269D patent/NL30269C/xx active
-
1930
- 1930-02-26 DE DE1930567542D patent/DE567542C/en not_active Expired
- 1930-09-29 FR FR702760D patent/FR702760A/en not_active Expired
- 1930-10-04 GB GB29733/30A patent/GB362579A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
BE373771A (en) | |
NL30269C (en) | |
FR702760A (en) | 1931-04-16 |
DE567542C (en) | 1933-01-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Lewis et al. | Concentration of H2 isotope | |
US2795541A (en) | Electrolytic production of percompounds | |
GB362579A (en) | Process and apparatus for carrying out electrolyte processes, more particularly those with decomposable end products, such as for instance the manufacture of persulphuric acid or of its salts by electrolysis | |
US892983A (en) | Manufacture of hypochlorite solutions by electrolytic methods. | |
NO172946B (en) | PROCEDURE AND APPARATUS FOR AA ELECTROLYTIC TO AND FROM A BIPOLARALLY CONNECTED ELECTROLYCLE CELL | |
US2033732A (en) | Process for the working up of soaps | |
GB512966A (en) | Improvements in or relating to process for the electrolytic production of persulphuric acid and persalts and apparatus for carrying out the process | |
US1837177A (en) | Electrolytic process and apparatus | |
US2224831A (en) | Electrolysis cell | |
US646313A (en) | Apparatus for decomposing alkali sulfates. | |
SU716525A3 (en) | Vertical mercury cathode electrolyzer | |
US666387A (en) | Apparatus for producing alkali, electricity, and hydrogen from alkali-metal amalgam. | |
GB468589A (en) | Improvements in and relating to electrolytic water decomposing apparatus with concentrically arranged electrodes | |
US2297252A (en) | Process for the purification of solutions that serve as generators for percompounds | |
IE894003L (en) | Electrochemical generation of dinitrogen pentoxide in nitric¹acid | |
US877537A (en) | Method of electrolyzing salts. | |
US2105438A (en) | Process and apparatus for producing percompounds | |
US1806801A (en) | Teners limited | |
US1937621A (en) | Electrolytic apparatus | |
GB465737A (en) | Improvements in or relating to electrolytic processes and apparatus | |
US2324002A (en) | Electrolytic cell | |
US861226A (en) | Electrolysis. | |
US1056118A (en) | Method of electrolyzing streaming electrolytes. | |
US2285858A (en) | Electrolytic process for the production of quinone and hydroquinone | |
US528322A (en) | Hamilton young castner |