GB190100393A - Improvements in Electrolysis and Apparatus therefor. - Google Patents

Improvements in Electrolysis and Apparatus therefor.

Info

Publication number
GB190100393A
GB190100393A GB190100393DA GB190100393A GB 190100393 A GB190100393 A GB 190100393A GB 190100393D A GB190100393D A GB 190100393DA GB 190100393 A GB190100393 A GB 190100393A
Authority
GB
United Kingdom
Prior art keywords
chlorate
cell
cells
solution
current
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
Application number
Inventor
Philip Arthur Newton
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Application granted granted Critical
Publication of GB190100393A publication Critical patent/GB190100393A/en
Expired legal-status Critical Current

Links

Abstract

393. Newton, P. A., [National Electrolytic Co.]. Jan. 7. Alkaline chlorates.-Relates to a process and apparatus for electrolysing solutions, particularly for preparing sodium and potassium chlorates. The electrolyte flows continuously through the cell. The electrodes are in close proximity to one another, about one-sixteenth to oneeighth of an inch apart, and are insulated from one another, but otherwise only separated by the liquid itself. The current employed is about 2 to 4 ampÞres per square inch of electrode surface, and the capacity of a cell is from 2 to 4 cubic inches per square inch of electrode surface. The result of this is that the current itself raises the electrolyte to the required temperature, namely, between 90‹ and 200‹ F., and preferably between 110‹ and 120‹ F. The temperature may be controlled by regulating the rate of flow of the liquid, whether the source of heat be the current itself, or wholly or partly external to the cell. The solution obtained is very weak, preferably containing less than 3 per cent. of chlorate. Several cells are built up together, through which the current is passed in series. In the example shown, each cell is made of a frame A having a metallic resisting lining B. One side is constructed of a metallic-plate D faced with platinum or other non- attackable material E and forming the anode. At the other side there are a number of vertical parallel rods or wires C, preferably of copper, which form the cathode and prevent polarization. They are separated from the opposing anode by horizontal insulating-rods O. The solution is charged through tubes G reaching to near the bottom of the cell, and overflows through the outlet H. The hydrogen developed rises freely up the rods or wires, and also escapes through the outlet H. A number of these cells are connected together by plates K, J and bolts L, a gasket F being placed between each pair of cells to insulate the opposing anode and cathode. The first and last cells are connected up to the two leads. The weak chlorate solution obtained is led away to a cooling-vessel, in which the chlorate separates. The solution is then pumped up to a tank, where it mixes with fresh salt, and is again led to the electrolysing-cells. If a chlorate, such as that of sodium, is produced which is more soluble than the corresponding chloride, the latter is separated out by crystallization, and the chlorate obtained by evaporating the solution left.
GB190100393D 1901-01-07 1901-01-07 Improvements in Electrolysis and Apparatus therefor. Expired GB190100393A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB190100393T 1901-01-07

Publications (1)

Publication Number Publication Date
GB190100393A true GB190100393A (en) 1901-03-30

Family

ID=32363163

Family Applications (1)

Application Number Title Priority Date Filing Date
GB190100393D Expired GB190100393A (en) 1901-01-07 1901-01-07 Improvements in Electrolysis and Apparatus therefor.

Country Status (1)

Country Link
GB (1) GB190100393A (en)

Similar Documents

Publication Publication Date Title
US4139447A (en) Electrolyzer for industrial production of fluorine
US3676315A (en) Production of sodium chlorate
US4057474A (en) Electrolytic production of alkali metal hydroxide
US3607684A (en) Manufacture of alkali metals
DK154027B (en) METHOD AND APPARATUS FOR ELECTROLYSEING Aqueous SOLUTION CONTAINING SODIUM AND / OR POTASSIUM SALTS
US3791947A (en) Electrolytic cell assemblies and methods of chemical production
US3824172A (en) Electrolytic cell for alkali metal chlorates
GB880838A (en) Improvements in or relating to electrolytic cells
US3385779A (en) Electrolytic cell for the production of halogenous oxy-salts
US1543357A (en) Process for the recovery of hydrogen and oxygen by electrolysis
US3930980A (en) Electrolysis cell
JPS6041153B2 (en) Diaphragmless electrolytic cell
US1109311A (en) Method and means for electrolyzing saline solutions.
Chikhi et al. Current distribution in a chlor-alkali membrane cell: experimental study and modeling
US665426A (en) Art of obtaining chlorates by electrolysis.
GB190100393A (en) Improvements in Electrolysis and Apparatus therefor.
WO1980001575A1 (en) Electrochemical apparatus and process for manufacturing halates
US2749301A (en) Mercury type, caustic, chlorine cell
US3140991A (en) Mercury cathode electrolytic cells
GB1028478A (en) Alkali metal chlorate electrolytic cells and their operation
Wallden et al. Electrolytic copper refining at high current densities
US3553088A (en) Method of producing alkali metal chlorate
US2281090A (en) Electrolytic manufacture of potassium persulphate
US512266A (en) Emile andreoli
US4101406A (en) Simplified electrolytic system