[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

US1186937A - Electrolytic apparatus. - Google Patents

Electrolytic apparatus. Download PDF

Info

Publication number
US1186937A
US1186937A US79297313A US1913792973A US1186937A US 1186937 A US1186937 A US 1186937A US 79297313 A US79297313 A US 79297313A US 1913792973 A US1913792973 A US 1913792973A US 1186937 A US1186937 A US 1186937A
Authority
US
United States
Prior art keywords
salt
collector
metal
electrolytic apparatus
receptacle
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
Application number
US79297313A
Inventor
Johannes Pfleger
Friedrich Ott
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.)
Roessler and Hasslacher Chemical Co
Original Assignee
Roessler and Hasslacher Chemical Co
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 Roessler and Hasslacher Chemical Co filed Critical Roessler and Hasslacher Chemical Co
Priority to US79297313A priority Critical patent/US1186937A/en
Application granted granted Critical
Publication of US1186937A publication Critical patent/US1186937A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/005Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells of cells for the electrolysis of melts

Definitions

  • the electrolyte reaches somewhat below the rim of vessel A and leavesample space between anode and receptacle 4 into,which the chlorin gas escapes.
  • The. outside of the receptacle 4, which is exposed to said chlorin gas, is covered with a layer 5, thus protecting Inside receptacle 4 the level of the electrolyte is somewhat higher than outside, owing to the low specific, gravity of the metal 6 as obtained by the process.
  • the chlorin gas generated escapes" through pipe 7.
  • the metal obtained by the electrolysis may be removed in any of the well known ways,
  • the salt or mixture of salts is applied as a protective coat to the outside. of the -collector-by dipping the same, closed below by a detachable bottom, into the fused salt and removing it again quickly from the same, there may also be added to the salt such materials which with the prevailing working conditions are indifferent to the electrolytic products. It is not necessary that. the insulating layer be perfectly solidi or the drainage of said fied, as viscid homogeneous coats may also provide sufficient protection.
  • the change'of physical state consisting in the transformation of the salt layer from the solid to the yiscid state or vice versa as well as the maintenance of the viscid state is effected in the simplest way byconducting off the re quired quantitiesof heat from the collector.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Description

.I. PFLEGER & F. OTT.
ELECTROLYTIC APPARATUS.
APPLICATION FILED ocr. 2. 191a.
1,186,937. T v Patented June 13, 191
- UNITED J'OHANNES IBFLEGER AND FRIEDRICH OTT, OF FRANKFORT-O N THE-MAIN, GERMANY,
ASSIGNOBS TO ROESSLER- AND HASSLACHER CHEMICAL COMPANY, YORK,
N. Y., A CORPORATION OF NEW YORK.
ELECTROLYTIC APPARATUS.
Specification of Letters Patent. 7
Patented June 13, 1916.
Application filed October 2, 1913. Serial No. 792,973.
To all whom it may concern Be it known that we, JOHANNES PFLEGER and FRIEDRICH OTT, subjects of the Emperor of Germany, and 'bothresidents of Frankfort-on-the--Main, -Germany, have invented certain new and useful Improvements in Electrolytic Apparatus, of which the following is a specification.
This invention relates to an improvement in electrolytic apparatus for the production of alkali metal, such as metallic sodium, from molten alkali haloids, such as sodium chlorid, and it refers particularly to the protection of an essential part of the apparatus against the harmful action of products generated in the process, such as chlorin gas for instance.
In a copending application filed June 16, 1913, Serial No. 774,039, wehave shown how to make the well known apparatus of Castner a. universal apparatus for the electrolytic production of alkali metal and to i use said apparatus especially for the utiliza- I such as sodlum tion of alkali-haloids, by protecting the outer surfaceof -the collector of the 'generated alkali metal by a material resistant to the action of the, products generated'at the anode;
We have found that one may use advantageously for the protection of the collector a solidified or homogenous layer of salt,
. such as sodium c'hlorid, or a mixture of salts",
chlo'rid and potassium chlorid, resistant to the products generated by the electrolysis.
In order to constantly maintain the protecting layer it is advisable in some cases to continuously or from time to time conduct off some heat from the metal collector. This is simply effected by partly constructing the collector as a-hollow cylinder, through which a cold gas or liquid current of an adequatestrength can be passed.
For the better understanding of ourinvention reference is made to the accompanying drawing, which represents a sectional elevation of a convenientform of apparatus for carrying our invention into effect.
The apparatus comprises a receptacle A, of iron or any suitable material, which serves as a container for the electrolyte as well as for the electrodes with the other appurtenances necessary thereto. The cathode 1, of lI'OIl or any other suitable material,
formed of a salt or mixture of salts,
receptacle 4' against the chlorin.
is entered preferably from below through the bottom of A. and extends upward into the vessel from which it. is suitably insulated. -The anode 2,preferably made of carcathode 1. The electrodes 1 and 2 are separated by a wire screen 3 which is connected with an iron receptacle/1, theupper end of which is closed by a lid.-
The electrolyte reaches somewhat below the rim of vessel A and leavesample space between anode and receptacle 4 into,which the chlorin gas escapes. The. outside of the receptacle 4, which is exposed to said chlorin gas, is covered with a layer 5, thus protecting Inside receptacle 4 the level of the electrolyte is somewhat higher than outside, owing to the low specific, gravity of the metal 6 as obtained by the process. The chlorin gas generated escapes" through pipe 7. The metal obtained by the electrolysis may be removed in any of the well known ways,
. either by dippin same out or by providing a contrivance metal.
The salt or mixture of salts is applied as a protective coat to the outside. of the -collector-by dipping the same, closed below by a detachable bottom, into the fused salt and removing it again quickly from the same, there may also be added to the salt such materials which with the prevailing working conditions are indifferent to the electrolytic products. It is not necessary that. the insulating layer be perfectly solidi or the drainage of said fied, as viscid homogeneous coats may also provide sufficient protection. The change'of physical state consisting in the transformation of the salt layer from the solid to the yiscid state or vice versa as well as the maintenance of the viscid state is effected in the simplest way byconducting off the re quired quantitiesof heat from the collector. The loss caused by-the quantities of heat thus conducted off in order to accomplish this purpose is practically of no importance. Conducting ofi'the heat oflers also the further advantages that the separated alkali metal iscooled off somewhat, which is de- .sirable in any case, whether one dips out the alkali metal or whether one drains same 0 Where we use the general expression salt in the claims, we mean to include both a mixture of salts as well as a single salt, and when we use the term solidified in the claims we mean to include the salt in such physical state that it will form a protective coating on the outer wall of the collector of the generated alkali metal,
whether the salt is actually solid or not.
We claim:
1. In an apparatus for the electrolysis of fused alkali salts, the combination with positive and negative electrodes having their working faces in close juxtaposition to each other, of'a gauze .or screen interposed between said electrodes, a superposed vessel or dome for receiving the separated metal Y and a halogen-resisting coating on the outer surface of said receiving vessel comprising solidified salt.
2:111 an apparatus for the electrolysis of fused alkali salts, the combination with positive and negative electrodes having their other, of a gauze or screen interposed between said electrodes, a superposed vessel or dome for receiving the separated metal and a chlorin-resisting coating on the outer surface of said receiving vessel comprising solidified sodium chlorid.
In testimony whereof we have signed our 1 names to this specification in the presence of two subscribing witnesses.
J OHANNES PFLEGER. FRIEDRICH OTT.
WVitnesses:
JEAN GRUND, CARL GRUND.
US79297313A 1913-10-02 1913-10-02 Electrolytic apparatus. Expired - Lifetime US1186937A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US79297313A US1186937A (en) 1913-10-02 1913-10-02 Electrolytic apparatus.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US79297313A US1186937A (en) 1913-10-02 1913-10-02 Electrolytic apparatus.

Publications (1)

Publication Number Publication Date
US1186937A true US1186937A (en) 1916-06-13

Family

ID=3254897

Family Applications (1)

Application Number Title Priority Date Filing Date
US79297313A Expired - Lifetime US1186937A (en) 1913-10-02 1913-10-02 Electrolytic apparatus.

Country Status (1)

Country Link
US (1) US1186937A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3453187A (en) * 1965-09-23 1969-07-01 Timax Associates Apparatus and process for reduction of hydrogen chloride

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3453187A (en) * 1965-09-23 1969-07-01 Timax Associates Apparatus and process for reduction of hydrogen chloride

Similar Documents

Publication Publication Date Title
US3607684A (en) Manufacture of alkali metals
US2234967A (en) Production of alkali metals
NO117861B (en)
US1186937A (en) Electrolytic apparatus.
NO115607B (en)
US3464900A (en) Production of aluminum and aluminum alloys from aluminum chloride
US1854684A (en) Production of aluminum
US510276A (en) Fused
US1567318A (en) Method of making metallic magnesium
US1197137A (en) Method of reducing metals.
US1186936A (en) Electrolytic apparatus.
US3201229A (en) Cesium production
US778270A (en) Production of metallic magnesium.
US2893935A (en) Electrolytic process for producing metallic titanium
US692688A (en) Apparatus for producing fluorin.
US2291644A (en) Apparatus for electrolysis of fused electrolytes
RU2756775C9 (en) Method and electrochemical cell for synthesising an electrolyte for producing rhenium
GB865712A (en) Improvements in or relating to a process and apparatus for the electrolytic production of metallic titanium
US517001A (en) Nitric acid and metals from nitrates
US922079A (en) Cell for electrolytic or other purposes.
US1116865A (en) Process of producing alkali and alkaline-earth metals.
US735464A (en) Electrolytic diaphragm.
US527848A (en) Process of reducing aluminium
US1882525A (en) Process for the electrolytic production of metals of the alkalis or alkaline earths
US715625A (en) Process of obtaining metallic aluminium or other metals by electrolysis.