US560518A - meyrueis - Google Patents

meyrueis Download PDF

Info

Publication number
US560518A
US560518A US560518DA US560518A US 560518 A US560518 A US 560518A US 560518D A US560518D A US 560518DA US 560518 A US560518 A US 560518A
Authority
US
United States
Prior art keywords
solution
sodium
cells
meyrueis
soda
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
Publication date
Application granted granted Critical
Publication of US560518A publication Critical patent/US560518A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B4/00Electrothermal treatment of ores or metallurgical products for obtaining metals or alloys

Definitions

  • IINDREW BGHMIAM PHOTOUI'HUJIRSNINII'WLQC.
  • the purpose of this invention is to provide a method of treating sodium chlorid so that various products may be obtained therefrom-namely, white lead, bicarbonate of soda, and chlorin.
  • Figure 1 is an elevational diagram of part of the apparatus.
  • Fig. 2 is a similar view, partly in section, of the remainder of the apparatus. tusnamely, the electrolyzing-cells-in section.
  • the sodium chlorid in solution in water is subjected to the electrolytic action of an electric current in a cell or series of cells X, divided by a porous diaphragm a, separating the electrolyte in which the anode dips from that in which the cathode is situated.
  • This series of cells X is shown in Fig.
  • a represents the poro us diaphragms in the form of closed vessels; 1) b b, the anodes; c c c, the cathodes; d d d, the metallic connections between the anodes and the cathodes of the series of cells; 6 e e, the pipes with thistle -tops receiving the solution for the cathodes in each cell and carrying said solution first to the bottom of'the cell.
  • f f f are the deliiery-pipes for the overplus of solution from the cells, the last of which empties into the pipe X, by which the'solu- 'tion is carried to vessel A for further treatspaces of the porous cells a a to together at their upper parts, the last porous cell communicating with the pipe X by which, as hereinafter described, the chlorin gas developed in the porous cells a is carried off.
  • h h h Fig. 3 shows part of the appararepresent the exterior cells of the battery or series X.
  • t' is the pipe supplying the last-mentioned electrolyte to the first thistle-tube e.
  • the former electrolyte is left at rest and consists of a solution of chlorid of sodium kept always concentrated and also acidified by addition of hydrochloric acid.
  • the latter electrolyte for the cathode is composed of a solution of chlorid of sodium more or less concentrated and is kept in movement.
  • the chlorin gas given off from the former solution when the electric current is passed through the battery is drawn off and serves for use, as hereinafter shown, while the second solution becomes constantly more and more saturated with hydrate of soda. It is this gradual enrichment of the solution with sodium hydrate and the faculty of drawing off the solution continuously or otherwise, just as it contains the desired percentage of sodium hydrate,
  • the apparatus is regulated to deliver a liquor having about one hundred and twenty grams of caustic soda in each liter of solution.
  • This liquid received as before in the vessel A, is run off continuously through pipe B to the vessel or boiler O, in which is the mechanical mixer D.
  • This boiler will have been previously partially filled with a charge of litharge.
  • a furnace E is placed under the boiler 0, since heat assists the solution of the litharge in the liquor.
  • This hot solution runs off continuously at the pipe F into carbonators or carbonating vessels G G, traversed by a current of carbonic acid.
  • the white lead being insoluble separates as a precipitate and may be removed by passing the solution through a filter-press.
  • the alkaline liqu or remaining is then similarlypassed through the carbonators K K.
  • the bicarbonate of soda then formed being almost insoluble in solution of the chlorid of soda also separates in the form of crystals, which may be separated from the mother liquor on evaporation.
  • the mother liquor is returned to the electrodialyzing apparatus X for use again.
  • the bicarbonate of soda can be transformed into the carbonate, if desired.
  • any further treatment the aforesaid electrodialyzing process produces chlorin suitable for bleaching, and a solution more or less concentrated of sodium hydrate suitable as a lye in many manufactures-for instance, in paper-mills and Wool and cloth Works.
  • I claim as my invention- The method of manufacturing chlorin, white lead, and bicarbonate of soda consistin g in exposing to an electric current an alkaline solution of chlorid of sodium circulating in negative cells and an acidulated solution of chlorid of sodium and hydrochloric acid at rest in positive cells, said negative and positive cells being separated from each other by porous diaphragms; drawing off the chlorin from said positive cells and the solution of enccof two Witnesses, this 1st day of July,

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Description

(No Model.) I 2Sheets-Sheet 1.
J. MEYRUEIS. TREATMENT OF SODIUM GHLORID.
"No. 560,518. Patented May 19, 1896.
IINDREW BGHMIAM. PHOTOUI'HUJIRSNINII'WLQC.
(1 10 ModeIT) 2 Sheet ;s-Sheet 2' v J. MEYRUEIS.
TREATMENT OF SODIUM GHLORID.
Patented May 19, 1896.
Uu M
ANDREW mnlhmnmo-ummwnsmumu.nc'
ATENT Fries.
.IULES MEYRUEIS, or PARIS, FRANCE.
TREATMENT QF SODIUM CHLORID.
SPECIFICATION forming part of Letters Patent No. 560,518, dated May 19, 1896. Application filed July 24, 1898. Serial No. 481,371. (No specimens.) Patented in France January 31,1893, No. 227,540.
To all whom it may concern.-
Be it known that I, J ULns MEYRUEIS, of the Oompagnie Electro-Chimique de St. Bron, a
citizen of the French Republic, and a resident of Paris, Department of the Seine, France, have invented a certain new and useful Improvement in the Treatment of Sodium Ohlorid for the Production of WVhite Lead, Soda, and Ohlorin, (for which a patent has been granted in France, No. 227,540, dated January 31, 1893,) of which the following is a specification.
The purpose of this invention is to provide a method of treating sodium chlorid so that various products may be obtained therefrom-namely, white lead, bicarbonate of soda, and chlorin.
Reference being made to the annexed drawings, Figure 1 is an elevational diagram of part of the apparatus. Fig. 2 is a similar view, partly in section, of the remainder of the apparatus. tusnamely, the electrolyzing-cells-in section.
According to the present invention the sodium chlorid in solution in water is subjected to the electrolytic action of an electric current in a cell or series of cells X, divided by a porous diaphragm a, separating the electrolyte in which the anode dips from that in which the cathode is situated. This series of cells X is shown in Fig. 3, in which, as aforesaid, a represents the poro us diaphragms in the form of closed vessels; 1) b b, the anodes; c c c, the cathodes; d d d, the metallic connections between the anodes and the cathodes of the series of cells; 6 e e, the pipes with thistle -tops receiving the solution for the cathodes in each cell and carrying said solution first to the bottom of'the cell.
f f f are the deliiery-pipes for the overplus of solution from the cells, the last of which empties into the pipe X, by which the'solu- 'tion is carried to vessel A for further treatspaces of the porous cells a a to together at their upper parts, the last porous cell communicating with the pipe X by which, as hereinafter described, the chlorin gas developed in the porous cells a is carried off. h h h Fig. 3 shows part of the appararepresent the exterior cells of the battery or series X.
t' is the pipe supplying the last-mentioned electrolyte to the first thistle-tube e. The former electrolyte is left at rest and consists of a solution of chlorid of sodium kept always concentrated and also acidified by addition of hydrochloric acid. The latter electrolyte for the cathode is composed of a solution of chlorid of sodium more or less concentrated and is kept in movement. The chlorin gas given off from the former solution when the electric current is passed through the battery is drawn off and serves for use, as hereinafter shown, while the second solution becomes constantly more and more saturated with hydrate of soda. It is this gradual enrichment of the solution with sodium hydrate and the faculty of drawing off the solution continuously or otherwise, just as it contains the desired percentage of sodium hydrate,
that enable the products before mentioned to be obtained.
The apparatus is regulated to deliver a liquor having about one hundred and twenty grams of caustic soda in each liter of solution. This liquid, received as before in the vessel A, is run off continuously through pipe B to the vessel or boiler O, in which is the mechanical mixer D. This boiler will have been previously partially filled with a charge of litharge. A furnace E is placed under the boiler 0, since heat assists the solution of the litharge in the liquor. This hot solution runs off continuously at the pipe F into carbonators or carbonating vessels G G, traversed by a current of carbonic acid. The white lead being insoluble separates as a precipitate and may be removed by passing the solution through a filter-press. The alkaline liqu or remaining is then similarlypassed through the carbonators K K. The bicarbonate of soda then formed being almost insoluble in solution of the chlorid of soda also separates in the form of crystals, which may be separated from the mother liquor on evaporation. The mother liquor is returned to the electrodialyzing apparatus X for use again. The bicarbonate of soda can be transformed into the carbonate, if desired.
\Vithout any further treatment the aforesaid electrodialyzing process produces chlorin suitable for bleaching, and a solution more or less concentrated of sodium hydrate suitable as a lye in many manufactures-for instance, in paper-mills and Wool and cloth Works.
I claim as my invention- The method of manufacturing chlorin, white lead, and bicarbonate of soda consistin g in exposing to an electric current an alkaline solution of chlorid of sodium circulating in negative cells and an acidulated solution of chlorid of sodium and hydrochloric acid at rest in positive cells, said negative and positive cells being separated from each other by porous diaphragms; drawing off the chlorin from said positive cells and the solution of enccof two Witnesses, this 1st day of July,
J ULES MEYRUEIS. \Vitnesses:
Rona. M. lloornn, ARTHUR Goon.
US560518D meyrueis Expired - Lifetime US560518A (en)

Publications (1)

Publication Number Publication Date
US560518A true US560518A (en) 1896-05-19

Family

ID=2629240

Family Applications (1)

Application Number Title Priority Date Filing Date
US560518D Expired - Lifetime US560518A (en) meyrueis

Country Status (1)

Country Link
US (1) US560518A (en)

Similar Documents

Publication Publication Date Title
KR840001427B1 (en) Method for producing chromic acid using 2 compartment electrolyzer and 3 compartment electrolyzer
GB1185507A (en) Improvements in or relating to Methods of and Device for Manufacturing Alkaline Chlorates, Notably Sodium Chlorate, by an Electrolytic Process.
JPH08512099A (en) Production of polysulfide by electrolysis of white liquor containing sulfide
JPS63247387A (en) Continuous production of sodium chlorate
CN105154910B (en) A kind of production technology of alkali
KR910001138B1 (en) Combined process for production of clorine dioxine and sodium hydroxide
US3883406A (en) Process for recovering electrolytically produced alkali metal chlorates
US3723266A (en) Catholyte recirculation in diaphragm chlor-alkali cells
US20040124094A1 (en) Process for producing alkali metal chlorate
EP0532535B2 (en) Electrochemical production of acid chlorate solutions
US4294815A (en) Process of producing chlorine dioxide and, if desired, chlorine
US4176168A (en) Process for producing chlorine dioxide
JP2024511822A (en) Method for producing high purity lithium hydroxide monohydrate
US1246099A (en) Process for the extraction of chlorin.
US3454478A (en) Electrolytically reducing halide impurity content of alkali metal dichromate solutions
US1126627A (en) Process for electrolyzing alkali-chlorid solution.
US802205A (en) Process of producing chlorates and bichromates.
US3407128A (en) Process for the manufacture of chlorine, sodium hydroxide and hydrogen by the electrolysis of sodium chloride in mercury cells
US3553088A (en) Method of producing alkali metal chlorate
US415644A (en) Georg keener
SE455706B (en) SET FOR PREPARATION OF ALKALIA METAL CHLORATE
RU2154125C1 (en) Sodium chlorate production process
US779705A (en) Method of treating alkaline solutions of chromate of soda.
US492003A (en) amaury de villardy de montlaur
US537179A (en) Electrolysis