US1254531A - Method or process of smelting zinc. - Google Patents
Method or process of smelting zinc. Download PDFInfo
- Publication number
- US1254531A US1254531A US7572316A US7572316A US1254531A US 1254531 A US1254531 A US 1254531A US 7572316 A US7572316 A US 7572316A US 7572316 A US7572316 A US 7572316A US 1254531 A US1254531 A US 1254531A
- Authority
- US
- United States
- Prior art keywords
- zinc
- furnace
- hypochlorite
- chlorin
- blue powder
- 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
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title description 29
- 238000000034 method Methods 0.000 title description 25
- 239000011701 zinc Substances 0.000 title description 21
- 229910052725 zinc Inorganic materials 0.000 title description 18
- 238000003723 Smelting Methods 0.000 title description 5
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 14
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 10
- 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 10
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 229910002804 graphite Inorganic materials 0.000 description 4
- 239000010439 graphite Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- OXCRJCXSFXJLFS-UHFFFAOYSA-N zinc;dihypochlorite Chemical compound [Zn+2].Cl[O-].Cl[O-] OXCRJCXSFXJLFS-UHFFFAOYSA-N 0.000 description 3
- RNWHGQJWIACOKP-UHFFFAOYSA-N zinc;oxygen(2-) Chemical compound [O-2].[Zn+2] RNWHGQJWIACOKP-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- XSOKHXFFCGXDJZ-UHFFFAOYSA-N telluride(2-) Chemical compound [Te-2] XSOKHXFFCGXDJZ-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B13/00—Obtaining lead
- C22B13/04—Obtaining lead by wet processes
Definitions
- This invention relates to a method or process of separating pure metallic zinc from its ores and, more particularly speaking has reference to the electrolytical treatment of the so-called blue powder which consists essentially of metallic zinc commingled with zinc oxid.
- one object of the present invention resides in devising a method or process by means of which zinc may be smelted in an electric furnace and which eliminates the main difficulty heretofore attendant upon processes of this class wherein the zinc is va orized in the furnace and upon being con ensed the greater proportion of it can only be recovered in a finely divided or pulverulent form technically known as blue powder and which consists essentially of metallic zinc and zinc oxid.
- this invention has for another object, the treatment of the blue powder in subsequent commercial steps to obtain, by a Slhgle process, the pure marketable metallic ZlIlC.
- the apparatus illustrated in the single figure of the drawing is typical of one of many devices which may be constructed for practising the present invention.
- the apparatus comprises a furnace A preferably of fire brick and having a bottom 1, side walls 2 which may be covered on the interior with fire clay or other refractory material, and a dome shaped top 3.
- a door opening 4 is provided which is normally closed by a door 5.
- the bottom 1 of the furnace is formed similar to the side walls 2 and is provided with an iron plate 7 on the interior surface thereof for purposes to be hereinafter described.
- a tubular member 8 projecting through an aperture in the dome shaped top 3-of the furnace is a tubular member 8, preferably of graphite, and the outer end of which connects, as shown, ing to the bottom of a receiver 10 from the top of which into the reaction zone of the furnace A.
- a heating element'l2 which may be in the form of a blast burner if desired and is adapted to raise the temperature of the interior of the furnace to 500 or 600 C. if desired.
- a wire 13 connects the positive pole of a battery or current source B with the graphite tubular member 8 through the agency of the binding post 6011 said member thus forming one electrode of the furnace, whereas a similar wire 14 connects the iron plate 7 with the negative pole of the battery or current source B thus forming the other electrode of the furnace A.
- the electric current is then started and the furnace A is heated, either by the electric current passing through the resistance bath of zinc chlorid and zinc hypochlorite, or by the heating element 12 or by both to a temperature of from 500 to 600 C. in order to keep any metallic zinc present and the :hlorid and hypochlorite in a liquid condiion.
- a necessary step in the process is to fuse the zinc chlorid and hypochlorite at a temperature of 500 to 600 C.
- the blue powder may, if desired, be briqueted with a suitable binding material and used for the anode in an electrolytic cell, in which case the cathode will be an iron plate and upon the start of the electric current the electrolysis of the zinc will take place and electrolytic deposition of the zinc on the cathode will be the result.
- the blue powder, briquet'ed or otherwise may be directly used in electroplating iron. The molten metal in whichever method is employed, may be removed through an opening in the side wall of the furnace closed by a plug 15.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
I. PARTANEN.
METHOD 0R PROCESS OF S'MELTING zmc.
APPLICATION FILED FEB. 2. I916.
Patented Jan 22,1918.
E E D Y T o I: R H T m C E R L G B INVENTOH S E S S E N W W ATTORNEY ISAK PAJRTANEN, 0F TELLURIJDE, COLORADO.
METHOD 0R PROCESS OF SMEL'IIN G ZINE).
Specification ofLetters Patent.
Patented Jan. 22, IQI.
Application filed February 2, 1916. Serial Ito. 75,723.
To all whom it may concern."
Be it known that I, ISAK PARTANEN, a subject of the Emperor of Russia, having declared my intention of becoming a citizen of the United States, residing at Telluride, in the county of San Miguel and State of Colorado, have invented certain new and useful Improvements in Methods or Processes of Smelting Zinc, of which the following is a specification.
This invention relates to a method or process of separating pure metallic zinc from its ores and, more particularly speaking has reference to the electrolytical treatment of the so-called blue powder which consists essentially of metallic zinc commingled with zinc oxid.
Therefore, one object of the present invention resides in devising a method or process by means of which zinc may be smelted in an electric furnace and which eliminates the main difficulty heretofore attendant upon processes of this class wherein the zinc is va orized in the furnace and upon being con ensed the greater proportion of it can only be recovered in a finely divided or pulverulent form technically known as blue powder and which consists essentially of metallic zinc and zinc oxid.
Therefore, since the treatment of the complex ores of zinc to the point where the zinc is obtained in a blue powder form is well own and is easily carried on in a practical manner, this invention has for another object, the treatment of the blue powder in subsequent commercial steps to obtain, by a Slhgle process, the pure marketable metallic ZlIlC.
With the above and other objects in View, will now proceed to describe the present method or process in connection with the apparatus illustrated in the accompanying rawing wherein:
The apparatus illustrated in the single figure of the drawing is typical of one of many devices which may be constructed for practising the present invention.
In detail:
The apparatus, as herein illustrated, comprises a furnace A preferably of fire brick and having a bottom 1, side walls 2 which may be covered on the interior with fire clay or other refractory material, and a dome shaped top 3. In one side a door opening 4 is provided which is normally closed by a door 5. The bottom 1 of the furnace is formed similar to the side walls 2 and is provided with an iron plate 7 on the interior surface thereof for purposes to be hereinafter described. Also, projecting through an aperture in the dome shaped top 3-of the furnace is a tubular member 8, preferably of graphite, and the outer end of which connects, as shown, ing to the bottom of a receiver 10 from the top of which into the reaction zone of the furnace A. Beneath the bottom 7 of the furnace is located a heating element'l2 which may be in the form of a blast burner if desired and is adapted to raise the temperature of the interior of the furnace to 500 or 600 C. if desired. A wire 13 connects the positive pole of a battery or current source B with the graphite tubular member 8 through the agency of the binding post 6011 said member thus forming one electrode of the furnace, whereas a similar wire 14 connects the iron plate 7 with the negative pole of the battery or current source B thus forming the other electrode of the furnace A.
The blue powder obtained from the complex ores and perhaps containing moisture is placed within the furnace A and a supply of free or nascent chlorin passed in intimate contact therewith. Thus the free zinc and zinc oxid react with the chlorin to form zinc chlorid and following reactions occurring:
The electric current is then started and the furnace A is heated, either by the electric current passing through the resistance bath of zinc chlorid and zinc hypochlorite, or by the heating element 12 or by both to a temperature of from 500 to 600 C. in order to keep any metallic zinc present and the :hlorid and hypochlorite in a liquid condiion.
The action of the current decomposes or breaks down the zinc chlorid and zinc hypochlorite since electrolytid decomposition takes place due to the fact that the graphite member 8 forms an anode and the iron plate 7 forms a cathode. The result is that the anions, which in this instance are free or nascent chlorin, pass out through the tubular member at the top of the furnace and the cations, which in this instance are pure metallic zinc, collect at the cathode.
a gas conduit 11 leads backzinc hypochlorite, the
with a gas conduit 9 lead-- ZnCl -l-electric current -Zn+2Cl. Zn (0C1) }electric current=Zn+2OCL The (OCl) radical is unstable under the conditions prevailing in the furnace and breaks down or decomposes into free chlorin and oxygen, the latter element combining to a great extent with the carbon or graphite of the anode and thus producing an oxid of carbon having no effect on the continuation of the electrolysis taking place within the furnace and having no effect on the reactions by which the zinc chlorid and zinc hypochlorite are formed.
It is to be noted that a necessary step in the process is to fuse the zinc chlorid and hypochlorite at a temperature of 500 to 600 C.
Instead of pursuing the above method or process, specifically the blue powder may, if desired, be briqueted with a suitable binding material and used for the anode in an electrolytic cell, in which case the cathode will be an iron plate and upon the start of the electric current the electrolysis of the zinc will take place and electrolytic deposition of the zinc on the cathode will be the result. Thus pure zinc in a commercial form is likewise obtained. Also the blue powder, briquet'ed or otherwise, may be directly used in electroplating iron. The molten metal in whichever method is employed, may be removed through an opening in the side wall of the furnace closed by a plug 15.
While, in the foregoing, I have outlined specific steps of the process or method hereinbefore described, it is nevertheless to be understood that in practice, such practical variations may be resorted to as fall within the scope of the invention as defined in the appended claims.
I claim:
1. The method of electrolytically smelting zinc, which consists in chloridizing blue powder with chlorin, fusing the zinc chlorid and hypochlorite thus produced, and then electrolyzing the said zinc chlorid and hypochlorite to separate the pure metal.
2. The method of electrolytically smelting zinc, which consists in chloridizing blue powder with chlorin in the presence of moisture, fusing the zinc chlorid and hypochlorite thus produced, and then electrolyzingthe same to separate the pure metal.
3. The method of electrolytically smelting zinc which consists in chloridizing the blue powder with chlorin in the presence of moisture, fusing the zinc chlorid and hypochlorite thus produced to free pure metal and nascent chlorin, withdrawing the pure metal and chlorin replenishing the supply of blue powder, and then reintroducing the nascent chlorin previously freed.
In testimony whereof I aiiix my signature in presence of two witnesses.
' ISAK PARTANEN. Witnesses: ISAAC NENALA,
JACOB WmsULA.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US7572316A US1254531A (en) | 1916-02-02 | 1916-02-02 | Method or process of smelting zinc. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US7572316A US1254531A (en) | 1916-02-02 | 1916-02-02 | Method or process of smelting zinc. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1254531A true US1254531A (en) | 1918-01-22 |
Family
ID=3322234
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US7572316A Expired - Lifetime US1254531A (en) | 1916-02-02 | 1916-02-02 | Method or process of smelting zinc. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1254531A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3368960A (en) * | 1961-02-21 | 1968-02-13 | Elektrokemisk As | Alumina reduction cell |
| US4168215A (en) * | 1978-03-09 | 1979-09-18 | Aluminum Company Of America | Situ cleaning of electrolytic cells |
-
1916
- 1916-02-02 US US7572316A patent/US1254531A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3368960A (en) * | 1961-02-21 | 1968-02-13 | Elektrokemisk As | Alumina reduction cell |
| US4168215A (en) * | 1978-03-09 | 1979-09-18 | Aluminum Company Of America | Situ cleaning of electrolytic cells |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Ling et al. | A review of the technologies for antimony recovery from refractory ores and metallurgical residues | |
| CN106381399B (en) | A method of recycling tellurium from high tellurium slag charge | |
| US2302604A (en) | Fused bath electrolytic production of ferrochromium | |
| CN101517129B (en) | Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes | |
| US5467365A (en) | Process for the recovery of lead arising especially from the active material of spent batteries, and electric furnace intended especially for the use of the process | |
| US1254531A (en) | Method or process of smelting zinc. | |
| CN117568624A (en) | Bismuth purification method | |
| JPS5836654B2 (en) | Method for producing lead from materials containing lead sulfide | |
| US2870071A (en) | Electrolytic production of titanium tetrahalides | |
| JP4198439B2 (en) | Consumable carbon anode for smelting titanium metal | |
| US20140116886A1 (en) | Method for extracting noble and non-ferrous metals from refractory raw materials | |
| US2384479A (en) | Process fob the production of | |
| US618575A (en) | Oiqrneys | |
| US881527A (en) | Process for treating complex cobalt ores and for refining cobalt from nickel, arsenical, and silver-bearing ores. | |
| US1634497A (en) | Metallurgical process | |
| CN107287441A (en) | A kind of method that bottom lead depth removes antimony | |
| US596458A (en) | Process of and apparatus for extracting metals from ores | |
| CN116005011B (en) | A method for preparing high-purity metallic vanadium | |
| US949003A (en) | Process of producing electrolytic copper. | |
| US3323910A (en) | Zinc recovery | |
| US1066787A (en) | Process of producing zinc from blue powder. | |
| US1647279A (en) | Process for recovering zinc oxide | |
| US1299559A (en) | Method of extracting and recovering molybdenum from its ores and concentrates. | |
| US489303A (en) | Process of manufacturing manganese and alloys of manganese free from carbon | |
| US1209835A (en) | Process of treating materials electrolytically. |