US483652A - Christopher james - Google Patents
Christopher james Download PDFInfo
- Publication number
- US483652A US483652A US483652DA US483652A US 483652 A US483652 A US 483652A US 483652D A US483652D A US 483652DA US 483652 A US483652 A US 483652A
- Authority
- US
- United States
- Prior art keywords
- zinc
- oxide
- furnace
- ores
- sulphur
- 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 description 27
- 229910052725 zinc Inorganic materials 0.000 description 27
- 239000011701 zinc Substances 0.000 description 27
- 238000000034 method Methods 0.000 description 11
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 6
- 239000005864 Sulphur Substances 0.000 description 6
- 239000003245 coal Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 238000006722 reduction reaction Methods 0.000 description 4
- 238000001354 calcination Methods 0.000 description 3
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 150000003568 thioethers Chemical class 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 241000005139 Lycium andersonii Species 0.000 description 1
- 229910000635 Spelter Inorganic materials 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
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
- C22B19/00—Obtaining zinc or zinc oxide
- C22B19/04—Obtaining zinc by distilling
Definitions
- This invention relates to an improved method of or process for producing metallic zinc from ores or compounds containing the same, and has for its object the diminution of the usual known calcining operations, the utilization of sulphur to assist or eiiect reduction, the employment of reverberatory or gas furnaces instead of the costly and troublesome retort-fu rnaces hitherto used, the greater percentage of metallic zinc recovered from the ore, and the better collection of the zinc in a distinct condenser, avoidingthe present heavy losses through cracked retorts, imperfect clay connections, and Waste of metal in the retortrefuse.
- Enormous losses occur through the cracking and breaking of the clay retorts, and the process is generally extravagent in labor, coal, and zinc.
- the resultant zinc would be volatilize'd by the high temperature of the furnace and, is conducted into a separate condensing-chamber surrounded by a water-jacket casing or partly filled with tubes, through which the zinc-gas passes, the tubes being surrounded by water. In the chamber or tubes the zinc is condggged and is then ladled outready'fortifi market.
- Aprocess for the treatment of zinc ores consisting of mixing any natural or other oxide of zinc with sulphur or sulphides of any metal, subjecting the same to a melting heat in a
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
UNITED STATES PATENT OFFICE.
CHRISTOPHER JAMES, OF SXVANSEA, ENGLAND.
PROCESS OF REDUCING ZINC.
.SPEGIFICATION forming part of Letters Patent No. 483,652, dated October 4, 1892.
Application filed December 28,1891. $erial No. 416,370. (No specimens.) Patented in England July 7,1891, No.11,563,' in Belgium August 17,1891,N0.95,768; in Spain September 23, 1891,N0.1Z,373, and in France November 16,1891, No. 215,113-
To all whom it may concern.-
Be it known that I, CHRISTOPHER JAMES, residing at Swansea, Great Britain, have invented an Improved Method or Process for the Production of Zinc or Spelter from Ores or Compounds Containing the Same, (which has been patented to me under No.11,563 and dated July '7, 1891, in Great Britain and Ireland; also, in Belgium under No. 95,768 and dated August 17,1891; in Spain under No. 12,373 and dated September 23, 1891, and in France under No. 215,113 and dated November 16, 1891,) of which the following is a specification.
This invention relates to an improved method of or process for producing metallic zinc from ores or compounds containing the same, and has for its object the diminution of the usual known calcining operations, the utilization of sulphur to assist or eiiect reduction, the employment of reverberatory or gas furnaces instead of the costly and troublesome retort-fu rnaces hitherto used, the greater percentage of metallic zinc recovered from the ore, and the better collection of the zinc in a distinct condenser, avoidingthe present heavy losses through cracked retorts, imperfect clay connections, and Waste of metal in the retortrefuse. In the ordinary methods now in use zinc ores are calcined till all the zinc present either as carbonate or sulphide is changed to an oxide. This is then mixed with coal or other carbonaceous matter, placed in retorts, a large number of which are arranged in the same furnace, and subjected to a great heat. The oxide of zinc formed by the calcination is reduced by the coal added to the charge as expressed by the equation duced by the coal, and so much zinc is left in the retort-refuse that ores containing a large percentage of zinc cannotbeprofitably worked.
Enormous losses occur through the cracking and breaking of the clay retorts, and the process is generally extravagent in labor, coal, and zinc.
In my present process for the reduction of the zinc, instead of producing an oxide of zinc from the blend by calcination, as described in a companion application, I take any natural or other oxide of zinc and melt the same in a neutral or slightly-reducing reverberatory or refinery furnace with sulphur, sulphide of zinc, or a sulphide of other metal, such as sulphide of iron, (iron pyrites.) The proportion of the said zinc oxide and sulphur or sulphides would be such that the oxygen of the oxide and the sulphur would combine entirely to form 80,,
reducing the zinc to its metallic form, thus:
The resultant zinc would be volatilize'd by the high temperature of the furnace and, is conducted into a separate condensing-chamber surrounded by a water-jacket casing or partly filled with tubes, through which the zinc-gas passes, the tubes being surrounded by water. In the chamber or tubes the zinc is condggged and is then ladled outready'fortifi market.
One greatsgperioi'ity of this process arises from the collection and condensation of the zinc being effected in a large, distinct, and easily-accessible chamber or in an apparatus equally open to frequent examination, so that no loss of zinc takes place through leakage, while the small amount of oxide of zinc which may be formed by any free oxygen which can pass into the furnace I collect in suitable flues and chambers, to be again used as calcined zinc ores. The expense of working such a furnace will be very small compared to the ordinary retort-furnace, the repairs much less, while the labor and loss of time caused by the breaking and consequent changing of damaged retorts are entirely avoided.
By my above method of reduction ores containing less than ten per cent. of zinc can be profitably Worked in consequence of the decreased cost following the use to effect reduc tion of sulphur in lieu of coal, which latter is not only expensive itself, but renders the retort-refuse unfit for any after treatment for the recovery of other metals than zinc contained in the ore. By my method the refuse from the retorts or furnace will be in a better condition for further treatment; While Very nearly all the zinc originally present in the ore is driven oif and condensed. Having now described my invention, What 10 I claim is;-
Aprocess for the treatment of zinc ores, consisting of mixing any natural or other oxide of zinc with sulphur or sulphides of any metal, subjecting the same to a melting heat in a
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US483652A true US483652A (en) | 1892-10-04 |
Family
ID=2552502
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US483652D Expired - Lifetime US483652A (en) | Christopher james |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US483652A (en) |
-
0
- US US483652D patent/US483652A/en not_active Expired - Lifetime
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