US480956A - Bernard moebius - Google Patents
Bernard moebius Download PDFInfo
- Publication number
- US480956A US480956A US480956DA US480956A US 480956 A US480956 A US 480956A US 480956D A US480956D A US 480956DA US 480956 A US480956 A US 480956A
- Authority
- US
- United States
- Prior art keywords
- retort
- bullion
- moebius
- bernard
- copper
- 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
- 229910052802 copper Inorganic materials 0.000 description 16
- 239000010949 copper Substances 0.000 description 16
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 16
- 238000000034 method Methods 0.000 description 16
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 14
- 229910052753 mercury Inorganic materials 0.000 description 14
- 229910000497 Amalgam Inorganic materials 0.000 description 10
- 239000010953 base metal Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 10
- 230000001590 oxidative Effects 0.000 description 10
- 239000002253 acid Substances 0.000 description 8
- 238000002386 leaching Methods 0.000 description 8
- 238000004821 distillation Methods 0.000 description 6
- 229910052709 silver Inorganic materials 0.000 description 6
- 239000004332 silver Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- YEXPOXQUZXUXJW-UHFFFAOYSA-N oxolead Chemical compound [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000010970 precious metal Substances 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 4
- 235000011149 sulphuric acid Nutrition 0.000 description 4
- 239000001117 sulphuric acid Substances 0.000 description 4
- 229910001018 Cast iron Inorganic materials 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 2
- 229910052787 antimony Inorganic materials 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000875 corresponding Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 239000002965 rope Substances 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-N sulfonic acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 2
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
- C22B21/00—Obtaining aluminium
- C22B21/0038—Obtaining aluminium by other processes
- C22B21/0053—Obtaining aluminium by other processes from other aluminium compounds
- C22B21/0061—Obtaining aluminium by other processes from other aluminium compounds using metals, e.g. Hg or Mn
Definitions
- Another method frequently used consists in melting and granulating the retorted bullion and heating the same in a reverberatory or roasting furnace, so as to oxidize the copper.
- the oxidation does not penetrate deep into the granules, but only affects the surface.
- the roasted material is treated with sulphuric acid, which dissolves the scale of oxide of copper, and the remaining part goes to the roasting-furnace again, and so on, until all of the copper is oxidized and dissolved.
- This method involves a great loss of time, labor, and fuel.
- the object of my invention is to have the base-bullion resulting from retorting in such a condition that the greater part of the copper is already oxidized, and therefore readily dissolved by acids without requiring any further roasting, and for this purpose, during and after retorting, I subject the heated mass to a comminuting action, While at the same time exposing it to the oxidizing action of a current of air, so as to obtain a nely-divided residue containing oxidized base metals, together with the precious metals, and which residue after leaching leaves a bullion sufficiently rich to be parted by any partingprocess.
- Figure 1 is a front View of the apparatus, and Fig. 2 a longitudinal section of the same in the plane at, Fig. l.
- the retort A is mounted in a suitable furnace, so as to be free to rotate.
- K is the fireplace, L the ash-pit, and M the chimney, of the furnace.
- the flange g is supported upon rollers 7L h, mounted in brackets secured to the furnace-plates.
- an extension B To the neck a of the retort is bolted an extension B, the flange c'of which is supported upon rollers j.
- the extension B of the neck ct is connected with a U shaped condenser-pipe D, the upper end of which is connected with the chimney by a pipe E. Draft through the retort may be increased when desired, by well-known means.
- the two vertical branches of the pipeD are cooled by water in vessels F F', the water entering near the bottom and leaving near the top.
- the lowest part of the condenser-pipe is provided with a small discharge-pipe L, formingatrap, so that the condensed mercury can run into a tank J, but preventing air passing into the condenser.
- My invention is not restricted to the use of the apparatus shown and described, since a great variety of apparatus may be designed for accomplishing the same result.
- I ⁇ produce the sulphurous acid by burningfsulphur in the usual manner vand drawing the' products of combustion by a lead-lined steamjet apparatus (exhauster and compressorlintol the leachingtanks containing the retorted bullion-powderand water.
- a lead-lined steamjet apparatus exhaust and compressorlintol the leachingtanks containing the retorted bullion-powderand water.
- thesulplrutrL ous acid is rapidly converted into sulphuric acidi,whichlrapidly dissolves the oxide ot copper, while forming with the oXideof leady a, sulphate which remains undjssolved with thef precious metals, but goes intoA thefslag when the bullionis melted;
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
(No Mode1.\
B. MOEBIUS.
PROCESS 0F TREATING BASE BULLION AMALGAM.
Patented Aug. 16, 1892.
INVENTR' mu Ev.
run Noms Penas co.. wmuwo UNITED STATES PATENT OFFICE.
BERNARD MOEBIUS, OF NEW YORK, N. Y.
PROCESS OF TREATING BAASEBULLIONAMALGAM.
SPECIFICATION forming part of Letters Patent No. 480,956, dated August 16, 1892. Application letl December 31, 1891. Serial No, 416,663. (No specimens.)
T all whom t may concern:
Be it known that I, BERNAEDhMoEBIUs, a citizen of the German Empire, having declared my intention to become a citizen of the United States, and a resident of New York, in the county and State of New York, have invented a new and useful Improvement in the Process of Treating Base-Bullion Amalgam, of which the following is a specication.
Heretofore the bullion resulting from retorting (distilling off the mercury) of the amalgam containing, besides silver and gold, a large percentage of copper and variable quantities of lead, antimony, tbc., has been refined by different more or less tedious and expensive methods, subject to great loss of silver ,by volatilization. The method most generally used consists in cupelling the bullion with lead, whereby the impurities-such as copper, &c.-go into the litharge, but with them also considerable silver. As the byproducts have to be worked over again, this method can only be employed at smelting and refining Works. Another method frequently used consists in melting and granulating the retorted bullion and heating the same in a reverberatory or roasting furnace, so as to oxidize the copper. The oxidation, however, does not penetrate deep into the granules, but only affects the surface. The roasted material is treated with sulphuric acid, which dissolves the scale of oxide of copper, and the remaining part goes to the roasting-furnace again, and so on, until all of the copper is oxidized and dissolved. This method involves a great loss of time, labor, and fuel.
The object of my invention is to have the base-bullion resulting from retorting in such a condition that the greater part of the copper is already oxidized, and therefore readily dissolved by acids without requiring any further roasting, and for this purpose, during and after retorting, I subject the heated mass to a comminuting action, While at the same time exposing it to the oxidizing action of a current of air, so as to obtain a nely-divided residue containing oxidized base metals, together with the precious metals, and which residue after leaching leaves a bullion sufficiently rich to be parted by any partingprocess.
In the annexed drawings I have shown an example of an apparatus for carrying out my process.
In the drawings, Figure 1 is a front View of the apparatus, and Fig. 2 a longitudinal section of the same in the plane at, Fig. l.
Similar letters refer to corresponding parts.
A is a cast-iron cylinder or retort with a flanged neck a. The front end of the retort is closed by a door Gr, having a hole ZJ in the center, which is closed by a screw-cap c. The door Gis bolted to a flange g of the retort and forms a stopper, having an extension d d e e, the cylindrical part CZ d of which is surrounded by asbestus rope or other suitable packing material. The air-spacefbetween the cover and its extension keeps the heat from the front part and also prevents the accumulation in front of the material to be treated.
^ The retort A is mounted in a suitable furnace, so as to be free to rotate. K is the lireplace, L the ash-pit, and M the chimney, of the furnace. The flange gis supported upon rollers 7L h, mounted in brackets secured to the furnace-plates. To the neck a of the retort is bolted an extension B, the flange c'of which is supported upon rollers j.
Slow rotary motion is imparted to the retort A by suitable means, such as the chain 7o, passing over a sprocket-flange Zon the retort and over a sprocket-Wheel 'm on driving-shaft n. Iron or stone balls H or other suitable bodies serve to comminute the material within the rotating retort.
By means of a stuffing-box O the extension B of the neck ct is connected with a U shaped condenser-pipe D, the upper end of which is connected with the chimney by a pipe E. Draft through the retort may be increased when desired, by well-known means. The two vertical branches of the pipeD are cooled by water in vessels F F', the water entering near the bottom and leaving near the top. The lowest part of the condenser-pipe is provided with a small discharge-pipe L, formingatrap, so that the condensed mercury can run into a tank J, but preventing air passing into the condenser.
My invention is not restricted to the use of the apparatus shown and described, since a great variety of apparatus may be designed for accomplishing the same result.
IOO
In carrying out my process I remove the door Gr and charge the retort with the amalgam in small lum-ps, togetherwith a number of balls H, and then replace the door G with the cap c screwed on, whereupon the cylinder is set in rotation and a good heat given. When distillation is fairly under way, I- remove the cap c, so as to allow atmospheric air to be drawn through the retort for the purpose of oxidizing the base metals. The mercury is condensed in the pipe D and flows through the pipe I into the tank J. This arrangement admits of the-close observationoi:`
the progress of distillation by the quantity of condensed mercury discharged through thepipe I. After distillation has ceased and a test sample of the retorted bullion showsthat the base metals are suiiiciently oxidized, yfiring is stopped, the door G removed,.andthe mass Withdrawn from the furnace.` thus obtained as a powder isi` leached inthe well-known manner with, diluted sulphumc acid which dissolves the oxideot copper as sulphate, which is used over again in the process of amalgamating. In remote locali-ties where sulphuric acid is expensive I use by preference sulphurous acid` for leaching. I` produce the sulphurous acid by burningfsulphur in the usual manner vand drawing the' products of combustion by a lead-lined steamjet apparatus (exhauster and compressorlintol the leachingtanks containing the retorted bullion-powderand water. In the presence of metallic oxides, air, and steam thesulplrutrL ous acid is rapidly converted into sulphuric acidi,whichlrapidly dissolves the oxide ot copper, while forming with the oXideof leady a, sulphate which remains undjssolved with thef precious metals, but goes intoA thefslag when the bullionis melted;
While by the ordinary retortingth'e resulting bullion is in lumps which are scarcelyoxii dized, by my processit is obtained as a powder because during the process the chargev is 'llhe bullion 1 dation, whereby the whole or the greater part of the base` metals is oxidized and prevented from agglomerating. Dierent means may be used for comminuting the mass in the distillin g apparatus, although a rotary retort and .balls are the simplest. For some material the rotation of the retort without balls willtsuiiiciently agitate the mass to prevent sticking together.
What I claim as my invention, and desire to secure by Letters Patent, is'- 1., The process of treating amalgam of the character specified, which consists in'charging the same into an apparatus for distilling o and collecting the mercury and subjecting lthe heated chargetoa comminuting action, Ywhile at the same time oxidizing the base metals by a. current of air.
2; Thev process ot" treating amalgamof` the :character specified, which consists in charging the same into an apparatus for distilling oit and collectingthe mercury, subjecting the 4at the same time oxidizing the base metals by a current of` air, and leaching the finely-divided residue, substantially as specified;
3. The process ot" treatingl amalgam of' the character specified, which consists inV charging the same intoan apparatus for distilling oft and collecting the mercury, subjectingthe at thesame time oxidizing the base metalsfby a current of air, and leaching the iinely-dividedresidue bysuilphuric acid; substantially as speciied.
In testimony that I claim the foregoingas my invention I' have signed my name, in pres- .encelof twowitnessesmhis 30th day of December, 1891. Y
BERNARD VMOEBIUS.
Witnesses:
A. FABER DU FAUR, J'osEBH ELIAS.
heated charge to a comminuting action, while heatedy chargeto a comminuting action, while subjected to a comminuting action and to oxi-
Publications (1)
Publication Number | Publication Date |
---|---|
US480956A true US480956A (en) | 1892-08-16 |
Family
ID=2549808
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US480956D Expired - Lifetime US480956A (en) | Bernard moebius |
Country Status (1)
Country | Link |
---|---|
US (1) | US480956A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110220983A1 (en) * | 2006-03-31 | 2011-09-15 | Semiconductor Energy Laboratory Co., Ltd. | Method for deleting data from nand type nonvolatile memory |
-
0
- US US480956D patent/US480956A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110220983A1 (en) * | 2006-03-31 | 2011-09-15 | Semiconductor Energy Laboratory Co., Ltd. | Method for deleting data from nand type nonvolatile memory |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US1386503A (en) | And milo w | |
US480956A (en) | Bernard moebius | |
US1396740A (en) | Process of treating complex zinc-lead ores | |
US748662A (en) | Beibl sebillot | |
US1103258A (en) | Process of manufacturing pure iron or manganese metal from pure or impure iron or manganese-metal oxids. | |
SE406929B (en) | PROCEDURE FOR THE MANUFACTURE OF IRON SULFID-CONTAINING RAILS | |
US486698A (en) | Louis clxment datimas | |
US475907A (en) | Process of refining silver sulphides | |
SE412766B (en) | PROCEDURE FOR THE MANUFACTURING AND REFINING OF RABLY FROM ARSENIC CONTRIBUTION | |
US589959A (en) | Process of treating copper sulfids | |
US1585344A (en) | Metallurgical apparatus | |
US1605641A (en) | Recovering metal | |
US2182129A (en) | Metallurgy | |
US553115A (en) | Reff galbraith | |
US683325A (en) | Extraction of precious metals from their ores. | |
US489460A (en) | Parker c | |
US739374A (en) | Process of treating refractory complex ores of gold and silver. | |
US607817A (en) | John armstrong | |
US543753A (en) | Peocess of and apparatus for separating metals | |
US1375002A (en) | Treatment of ores | |
US1114036A (en) | Metallurgy of zinc. | |
US841721A (en) | Process of treating ores. | |
US875578A (en) | Process of treating zinc and lead sulfid ores. | |
US1526910A (en) | Method of dezincing | |
US700311A (en) | Treatment of complex and refractory ores. |