DE525687C - Extraction of tin-containing fly dust from tin-containing ores and hut products with the formation of tin sulfide - Google Patents
Extraction of tin-containing fly dust from tin-containing ores and hut products with the formation of tin sulfideInfo
- Publication number
- DE525687C DE525687C DEK95289D DEK0095289D DE525687C DE 525687 C DE525687 C DE 525687C DE K95289 D DEK95289 D DE K95289D DE K0095289 D DEK0095289 D DE K0095289D DE 525687 C DE525687 C DE 525687C
- Authority
- DE
- Germany
- Prior art keywords
- tin
- sulfide
- formation
- batch
- extraction
- 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
Links
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
- C22B25/00—Obtaining tin
- C22B25/02—Obtaining tin by dry processes
-
- 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
- C22B25/00—Obtaining tin
-
- 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
- C22B25/00—Obtaining tin
- C22B25/06—Obtaining tin from scrap, especially tin scrap
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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
Gewinnung eines zinnhaltigen Flugstaubes aus zinnhaltigen Erzen und Hüttenprodukten unter Bildung von Zinnsulfid Die Erfindung betrifft ein Verfahren zur Gewinnung eines zinnhaltigen Flugstaubes aus zinnhaltigen Erzen und Hüttenprodukten unter Bildung von Zinnsulfid. Auf diesem Gebiete sind bereits verschiedene Vorschläge gemacht worden. «Neuerdings hat man vorgeschlagen, das Zinnsulfid dadurch zu bilden, daß über das metallhaltige Gut bei erhöhter Temperatur ein reduzierendes schwefelhaltiges Gasgemisch geleitet und die dabei verflüchtigte Metallschwefelverbindung verdichtet wird.Extraction of tin-containing fly ash from tin-containing ores and Metallurgical products with the formation of tin sulfide The invention relates to a method for the extraction of tin-containing fly ash from tin-containing ores and metallurgical products with the formation of tin sulfide. Various proposals have already been made in this area been made. «It has recently been suggested that tin sulfide be formed by that over the metal-containing material at elevated temperature a reducing sulfur-containing Gas mixture passed and the volatilized metal-sulfur compound is compressed will.
Gegenüber den bekannten Verfahren besteht die Erfindung darin, daß das Zinnsulfid, das entweder in der Charge enthalten ist oder infolge Vorhandenseins oder durch Zuschlag schwefelhaltiger Stoffe während des Prozesses innerhalb der Schicht gebildet wird, aus der Charge heraus als solches verflüchtigt wird, wobei innerhalb der Charge und, soweit möglich, auch an der Oberfläche der Schicht reduzierende Bedingungen eingehalten werden.Compared to the known method, the invention consists in that the tin sulfide, either in the batch or as a result of its presence or by adding sulfur-containing substances during the process within the Layer is formed, is volatilized out of the batch as such, wherein within the batch and, as far as possible, also on the surface of the layer Conditions are met.
Das Verfahren kann im kontinuierlichen Betrieb in einem direkt beheizten Drehofen ausgeführt werden. Falls eine Zugabe von Schwefel erforderlich ist, kann dieser in Form von Metallsulfid, z. 1i. Pyrit, Schwefelkies o. dgl., zugeschlagen «-erden. Durch Einhalten von reduzierenden Bedingungen innerhalb der Charge wird in dieser und auch unmittelbar an der Oberfläche derselben eine Oxvdation des Sulfides und damit eine Röstung des Stannosulfides vermieden. Die übrige Atmosphäre des Ofens kann hierbei eine oxydierende sein, denn es ist nicht erforderlich, daß auch in der Atmosphäre des Ofens reduzierende Bedingungen herrschen. Ist die Atmosphäre eine oxydierende, so kann das Zinnsulfid sofort bei dem Austritt aus der Charge verbrannt werden. Die Konzentration des Zinnsulfiddampfes in und über der Charge ist dann nur sehr gering, so daß die Umsetzung schnell und vollständig erfolgt. Die Vorteile des Verfahrens sollen an folgendem Ausführungsbeispiel gezeigt werden.The process can run continuously in a directly heated Rotary kiln are run. If an addition of sulfur is required, can this in the form of metal sulfide, e.g. 1i. Pyrite, pebbles or the like, slammed "-earth. By observing reducing conditions within the batch in this, and also immediately on the surface, an oxidation of the sulphide and thus avoids roasting of the stannous sulfide. The rest of the atmosphere in the oven can be an oxidizing one, because it is not necessary that in the atmosphere of the furnace is reduced. Is the atmosphere an oxidizing one, the tin sulphide can be released immediately upon leaving the batch to be burned. The concentration of tin sulfide vapor in and above the batch is then only very low, so that the implementation takes place quickly and completely. The advantages of the method are to be shown in the following exemplary embodiment.
Es wurde aus einer zinnhaltigen Schlacke etwa 1o °,!o Sn im Großbetrieb bei Zusatz von 8 "/o Pyrit und zo °/o feinem Abfallbrennstoff und bei einem Verbrauch von ; 0,/. Kohlenstaub in der Flammenbeheizung eine Zinnverflüchtigung von 96 bis 97 ° , im Durchschnitt der längeren Betriebsperiode erreicht.It was made from a tin-containing slag about 1o °, o Sn in large company with the addition of 8 "/ o pyrite and zo ° / o fine waste fuel and with a consumption of;!. 0, / pulverized coal in the burner heating a Zinnverflüchtigung 96-97 °, achieved on average over the longer operating period.
Wie schon oben gesagt, wird das Verfahren zweckmäßig in einem direkt beheizten Drehofen im kontinuierlichen Betrieb ausgeübt. Die-Brennstoffausnutzung bei der direkten Beheizung ist wesentlich vorteilhafter als bei der indirekten Wärmezufuhr, die früher bei bekannten Verfahren vorgeschlagen war. .As said above, the procedure is expedient in a direct way heated rotary kiln exercised in continuous operation. Die-fuel economy with direct heating is much more advantageous than with indirect heat supply, previously suggested in known methods. .
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEK95289D DE525687C (en) | 1925-08-08 | 1925-08-08 | Extraction of tin-containing fly dust from tin-containing ores and hut products with the formation of tin sulfide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEK95289D DE525687C (en) | 1925-08-08 | 1925-08-08 | Extraction of tin-containing fly dust from tin-containing ores and hut products with the formation of tin sulfide |
Publications (1)
Publication Number | Publication Date |
---|---|
DE525687C true DE525687C (en) | 1931-05-28 |
Family
ID=7238096
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEK95289D Expired DE525687C (en) | 1925-08-08 | 1925-08-08 | Extraction of tin-containing fly dust from tin-containing ores and hut products with the formation of tin sulfide |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE525687C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2501721A1 (en) * | 1981-03-13 | 1982-09-17 | Samim Soc Azionaria Minero Met | METHOD AND APPARATUS FOR CONCENTRATING NON-FERROUS METALS SUCH AS ANTIMONY AND TIN BY VOLATILIZATION FROM RESPECTIVE ORES OR BYPRODUCTS, AND PROCESS FOR OBTAINING ANTIMONY AND TIN IN THE METAL STATE |
-
1925
- 1925-08-08 DE DEK95289D patent/DE525687C/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2501721A1 (en) * | 1981-03-13 | 1982-09-17 | Samim Soc Azionaria Minero Met | METHOD AND APPARATUS FOR CONCENTRATING NON-FERROUS METALS SUCH AS ANTIMONY AND TIN BY VOLATILIZATION FROM RESPECTIVE ORES OR BYPRODUCTS, AND PROCESS FOR OBTAINING ANTIMONY AND TIN IN THE METAL STATE |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE525687C (en) | Extraction of tin-containing fly dust from tin-containing ores and hut products with the formation of tin sulfide | |
EP0033021B1 (en) | Process for the direct reduction in a rotary furnace of matter that contains iron oxide | |
DE635115C (en) | Process for obtaining elemental sulfur by melting pyrite | |
DE452784C (en) | Extraction of zinc from oxide ores | |
DE494454C (en) | Extraction of zinc oxide from sulfidic ores or from hut products converted into sulfidic form, etc. like. by blowing | |
DE356532C (en) | Process for treating metals in material containing metal | |
DE171215C (en) | ||
DE250773C (en) | ||
DE359775C (en) | Process for the production of ore briquettes that are durable in the blast furnace | |
DE580166C (en) | Process for the enrichment of germanium | |
DE753119C (en) | Process for the production of sodium silicate from soda ash | |
DE473016C (en) | Process for the extraction of volatilizable metals from ores, hut products and residues of all kinds | |
DE587458C (en) | Process for the extraction of metals such as tin, lead, antimony, bismuth or their alloys from sulphidic ores or hut products | |
DE680520C (en) | Process for the removal of arsenic from Huettenmaennischen intermediate and waste products | |
DE429938C (en) | Process for processing complex ores and hut products | |
DE463857C (en) | Processing of complex ores and intermediate products | |
DE312935C (en) | ||
DE492697C (en) | Processing of sulphide ores and hut products | |
DE583380C (en) | Process and device for pyrite melting | |
DE460797C (en) | Process for the refining of zinc-containing products and mixer ores in the iron blast furnace | |
DE840441C (en) | Process for the extraction of nickel and copper from sulphides containing nickel and copper | |
DE475115C (en) | Extraction of volatile metals from sulfidic ores, hut products and residues of all kinds | |
DE10716C (en) | Process for the preparation of gold and silver from ores containing sulfur, antimony and arsenic by annealing them in a stream of hydrogen to sublimate arsenic, roasting the residue containing sulfur copper and antimony compounds, extracting copper oxide and copper sulfate with sulfuric acid, the antimony from the remaining residues with hydrochloric acid and extraction of the silver and gold from the residue by the wet route (sulphatisation of the silver, amalgamation) or by the dry route by leading | |
DE625149C (en) | Process for roasting sulfidic ores | |
DE542973C (en) | Process for the treatment of carbonaceous residues from volatilization processes in rotary tube furnaces |