PL7669B1 - Processing of ores containing antimony, in particular tin ores with antimony content. - Google Patents
Processing of ores containing antimony, in particular tin ores with antimony content. Download PDFInfo
- Publication number
- PL7669B1 PL7669B1 PL7669A PL766926A PL7669B1 PL 7669 B1 PL7669 B1 PL 7669B1 PL 7669 A PL7669 A PL 7669A PL 766926 A PL766926 A PL 766926A PL 7669 B1 PL7669 B1 PL 7669B1
- Authority
- PL
- Poland
- Prior art keywords
- antimony
- ores
- ore
- processing
- particular tin
- Prior art date
Links
- 229910052787 antimony Inorganic materials 0.000 title claims description 13
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 title claims description 12
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 title claims description 5
- 238000000034 method Methods 0.000 claims description 9
- 239000002253 acid Substances 0.000 claims description 8
- 238000002386 leaching Methods 0.000 claims description 6
- 229910052742 iron Inorganic materials 0.000 claims description 5
- 229910052802 copper Inorganic materials 0.000 claims description 4
- 229910052785 arsenic Inorganic materials 0.000 claims description 3
- 229910052797 bismuth Inorganic materials 0.000 claims description 3
- 238000001354 calcination Methods 0.000 claims description 3
- 239000003638 chemical reducing agent Substances 0.000 claims description 3
- 229910052745 lead Inorganic materials 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 150000002739 metals Chemical class 0.000 claims description 2
- 230000001590 oxidative effect Effects 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 7
- 150000007513 acids Chemical class 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- AHBGXHAWSHTPOM-UHFFFAOYSA-N 1,3,2$l^{4},4$l^{4}-dioxadistibetane 2,4-dioxide Chemical compound O=[Sb]O[Sb](=O)=O AHBGXHAWSHTPOM-UHFFFAOYSA-N 0.000 description 1
- 229940058905 antimony compound for treatment of leishmaniasis and trypanosomiasis Drugs 0.000 description 1
- 150000001463 antimony compounds Chemical class 0.000 description 1
- 229910000411 antimony tetroxide Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 150000001879 copper Chemical class 0.000 description 1
- 229960002089 ferrous chloride Drugs 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000005324 oxide salts Chemical class 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 1
- 229910052683 pyrite Inorganic materials 0.000 description 1
- 239000011028 pyrite Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
Description
Jak wiadomo, oddzielanie antymonu od rud zawierajacych go jako domieszke, a szczególniej od cyny w rudach cynowych, zawierajacych antymon, jest bardzo uciaz¬ liwe.Szczególnie znaczne trudnosci napoty¬ ka sie jesli przed lugowaniem poddac ru¬ dy uprzednio prazeniu. Zwiazki antymo¬ nu przechodza wtedy w czterotlenek anty¬ monu Sb2 04, prawie nierozpuszczalny w kwasach.Przy prazeniu wiec dotychczas znanemi sposobami rud cynowych, zanieczyszczo¬ nych antymonem, i przy nastepujacem lu¬ gowaniu kwasami wieksza czesc antymonu pozostawala w nierozpuszczonej pozostalo¬ sci, zawierajacej cyne.Wynalazek niniejszy w ten sposób roz¬ wiazuje problem oddzielania antymonu, ie rude przed lub podczas lugowania podda¬ je sie redukcji.Mozna np. rude prazyc w tym celu z do¬ datkiem substancji redukujacej, np. wegla drzewnego i t. d. Jezeli potem przedsie¬ wziac lugowanie stezonemi kwasami, to w pozostalosci po lugowaniu zostanie znikoma pzesc antymonu, który prawie calkowicie przechodzi do roztworu.Mozna tez proces prowadzic inaczej, a mianowicie lugowac rude kwasem z dodat-kiem soli pódtlenkowych np, soli zelaza¬ wych, miedzianych i innych. W ten spo¬ sób udaje sie prawie calkowicie usunac z rud antymon.Jezeli do lugowania rudy stosowac kwas solny z siarczanem zelazawym, lub kwa¬ sny roztwór chlorku zelazawego, wtedy o- prócz antymonu prawie calkowicie prze¬ chodza do roztworu miedz, bizmut, arsen i zelazo oraz wieksza czesc olowiu. Obrobio¬ na w ten (Sposób rude mozna poddac reduk¬ cji w piecu plomiennym bez uprzedniego prazenia chlorujacego, majacego na celu usuniecie z niej Cu, Bi, As, Pb i Fe. Jedynie przy wiekszych ilosciach zelaza, jak przy pirycie wzglednie bialym pirycie niklowym (Arsenkies) korzystne jest stosowanie na¬ stepnie prazenia utleniajacego. Otrzymywa¬ nie poszczególnych metali z lugu Wzgled¬ nie rudy odbywa sie sposobami znanemi. PL PLAs is known, the separation of antimony from ores containing it as an admixture, and more particularly from tin in tin ores containing antimony, is very difficult. Particularly significant difficulties arise if the pipes are pre-calcined with prolonged leaching. The antimony compounds are then converted to antimony tetroxide Sb2 04, which is almost insoluble in acids. Therefore, when calcined by previously known methods of tin ores, contaminated with antimony, and with the subsequent leaching with acids, most of the antimony remained in an undissolved residue, The present invention thus solves the problem of antimony separation, so that the ore is reduced before or during leaching. For example, the ore may be ironed for this purpose with the addition of a reducing substance, e.g. charcoal, and then If you undertake leaching with moderate acids, the residue after leaching will leave a negligible amount of antimony, which will almost completely go into solution. You can also conduct the process differently, i.e. leach the red acid with the addition of oxide salts, e.g. iron, copper and copper salts. other. In this way, it is possible to almost completely remove antimony from the ores. If hydrochloric acid with ferrous sulfate or an acid solution of ferrous chloride is used to leach the ore, then apart from antimony almost completely goes into the solution of copper, bismuth, arsenic and iron, and most of the lead. Processed in this way (The ore process can be reduced in a flare furnace without first chlorinating calcining to remove Cu, Bi, As, Pb and Fe from it. Only with higher amounts of iron, as in the case of a relatively white nickel pyrite. (Arsenkies), it is preferable to apply the oxidative calcination stepwise. Obtaining individual metals from the slurry. The ore is obtained by methods known in the art.
Claims (4)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL7669B1 true PL7669B1 (en) | 1927-07-30 |
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