US1905460A - Process for converting into soluble salts lead and other metals contained in lead bearing ores - Google Patents
Process for converting into soluble salts lead and other metals contained in lead bearing ores Download PDFInfo
- Publication number
- US1905460A US1905460A US543819A US54381931A US1905460A US 1905460 A US1905460 A US 1905460A US 543819 A US543819 A US 543819A US 54381931 A US54381931 A US 54381931A US 1905460 A US1905460 A US 1905460A
- Authority
- US
- United States
- Prior art keywords
- lead
- converting
- roasting
- soluble salts
- metals
- 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
- 239000002184 metal Substances 0.000 title description 20
- 229910052751 metal Inorganic materials 0.000 title description 20
- 238000000034 method Methods 0.000 title description 15
- 150000002739 metals Chemical class 0.000 title description 14
- 150000003839 salts Chemical class 0.000 title description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 14
- 239000002253 acid Substances 0.000 description 10
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 8
- 229910052709 silver Inorganic materials 0.000 description 8
- 239000004332 silver Substances 0.000 description 8
- 229910021653 sulphate ion Inorganic materials 0.000 description 8
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 7
- 239000012267 brine Substances 0.000 description 7
- 229910052802 copper Inorganic materials 0.000 description 7
- 239000010949 copper Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 7
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 150000004763 sulfides Chemical class 0.000 description 6
- 229910052725 zinc Inorganic materials 0.000 description 6
- 239000011701 zinc Substances 0.000 description 6
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 5
- 235000011941 Tilia x europaea Nutrition 0.000 description 5
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000004571 lime Substances 0.000 description 5
- -1 salts metals Chemical class 0.000 description 5
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 4
- 150000001805 chlorine compounds Chemical class 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000019628 coolness Nutrition 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 229910052949 galena Inorganic materials 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- HWSZZLVAJGOAAY-UHFFFAOYSA-L lead(II) chloride Chemical compound Cl[Pb]Cl HWSZZLVAJGOAAY-UHFFFAOYSA-L 0.000 description 1
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 1
- 229910001510 metal chloride Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000135 prohibitive effect Effects 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C22B13/00—Obtaining lead
Definitions
- the process pursuant to this invention consists essentially in combining a chlorinating and sulphating roasting with a subsequent 39 treatment of the roasted material by means of a strong acid and thereafter by means of a brine.
- the first step consists in roasting the ore in the presence of both a small quantity of sulphate of lime and of a quantity of alkaline chloride or of earth-alkaline chloride which is very much less than the theoretical amount needed to chlorinate the whole of the lead.
- the ore is thereby very quickly rid of sulphur while furnishing a mixture of lead chloride and sulphate.
- the alkaline or earth-alkaline chloride used acts only as a catalytic agentin the desulphuriz- 5 ing of the lead.
- the process may be carried out in an ordinary roasting oven (Wedge or any other) with an air inlet and it requires a moderate temperature only.
- the roasted material, containing especialformed, is then treated by means of a small, quantity of strong acid, corresponding only to the quantity ofsulphide which has not been converted. by roasting.
- the chloride of lead thus obtained may be crystallized or be used forthe preparation of metallic lead or compounds thereof by any known method.
- I 7 u The process isexemplified by'the following illustration which does not restrict the scope of the invention: a
- the ore thus crushed is thereupon mixed with kg at least of chloride of sodium and 20 kg OaSO and the whole mass is roasted in an oxidizing atmosphere, the temperature being gradually raised to 460-490 0.
- the roasted ore is thereupon washed with 1 500 litres of water containing litres SOH at 53-55 B. This washing completes the conversion of the insoluble salts into soluble salts and the whole of the zinc, copper and other soluble metals may be eliminated by lixiviation and filtration.
- the remaining roasted ore which contains lead is then lixiviated with 4 cubic metres of a brine containing at least 250 grammes of NaClper litre and a total quantity of 6 litres of commercial HCl (22 B.).
- the solution The silver, for'example, may be precipitate ed in mother-lyes containing spongious lead obtained in any known manner. er-lyescontaining lead may be used afresh, to dissolve the lead contained in the roasted ore'of another cycle of operations.
- Process for converting intosoluble salts metals contained in lead bearing sulphide ores which consists in roasting said ores at a moderate temperature in the presence of a small quantity of sulphate of lime and of alkaline or earth-alkaline chlorid, then in treating the roasted material successively with a strong acid having the property'of converting into soluble salts the sulphides or traces of oxides left unconverted after -ro'asting, lixiviating the mass to separate the salts ofsoluble metals, such as those of zinc or copper, and treating with a brine to bring into solution the lead, the silver and the metals associated therewith.
- Process for converting'into soluble salts metals contained in lead bearing sulphide ores which consists in roasting said ores at a moderate temperature n the presence of a small quantity of sulphate of lime and of alkaline ore'arth 'alkaline chlorid, in treating the roasted material by sulphuric acid so as to convert intosulphates the sulfides or traces of oxides left unconverted after roasting, and
- ores which consists in roasting said ores at a moderate temperature in theipresence of a small quantity of sulphate of lime and of alkaline or earth-alkaline chlorid, then in treating the roasted material with hydro
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
Patented Apr. 25, 1933 PATENTTOF'FICE? UNITED STATES PAUL GAMICHON, OF PARIS, FRANCE PROCESS FOR CONVERTING INTO SOLUBLE SALTS LEAD ANI JOTHER METALS CONTAINED p IN LEAD BEARING ORES No Drawing. Application filed June 12, 1931, Serial No. 3,819, and in France Jiine 17, 1930.
The various known processes for roasting lead'bearing' sulphide ores with a view to their subsequent treatment by dissolution and wet meansmay be restricted to two:
5 (1) Sulphating roasting. In this case, the.
conversion of the sulphide ore is somewhat slow and difficult to carry out It is, furtherly sulphates and chlorides which have been more, always veryincomplete. y
(2) Chlorinating roasting. In this case, to be complete, the reaction requires a considerable excess of alkaline .or earth-alkaline chloride, the cost of which renders its use prohibitive. It requires a somewhathigh temperature (dark red at least) whereby considerable volatilization of theheavy metal chlorides is caused and especially those of lead. Furthermore, neither of these roasting processes can be used successfully to bring to the condition of soluble salts the whole of the metals contained in the ores. If roasting is continued too long or if too high a tempera ture is applied, oxides are formed, and sometimes even the metal itselfis reached and in all cases heavy losses are incurred due to the volatilization ofthe sulphate or chloride' The process pursuant to this invention consists essentially in combining a chlorinating and sulphating roasting with a subsequent 39 treatment of the roasted material by means of a strong acid and thereafter by means of a brine.
The first step consists in roasting the ore in the presence of both a small quantity of sulphate of lime and of a quantity of alkaline chloride or of earth-alkaline chloride which is very much less than the theoretical amount needed to chlorinate the whole of the lead. The ore is thereby very quickly rid of sulphur while furnishing a mixture of lead chloride and sulphate.
It would appear that, in point of fact, the alkaline or earth-alkaline chloride used acts only as a catalytic agentin the desulphuriz- 5 ing of the lead.
The process may be carried out in an ordinary roasting oven (Wedge or any other) with an air inlet and it requires a moderate temperature only.
The reaction so obtainedis much faster acid and more complete than is the case in roastng which is solely sulphating, notwithstand- 111g the small proportion of added chloride. By this means, furthermore, all formation of oxide (PhD) is practically avoided, which is impossible in the case of sulphating roasting.
The roasted material, containing especialformed, is then treated by means of a small, quantity of strong acid, corresponding only to the quantity ofsulphide which has not been converted. by roasting. t
Should the acid used be sulphuric acid, the traces of galena or of sulphides which have not been converted, together with the traces of oxidesyare converted into sulphates. V The sulphates of soluble metals (Zn, Cu, etc.) are easily separated by washing and their solutions may be treated subsequently byIone of the usual methods. n
place of sulphuric'acid, hydrochloric and other strong acids having the same properties may be used, with corresponding differences in results with respect to the salts obtained. u o
If the remainder of the roasted ore be thereafter washed hot with brine, the whole of the'lead and silver is recoveredas soluble chlorides, which is impossible with any of the known roasting processes.
The chloride of lead thus obtained may be crystallized or be used forthe preparation of metallic lead or compounds thereof by any known method. I 7 u The process isexemplified by'the following illustration which does not restrict the scope of the invention: a
1000 kg of ore is crushed, which contains as sulphides 300kg lead and 150-kg zinc, as well as 400 grams silver and 1500 grams copper, so that the whole is adapted to pass through a sieve of approximately 20 mesh.
The ore thus crushed is thereupon mixed with kg at least of chloride of sodium and 20 kg OaSO and the whole mass is roasted in an oxidizing atmosphere, the temperature being gradually raised to 460-490 0.
As soon as thistemperature is reached, reaction takes place almost immediately.
The roasted ore is thereupon washed with 1 500 litres of water containing litres SOH at 53-55 B. This washing completes the conversion of the insoluble salts into soluble salts and the whole of the zinc, copper and other soluble metals may be eliminated by lixiviation and filtration.
The remaining roasted ore which contains lead, is then lixiviated with 4 cubic metres of a brine containing at least 250 grammes of NaClper litre and a total quantity of 6 litres of commercial HCl (22 B.). The solution The silver, for'example, may be precipitate ed in mother-lyes containing spongious lead obtained in any known manner. er-lyescontaining lead may be used afresh, to dissolve the lead contained in the roasted ore'of another cycle of operations.
I claim:
1. Process for converting intosoluble salts metals contained in lead bearing sulphide ores, which consists in roasting said ores at a moderate temperature in the presence of a small quantity of sulphate of lime and of alkaline or earth-alkaline chlorid, then in treating the roasted material successively with a strong acid having the property'of converting into soluble salts the sulphides or traces of oxides left unconverted after -ro'asting, lixiviating the mass to separate the salts ofsoluble metals, such as those of zinc or copper, and treating with a brine to bring into solution the lead, the silver and the metals associated therewith.
2. Process for converting into soluble salts metals contained in lead bearing sulphide ores, whichconsists in'roasting said ores at a moderate temperature in the presence of a small quantity of sulphate oflime and of alkaline or earth-alkaline chlorid, then in treating the roasted material withsulphuric acid to convert into sulphates thesulfides or traces of oxides left unconverted after roasting, and in lixiviating the mass to separate the salts of soluble metals, such as those-of zinc or copper, and in treating with a brine to bring into solution the lead, the silver and the metals associated therewith.
3. Process for converting into soluble salts metals containedjin lead bearing sulphide The mothchloric acid to convert into chlorides the sulfides or traces of oxides left unconverted after roasting, and in lixiviating the mass to separate the salts of soluble metals, such as those of zinc or copper, and in treating with a brineto bring into solution the lead, the silver and the metals associated therewith.
, 4. Process for converting into soluble salts metals contained in lead bearing sulphide ores, which consists in roasting said ores at a moderate temperature in the presence of a 1 small quantity of sulphate of lime and of alkaline or earth-alkaline chlorid used in much smaller quantity than the theoretic amount required to chlorinate the, whole of the lead of the ore, then in treating the roasted material successively by a strong acid having the property of 'convertinginto soluble salts the sulphides or traces of oxides left unconverted after roasting, and then with a brine.
5. Process for converting'into soluble salts metals contained in lead bearing sulphide ores, which consists in roasting said ores at a moderate temperature n the presence of a small quantity of sulphate of lime and of alkaline ore'arth 'alkaline chlorid, in treating the roasted material by sulphuric acid so as to convert intosulphates the sulfides or traces of oxides left unconverted after roasting, and
in lixiviating the mass to separate the salts of soluble metals, such as those 'ofzinc or copper, and in treating with a brine to bring into solution the lead, the silver and the metals as sociated therewith, and finally in filtering the hot liquor obtained after precipitation of metals other than leadand silver and in cool ing said liquor for the crystallization of the chloride of lead.
In testimonywhereof I have signed this specification. PAUL GAMIOHON.
ores, which consists in roasting said ores at a moderate temperature in theipresence of a small quantity of sulphate of lime and of alkaline or earth-alkaline chlorid, then in treating the roasted material with hydro
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1905460X | 1930-06-17 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1905460A true US1905460A (en) | 1933-04-25 |
Family
ID=9682123
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US543819A Expired - Lifetime US1905460A (en) | 1930-06-17 | 1931-06-12 | Process for converting into soluble salts lead and other metals contained in lead bearing ores |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1905460A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4090871A (en) * | 1975-07-08 | 1978-05-23 | Societe Miniere Et Metallurgique De Penarroya | Process for the recovery and purification of germanium from zinc ores |
-
1931
- 1931-06-12 US US543819A patent/US1905460A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4090871A (en) * | 1975-07-08 | 1978-05-23 | Societe Miniere Et Metallurgique De Penarroya | Process for the recovery and purification of germanium from zinc ores |
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