US1013511A - Process of producing pure zinc sulfid and thiosulfates. - Google Patents
Process of producing pure zinc sulfid and thiosulfates. Download PDFInfo
- Publication number
- US1013511A US1013511A US45317908A US1908453179A US1013511A US 1013511 A US1013511 A US 1013511A US 45317908 A US45317908 A US 45317908A US 1908453179 A US1908453179 A US 1908453179A US 1013511 A US1013511 A US 1013511A
- Authority
- US
- United States
- Prior art keywords
- zinc
- sulfid
- alkaline
- thiosulfates
- sulfur
- 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
- DRDVZXDWVBGGMH-UHFFFAOYSA-N zinc;sulfide Chemical compound [S-2].[Zn+2] DRDVZXDWVBGGMH-UHFFFAOYSA-N 0.000 title description 17
- 238000000034 method Methods 0.000 title description 12
- 150000004764 thiosulfuric acid derivatives Chemical class 0.000 title description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 14
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 13
- 229910052717 sulfur Inorganic materials 0.000 description 13
- 239000011593 sulfur Substances 0.000 description 13
- 239000000243 solution Substances 0.000 description 12
- 229910052725 zinc Inorganic materials 0.000 description 12
- 239000011701 zinc Substances 0.000 description 12
- 238000009835 boiling Methods 0.000 description 10
- 239000003513 alkali Substances 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 7
- 239000007788 liquid Substances 0.000 description 6
- 239000003518 caustics Substances 0.000 description 5
- 150000002739 metals Chemical class 0.000 description 5
- 239000002244 precipitate Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000012670 alkaline solution Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000009466 transformation Effects 0.000 description 3
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 2
- -1 blende Chemical compound 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- DHCDFWKWKRSZHF-UHFFFAOYSA-L thiosulfate(2-) Chemical compound [O-]S([S-])(=O)=O DHCDFWKWKRSZHF-UHFFFAOYSA-L 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910000010 zinc carbonate Inorganic materials 0.000 description 2
- RNWHGQJWIACOKP-UHFFFAOYSA-N zinc;oxygen(2-) Chemical compound [O-2].[Zn+2] RNWHGQJWIACOKP-UHFFFAOYSA-N 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 241001397173 Kali <angiosperm> Species 0.000 description 1
- FMRLDPWIRHBCCC-UHFFFAOYSA-L Zinc carbonate Chemical compound [Zn+2].[O-]C([O-])=O FMRLDPWIRHBCCC-UHFFFAOYSA-L 0.000 description 1
- CJOBVZJTOIVNNF-UHFFFAOYSA-N cadmium sulfide Chemical compound [Cd]=S CJOBVZJTOIVNNF-UHFFFAOYSA-N 0.000 description 1
- CFEAAQFZALKQPA-UHFFFAOYSA-N cadmium(2+);oxygen(2-) Chemical compound [O-2].[Cd+2] CFEAAQFZALKQPA-UHFFFAOYSA-N 0.000 description 1
- DQSNUOLMAKKASD-KUNOYEQWSA-N calamin Chemical compound C=1([C@H]2[C@]3(C)CCC4[C@@](C(C(=O)[C@H](O)[C@@]4(C)[C@]33O[C@@H]3C(=O)O2)C(C)(C)O)(C)[C@@H](O)CC(=O)OC)C=COC=1 DQSNUOLMAKKASD-KUNOYEQWSA-N 0.000 description 1
- DQSNUOLMAKKASD-UHFFFAOYSA-N calamin Natural products COC(=O)CC(O)C1(C)C2CCC3(C)C(OC(=O)C4OC34C2(C)C(O)C(=O)C1C(C)(C)O)c5cocc5 DQSNUOLMAKKASD-UHFFFAOYSA-N 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 235000004416 zinc carbonate Nutrition 0.000 description 1
- 239000011667 zinc carbonate Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G9/00—Compounds of zinc
- C01G9/02—Oxides; Hydroxides
Definitions
- This invention relates to an improved process for preparing zinc sulfid and alkali thiosulfates.
- the zinc sulfid obtained by this method is ery bulky, and is in a sort of collodial form; it can .be filtered only with great difliculty, and cannot be washed easily.
- the precipitation is not an immediate one, it is the result of a series of progressive transformations terminating finally in the production of the sulfid desired, moreover, it is completed only after long boiling.
- the same-solutions are precipitated by means of an alkaline sulfid prepared in advance, it is well known that in such conditions the precipitation is immediate and complete.
- This process is applicable to carbonates and compounds of other metals of the zinc group.
- the compound of ;metal and-al kali reacts then on thenascentfsulfid, and
- the precipitates obtained by this process are in the form of microscopic grains of great density, the Washing and drying operations become very easy, so that it is possible to obtain pure products of unctuousness equal to that of talc, in all 'cases in which the ordinary processes give merely gelatinous collodial precipitates which it is impossible to wash completely.
- Alkaline liquids used for the transformation of oxids of ores intometallic sulfids can be utilized a great number of'times, until the contents of alkaline thiosulfate which is formed as a by-product'owing to the long contact with the air becomes so great that it is advisable to eifcct its crystallization.
- cadmium oxid, carbonate or acetate may be employed in order to obtain in the same manner cadmium sulfid.
- Alkaline liquid used for the transformation of oxids or ores into unctuous sulfids can be utilized a great number of times, until the contents of alkaline thiosulfate which is formed as a byproduct, owing to the long contact with the air, become so greatthat it is advisable to effect its crystallizations.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
PIERRE PIPEREAUT AND ANTONY VILA, 0F PARIS, FRANCE.
PROCESS OF PRODUCING PURE ZINC SULFID AND TI-IIOSULFATES.
No Drawing.
Specification of Letters Patent.
Application filed September 15, 1908.
Patented J an. 2, 1912.
Serial No. 453,179.
" To all whom it may concern:
Be it known that we, PIERRE PIPEREAUT and ANTONY VILA, chemical engineers, citizens of the Republic of France, residing at 13 Avenue des Gobelins, Paris, in the Department of Seine, in the Republic of France, have invented certain new and us ful Improvements in Processes of Producing Pure Zinc Sulfid and Thiosulfates, for which we have obtained a patent in Belgium, No.
202,686, dated September 19, 1907, and applied for a patent in Germany, dated November 29, 1907; and we do hereby declare the following to be a full, clear, and, exact description of the invention, such as will enable others skilled in the art to which it appertains to make and use the same.
This invention relates to an improved process for preparing zinc sulfid and alkali thiosulfates.
It is old to produce zinc sulfid by causing alkaline sulfids to lixiviate with alkaline solution of zinc. The zinc sulfid obtained by this method is ery bulky, and is in a sort of collodial form; it can .be filtered only with great difliculty, and cannot be washed easily.
We have found that in the case of zinc, it
is suflicient to take ores of zinc, blende, calamin, smithsonite, Broken Hill ore, Greensbit ore, etc., and roast them in order to obtain an oxid or roasted product and to subject them to the action of a caustic alkaline lye such as soda. The decanted clear solution is then boiled, and then pulverized sulfur is added to it in the required quantity and suf' ficient to convert all metals dissolved, except that which is desired to recover, into insoluble sulfids, which are first precipitated as impurities. After the separation of these impurities, to the solution is then added, in small amounts, sufficient sulfur to convert the metal remaining in solution-into sulfid. Alkaline sulfid in nascent state is thereby produced.
This process difi'ers entirely from the action of alkaline sulfids, previously manufactured, on alkaline solutions of metals.
In the process according to this invention, the precipitation is not an immediate one, it is the result of a series of progressive transformations terminating finally in the production of the sulfid desired, moreover, it is completed only after long boiling. On the contrary, when the same-solutions are precipitated by means of an alkaline sulfid prepared in advance, it is well known that in such conditions the precipitation is immediate and complete. It has been found that zinc sulfid can be obtained in an easily filterable granular state, if one does not heat the alkaline solutions of zinc with already formed, alkaline sulfide, but if one heats these alkaline solutions of zinc, with the sulfur under the conditions described the al ka-' line sulfid in a nascent state, reacts with the zincates.
This process is applicable to carbonates and compounds of other metals of the zinc group. The compound of ;metal and-al kali reacts then on thenascentfsulfid, and
the reaction once having eh started, continues gradually, as in the case of zinc.
The precipitates obtained by this process are in the form of microscopic grains of great density, the Washing and drying operations become very easy, so that it is possible to obtain pure products of unctuousness equal to that of talc, in all 'cases in which the ordinary processes give merely gelatinous collodial precipitates which it is impossible to wash completely.
. Alkaline liquids used for the transformation of oxids of ores intometallic sulfids, can be utilized a great number of'times, until the contents of alkaline thiosulfate which is formed as a by-product'owing to the long contact with the air becomes so great that it is advisable to eifcct its crystallization.
If we are examining the example given for zinc sulfid, we find the well known equations It is Well known that if sulfur is added to a pure boiling alkaline liquor, there are hydrated sulfids formed after the quantities taking part in the reaction: Na S,9H O (KircherAnnaZ der Ph. t. XXXl, p. 339). Na,S,5H O and Na S ,5I-I O ('Bottger- Arm, 0h. Pkg s. Liebig223, 535-1884). Na,S .6H O (Schone, Ann. Ph. 0h. Pogg.
.131", 386-1867).' Na S and Na S, (Bloxa. J. Chem. Sec. 77, 7531900). There is also sodium thiosulfate formed S O Na ,5H O.
If these hydrated sulfids are added by themselves to a solution of alkaline zincate, there is immediately formed a precipitate of Z1110 sulfid.
I In the operation described, the sulfur is introduced' into the boiling alkaline s0lu-' boiling liquid looses slowly its yellow color vand produces a fine white powder.
advisable to replace a small fraction of the and is quite colorless when the reaction is finished.
- The following equation is given by way of example:
This compound, in contact with ZnO Na w1ll soon dissociate and give:
(nascent) We use for a quantity of 100 kgs. of molten ore, containing about 30 kgs. of metallic zinc, 80 kgs. ofcaustic soda diluted in 60 liters of water; the whole is heated in an apparatus of iron plate, or other iron apparatus. We heat to ebullition for 6 hours at 130-1et0 C.; after cooling we add water to form 100 liters of solution. After 12 hours, 90 liters of clear liquid can be decanted. To this liquor, while boiling we add a small quantity of pulverized sulfur after 3 hours boiling the colored sulfids are precipitated, they are separated; and to the decanted and purified liquor, we add 10 kgs. of pulverized sulfur, and we boil throughout 4 hours to finish the reaction. The zinc sulfid obtained by this method is washed and dried It is alkaline lye after each operation.
The operation is carried out in the following way: A solution of zinc, oxid in caustic alkali, for instance, NaOH, is made at first; this solution is kept boiling and the quantity of sulfur'necessary to form zinc sulfid is added while boiling. At first, the
sulfur dissolves without glving any pre cipitate; after a certain time of heating there is found a granular zinc sulfid pre cipitate, which settles very well to the bot tom and can easily be filtered and washed. Instead of Zinc oXid dissolved in alkali one can use also a solution of zinc carbonate in caustic alkali solutions.
Instead of zinc oxid or carbonate, cadmium oxid, carbonate or acetate may be employed in order to obtain in the same manner cadmium sulfid. Alkaline liquid used for the transformation of oxids or ores into unctuous sulfids, can be utilized a great number of times, until the contents of alkaline thiosulfate which is formed as a byproduct, owing to the long contact with the air, become so greatthat it is advisable to effect its crystallizations.
We claim: i
1. The process for treating zinc sulfid ore to recover zinc sulfid in a'granular form,
which consists in lixiviating the ore with caustic alkali solution thereby forming alkali zincate, heating to boiling, adding sufficient free sulfur to precipitate the metals other than zinc, in the form of sulfids, and separating the same from the solution prior to the precipitation of the zinc sulfid and then adding, in small amounts, sufficient free sulfur to precipitate the zinc present,
while keeping the liquid hot.
2. The process for treating zinc sulfid ore to recover zinc sulfid in a granular form, which consists in lixiviating the ore with caustic alkali solutionthereby forming alkali zincate, heating to boiling, adding sufficient free sulfur to precipitate the metals other than zinc, in the form of sulfide, separating the same from the solution prior to the precipitation of the zinc sulfid and then adding, in small amounts, suflicient free sulfur to precipitate the zinc present while keeping the liquid hot, and filtering to remove the zinc sulfid. I
In testimony whereof we our signatures.
' PIERRE PIPEREAUT.
ANTONY VILA. In the presence of-- THEODORE REDIG, HERMANN LUTHER.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US45317908A US1013511A (en) | 1908-09-15 | 1908-09-15 | Process of producing pure zinc sulfid and thiosulfates. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US45317908A US1013511A (en) | 1908-09-15 | 1908-09-15 | Process of producing pure zinc sulfid and thiosulfates. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1013511A true US1013511A (en) | 1912-01-02 |
Family
ID=3081819
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US45317908A Expired - Lifetime US1013511A (en) | 1908-09-15 | 1908-09-15 | Process of producing pure zinc sulfid and thiosulfates. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1013511A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3088803A (en) * | 1958-03-11 | 1963-05-07 | Sherritt Gordon Mines Ltd | Method of separating metal values from ammoniacal solutions |
| US3427126A (en) * | 1963-07-01 | 1969-02-11 | Livio Cambi | Preparation of water-insoluble sulphides |
| US4282191A (en) * | 1980-07-25 | 1981-08-04 | Reynolds Metals Company | Zinc removal from aluminate solutions |
| US8524177B2 (en) | 2011-09-09 | 2013-09-03 | Canadus Chemical LLC | Process for purifying zinc oxide |
-
1908
- 1908-09-15 US US45317908A patent/US1013511A/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3088803A (en) * | 1958-03-11 | 1963-05-07 | Sherritt Gordon Mines Ltd | Method of separating metal values from ammoniacal solutions |
| US3427126A (en) * | 1963-07-01 | 1969-02-11 | Livio Cambi | Preparation of water-insoluble sulphides |
| US4282191A (en) * | 1980-07-25 | 1981-08-04 | Reynolds Metals Company | Zinc removal from aluminate solutions |
| US8524177B2 (en) | 2011-09-09 | 2013-09-03 | Canadus Chemical LLC | Process for purifying zinc oxide |
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