US709482A - Process of eliminating the sulfur from sulfid ores. - Google Patents
Process of eliminating the sulfur from sulfid ores. Download PDFInfo
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- US709482A US709482A US4836801A US1901048368A US709482A US 709482 A US709482 A US 709482A US 4836801 A US4836801 A US 4836801A US 1901048368 A US1901048368 A US 1901048368A US 709482 A US709482 A US 709482A
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- US
- United States
- Prior art keywords
- sodium
- sulfid
- sulfur
- carbon
- ores
- 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.)
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- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title description 31
- 229910052717 sulfur Inorganic materials 0.000 title description 30
- 239000011593 sulfur Substances 0.000 title description 30
- 238000000034 method Methods 0.000 title description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 30
- 229910052799 carbon Inorganic materials 0.000 description 30
- 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 22
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 22
- 239000000203 mixture Substances 0.000 description 22
- 239000011734 sodium Substances 0.000 description 22
- 229910052708 sodium Inorganic materials 0.000 description 22
- 238000010438 heat treatment Methods 0.000 description 17
- 230000003647 oxidation Effects 0.000 description 14
- 238000007254 oxidation reaction Methods 0.000 description 14
- 230000008030 elimination Effects 0.000 description 13
- 238000003379 elimination reaction Methods 0.000 description 13
- 229910052742 iron Inorganic materials 0.000 description 11
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 8
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 5
- 229910052709 silver Inorganic materials 0.000 description 5
- 239000004332 silver Substances 0.000 description 5
- 159000000000 sodium salts Chemical class 0.000 description 5
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 4
- 229910052737 gold Inorganic materials 0.000 description 4
- 239000010931 gold Substances 0.000 description 4
- 229910052785 arsenic Inorganic materials 0.000 description 3
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 3
- 229910052714 tellurium Inorganic materials 0.000 description 3
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- 238000005267 amalgamation Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005660 chlorination reaction Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 235000009508 confectionery Nutrition 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Substances [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 2
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- MJLGNAGLHAQFHV-UHFFFAOYSA-N arsenopyrite Chemical compound [S-2].[Fe+3].[As-] MJLGNAGLHAQFHV-UHFFFAOYSA-N 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910052949 galena Inorganic materials 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229920001021 polysulfide Polymers 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/02—Roasting processes
Definitions
- the roasting period is reduced to a small fraction of the time hitherto required, and the sulfur is'either completely eliminated, if the process is perfect, or if not, left only in small quantities in the form of soluble or insoluble sulfates of the metals present, which will not interfere with subsequent extraction operations for gold or silver.
- the mixed mass may be placed in a layer a few inches deep upon a plate heated by a fire below, and a suitable cover should be placed over the plate to more or less exclude air.
- A indicates the plate
- B the fireplace below it
- O the cover
- the cover When the mass has become sufficiently heated, the cover may be removed and the mass raked oif and exposed to air and rabbled to allow of its oxidation, or it may be allowed to oxidize on the plate, or the preliminary heating might be effected in other forms of furnace in a neutral or reducing flame and subsequently oxidized, or the heating and oxidation may be carried on continuously.
- Powdered carbon equal to about one-fifth of the total sulfur present with the addition of a suitable sodium saltsay of dry sulfid of sodium (Na S)which shall be equivalent to about one-fifth of the weight of carbon, or, if a mother-liquor of sodium sulfid crystals be employed, a weight of this equal to half the carbon used.
- Na S dry sulfid of sodium
- This reaction has the further advantage that it can be used with great efficiencyin producing what is known as a chloridizing roast'.
- This operation is frequently employed in the treatment of ores which contain sulfid, antimonid, &c., of silver associated with other metallic sulfids. If such an ore be roasted in the ordinary way, with the addition of the requisite quantity of sodium chlorid, the silver is found in the form of chlorid at the end of the roasting operation. The degree of heat and the length of time, however, required under such cir-,
- the sodium chlorid required may be added before the commencement of the roast or at any stage prior to the final breaking up of the sulfates.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Patented Sept. 23,1902.-
. A. GUTENSUHN.
PROCESS OF ELIMINATING THESULFUR FROM SULFID ORES.
(Application filed Feb. 21, 1901.)
(No Model.)
umu. WASHINGTON n c UNITED STATES PATENT OFFICE.
ADOLPII GUTENSOIIN, OF LONDON, ENGLAND, ASSIGNOR TO SULPHUR ELIMINATION SYNDICATE, LIMITED, OF LONDON, ENGLAND.
PROCESSOF ELIMINATING THE SULFUR FROM SULFiD ORES.
SPECIFICATION forming partof Letters Patent No. 709,482, dated September 23, 1902.
Application filed February 21, 1901. Serial No. 48,368. (No specimens.)
To all whom it may concern/.-
&c.--and also from ores in which sulfids may be associated with arsenic, tellurium, or other volatile elements, or from artificial products, such as concentrates or mattes. Where arsenic, tellurium, &c., are present, the substances Will be eliminated with the sulfur. All methods hitherto used demand a prolonged roasting period and a consumption of a considerable proportion of fuel. Moreover, it is always a matter of extreme difficulty by such methods to eliminate the last portions of the sulfur and to obtain a dead or sweet roast. This difficulty is greater still when arsenic, antimony, or tellurium are present, also blende and galena. By this process these difficulties are either entirely avoided or greatly minimized. The roasting period is reduced to a small fraction of the time hitherto required, and the sulfur is'either completely eliminated, if the process is perfect, or if not, left only in small quantities in the form of soluble or insoluble sulfates of the metals present, which will not interfere with subsequent extraction operations for gold or silver.
The accompanying drawing shows a trans verse section of a furnace which may be employed.
According to this invention I mix suitablycrushed iron pyrites', or iron pyrites admixed with other sulfid ores, or sulfid ores without such admixture, with a certain proportion of similarly-powdered carbon or suitable carbonaceous material and add to the mixture or to the carbon, (gZJCr, beforehand a further suitable proportion of sodium sulfid, or a mixture of carbon and sodium sulfate, or sodium carbonate, or sodium hydroxid, or such other suitable salt of sodium, as by interaction with carbon and a metallic sulfid, shall be capable of producing during the first stage of the operation sul fid of sodium. The mixture is then exposed to a low heat-say approaching incipient redness-for a short time. This time will naturally vary according to the richness of the orein sulfur and to the fineness to which it has been ground,and may be from a few minutes. t0,say, half an hour, according to the circumstances of the case. Probably what takes place when the mixture of iron pyrites, sodium sulfid, and carbon are first heated is thatacertain amount of carbon disulfid is formed and also sodium polysulfid and the iron reduced to the state of monosulfid of iron. This may be expressed by the following equation:
(Note, x denoting an excess quantity.) The crystals of FeS thus become broken down and the FeS is left in a minutely-divided condition intimately mingled with finely-divided carbon, which keeps the heated mass in an open porous condition, through which air can freely penetrate. On removing the charge from the source of heat and exposing to air rabbling, if necessary-or by freely admitting air after this first stage of the operation oxidation proceeds with the greatest rapidity, partly by reason of the mass being already heated to a heat approaching incipient redness, partly by reason of its open porous condition, and partly because the carbon itself becomes oxidized and aids in further heating the mass. The mass becomes heated to a red heat, and the carbon and much of the sulfur are burned off, leaving the iron in the form of red oxid (Fe O and the sodium in the form of sulfate, which can readily be removed and allow of gold, silver, 850., being extracted by any suitable means, such as by chlorination, amalgamation, or by cynidation. This may be expressed by the following equation:
To heatthe mixed ore, carbon, and sulfid of sodium before exposing it to air, the mixed mass may be placed in a layer a few inches deep upon a plate heated by a fire below, and a suitable cover should be placed over the plate to more or less exclude air.
In the drawing, A indicates the plate, B the fireplace below it, and O the cover.
When the mass has become sufficiently heated, the cover may be removed and the mass raked oif and exposed to air and rabbled to allow of its oxidation, or it may be allowed to oxidize on the plate, or the preliminary heating might be effected in other forms of furnace in a neutral or reducing flame and subsequently oxidized, or the heating and oxidation may be carried on continuously.
I find that pyrites or mispickel charges which hitherto would have required a calcination period of many hours, even in some cases up to twenty-four hours, can when heated in the manner above described be freed from sulfur and brought to the state of a dead or sweet roast after a period of from, say, one hour to two hours in the furnace, the completion of the oxidation being effected by exposure to the open air.
In view of the wide variations in composition of the ores before mentioned it is not easy to give definite proportions of the materials to be used in every case; but I have found a useful admixture to be the following: Powdered carbon equal to about one-fifth of the total sulfur present with the addition of a suitable sodium saltsay of dry sulfid of sodium (Na S)which shall be equivalent to about one-fifth of the weight of carbon, or, if a mother-liquor of sodium sulfid crystals be employed, a weight of this equal to half the carbon used. After the reaction is complete the sodium will be found to be present as sodium sulfate, while the carbon has nearly or entirely disappeared. This reaction has the further advantage that it can be used with great efficiencyin producing what is known as a chloridizing roast'. This operation is frequently employed in the treatment of ores which contain sulfid, antimonid, &c., of silver associated with other metallic sulfids. If such an ore be roasted in the ordinary way, with the addition of the requisite quantity of sodium chlorid, the silver is found in the form of chlorid at the end of the roasting operation. The degree of heat and the length of time, however, required under such cir-,
cumstances give rise to considerable losses of the precious metals as volatilized chlorids, whereas the low temperature and the short period required by my method avoids these serious chloridizing losses. The sodium chlorid required may be added before the commencement of the roast or at any stage prior to the final breaking up of the sulfates.
I do not necessarily bind myself to the proportions given, as it will ,be evident that a certain minimum proportion of carbon is required even in ores very poor in sulfur, but state the above as an example of the admixture which I have found to be efficacious in the treatment of rich pyritic and arsenical gold ores and concentrates. The gold and silver can be extracted from the residues by any suitable means, such as by chlorination, amalgamation, cyanidation, &c.
What I claim is 1. The hereinbefore-described process for the elimination of sulfur from sulfid ores, consisting in crushing the ore, mixing it with carbon and a sodium salt which will yield sulfid of sodium when the mixture is heated, the amount of carbon added being largely in excess of the amount required to form the sulfid of sodium heating the mixture to a temperature approaching incipient redness, and then exposing it freely to air to elfect its oxidation and burn off all sulfur that is set free.
2. The hereinbefore-described process for the elimination of sulfur from sulfid ores, consisting in crushing the ore, mixing it with carbon and sodium sulfid, heating the mixture to a temperature approaching incipient redness, and then exposing it freely to air to effect its oxidation and burn off all sulfur that is set free.
3. The hereinbefore-described process for the elimination of sulfur from sulfid ores, consisting in crushing the ore, mixing it with crushed iron pyrites, carbon and a sodium salt which will yield sulfid of sodium when the mixture is heated, the amount of carbon added being largely in excess of the amount required to form the sulfid of sodium heating the mixture to a temperature approaching incipient redness, and then exposing it freely to air to efiect its oxidation and burn off all sulfur that is set free.
4. The hereinbefore-described process for the elimination of sulfur from sulfid ores, consisting incrushing the ore, mixing it with crushed iron pyrites, carbon and sodium sulfid, heating the mixture to a temperature approaching incipient redness, and then exposing it freely to air to efiect its oxidation and burn off all sulfur that is set free.
5. The hereinbefore-described process for the elimination of sulfurfrom sulfid ores, consistingin crushing the ore, mixing it with carbon, sodium chlorid and a sodium salt which will yield sulfid of sodium when the mixture is heated, the amount of carbon added being largely in excess of the amount required to form the sulfid of sodium, heating the mixture to a temperature approaching incipient redness, and then exposing it freely to air to effect its oxidation and burn off all sulfur that is set free.
6. The hereinbefore-described process for the elimination of sulfur from sulfid ores, consisting in crushing the ore, mixing it with carbon, sodium chlorid and sodium sulfid, heating the mixture to a temperature approaching incipient redness, and then exposing it freely to air to effect itsoxidation and burn oif all sulfur that is set free.
7. The hereinbefore-described process for the elimination of sulfurfrom sulfid ores, consisting in crushing the ore, mixing it with crushed iron pyrites, carbon, sodium chlorid and a sodium salt which will yield sulfid of sodium when themixture is heated, the amount of carbon added being largely in excess of:
the amount required to form the sulfid of sodium, heating the mixture to a temperature approaching incipient redness, and then exposing itfreely to air to eifect its oxidation and burn off all sulfur that is set free.
8. The hereinbefore-described process for the elimination of sulfur from sulfid ores, conassisting in crushing the ore, mixing it with a crushed iron pyrites, carbon, sodium, chlorid,
and sodium sulfid, heating the mixture to a temperature approaching incipient redness, andthen exposing it freely toair to effect its oxidation and burn off all sulfur that is set free. i
i i 9. The hereinhefore-described process for the elimination of sulfur from sulfid ores, consisting in crushing the ore, mixing it with care hon and a sodium salt which will yield sulfid of sodium when the mixture is heated, the amountof carbon added beinglargelyin excess of the amountrequired to form the sulfid of sodium, heating the mixture to a temperature approachingincipient redness,adding sodium chlorid during the heating, and then exposing it freely to air to effect its oxidation and burnoff all sulfur that is set free.
10. The hereinbeforedescribed process for the elimination of sulfurfrom sulfid ores, consisting in crushing the ore, mixing it with carbon and sodium sulfid, heating the mixture to a temperature approaching incipient redness, adding sodium chlorid during the heating, and then exposing it freely to air to effect its oxidation and burn off all sulfur that is set free.
11. The hereinbefore-described process for the elimination of sulfur from sulfid ores, consisting in crushing the ore, mixing it with crushed iron pyrites, carbon and a sodium saltwhich will yield sulfid of sodium when the mixture is heated, the amount of carbon added being largely in excess of the amount required to form the sulfid of sodium, heating the mixture to a temperatureapproaching incipient redness, adding sodium chlorid during the heating, and then exposing it freely to air to effect its oxidation and burn ofi all sulfur that is set free.
12. The hereinbefore-described process for the elimination of sulfur from sulfid ores, con-
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US4836801A US709482A (en) | 1901-02-21 | 1901-02-21 | Process of eliminating the sulfur from sulfid ores. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US4836801A US709482A (en) | 1901-02-21 | 1901-02-21 | Process of eliminating the sulfur from sulfid ores. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US709482A true US709482A (en) | 1902-09-23 |
Family
ID=2778008
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US4836801A Expired - Lifetime US709482A (en) | 1901-02-21 | 1901-02-21 | Process of eliminating the sulfur from sulfid ores. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US709482A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4497778A (en) * | 1981-04-06 | 1985-02-05 | University College Cardiff Consultants Limited | Microbial leaching of sulphide-containing ores |
-
1901
- 1901-02-21 US US4836801A patent/US709482A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4497778A (en) * | 1981-04-06 | 1985-02-05 | University College Cardiff Consultants Limited | Microbial leaching of sulphide-containing ores |
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