US765000A - Process of making copper sulfate. - Google Patents
Process of making copper sulfate. Download PDFInfo
- Publication number
- US765000A US765000A US14637103A US1903146371A US765000A US 765000 A US765000 A US 765000A US 14637103 A US14637103 A US 14637103A US 1903146371 A US1903146371 A US 1903146371A US 765000 A US765000 A US 765000A
- Authority
- US
- United States
- Prior art keywords
- sulfate
- copper
- ore
- copper sulfate
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 5
- 230000008569 process Effects 0.000 title description 5
- 229910000365 copper sulfate Inorganic materials 0.000 title description 3
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 title description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 15
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 14
- 239000010949 copper Substances 0.000 description 14
- 229910052802 copper Inorganic materials 0.000 description 13
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 229910052742 iron Inorganic materials 0.000 description 6
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 3
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000010494 dissociation reaction Methods 0.000 description 2
- 230000005593 dissociations Effects 0.000 description 2
- GDPKWKCLDUOTMP-UHFFFAOYSA-B iron(3+);dihydroxide;pentasulfate Chemical compound [OH-].[OH-].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O GDPKWKCLDUOTMP-UHFFFAOYSA-B 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 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
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000003643 water by type 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
- C22B47/00—Obtaining manganese
- C22B47/0018—Treating ocean floor nodules
- C22B47/0045—Treating ocean floor nodules by wet processes
- C22B47/0054—Treating ocean floor nodules by wet processes leaching processes
- C22B47/0063—Treating ocean floor nodules by wet processes leaching processes with acids or salt solutions
Definitions
- This invention relates to certain improvements in the treatment of sulfurous ores of copper or mattes resulting from the various ores of this metal.
- FIG. 1 is a longitudinal sectional view through a roasting-furnace provided with a cooling-passage.
- Fig. 2 is a vertical sectional view through the apparatus for lixiviating the sulfated ores and the digesting-pans.
- A represents a furnace in which the ore is roasted
- B represents a cooling-passage to which the ore is transferred from the furnace after the roasting is completed.
- the apparatus for lixiviating the sulfated ores is designated as a whole by the letter C and is preferably provided with mixing devices which are adapted to be driven in any suitable manner.
- the solution from the lixiviating apparatus is drawn off into the digesting-pans D, where it is heated, and made to pass over ore that has been roasted to complete oxidation.
- the process of obtaining sulfate of copper from sulfur ores or mattes which consists in roasting the ores in an oxidizing atmosphere until the sulfur is dispelled from the ore, cooling the roasted ore in contact with the gases from the roasting to form sulfate of copper and ferric sulfate; lixiviating the mass thus formed, then digesting the solution with ore previously roasted to complete oxidation whereby sulfate of copper is formed and peroxid of iron is precipitated.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Ocean & Marine Engineering (AREA)
- Oceanography (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
PATENTBD JULY 12, 1904.
G. G'IN. PROCESS OF MAKING COPPER SULFATE.
APPLICATION FILED MAB. 5,1903.
N0 MODEL.
Jflmmlar WMQ 1266666. if Q 0% Patented July 12, 1904.
GUSTAVE GIN, OF PARIS, FRANCE.
PROCESS OF MAKING COPPER SULFATE.
SPECIFICATION forming part of Letters Patent No. 765,000, dated. July 12, 1904. Application filed March 5, 1903. Serial No. 146,371. (No specimens.)
To all whom it may concern:
Be it known that I, GUs'rAvE GIN. a citizen of the French Republic, and a resident of Paris, France, have invented certain new and useful Improvements in Processes of Manur facturing Sulfate of Copper by the Direct Sulfatation of the Ores 0r Mattes, of which the following is a specification.
This invention relates to certain improvements in the treatment of sulfurous ores of copper or mattes resulting from the various ores of this metal.
This process is preferably carried out in an apparatus such as shown in the accompanying drawings, in which Figure 1 is a longitudinal sectional view through a roasting-furnace provided with a cooling-passage. Fig. 2 is a vertical sectional view through the apparatus for lixiviating the sulfated ores and the digesting-pans.
As shown in Fig. 1, A represents a furnace in which the ore is roasted, and B represents a cooling-passage to which the ore is transferred from the furnace after the roasting is completed. The apparatus for lixiviating the sulfated ores is designated as a whole by the letter C and is preferably provided with mixing devices which are adapted to be driven in any suitable manner. The solution from the lixiviating apparatus is drawn off into the digesting-pans D, where it is heated, and made to pass over ore that has been roasted to complete oxidation.
Under my invention when the ore or matte has been properly pulverized it is put into a muffle-furnace A and subjected to roasting in an oxidizing atmosphere in order that the whole of the sulfur in the copper may be transformed into oxid or sulfate. This result is attained after complete dissociation of the ferrous sulfate and the partial decomposition of the sulfate of copper that is formed. When the operation is complete, the ore is transferred from the sole of the muffle-furnace to the floor of a cooling-passage B, into which are directed the sulfurous gases arising from the roasting, with the addition of a suitable quantity of air. These gases travel with the ore, which is gradually shoveled along toward the end of the cooling-passage farthest from the roastingfurnace. As a result of the lowering of the temperature there occurs aseries of chemical changes between the ore and the sulfurous gases that end in reactions which are substantially the inverse of those which occur during the roasting. Thus a mixture of sulfurous auhydrid and of air is brought into the presence of the calcined ore, which owing to the wellknown catalytic action of peroxid of iron and of sulfate of copper forms sulfuric anhydrid, which rapidly transforms first the oxid of copper, then the peroxid of iron, into sulfates. The transformation of the sulfurous anhydrid into sulfuric anhydrid is effected as soon as the temperature falls below 7 50 centigrade, and the rapidity of this reaction is at its maximum between 440. and 400 centigrade; but in practice it is advisable not to go below 500 centigrade, so as to avoid the formation offerrous sulfate according to the reaction:
Above 500 there can be formed only basic ferric sulfate, (FGZSOGJ and that is a very important point for the result of the operations. It is advisable not to limit the proportion of this sulfate, but, on the contrary, to get as much of it as possible, for, as will be seen, it serves as a vehicle for converting the copper of another mass of ore into sulfate. IV hen the mass that has been converted to sulfate is lixiviated, it gives a solution containing sulfate of copper and basic ferric sulfate. This solution is then heated to about 90 centigrade and made to pass over another mass of ore that has been roasted to complete oxidation and that consequently contains all its copper as cupric oxid, in the presence of which the peroxid of iron is precipitated according to the exothermic reactions:
Fe SO +():CuSO,-|%(+45.9 calories).
By cooling, a part of the sulfate of copper that has been dissolved-about three-fourthsis isolated, and the mother-waters are recovered and heated in order to serve for new lixiviation. In regulating and limiting the degree of cooling I also use certain known properties with regard to the stability of certain sulfates and the instability of others at determined temperatures. I am not unaware that the utilization of these properties of the sulfates has already been protected by an American patent, No. 692,008, the object of which is the separation of metals from their ores; but I wish to observe that if I take advantage of the differences of stability of sulfates of iron at different degrees of oxidation it is for quite a different purpose than that aimed at in the above-mentioned patent. As a matter of fact, my aim is not to get rid of the ferric sulfate by dissociation in order to leave behind only the sulfate of copper. On the contrary, I wish to keep along with the sulfate of copper the largest possible quantity of ferric sulfate, which is intended to serve as a vehicle for the sulfuric acid. This latter it carries to the cupric oXid of another mass of ore, while at the same time the peroxid of iron is precipitated.
Having now fully described my invention, what I claim, and desire to secure by Letters Patent, is-
The process of obtaining sulfate of copper from sulfur ores or mattes, which consists in roasting the ores in an oxidizing atmosphere until the sulfur is dispelled from the ore, cooling the roasted ore in contact with the gases from the roasting to form sulfate of copper and ferric sulfate; lixiviating the mass thus formed, then digesting the solution with ore previously roasted to complete oxidation whereby sulfate of copper is formed and peroxid of iron is precipitated.
In testimony whereof I have hereunto set my hand in presence of two witnesses.
GUSTAVE GIN.
Witnesses:
ADoLrHE STURM, J. ALLISON BOWEN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US14637103A US765000A (en) | 1903-03-05 | 1903-03-05 | Process of making copper sulfate. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US14637103A US765000A (en) | 1903-03-05 | 1903-03-05 | Process of making copper sulfate. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US765000A true US765000A (en) | 1904-07-12 |
Family
ID=2833486
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US14637103A Expired - Lifetime US765000A (en) | 1903-03-05 | 1903-03-05 | Process of making copper sulfate. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US765000A (en) |
-
1903
- 1903-03-05 US US14637103A patent/US765000A/en not_active Expired - Lifetime
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