US1566183A - Method of producing zinc or zinc and lead - Google Patents
Method of producing zinc or zinc and lead Download PDFInfo
- Publication number
- US1566183A US1566183A US487990A US48799021A US1566183A US 1566183 A US1566183 A US 1566183A US 487990 A US487990 A US 487990A US 48799021 A US48799021 A US 48799021A US 1566183 A US1566183 A US 1566183A
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- US
- United States
- Prior art keywords
- zinc
- powder
- furnace
- lead
- reduction
- Prior art date
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- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title description 70
- 229910052725 zinc Inorganic materials 0.000 title description 59
- 239000011701 zinc Substances 0.000 title description 59
- 238000000034 method Methods 0.000 title description 18
- 239000011133 lead Substances 0.000 title description 2
- 239000000843 powder Substances 0.000 description 25
- 239000007788 liquid Substances 0.000 description 16
- 230000009467 reduction Effects 0.000 description 15
- 238000006722 reduction reaction Methods 0.000 description 15
- 239000000463 material Substances 0.000 description 12
- 230000008569 process Effects 0.000 description 10
- 239000002893 slag Substances 0.000 description 10
- 239000002184 metal Substances 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 7
- 230000009471 action Effects 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000003723 Smelting Methods 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- 150000002739 metals Chemical class 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000003575 carbonaceous material Substances 0.000 description 4
- JQJCSZOEVBFDKO-UHFFFAOYSA-N lead zinc Chemical compound [Zn].[Pb] JQJCSZOEVBFDKO-UHFFFAOYSA-N 0.000 description 4
- 229910000635 Spelter Inorganic materials 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 229910001338 liquidmetal Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 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
- 238000007792 addition Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000009858 zinc metallurgy Methods 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
- C22B19/00—Obtaining zinc or zinc oxide
- C22B19/04—Obtaining zinc by distilling
- C22B19/16—Distilling vessels
- C22B19/18—Condensers, Receiving vessels
Definitions
- the present invention is a process for making zinc or spelter or zinc-lead characterized by the fact that the metallic vapors coming from a reduction furnace are exposed to a sufliciently low temperature to convert the vapors to a powder without any formation of liquid zinc, and by the fact that this powder is transferred to a suitable device in order to convert the free metallic content of the same to the liquid state.
- My invention difl'ers from anyflprevious practice in the art in that it is aimed to condense as much as possible of the zinc into powder, in order to convert the free metallic content of the powder into li uid zinc, whereas in all previous practice it was the object to condense as littleQas possible of the zincinto powder to ultimately produce liquid zinc.
- My invention may be applicable to most exlsting processes for making zinc but it has its greatestapplication in connection, with the continuously operated furnaces or retorts,,that is, in a process where the reduction of the ore or the zinkiferous material and the distilling of the metal are effected in a continuous operation.
- the accompanying drawing illustrates the method of continuously charging the zinc material, and its continuous reduction, its continuous vaporizing and the continuous condensation of the reduced zinc vapors.
- 1 indicates a hopper for the zinc containing material
- 2 a conveyor for trans orting the charge through the opening 3
- 4 t e furnace or retort in which the reduction .iscarried out
- 5 the tapping hole for slag
- condenser may be emptied by opening the damper 8, and the condensed zinc powder transmitted to the receiver 9.
- Said receiver maybe put in communication with the removable receiver 14 through the pipe 11.
- the receiver 14, which receives the powder from the receiver 9 by opening the damper 10 and placing the receiver 14 with its opening 12 beneath the pipe 11, may be carried over to a suitable apparatus for the extraction of .the metal from the powder.
- By closing the shutter 13 the air is prevented from coming in contact with the powder in the receiver during the transport of the same.
- opening the shutter 15 the receiver 1.4 will be emptied and its content of powder will be withdrawn.
- the ore or zinkiferous material that is to be treated is mixed with the necessary proportion of solid carbonaceous material, such as coke, breeze, or fines, to effect reduc ion of the zinc; and if the gangue of the ore does not contain the requisite quantities of silica, iron and lime, wherewith to combine in the formation of a proper slag, additions of fluxes for that purpose are made.
- the charge of ore, or zinkiferous material, thus prepared, is subjected to combined smelting and distillation in a suitable furnace, which is heated electrically or in any convenient manner.
- the smelting and distillation proceed in accordance with well known metallurgical principles.
- a slag which becomes molten, while iron, copper and sulphur unite in the formation of a matte, which collects the major part of the gold and silver if such metals exist in the ore.
- the slag and matte may be tapped from the bottom of the fun nace in the usual manner, well known to those versed in the art of smelting.
- the zinc of the ore, and the lead also if it be present. are reduced and volatilized to the major extent. only small proportions of these metals entering the slag. It has been found in practice that to accomplish the best results with respect to extraction of the zinc in this way it is desirable so to flux the ore to be treated that the slag will be highly silicious. In practice a slag containing about 50% silica has been found to be most advantageous.
- the design of the condenser may provide for internal cooling or for arrangement of parts that will occur to persons experienced in the art of zinc metallurgy.
- the zinc obtained in the condenser is accumulated in a receptacle thereof, from which it may. be drawn for use in the form of powder, for any purpose, but from which in the common practice of my invention it is drawn and conveyed to a furnace wherein it is largely converted into a liquid state by heating it in a furnace wherein it is subjected to a rubbing or attritionary action.
- the carbonaceous gases out of which the condensed zinc is dropped escape through an outlet from the condenser and may be caused to pass through a water trap or any filtering device whereby any condensed zinc that has failed to deposit itself is caused to settle and fallsdown into a receptacle.
- the reduction furnace from which the zinc vapors are produced may be interiorly or exteriorly heated by any suitable means such as with electricity, fuel or both simultaneously.
- this invention evidently refers also to the production of lead and the treatments of such products from a reduction furnace as contain lead.
- zinkiferous material consisting in adding carbonaceous material for reduction of zinc and proper material for fluxing the gangue, heating the mixture in a furnace to such temperature as to produce a slag and to reduce and volatilize the zinc, conveying the zinc vapor into a suitable apparatus for condensation, condensing the zinc vapor by a sudden chilling to cause it to precipitate mainly in the form of powder, washing or filtering the eflluent gas, and transferring the condensed and precipitated powder to another furnace and subjecting the same to a mechanical action to convert it largely into liquid form.
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- 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
Dec. 15, 1925- 1,566,183
c. E. CORNELIUS METHOD OF PRODUCING ZINZ 0R ZINC AND LEAD Filed July 27, 1921 INVENTOR. C. E. Corelium BY mxw ATTORNEYS,
Patented Dec. 15, 1925.
UNITED STATES PATENT OFFICE.
CORNELIUS ERIK CORNELIUS, OF STOCKHOLM, SWEDEN, ASSIGNOR TO TROLL- H A'ITANS ELEKTROTI-IF RMISKA AKTIEBOLAG, OF STOCKHOLM, SWEDEN.
METHOD OF PRODUCING ZINC 0R ZINC AND LEAD.
Application filed July 27, 1921. a Serial No. 487,990.
To allwhom it may concern:
Be it known, that I CORNELIUS ERIK Con- NELIUS, a. subject of the King of Sweden, residing at Stockholm, Sweden, have invented certain new and useful Improvements in Methods of Producing Zinc or Zinc and Lead, of which the following is a specification.
As is well known it has hitherto been practically impossible to obtain the entire uantity of metal coming from a zinc reduction furnace in a liquid state. This is essentially due to the fact that it is practically impossible to control the temperature of the condenser and that the zinc vapors are always more or less diluted by a quantity of hydro-carbons and carbon. oxides, (mono and dioxides) which counteract the formation of liquid zinc. The zinc vapors from the distilling furnace, which, due to the above mentioned reasons, are notobtainable as liquid metal are however condensed in the form of 'metallic dust, poussiere or powder, the product being commerically known as zinc dust or blue powder.
Many unsuccessful attempts have been made to minimize the formation of the blue powder and also to recover the zinc in the same by heating it separately by process where the expensive redistilling could be avoided. Since the inventon of S. Huldt disclosed in U. S. Patent- No. 1,266,808, however, any powder containing zinc in the free metallic state, that-is powder containing zinc not chemically combined with any other elements can, depending on the amount of the free metallic content, largely. be converted to the liquid state.
As this invention solves the problem of converting the major portion'of blue powder into liquid metal in a convenient .and economcal way the formation of blue powder may no longer be looked upon as undesirable but rather in many cases as a desirable product in the production of zinc.
The present invention is a process for making zinc or spelter or zinc-lead characterized by the fact that the metallic vapors coming from a reduction furnace are exposed to a sufliciently low temperature to convert the vapors to a powder without any formation of liquid zinc, and by the fact that this powder is transferred to a suitable device in order to convert the free metallic content of the same to the liquid state.
In conveying the blue powder to this device it should as much as possible be pro tected against the air in order to avoid any unnecessary oxidation of the metallic zinc.
My invention difl'ers from anyflprevious practice in the art in that it is aimed to condense as much as possible of the zinc into powder, in order to convert the free metallic content of the powder into li uid zinc, whereas in all previous practice it was the object to condense as littleQas possible of the zincinto powder to ultimately produce liquid zinc.
I am aware that zinc is sometimes intentionally condensed as far as possible in the form of powder, but this has been done for thepurpose of producing a commercial product known as zinc dust or zinc grey in which connection it is an object to keep the oxidation. of the zinc within the narrow hmits fixed by the trade.v My resent invention differs from, that practice in 'that the final product is liquid zinc or spelter or zinc-lead and in that while oxidation of.the .zmc condensing asv blue powder is undesirable it need not be confined within narrow limits.
My invention may be applicable to most exlsting processes for making zinc but it has its greatestapplication in connection, with the continuously operated furnaces or retorts,,that is, in a process where the reduction of the ore or the zinkiferous material and the distilling of the metal are effected in a continuous operation.
The accompanying drawing illustrates the method of continuously charging the zinc material, and its continuous reduction, its continuous vaporizing and the continuous condensation of the reduced zinc vapors.
1 indicates a hopper for the zinc containing material, 2 a conveyor for trans orting the charge through the opening 3, 4 t e furnace or retort, in which the reduction .iscarried out, 5 the tapping hole for slag and,
matte, 6 the channel between the reduction .furnace 4. and the cooled condenser 7.
Between the condenser 7 and the receiver.
9 is provided a damper-8, and the receiver 9 is closed b an adjustable damper 10. The
condenser may be emptied by opening the damper 8, and the condensed zinc powder transmitted to the receiver 9. Said receiver maybe put in communication with the removable receiver 14 through the pipe 11.
The receiver 14, which receives the powder from the receiver 9 by opening the damper 10 and placing the receiver 14 with its opening 12 beneath the pipe 11, may be carried over to a suitable apparatus for the extraction of .the metal from the powder. By closing the shutter 13 the air is prevented from coming in contact with the powder in the receiver during the transport of the same. By opening the shutter 15, the receiver 1.4 will be emptied and its content of powder will be withdrawn.
Preferably the ore or zinkiferous material that is to be treated is mixed with the necessary proportion of solid carbonaceous material, such as coke, breeze, or fines, to effect reduc ion of the zinc; and if the gangue of the ore does not contain the requisite quantities of silica, iron and lime, wherewith to combine in the formation of a proper slag, additions of fluxes for that purpose are made. The charge of ore, or zinkiferous material, thus prepared, is subjected to combined smelting and distillation in a suitable furnace, which is heated electrically or in any convenient manner. The smelting and distillation proceed in accordance with well known metallurgical principles. The silica, iron and lime. together with other basic elements. combine in a slag, which becomes molten, while iron, copper and sulphur unite in the formation of a matte, which collects the major part of the gold and silver if such metals exist in the ore. The slag and matte may be tapped from the bottom of the fun nace in the usual manner, well known to those versed in the art of smelting. The zinc of the ore, and the lead also if it be present. are reduced and volatilized to the major extent. only small proportions of these metals entering the slag. It has been found in practice that to accomplish the best results with respect to extraction of the zinc in this way it is desirable so to flux the ore to be treated that the slag will be highly silicious. In practice a slag containing about 50% silica has been found to be most advantageous.
In this case it has been found by experience in many experimentations that in such a method of reduction and distillation only a rather small amount of the vapors will be converted into liquid zinc, the major part will condense as blue powder which has to be charged into the furnace again for redistilling of the zinc.
In order to produce merely a powder the free metallic. content of which in another process may be turned into liquid zinc, the products coming from the continuously operated distilling furnace have to be sharply cooled. This cooling of the gas and vapor coming from the reduction furnace may be effected in any suitable way, but in practice I have found it preferable to accomplish this by introducing the gas and vapor into and passing them through channels or tubes or the like, which are cooled externally b means of water or air, or by means of both simultaneously.
The design of the condenser may provide for internal cooling or for arrangement of parts that will occur to persons experienced in the art of zinc metallurgy.
The zinc obtained in the condenser is accumulated in a receptacle thereof, from which it may. be drawn for use in the form of powder, for any purpose, but from which in the common practice of my invention it is drawn and conveyed to a furnace wherein it is largely converted into a liquid state by heating it in a furnace wherein it is subjected to a rubbing or attritionary action.
The carbonaceous gases out of which the condensed zinc is dropped escape through an outlet from the condenser and may be caused to pass through a water trap or any filtering device whereby any condensed zinc that has failed to deposit itself is caused to settle and fallsdown into a receptacle.
The reduction furnace from which the zinc vapors are produced may be interiorly or exteriorly heated by any suitable means such as with electricity, fuel or both simultaneously.
As the zinc ores and zinkiferous material generally used in connection with this process also contain lead, this invention evidently refers also to the production of lead and the treatments of such products from a reduction furnace as contain lead.
In the case of a zinc ore containing lead, a considerable proportion of the leadcom tent thereof will distil with the 'zinc, and
will collect and will be condensed with the.
blue powder. and the product from such a powder will be a leady spelter.
Inmy application 292,952 filed April 26, 1919, ofwhich the present application is a continuationin part, I have disclosed but not so much in detail the process of the present application.
What I claim as my invention, and desire to secure by Letters-Patent is:
1. The method of producing volatile metals consisting in generating metal vapors by a reduction process, then conducting the vapors without allowing their contact with the air and subjecting themto a temperature sufficiently low to convert substantially the whole bulk of condensible vapors into a powdered state, then conducting said powder avoiding its contact with the air and subjecting the powder to a heating and mechanical action to convert the same into a liquid state.
2. The method of producing zinc, or zinclead, consisting in the continuous reduction and distillation of zinc, or zinc-lead, in a heated furnace or retort, and subjecting the gases and vapors as they come from the furnace or retort, without allowing their contact with air, to a temperature sufficiently low to convert substantially all of the vaporized metals into powdered state, and subjecting the powder to a heating and me chanical action to convert the same into a liquid state.
3. The method of producing zinc or zinclead, consisting in the continuous reduc tion and distillation of zinc, or zinc-lead, in a furnace or retort, heated electrically, and subjecting the gases and vapors as they come from the furnace or retort, without allowing their contact with air, to a telnrature sufficiently low to convert substantially all of the vaporized metals into a powdered state, and subjecting the powder to a heating and rubbing or attrition action to convert the same into a liquid state.
4. The process of smelting zinc ore, or zinkiferous material. consisting in adding carbonaceous material for reduction of zinc and proper materials for fluxing the gangue, heating the mixture in a furnace to such temperature as to produce a slag and to reduce and volatilize zinc, conveying the zinc vapor into a suitable apparatus for con- (lensation, condensing the zinc vapor by a sudden chilling to cause it to precipiatate mainly in the form of powder, and transfering the condensed and precipitated powder to another furnace and subjecting the same to a mechanical action to convert it largely into liquid form.
5. The process of smelting zinc ore, or
zinkiferous material, consisting in adding carbonaceous material for reduction of zinc and proper material for fluxing the gangue, heating the mixture in a furnace to such temperature as to produce a slag and to reduce and volatilize the zinc, conveying the zinc vapor into a suitable apparatus for condensation, condensing the zinc vapor by a sudden chilling to cause it to precipitate mainly in the form of powder, washing or filtering the eflluent gas, and transferring the condensed and precipitated powder to another furnace and subjecting the same to a mechanical action to convert it largely into liquid form.
6. The process of smelting zinc ore or zinkiferous material, consistmg in adding carbonaceous material for reduction of zinc and proper materials for fluxing the gangue, subjecting the mixture continuousl in a furnace, electrically heated, to sue temperature as to produce a slag and to reduce and volatilize the zinc, conveying the zinc vapor into a suitable apparatus for condensation, condensing the zinc vapor by a sudden chilling so as to cause it to precipitate mainly in the form of power, washing or filtering the eflluent gas, and transferring the condensed and precipitated powder to another furnace and subjecting the same to a heating and mechanical action to convert it largely into liquid form.
In testimony whereof I aflix my signature.
CORNELIUS ERIK CORNELIUS.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US487990A US1566183A (en) | 1921-07-27 | 1921-07-27 | Method of producing zinc or zinc and lead |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US487990A US1566183A (en) | 1921-07-27 | 1921-07-27 | Method of producing zinc or zinc and lead |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1566183A true US1566183A (en) | 1925-12-15 |
Family
ID=23937931
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US487990A Expired - Lifetime US1566183A (en) | 1921-07-27 | 1921-07-27 | Method of producing zinc or zinc and lead |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1566183A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2432111A (en) * | 1944-07-03 | 1947-12-09 | Nitralloy Corp | Furnace for reducing and distilling volatile metals |
| US2598745A (en) * | 1950-08-25 | 1952-06-03 | New Jersey Zinc Co | Smelting of zinciferous ore |
-
1921
- 1921-07-27 US US487990A patent/US1566183A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2432111A (en) * | 1944-07-03 | 1947-12-09 | Nitralloy Corp | Furnace for reducing and distilling volatile metals |
| US2598745A (en) * | 1950-08-25 | 1952-06-03 | New Jersey Zinc Co | Smelting of zinciferous ore |
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