US68135A - Oscar -wasse - Google Patents
Oscar -wasse Download PDFInfo
- Publication number
- US68135A US68135A US68135DA US68135A US 68135 A US68135 A US 68135A US 68135D A US68135D A US 68135DA US 68135 A US68135 A US 68135A
- Authority
- US
- United States
- Prior art keywords
- lead
- zinc
- chloride
- silver
- work
- 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
- 241000501754 Astronotus ocellatus Species 0.000 title 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 58
- 229910052725 zinc Inorganic materials 0.000 description 58
- 239000011701 zinc Substances 0.000 description 58
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 56
- 238000000034 method Methods 0.000 description 34
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 32
- BQCADISMDOOEFD-UHFFFAOYSA-N silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 30
- 229910052709 silver Inorganic materials 0.000 description 30
- 239000004332 silver Substances 0.000 description 30
- 229910052742 iron Inorganic materials 0.000 description 16
- 238000007670 refining Methods 0.000 description 16
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 12
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 12
- 229910052787 antimony Inorganic materials 0.000 description 12
- 229940072033 potash Drugs 0.000 description 12
- 235000015320 potassium carbonate Nutrition 0.000 description 12
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 12
- 239000002184 metal Substances 0.000 description 10
- 229910052751 metal Inorganic materials 0.000 description 10
- 238000003723 Smelting Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000002844 melting Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000005755 formation reaction Methods 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate dianion Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 2
- 229910000754 Wrought iron Inorganic materials 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000023298 conjugation with cellular fusion Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 230000000875 corresponding Effects 0.000 description 2
- 230000001419 dependent Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002349 favourable Effects 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000013011 mating Effects 0.000 description 2
- 238000010309 melting process Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 235000012976 tarts Nutrition 0.000 description 2
- 230000021037 unidirectional conjugation Effects 0.000 description 2
- 239000011800 void material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
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
- C22B13/06—Refining
Definitions
- My inventioir consists in a new process for refining work lead after the same has been desilvered by means of metallic zinc, said process being based upon the application of chemical products.
- the process of desilvering work lead, or leadenriched by the Pattinson method, by means of metallic zinc, is already in practice, But the reason why this method has as yet been but little applied, is'to be found in the not inconsiderable loss of metal occasioned by the process oi separating thedesilvered lead and zinc.
- This separation of the desilvered lead from the zinc was hitherto effected by smelting in a reverberatory furnace,-or by smelting with iron dross in a vertical furnace.
- My process consists i n submitting red-hot desilvered lead, containing zinc, iron, and antimony, to the action ofchloride of lead.
- the chlorine of the chloride of lead combines with the zinc and iron, whilst the lead of the chloride of lead is combined with the lead to be refined.
- the desilvered lead is melted in crucibles or pans constructed of cast or wrought iron, the forms and sizes of which are immaterial. The larger in general these crucibles or pans are, in proportion to their depths, the more adaptable they becomefor my process.
- the antimony that is, perhaps, contained in the lead, is not fully expelled by the chloride of lead, and to clear the lead of this metal too it is treated with soda or potash (Natrz'um caustz'cum or Kalium caustz'cum) in like manner as described above for the chloride. of lead, without, however, allowing the temperature to surmount the melting point of the lead.
- soda or potash Naatrz'um caustz'cum or Kalium caustz'cum
- antimoniate ofsoda or antimoniate of potash is formed, which substance is taken off and used either for producing antimony-metal or for other purposes. (Hitherto antimony could only be ejected by melting.)
- a dress pf chloride of zinc is again formed, which is taken oil, and the remainder of the lead, rich of silver, is put in a refining furnace for the production of the silver.
- the total loss of lead in the purifying method above described including the loss originating through the process of refining the enriched lead, and again smelting the oxidized products, does not amount to one-quarter per cent. of the work lead.
- the dross of chloride of zinc, if it contains lead, is put on an inclined plane, and the effects of the open air allowed to operate on it.
- the chloride of zinc then absorbs water and runs down as a solution; itis then collected in vessels and used.
- the residuum rich of lead is worked for lead.
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
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IMPROVED rsocnss or nnrmrne LEAD.
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TO ALL WHOM IT MAY CONCERN:
Be it known that I, OscAn WASSEEMANN, of Call, in the Kingdom of Prussia, have invented a new and useful Process for Refining Work Lead; and I do hereby declare the following to be a full, clear, and exact description of this invention, which will enable those skilled in the art to make and use the same.
My inventioirconsists in a new process for refining work lead after the same has been desilvered by means of metallic zinc, said process being based upon the application of chemical products. The process of desilvering work lead, or leadenriched by the Pattinson method, by means of metallic zinc, is already in practice, But the reason why this method has as yet been but little applied, is'to be found in the not inconsiderable loss of metal occasioned by the process oi separating thedesilvered lead and zinc. This separation of the desilvered lead from the zinc was hitherto effected by smelting in a reverberatory furnace,-or by smelting with iron dross in a vertical furnace. In the first case a product of oxidation is received, which contains, beside oxide of lead, most of the extraneous admixtures. As this mass, produced by oxidation, m'usLagain be reduced to metallic lead, the consequence is a loss of lead amounting fromone and a half to one and three-quarters per cent. On the other hand, the zinocontained in the lead, in the shape of oxide of'zinc, is absorbed by the dross, whereas all the other constituents, as iron and antimony, are not expelled, for which reason a special treatment ofthe lead in reverheratories becomes necessary to clear it of these parts. Here the same loss of lead results as with Deviating from the various methods hitherto applied, I have invented a new process, by which the loss-of lead is avoided, and the zinc employed forthe abstraction of the silver is separated, and can be used over and over again, which latter never is the case with the other methods.
My process consists i n submitting red-hot desilvered lead, containing zinc, iron, and antimony, to the action ofchloride of lead. The chlorine of the chloride of lead combines with the zinc and iron, whilst the lead of the chloride of lead is combined with the lead to be refined. In practice the process is as follows: The desilvered lead is melted in crucibles or pans constructed of cast or wrought iron, the forms and sizes of which are immaterial. The larger in general these crucibles or pans are, in proportion to their depths, the more adaptable they becomefor my process. They are filled almost up to the brim, and the surface of the molten lead is subsequently covered with two-thirds of the requisite quantity of chloride of lead, and the temperature increased till the formation of chloride of zinc begins, which can he observed by the production of a liquid dross. This temperature is to be maintained, and after a lapse of three-quartersof an hour all the chloride of lead is decomposed,'and the lead covered with a layer of protochloride of zinc. This dross is taken ofl' by means of a. spoon, and nowth-e remaining third ofthe chloride of lead is added to the lead. After this quantity of chloride of lead has operatedfrom one hour and a half to two hours on the impure lead, it has freed the latter of all the iron and zin'citcontained. As it is the custom to apply a little more chloride of lead than-is theoretically requisite for the purification, this last dross still contains some undecomposed chloride of lead, and is therefore saved and again used in ,the next melting process. The lead is, however, fully cleared of zinc and iron, as also of copper, the latter having, during the operation of desilvering, combined with the zinc dross saturated with silver. The antimony that is, perhaps, contained in the lead, is not fully expelled by the chloride of lead, and to clear the lead of this metal too it is treated with soda or potash (Natrz'um caustz'cum or Kalium caustz'cum) in like manner as described above for the chloride. of lead, without, however, allowing the temperature to surmount the melting point of the lead. Hence antimoniate ofsoda or antimoniate of potash is formed, which substance is taken off and used either for producing antimony-metal or for other purposes. (Hitherto antimony could only be ejected by melting.)
After the addition of the last quantity of chloride of lead, it isinevitable that, through the high temperature, part of the .chloride of zinc evaporates, and it therefore becomes necessary to make provisions for the reception of these vapors and the protection of the workmen. This is accomplished by means of a bell of iron plate which covers the-pans or crucibles, and connects at the same time with a pipe conducting into a condensingchamber. The'quantity of the chloride of lead to be employed for clearing the desilvercdlead amounts to about two and three-quarters to three per cent. For the purpose of clearing the zinc dross enriched with silver, a greater quantityof chloride of lead is necessary, corresponding to the percentage of zinc, and this, with reference to the work lead, amounts from four and a half to five per cent., provided the work lead contains two hundred and fifty to one thousand grammes silver in one thousand kilogrammes lead.
-It is evident that to purify a very poor lead, for economys sake, a chloride of lead must be selected as void of silver as possible. Such a poor chloride of lead can be gained out of the not oxidated quick powder, consisting mostly of sulphuret and carbonate of lead collected in the chambers of lead-smelting furnaces, by treating .it with hydrochloric acid. Beside its use, the advantage is attained that this quick powder wants not to be treated as ordinarily, and is refined without any loss of lead and other expenses, so that the expenses for muriatic acidare thus more than reimbursed. In separating the zinc from the zinc dross containing much silver, it ought to be observed that a chloride of lead as rich as possible must be employed, else the percentage of silver contained in the lead reduced from the zinc dross would bedecreased by the lead in the chloride of lead. But since, for the production of such a chloride of lead, the proper compound of lead is diflicult to be had, the zinc dross is treated directly with muriatie acid. It must, however, be freed from lead to such a degree that it has the appearance of a'crumbling mass. By this treatment chloride of zinc and lead are the principal results, whereupon the mass is put in a pan or crucible to be melted down. Thus a dress pf chloride of zinc is again formed, which is taken oil, and the remainder of the lead, rich of silver, is put in a refining furnace for the production of the silver. The total loss of lead in the purifying method above described, including the loss originating through the process of refining the enriched lead, and again smelting the oxidized products, does not amount to one-quarter per cent. of the work lead. The dross of chloride of zinc, if it contains lead, is put on an inclined plane, and the effects of the open air allowed to operate on it. The chloride of zinc then absorbs water and runs down as a solution; itis then collected in vessels and used. The residuum rich of lead is worked for lead.
The expenses in melting down and treating the impure lead for its refinement arebalanced by the value of the chloride of zinc, so that in calculating the expenses of the desilvering and refining process, only those costs come into consideration which are attendant to the .desilvering process and one-quarter per cent. less of lead besides. The special expenses of the desilvering for work lead of two hundred and fifty to one thousand grammes silver in one thousand kilogrammes of lead, amount to ten cents; one-quarter per cent. less of lead, one cent; eleven cents total amount of expenses. As in the methods hitherto applied, and especially in the concentrating process of Pattinson so generally in use, the expenses of producing silver from work lead, as also for producing a pure lead for trade, amount to more than twenty-two cents per hundredweight of thework lead above described, a hundredweight of work lead is, by this new method, desilvered and refined more than eleven cents cheaper than could be accomplished by any other process known to me. If it is considered that in Pattin'sons concentrating process the lead produced for trade always has a quantity of silver of at least twenty grammes in one thousand kilogrammes of lead, as a further refining of silver would not be economical, and that in comparison to this method mydesilvering process, by means of zinc, is almost a. perfect one, and a mechanical removal of lead and silver is less attendant by the very trifling formation of oxidized produets,it is clearly evident that the production of silver here is much more favorable. ,A special advantage is also attained by the circumstance that the work load can always be quickly consumed without being dependent upon the large masses of not perfectly refined lead attending Pattinsons process. As all zinc and iron are abstracted from the poor lead by the chloride of lead, and all antimohy by the soda and potash, the lead produced for trade is free, from all metals it generally contains, and can be used as chemically pure lead, which advantage is certainly very important.
Should the work lead contain any antimony, the expenses for refining it become still less, as the antimoniateof soda and potash has a considerably greater value than the soda or potash employed for the removal of the antimony out of the lead. The new method of refining work lead desilvered by zinc metal is therefore based on the application of the two chemical'products, chloride of lead and soda, for which method in the annexed application I beg to request a patent.
Having now described the nature of my said invention, and in what manner the same can or may be performed, I wish it to be distinctly understood that I do claim as new, anddesire to secure by Letters Patent 1. Treating work lead, which has been desilvered by the aid of zinc, with'ehloride of lead, substantially ad and for the purpose described.
2. Treating work lead, which has been desilvered by the aid of zinc, with chloride of lead andalkalies, such as soda or potash, substantially as and for the purpose set forth.
OSCAR WASSERMANN.
Witnesses:
E. G'. Scorr, W. H. Vnsnr.
Publications (1)
Publication Number | Publication Date |
---|---|
US68135A true US68135A (en) | 1867-08-27 |
Family
ID=2137658
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US68135D Expired - Lifetime US68135A (en) | Oscar -wasse |
Country Status (1)
Country | Link |
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US (1) | US68135A (en) |
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0
- US US68135D patent/US68135A/en not_active Expired - Lifetime
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