US7661A - Improvement in processes for refining gold - Google Patents
Improvement in processes for refining gold Download PDFInfo
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- US7661A US7661A US7661DA US7661A US 7661 A US7661 A US 7661A US 7661D A US7661D A US 7661DA US 7661 A US7661 A US 7661A
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- US
- United States
- Prior art keywords
- gold
- silver
- solution
- chloride
- metallic
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- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 title description 138
- 229910052737 gold Inorganic materials 0.000 title description 138
- 239000010931 gold Substances 0.000 title description 138
- 238000000034 method Methods 0.000 title description 44
- 238000007670 refining Methods 0.000 title description 10
- 229910052709 silver Inorganic materials 0.000 description 84
- 239000004332 silver Substances 0.000 description 84
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 40
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 38
- 150000001805 chlorine compounds Chemical class 0.000 description 38
- 229910052751 metal Inorganic materials 0.000 description 28
- 239000002184 metal Substances 0.000 description 28
- 150000002739 metals Chemical class 0.000 description 28
- 238000001556 precipitation Methods 0.000 description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 28
- 239000002253 acid Substances 0.000 description 26
- 239000007788 liquid Substances 0.000 description 26
- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 26
- 229910052742 iron Inorganic materials 0.000 description 20
- 235000011149 sulphuric acid Nutrition 0.000 description 20
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 18
- 235000002639 sodium chloride Nutrition 0.000 description 18
- 239000011780 sodium chloride Substances 0.000 description 18
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 16
- 150000007513 acids Chemical class 0.000 description 14
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 14
- 239000002244 precipitate Substances 0.000 description 14
- 239000001117 sulphuric acid Substances 0.000 description 14
- 235000011167 hydrochloric acid Nutrition 0.000 description 12
- HCHKCACWOHOZIP-UHFFFAOYSA-N zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 12
- 239000011701 zinc Substances 0.000 description 12
- 229910052725 zinc Inorganic materials 0.000 description 12
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 10
- 239000011521 glass Substances 0.000 description 10
- 238000010438 heat treatment Methods 0.000 description 10
- 150000003839 salts Chemical class 0.000 description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 229910052573 porcelain Inorganic materials 0.000 description 8
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 8
- 229910052572 stoneware Inorganic materials 0.000 description 8
- 239000002023 wood Substances 0.000 description 8
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 6
- NAXKFVIRJICPAO-LHNWDKRHSA-N Allin Natural products OC[C@H]1O[C@H]2O[C@H]3[C@H](CO)O[C@H](O[C@H]4[C@H](CO)O[C@H](O[C@@H]5[C@@H](CO)O[C@H](O[C@H]6[C@H](CO)O[C@H](O[C@H]7[C@H](CO)O[C@@H](O[C@H]8[C@H](CO)O[C@@H](O[C@@H]1[C@@H]1S[C@@H]21)[C@@H]1S[C@H]81)[C@H]1S[C@@H]71)[C@H]1S[C@H]61)[C@H]1S[C@@H]51)[C@H]1S[C@@H]41)[C@H]1S[C@H]31 NAXKFVIRJICPAO-LHNWDKRHSA-N 0.000 description 4
- 206010022114 Injury Diseases 0.000 description 4
- VWDWKYIASSYTQR-UHFFFAOYSA-N Sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 4
- 238000007792 addition Methods 0.000 description 4
- 239000003518 caustics Substances 0.000 description 4
- XTEGARKTQYYJKE-UHFFFAOYSA-M chlorate Chemical compound [O-]Cl(=O)=O XTEGARKTQYYJKE-UHFFFAOYSA-M 0.000 description 4
- 238000000605 extraction Methods 0.000 description 4
- 239000003517 fume Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- PMZURENOXWZQFD-UHFFFAOYSA-L na2so4 Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 4
- 150000002978 peroxides Chemical class 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 230000001376 precipitating Effects 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 235000000346 sugar Nutrition 0.000 description 4
- 229910001018 Cast iron Inorganic materials 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 241000416536 Euproctis pseudoconspersa Species 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 235000015450 Tilia cordata Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 150000001447 alkali salts Chemical class 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical class [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010276 construction Methods 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
- 238000007865 diluting Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000000266 injurious Effects 0.000 description 2
- 200000000001 labour Diseases 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 235000013379 molasses Nutrition 0.000 description 2
- 230000001264 neutralization Effects 0.000 description 2
- 230000001473 noxious Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- -1 so asto form a Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 2
- 239000002699 waste material Substances 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
- C22B11/00—Obtaining noble metals
- C22B11/04—Obtaining noble metals by wet processes
Definitions
- the nature of my invention consists in the preparation of a solution of gold alloyed with silver or other metals, so as to convert them into chlorides, and a precipitation of metallic gold upon the chloride of silver and other in soluble chlorides; and-in the subsequent reduction and extraction of the silver or other metals from those insoluble chlorides, or the direct extraction of their chlorides by solution, in the manner hereinafter set forth, so as to leave the gold pure.
- the process for makiugthe solution is thus: To one part, by weight, of granulated gold that is, gold melted and cast into water-I take about one part of common salt, threefourths, or about three-fourths of one part, of nitrate'of potassa, or one-half of one part of nitrate of soda, and about one and one-half parts of oil of vitriol. I put the salts and gold into a wooden vessel, to be presently described, and, covering them with water, I admit steam into'the liquid until it attains a boiling-heat.
- the wooden vessel may beany ordinary vessel or vat, made with staves or otherwise, of any convenient size, the best proportion for which is a depth as great as or greater than its diameter, having about one-fourth of its cover fastened on the top and provided with a wooden trough passing into a chimneyor other flue and therest ol' the cover movable, so as to charge or empty the vat the more conveniently.
- the object of the trough is to carry off any fumes that might arise to annoy the operator during thcprocess, although little or none can arise except steam.
- the at, or a series of them may be set into a horizontal flue, which is connected with achimncy, and the vat or vats covered loosely with boards d urin gthe process.
- the steam admitted through the tube passes down through the wooden pipe and escapes freely into the liquid, heating it to any temperature required for the process.
- the advantages of the above method of solution are the use of cheap material's, avoiding the cost of previously preparing murlatic or nitric acid; cheapness in the use of vessels of wood in which solution or combination is effected; the use of steam for heating, which is safe, economical, and under contr'ohand when blown directly into the liquid also promotes solution by agitation; the gradual development of the acids with its attendant advantages, as previously mentioned
- the precipitation is thus: The precipitation of metallic gold is effected in the same vessel in which the solution is produced, and may be performed. as soon as the solution is completed.
- one part-J employ about five parts of crystallized copperas, which I prefer putting into the liquid gradually in the state of powder, although it may be dissolved in water and poured in, and continue the application of heat by blowing in steam until all the precipitant has been added, occasionally pouring in a little muriati'c or sulphuric acid to prevent the precipitation of peroxide of iron or a basic salt of the peroxide.
- the whole of the gold will be precipitated in the metallic state as a fine powder, which a continuance of heat will collect into a closer and more compact precipitate.
- the liquid above the precipitate is then decanted, or drawn ofi' by asiphou or some other convenient manner, and run into a suitable vat, to be further treated, it considered desirable, as will be described below.
- the precipitate may he once or twice washed in the same vessel used for solution and precipitation by pouring in water, allowing the precipitates to settle, and theudecanting or drawing oil the liquid; or it may be directly thrown upon a filter, and then washed with water until the water passes off colorless and gives a neutral test.
- Gopperas may be again obtained from the liquid after being drawn off by putting into it bars or scraps of metallic iron, by which the. sesqnioxide of iron is reduced to protoxide, and
- the process of dissolving out the chloride of silver and other insoluble chlorides is thus:
- the mixed metallic gold and chloride of silver are either partly washed in the solution-vat or wholly washed on a filter, and then thrown into a wooden vat lined'with lead.
- Granulated metallic zinc or scraps of iron to the amount of about one-third of the quantity of silver and of other metals forming insoluble chlorides, originally in the gold, are then thrown into the same leadvat, and water and sulphuric acid are added, and the whole is occasionally stirred.
- the chloride of silver is thus reduced to metallic silver.
- the solution ot'copperas thus obtained may be used to precipitate another solution of gold.
- the solution of zinc As closely as convenient from the reduced silver and gold the latter are thrown upon a filter. and thoroughly washed with water until the water ceases to give an acid reaction.
- the mixed "metallic gold and silver are next treated in vessels of glass or stone were by pure nitric acid, which dissolves out the. silver and other metals, if present, and leaves the gold. By drawing off the liquid and filtering and wash- .ing the remaining gold the gold is separated from silver and other metals, if present.
- the gold is melted in the usual manner.
- the silver is precipitated from its solution by common salt, as chloride of silver, which is reduced by zinc or iron and sulphuric and muriatic acid, as in the usual parting process.
- the form of the vessel may be varied. It might be made square, or oval, or round. It may be shallower or deeper; but I prefer the form I have described.
- the solution of gold may also be efl'ected in a similar manner to that above described in vessels of wood, as follows: I take one part of alloyed gold,
- the salt should be first put into the vessel, for the whole of the mnriatic acid may be put in at once and steam applied until it is well heated, and then nitrate of potassa or of soda gradually added.
- the mode of dissolving the gold may be further varied by putting one part gold and one part common salt into a vessel of wood, porcelain, stoneware, or glass, with a little water, heating the whole, and then adding strong nitric acid gradually until two and a half parts of nitric acid have been added.
- the second stage of the process-the precipitation of metallic gold in the solution-quay also be effected by adding to the solution containin g one part of gold, one part of sugar, molasses, or starch and a quantity of carbonated or caustic potassa or soda or caustic lime sufficient to superneutralize the free acid, keeping the whole in a boiling state until all, or nearly all, the gold is precipitated. If the precipitation be not immediately complete, it will complete itself by standing for some time. The liquid is drawn on from the gold after settling, the precipitate is washed, and then treated as above described for the separation of gold and chlorides.
- the third stage of the operation may be so varied that the chloride of silver and other insoluble chlorides are directly dissolved ontfrom the metallic gold by any convenient solventsuch as hyposulphite of lime or of soda or caustic aqua-ammonia.
- the washed gold is melted as usual.
- the silver is obtained from the solution by known methods, and if it contain gold they may be separated by nitric or sulphuric acid.
- nitric acid always leaves small quantities of silver and other metals when they have been melted with gold unless a very large excess of acid is employed, and in that event there would be no advantage in the process, as it would be too costly on a manufacturing or large scale.
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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
UNITED STATES JAS. G. BOOTH, OF PHILADELPHIA, PENNSYLVANIA.
IMPROVEMENT IN PROCESSES FOR REFlNlNG GOLD.
Specification forming part of Letters Patent No. 7,66l, dated Scpteniher24, 1850.
Q Philadelphia, in the county of Philadelphia,
in the State of Pennsylvania, have invcnted'a new and Improved and useful Mode or Process for Refining Gold and Separating it from Silver and other Metals and 1 do hereby declare that the following is a fulland exact description thereof.
The nature of my invention consists in the preparation of a solution of gold alloyed with silver or other metals, so as to convert them into chlorides, and a precipitation of metallic gold upon the chloride of silver and other in soluble chlorides; and-in the subsequent reduction and extraction of the silver or other metals from those insoluble chlorides, or the direct extraction of their chlorides by solution, in the manner hereinafter set forth, so as to leave the gold pure.
,Totenable others to make and use my inve'ntiou, I proceed to describe the manner of conducting the process and its operation.
First, Imake a solution of gold-containing silver and other metals, so as to convert them into chlorides; second,I precipitate gold in the metallic state from the solution, so that it mixes with uudissolved chloride of silver and other insoluble chlorides; third, I dissolve out the chloride of silver and other insoluble chlorides from the gold by means of aspecial menst-ruum, herein described, or I reduce thcchloride of silver and other insoluble chlorides to metals by zinc or iron and sulphuric or muriatic acid and dissolve out the metals reduced from their insoluble chlorides from the gold by nitric or sulphuric acid.
The process for makiugthe solution is thus: To one part, by weight, of granulated gold that is, gold melted and cast into water-I take about one part of common salt, threefourths, or about three-fourths of one part, of nitrate'of potassa, or one-half of one part of nitrate of soda, and about one and one-half parts of oil of vitriol. I put the salts and gold into a wooden vessel, to be presently described, and, covering them with water, I admit steam into'the liquid until it attains a boiling-heat. The wooden vessel may beany ordinary vessel or vat, made with staves or otherwise, of any convenient size, the best proportion for which is a depth as great as or greater than its diameter, having about one-fourth of its cover fastened on the top and provided with a wooden trough passing into a chimneyor other flue and therest ol' the cover movable, so as to charge or empty the vat the more conveniently. The object of the trough is to carry off any fumes that might arise to annoy the operator during thcprocess, although little or none can arise except steam.
Instead of the arrangemen of the cover and trough here indicated, the at, or a series of them, may be set into a horizontal flue, which is connected with achimncy, and the vat or vats covered loosely with boards d urin gthe process.
A stout piece of wood, bored through its entire length and open at each end, ,is'leeeured vertically to the inner side of the vat and a steam pipe or tube passed into the upper opening. The steam admitted through the tube passes down through the wooden pipe and escapes freely into the liquid, heating it to any temperature required for the process. When the water is sutlicicntly heated the oil'of vitriol, previonslydiluted with several parts of water, is added by degrees in successive portions, according as I observe the action to .progress.
The gradual addition of sulphuric acid generates muriatic and nitric acids or their elements slowly, so that they spend their full force upon the gold without escaping, thus preventing any annoyance to the operator from injurious vapors, while at the same time their more powerful nascent stateis employed in effecting combination and solution. I thus continue the addition of sulphuric acid and the admission of steam, say, for three or four hours, or until all or nearly all the gold is dissolved. The solution will then contain terchlorideot' gold and the sulphate of soda, or. sulphate of soda and of potassa, while chloride of silver and other insoluble chlorides will remain undissolved, and, if the process shall be conducted too hastily, also a small amount of gold. Sulphates or chlorides of other metals, if present, are also in solution.
The advantages of the above method of solution are the use of cheap material's, avoiding the cost of previously preparing murlatic or nitric acid; cheapness in the use of vessels of wood in which solution or combination is effected; the use of steam for heating, which is safe, economical, and under contr'ohand when blown directly into the liquid also promotes solution by agitation; the gradual development of the acids with its attendant advantages, as previously mentioned The precipitation is thus: The precipitation of metallic gold is effected in the same vessel in which the solution is produced, and may be performed. as soon as the solution is completed. For the above proportion of gold-say one part-J employ about five parts of crystallized copperas, which I prefer putting into the liquid gradually in the state of powder, although it may be dissolved in water and poured in, and continue the application of heat by blowing in steam until all the precipitant has been added, occasionally pouring in a little muriati'c or sulphuric acid to prevent the precipitation of peroxide of iron or a basic salt of the peroxide. In this way the whole of the gold will be precipitated in the metallic state as a fine powder, which a continuance of heat will collect into a closer and more compact precipitate. After stopping off the steam a sufficient repose of the liquid of from one to several hours will allow all the metallic gold and chloride of silver to collect at the bottom of the vessel. The liquid above the precipitate is then decanted, or drawn ofi' by asiphou or some other convenient manner, and run into a suitable vat, to be further treated, it considered desirable, as will be described below. The precipitate may he once or twice washed in the same vessel used for solution and precipitation by pouring in water, allowing the precipitates to settle, and theudecanting or drawing oil the liquid; or it may be directly thrown upon a filter, and then washed with water until the water passes off colorless and gives a neutral test.
The advantages of this mode of precipitation are economy in the use of the cheap material of copperas, rapidity of execution, complete precipitation of all the gold present in the solution, and in such a state that it will yield a soft and malleable gold free from brittleness when it is subsequently fused, the,
avoidance of all danger of loss which would result from drawingofl' or decanting a solution of gold from the chloride of silver or of transferring it to another vessel. By this method of precipitation the copperas or protosulphate of iron is converted into a mixture of sesquisulphate and sesquichlor'ide of iron, which are in the liquor drawn oil.
Gopperas may be again obtained from the liquid after being drawn off by putting into it bars or scraps of metallic iron, by which the. sesqnioxide of iron is reduced to protoxide, and
then crystallizingout the copperas and adding either the crystallized copperas or the conceutrated liquidwithoutcrystallization to the next solution of gold in order to precipitate it.
Although there is scarcely any economy in repreparing copperas, either crystallized or dissolved from the solution, yet it may have this advantage, that if the least particle of gold or of chloride of silver, through carelessness in operation or through. accident, should have been drawn off with the liquid it will then be recovered; but any possible loss of gold in this way, or of chloride of silver in solution. may also be entirely obviated by drawing ofi. the liquid into alarge vat, and then diluting it largely with water, whereby chloride of silver will precipitate and will collect together with the gold at the bottomof the vessel after sutficicnt repose.
The process of dissolving out the chloride of silver and other insoluble chlorides is thus: The mixed metallic gold and chloride of silver are either partly washed in the solution-vat or wholly washed on a filter, and then thrown into a wooden vat lined'with lead. Granulated metallic zinc or scraps of iron to the amount of about one-third of the quantity of silver and of other metals forming insoluble chlorides, originally in the gold, are then thrown into the same leadvat, and water and sulphuric acid are added, and the whole is occasionally stirred. The chloride of silver is thus reduced to metallic silver. The
gold is not attacked, and the excess of zinc or iron, if any, is dissolved out by sulphuric acid. If iron has been used to reduce chloride of silver, the solution ot'copperas thus obtained may be used to precipitate another solution of gold. After drawing oil the solution of zinc as closely as convenient from the reduced silver and gold the latter are thrown upon a filter. and thoroughly washed with water until the water ceases to give an acid reaction. The mixed "metallic gold and silver are next treated in vessels of glass or stone were by pure nitric acid, which dissolves out the. silver and other metals, if present, and leaves the gold. By drawing off the liquid and filtering and wash- .ing the remaining gold the gold is separated from silver and other metals, if present. The gold is melted in the usual manner. The silver is precipitated from its solution by common salt, as chloride of silver, which is reduced by zinc or iron and sulphuric and muriatic acid, as in the usual parting process.
Instead of dissolving out the reduced silver by nitric acid, it may also be dissolved out by heating the mixed silver and gold with oil ofvitriol in cast-iron vessels. Thevsolution of silver is precipitated by common salt or metallic copper, according to usual known methods. Although I prefer and claim as part of my 1 invention the use of vessels ofwood for mak ing solutions of alloyed gold, yet vessels of porcelain, stoneware, or of glass maybe used,
whichpmay be heated by steam, in a water bath, in a sand bath, or over the naked fire. Moreover, the form of the vessel may be varied. It might be made square, or oval, or round. It may be shallower or deeper; but I prefer the form I have described. The solution of gold may also be efl'ected in a similar manner to that above described in vessels of wood, as follows: I take one part of alloyed gold,
commerce, and three-fourths of one part of nitrate of potassa, or one-half of one part of nitrate of soda. 1 put the salt and gold, with a little water, into a wooden vessel like that before described, and pass steam into it. I then add about one-third of muriatic acid, still heating it, and after that. add the remaining two-thirds of the muiiatic acid gradually until solution is effected, as before.
The precipitation of metallic gold, reduction of chloride of silver, and dissolving out the metallic silver and other inetals are effected as before described. Vessels of porcelain, stoneware, or glass may also be employed in this variation of the process, and heated in the manner described.
It is not necessary that the salt should be first put into the vessel, for the whole of the mnriatic acid may be put in at once and steam applied until it is well heated, and then nitrate of potassa or of soda gradually added.
The mode of dissolving the gold may be further varied by putting one part gold and one part common salt into a vessel of wood, porcelain, stoneware, or glass, with a little water, heating the whole, and then adding strong nitric acid gradually until two and a half parts of nitric acid have been added.
The subsequent precipitation of metallic gold, reduction of chloride of silver, solution, and separation of metallic silver are the same ushave beendescribed. Another known method of dissolving gold may also be employed by the use ofa mixtnreofmuriatic and nitricacids, which process requires the use of vessels of porcelain, stoneware, or glass; or, if wooden vessels are employed, muriatic acid may he first put into such vessels, heated, and nitric acid gradually added. The subsequent steps of the process are the same as have been described.
The above processes may be still furthervaried by the use of chlorate of potassa instead otinitrate of soda or of potassa.
The second stage of the process-the precipitation of metallic gold in the solution-quay also be effected by adding to the solution containin g one part of gold, one part of sugar, molasses, or starch and a quantity of carbonated or caustic potassa or soda or caustic lime sufficient to superneutralize the free acid, keeping the whole in a boiling state until all, or nearly all, the gold is precipitated. If the precipitation be not immediately complete, it will complete itself by standing for some time. The liquid is drawn on from the gold after settling, the precipitate is washed, and then treated as above described for the separation of gold and chlorides.
The third stage of the operation may be so varied that the chloride of silver and other insoluble chlorides are directly dissolved ontfrom the metallic gold by any convenient solventsuch as hyposulphite of lime or of soda or caustic aqua-ammonia. The washed gold is melted as usual. The silver is obtained from the solution by known methods, and if it contain gold they may be separated by nitric or sulphuric acid. I
Some of the advantages of this invention for refining alloyed gold are that the largest quantities may be operated upon in a shorter time than is now practicable when acids alone are used; that this is the cheapest known method of refining gold, as the materialsor vchemical agents employed in this invention are of less cost than those used in any known plan; that the apparatus is one of easy and economical construction that the cost of previously preparing mnriatic or nitric acid,or both, may be saved by the use of the salts from which these acids are generated, instead of the acids themselves; that the processes under this invention may be conducted in cities and densely-populated places and districts without inconvenience or injury to the inhabitants; that they will yield a soft and malleable gold entirely free from silver and other metals,
which is not the case in the usualparting methods; that this invention will obviate the loss ofinterest attendant upon the keeping of a large amount of silver on hand for the purpose of refining gold, as is required in the usual processes, for in my invention the use of silver is not required; that by preventing the too rapid generation of volatile acid all waste in that article is avoided and the work men are enabled to proceed in their labors without any injury from the acids. Beside all these advantages, the gold,'when refined by this invention, is left in a suitably soft state, free from all brittleness, and ready at once for alloy for coining, which is frequently not the case with the known processes.
I do not claim the solution of gold in amix ture of nitric and mnriatic acids previously prepared, nor the methods of precipitation by copperas, nor by sugar and alkali, nor the reduction of chloride of silver by zinc and acid, unless the solution and precipitation be made in the same vessel without transfers. Small quantities of gold have beenrefined bya mixture of nitric and muriatic acids; but this method has not been carried out on a large scale, and has been deemed impracticable to a great extent on account of the cost of these acids, the noxious fumes arising from the process of solution, and the liability to loss in carrying or transferring a solution of gold. In the usual parting process nitric acid always leaves small quantities of silver and other metals when they have been melted with gold unless a very large excess of acid is employed, and in that event there would be no advantage in the process, as it would be too costly on a manufacturing or large scale.
What I claim as myinvention, and desire to secure by Letters Patent, is
1. The process of dissolving alloyed gold for refiningit by developing nitric acid or both nitric and muriatic acids gradually from their. salts, in the manner and for the purpose set forth in the specification.
2. The process of precipitating gold from its solution and removing therefrom the insoluble chlorides; as set forth.
3. The process of refiningalloyed gold without the use of-silver, so asto form a, solution of gold and other metals, and a residue of chloride of silver and of other insoluble chlorides, and then precipitating metallic gold npon'thosc insoluble chlorides in the same vessel without transfer after the solution is effected, and af- -terward dissolving out the insoluble chlorides from the gold or reducing the insoluble ch10 rides to the metallic state in the \vet way and dissolving out the metals from the gold, allin the manner hereinbefore described but I do the solvent liquids.
. JAS. O. BOOTH.
Witnesses:
LoUIs F. TOUCHERES, HENRY M". MOFFIT, W. THOMPSON.
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4857107A (en) * | 1985-09-12 | 1989-08-15 | Fine Metals Export Corporation Limited | Gold inquartation process |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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US4857107A (en) * | 1985-09-12 | 1989-08-15 | Fine Metals Export Corporation Limited | Gold inquartation process |
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