US605835A - Emile andreoli and gabriel andreoli - Google Patents
Emile andreoli and gabriel andreoli Download PDFInfo
- Publication number
- US605835A US605835A US605835DA US605835A US 605835 A US605835 A US 605835A US 605835D A US605835D A US 605835DA US 605835 A US605835 A US 605835A
- Authority
- US
- United States
- Prior art keywords
- andreoli
- amalgam
- mercury
- sodium
- emile
- 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
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- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 32
- 229910000497 Amalgam Inorganic materials 0.000 description 30
- 229910052753 mercury Inorganic materials 0.000 description 26
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 18
- 229910052802 copper Inorganic materials 0.000 description 18
- 239000010949 copper Substances 0.000 description 18
- 229910052708 sodium Inorganic materials 0.000 description 16
- 239000011734 sodium Substances 0.000 description 16
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 10
- 239000011248 coating agent Substances 0.000 description 8
- 238000000576 coating method Methods 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 8
- 239000002184 metal Substances 0.000 description 8
- 239000010454 slate Substances 0.000 description 8
- 229910001023 sodium amalgam Inorganic materials 0.000 description 8
- 210000000188 Diaphragm Anatomy 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000005755 formation reaction Methods 0.000 description 6
- 239000011521 glass Substances 0.000 description 6
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 6
- 229910052737 gold Inorganic materials 0.000 description 6
- 239000010931 gold Substances 0.000 description 6
- 229910052573 porcelain Inorganic materials 0.000 description 6
- WGSLWEXCQQBACX-UHFFFAOYSA-N Chlorin Chemical compound C=1C(C=C2)=NC2=CC(C=C2)=NC2=CC(C=C2)=NC2=CC2=NC=1CC2 WGSLWEXCQQBACX-UHFFFAOYSA-N 0.000 description 4
- 229920001875 Ebonite Polymers 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000005554 pickling Methods 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 229910052709 silver Inorganic materials 0.000 description 4
- 239000004332 silver Substances 0.000 description 4
- 241000700605 Viruses Species 0.000 description 2
- 238000005267 amalgamation Methods 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 150000004035 chlorins Chemical class 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 229910052571 earthenware Inorganic materials 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 238000005065 mining Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000009877 rendering Methods 0.000 description 2
- 238000009991 scouring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/02—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
- C25B11/033—Liquid electrodes
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/30—Cells comprising movable electrodes, e.g. rotary electrodes; Assemblies of constructional parts thereof
- C25B9/303—Cells comprising movable electrodes, e.g. rotary electrodes; Assemblies of constructional parts thereof comprising horizontal-type liquid electrode
Definitions
- the object of this invention is the electrolytic production of amalgams and their utilization with or without the electric current for coating copper or other metal plates in a simple, economical, and instantaneous manner, and thus rendering them available for the recovery of, gold or silver by amalgamation, or in the mortar-mill Where the auriferous ores are crushed, or for other suitable purposes.
- Figure 1 is a perspective view of what I call the electrolyzer.
- Figs. 2 and 3 are side elevations of a partition.
- Fig. 4 is a cross-section of .the same, and
- Fig. 5 is a cross-section of a special form of amalgamator.
- One of our apparatuses consists of a vessel where the amalgam is prepared, which we will call the electrolyzer, and another is a tank or vat which we will call the amalgamator.
- Fig. 1 shows the electrolyzer ready for working.
- A is a vat made of slate or earthenware or other convenient material, which is divided into positive and negative compartments by porous partitions a.
- the positive compartments 1) 1) contain anodes made of iron or copper plates or other suitable material. As soon as the current passes through the solution chlorin is formed in the positive compartments, which may be collected or allowed to pass off- The sodium goes throughthe partitions to the negative compartment 0, which contains mercury d, with which it unites and forms a sodium amalgam.
- the mercury is preferably covered with waterdeep enough to fill tity of sodium-i. 6., when thesodium amalgam is rich enough to amalgamate the copper -we open the tap f to allow it to run out and througha suitable pipe intothe amalgamator.
- the electrolyzer is refilled with fresh mercury and the electrolyticjoperation continues in the same manner with the formationof-chlorin or chlorin compounds at the positive and sodium amalgam at the negative poles.
- the partitions 0L1 can ;be ma de.ofporous' L porcelain or similar material.
- Fig. 2 shows a framed perforated slate plate a.
- rods 12 made of glass, porcelain,
- the amalgamator is a large shallow vat divided into three compartments and is of the same general construction as the electrolyzer.
- the two outer compartments are filled with a concentrated solution of chlorid of sodium and are provided with suitable anodes, while in the middle compartment the sodium amalgam arrives from the electrolyzer. It is connected to the negative pole of the source of electricity, so that while the amalgamating process is going on more metallic sodium is being supplied to the mercury from the outercompartments and partly keeps the strength of the amalgam.
- the amalgamator can be used dry; but it is sometimes advisable to cover the mercury amalgam with water.
- ⁇ Ve generally find it preferable to .do without the electrolyzer and to produce and apply the amalgam in the same vessel.
- Our preferred apparatus which will now be described, enables us to produce sodium amalgam on a large scale and to amalgamate large surfaces of metal plates with a comparatively small amount of mercury.
- the apparatus which may be of any dimensions, is divided into three compartments by means of porous partitions, as hereinbefore stated.
- the central compartment would require an enor: mous quantity of mercury to be proportionate with the surface of the porous diaphragms which separate the annode and cathode compartments, and this would not be practicable on account of the expense; but we overcome this difiiculty by fixing in the central compartment a rectangular mass 2' of cement or other substance in such a manner as to leave only a small interspace between it and the porous partitions, which a small quantity of quicksilver will fill up.
- the top of this mass 2' is covered with a layer of mercury, which extends down into and fills the said interspaces, forming a continuous body of mer-
- the sodium beinglighter rises as fast cury.
- the sodium is deposited on the vertical mecurial cathodes and rises to the surface, where the layer of mercury which covers the amalgamated mass absorbs it and forms an amalgam as rich as required, which may be used with or without the aid of the electric current either for mcrcurizing copper orother metal plates or in the mining districts for the recovery of gold in batteries or in amalgamating pans.
- the copper plates when undergoing the amalgamatin g process, are dipped into the vertical portions of tho mercury-cathode, as indicated at e, and this may be done simultaneously with the formation of the amalgam.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Description
(No Model.)
. & G. ANDREOLI;
vE ELECTROLYTIC PRODUCTION OF AMALGAMS No. 605,835.
,&c. Patented June 21',
INVENTORS llllllllll? N v 1 WITNESSES TH: wonms virus on. pnafouma. wAsulnarbN, u. c.
-* UN IT D STATES PATENT OFFICE.
EMILE ANDREOLI AN GABRIEL ANDREOLI, or LoNDoN, ENGLAND.
ELECTROLYTIC PRODUCTION OF AMALGAMS 84.0.
SPECIFICATION forming part of Letters Patent No. 605,835, dated June 21, 1898. Application filed September 1'7, 1895. Serial No. 562,8 14 (N0 model.) Patentedin England August 9, 1895, No. 15,024.
T0 at whom it may concern.-
Be it known that we, EMILE ANDREOLI and GABRIELANDR OLI, citizens of France, residing at London, in the county of Surrey, England, have invented certain new and useful Improvements in Electrolytic Production of Amalgams and their Utilization, ofwhich the following is a full, clear, and exact description, the same having been patented in England August 9, 1895, No. 15,024.
The object of this invention is the electrolytic production of amalgams and their utilization with or without the electric current for coating copper or other metal plates in a simple, economical, and instantaneous manner, and thus rendering them available for the recovery of, gold or silver by amalgamation, or in the mortar-mill Where the auriferous ores are crushed, or for other suitable purposes.
We shall hereinafter describe the formation of an amalgam of sodium and a processfor coating copper o'rothenmetal plates with nercury, so as to render them available for amalgamating gold or silver. In the ordinaryway this coating, requires skilled labor and consists of troublesome operations for scouringand pickling the, copper plates before they can absorbv quicksilver; but accordingto our invention" as soon as the amalgam comes in contact with the plates of copper or other metal they become thoroughly amalgamated without having been submitted to any scouring, cleaning, or pickling.
In the accompanying drawings, Figure 1 is a perspective view of what I call the electrolyzer. Figs. 2 and 3 are side elevations of a partition. Fig. 4 is a cross-section of .the same, and Fig. 5 is a cross-section of a special form of amalgamator. I
One of our apparatuses consists of a vessel where the amalgam is prepared, which we will call the electrolyzer, and another is a tank or vat which we will call the amalgamator.
Fig. 1 shows the electrolyzer ready for working.
A is a vat made of slate or earthenware or other convenient material, which is divided into positive and negative compartments by porous partitions a.
In the following'description of the working of the electrolyzer we will take as an illustrationthe formation of an amalgam from a concentrated chlorid-of-sodium solution and the coating of copper plates with mercury under the influence of the electric current in the cathode-compartment.
The positive compartments 1) 1) contain anodes made of iron or copper plates or other suitable material. As soon as the current passes through the solution chlorin is formed in the positive compartments, which may be collected or allowed to pass off- The sodium goes throughthe partitions to the negative compartment 0, which contains mercury d, with which it unites and forms a sodium amalgam. I
In order to expose a large area of mercury to the electrolytic action, the mercury is preferably covered with waterdeep enough to fill tity of sodium-i. 6., when thesodium amalgam is rich enough to amalgamate the copper -we open the tap f to allow it to run out and througha suitable pipe intothe amalgamator.
The electrolyzer is refilled with fresh mercury and the electrolyticjoperation continues in the same manner with the formationof-chlorin or chlorin compounds at the positive and sodium amalgam at the negative poles.
' From time to time the chlorid-of-sodium solution is strengthened by the addition of moresalt.
The partitions 0L1 can ;be ma de.ofporous' L porcelain or similar material.
We mayalso have-them constructed in thefollowing manner: Fig. 2 shows a framed perforated slate plate a. On the side facing the anolyte,where chlorin is formed, we cover this perforated plate with rods 12 made of glass, porcelain,
ebonite, paraffined wood, or the like, Fig. 3, which we fix on the slate close to one another, so as to form a sort of wall, which allows electrocapillarity, but not diffusion of liquids.
To make sure that there is no liquid passv ing from the positive to the negative compartments, we may cover the glass or other rods with a layer of peroxid of manganese 12 which is kept in situ by a second perfo- IOO rated plate a, of slate, ebonite, or other similar material, provided with glass, porcelain, or other rods, as hereinbefore described.
The amalgamator is a large shallow vat divided into three compartments and is of the same general construction as the electrolyzer. The two outer compartments are filled with a concentrated solution of chlorid of sodium and are provided with suitable anodes, while in the middle compartment the sodium amalgam arrives from the electrolyzer. It is connected to the negative pole of the source of electricity, so that while the amalgamating process is going on more metallic sodium is being supplied to the mercury from the outercompartments and partly keeps the strength of the amalgam.
The amalgamator can be used dry; but it is sometimes advisable to cover the mercury amalgam with water.
Our apparatus can be embodied in any con- "enient shape or size, and we do not confine ourselves to any particular form or dimension.
\Ve generally find it preferable to .do without the electrolyzer and to produce and apply the amalgam in the same vessel.
Our preferred apparatus, which will now be described, enables us to produce sodium amalgam on a large scale and to amalgamate large surfaces of metal plates with a comparatively small amount of mercury.
The apparatus, which may be of any dimensions, is divided into three compartments by means of porous partitions, as hereinbefore stated. Under ordinary circumstances the central compartment would require an enor: mous quantity of mercury to be proportionate with the surface of the porous diaphragms which separate the annode and cathode compartments, and this would not be practicable on account of the expense; but we overcome this difiiculty by fixing in the central compartment a rectangular mass 2' of cement or other substance in such a manner as to leave only a small interspace between it and the porous partitions, which a small quantity of quicksilver will fill up. The top of this mass 2' is covered with a layer of mercury, which extends down into and fills the said interspaces, forming a continuous body of mer- The sodium beinglighter rises as fast cury.
as it is produced by the electrolysis between the sides of the above-mentioned amalgamated mass i and the porous diaphragm. Th us however wide and long may be the thin layer of mercury on the top of the amalgamated mass, however shallow or deep may be the compartments, the conductivity and efiiciency of the electrolytic apparatus will be at the maximum, and plates forty square feet would be as well and rapidly amalgamated as if their surface was only four feet. The reaction which takes place is so well known that we need not state it. The sodium is deposited on the vertical mecurial cathodes and rises to the surface, where the layer of mercury which covers the amalgamated mass absorbs it and forms an amalgam as rich as required, which may be used with or without the aid of the electric current either for mcrcurizing copper orother metal plates or in the mining districts for the recovery of gold in batteries or in amalgamating pans. The copper plates, when undergoing the amalgamatin g process, are dipped into the vertical portions of tho mercury-cathode, as indicated at e, and this may be done simultaneously with the formation of the amalgam.
Other arrangements of the same kind can be devised for obtaining a large surface with a minimum quantity of quicksilver in the commercial production and application of amalgam.
Having now described our invention, what we claim is- An apparatus for the production of amalgam consisting of a cell provided with positive and negative compartments separated by porous diaphragms, the negative compartments having a raised middle portion in the form of a table or block between the sides of which and the said partitions are narrow vertical spaces, the top of the block or table and the vertical spaces being covered and filled with a continuous body of mercury forming acathode, substantiallyas described.
In testimony whereof we subscribe our signatures in presence of two witnesses.
E. ANDREOLI. GABRIEL ANDRROTJ. lVitnesses:
JOHN NETHERWAY, J. F. Gnavns.
Publications (1)
Publication Number | Publication Date |
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US605835A true US605835A (en) | 1898-06-21 |
Family
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US605835D Expired - Lifetime US605835A (en) | Emile andreoli and gabriel andreoli |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2773820A (en) * | 1944-09-14 | 1956-12-11 | Robert Q Boyer | Electrolytic process of salvaging uranium |
-
0
- US US605835D patent/US605835A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2773820A (en) * | 1944-09-14 | 1956-12-11 | Robert Q Boyer | Electrolytic process of salvaging uranium |
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