US1249787A - Apparatus for electrodeposition of metals. - Google Patents
Apparatus for electrodeposition of metals. Download PDFInfo
- Publication number
- US1249787A US1249787A US12380016A US12380016A US1249787A US 1249787 A US1249787 A US 1249787A US 12380016 A US12380016 A US 12380016A US 12380016 A US12380016 A US 12380016A US 1249787 A US1249787 A US 1249787A
- Authority
- US
- United States
- Prior art keywords
- electrolyte
- cathodes
- anodes
- tank
- cathode
- 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
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
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/463—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
-
- 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
- C25B9/13—Single electrolytic cells with circulation of an electrolyte
Definitions
- the invention re ates'more especially to apparatus of the character employed in electroplating and. resides in novel means whereby with great efiiciency and entire success the deposit may be carried on at a much greater speed than has heretofore been usual, without increasing the electro-motive force.
- a highly ionized solution or, electrolyte may be employed and a continuous and sound de position of the metal (copper or nickel) efliciently secured at more than the normal rate of speed incident to processes as heretofore practised.
- the invention resides more particularly in novel means within the tank of electrolyte and arranged with relation to the cathode and anode rods, whereby an eflicient and special agitation of the electrolytetakes place and the electrolyteis placed in steady circulation immediately adjacent to the cathode surfaces.
- my invention I maintain thesolution throughout the tank in substantially uniform condition by constantly moving the electrolyte upwardly along the cathode surfaces and bringing fresh electrolyte to said surfaces, not allowing the electrolyte .tov form into layers of di erent composition.
- My invention provides within the tankcontaining the electrolyte and having anode and cathode rods in proper distribution for supporting the anodes and cathodes, a series of perforated pipes to which air under pres sure in constant and proper quantity is sup-- moving away from the cathodes the exhausted or impoverished portions of the solution and creating a steady flow of the inexhaustedportions of the solution, at the cathode surfaces.
- My invention involves a new construction of apparatus and a novel method of procedure in the usethereof, whereby high eificiency and very beneficial results are attained.
- Figure 1 is a top view of a tank embodying the features of In invention
- Fig. 2 is a vertica f longitudinal section 2-2 of Fig. 1, the electrolyte being represented as in the tank and the arrows indicating, as nearly as may be, the-movement-of the electrolyte along the cathode surfaces under the force created by the air issuing from a series of air pi es located at the bottom of the tank with ue regard to the location of the cathodes and anodes;
- Fig. 3 is a transverse section through the tank
- Fig. 4 is a perspective view, partly broken away, of a modified arrangement of piping tncorppra-ting some of the features of my inventlon.
- 10 designates a customary lead-lined tank for holding the electrolyte 11.
- the tank 10 will vary in'size in accordance with the capacity desired for it.
- the free ends of the rods 14, 15 bear upon the bar 13 and the otherendsof the rods 14, 15 are provided respectively with book members 16,17 which engage upon metallic conducting rods 18, 19, respectively, which carry the current, as usual.
- the cathodes diagrammatically indicated in Fig.
- piping preferably lead, comprising pipe sections 24 extending along the inner loweredges of the sides of the tank, pipe sections 25 extending along the lower inner edges of the-ends of the tank and being in communication with the pipe sections 24 and transverse perforated pipe sectiom 26 connecting the aforesaid pipe sections 24.
- the pipe sections 25 are connected by vertical piping 27 with other piping 28 leadi'n from any suitable source of supply, not s own, of air. under pressure.
- the pipe sections 24, 25 are not perforated and all of the pi, e sections 26 are perforated and supplied with air under pressure from the pipe sections 24, and it is my purpose that the pipe sections 26 shall be supplied with a substantially constant volume ofair under uniform pressure, so that the air issuing from the perforations in said pipe sections 26 may act with uniformity on the electrolyte 11.
- pipe sections 26 are so disposed with respect to the locations for the anode and cathode rods 14, 15 that, as shown in Fig. 2, the air issuing from the perforations in the pipe sections 26 set up upward currents of the electrolyte between the cathodes and anodes.
- I preferably locate the pipe sections 26 so that in the arrangement of the anode and cathode rods and the anodes and cathodes suspended by them, said pipe sections 26 shall be slightly offset from the vertical plane of the faces of the cathodes on which the deposit is to take place, said pipe sections 26 thus being nearer to thecathodes than to the anodes, and this arrangement I deem highly desirable so as to obtain a greater agitation or a greater movement of the electrolyte along the cathode surfaces than along the anode surfaces.
- the more or less impoverished or exhausted electrolyte is naturally ator adjacent to the cathode surfaces, and for this reason I so dispose the pipe sections 26 that the air forcibly issuing from the perforations thereof may act against the electrolyte in close proximity to the cathode surfaces, said air operating to move the more or less impoverished or exhausted electrolyte from the front faces of the cathodes and causing the same to passover the cathodes and to the back thereof or to the spaces holding electrolyte which is in a less impoverished or exhausted state, whereby the electrolyte which has moved along the cathode surfaces becomes renewed and the electrolyte at the back of the cathodes is caused to flow up in between the cathodes and anodes and be efficient in the process being carried out.
- My invention regardless of the special character of the piping at the bottom of the tank, does, in respect to the perforations through which the air is forced, conform to the arrangement of the anode and cathode rods, the feature of the invention, regardless of thespecial piping, being that the air shall issue through a series of perforations directing it upwardly betwen the anodes and cathodes and preferably more closely along the front faces of the cathode than against the adjacent faces of the anodes, so that there may be a constant upward flow of the electrolyte along the front faces of the anodes, this flow or movement carrying away the partly exhausted or impoverished solution and replacing it with those parts of the solution which have not become so nearly exhausted or impoverished, and the constant change in the solution due to its agitation and flow, rendering the-solution substantlally uniform, since as ortions of the the solution become exhauste and move movement of the electrolyte in an upward direction along the front faces'of the cathodes.
- 30 indicates the supply pipes for air under pressure, 31 a non-perforated pipe to extend along the edges of the bottom of the tank, and 32 longitudinal perforated pipes con- ,necting the end members of .the piping 31.
- the perforations in the pipes 32 discharge upwardly between the cathodes and anodes and-are arranged to imitate, as far as possible," the.action of the perforated pipes shown in Fig. 1.
- Piping arranged as shown in Fig. 4 may be utilized to carry out my invention and effect the upward movement of the solution along the front faces of the cathodes by means of sheets of air bubbles, but it will be observed that in the'arrange, ment shown in Fig. 4 a larger number of pipes 32 must beemployed than the pipes 26 required in the arrangement shown in Fig. I.
- Apparatus of the character described I tor electroplating comprising a tank for the' electrolyte, anode and cathode supports,
- Apparatus of the character described for electroplating comprising a tank for the electrolyte, anode and cathode supports, with their current connections, means for suspending from said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of the inner walls of said tank and spaced apart, and piping at the bottom of said tank below said anodes and cathodes and affording a series of outlets .of suflicient area for the discharge of adequate quantities of air upwardly through the spaces separating the cathodes and anodes for acting on .the electrolyte and keeping the same in constant upward circulation and movin the impoverished electrolyte from the catihode surfaces and causin the same.
- An apparatus of the character described for ele'ctro-plating comprising a tank for the electrolyte, anode and cathode supports, with their current connections, means for suspending from said supports submerged in said electrolyte and free of the inner walls of said tank and spaced apart, and piping at the bottom of said tank below said anodes and cathodes and affording a series of outlets of sufiicient area for the discharge of adequate quantities of air upwardly through the spaces separating the cathodes and anodes for acting on the electrolyte and keeping the same in constant upward circulation and moving the impoverished electrolyte from the cathode surfaces and causing the same to pass over to the back thereof, and said iping comprising a. series of transverse per orated pipes disposed between the vertical planes of the cathodes and anodes and located closer to the plane of the front face of the cathodes than to the adjacent face of the anodes.
- Apparatus of the character described for electro-plating comprising a tank for the electrolyte,.anode and cathode supports, with .their current connections, means for suspending from'said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of the inner walls of said tank and spaced apart, and means at the bottom of saidtank below said anodes and cathodes and disposed between the vertical planes of the same forsupplying air under pressure and in adequate quantities for acting on the electrolyte between the anodes and cathodes and keeping said electrolyte inconstant upward circulation and moving the impoverished elec-' trolyte from the cathode surfaces and causing the same to pass over to the back thereof.
- Apparatus of the character described for electro-plating comprising a tank for the electrolyte, anode and cathode supports, with their current connections, means for suspending from said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of the inner walls of said. tank and spaced apart, and
- said air supplying means being disposed closer to the plane of-the front face bfthe cathodes than to the adjacent face of the anodes.
- Apparatus of the character described for electro-plating comprising a tank for the electrolyte, anode and cathode supports, with their current connections, means for suspending from said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of the inner walls of said tank and spaced apart, and piping at the bottom of said tank below said anodes and cathodes and affording a series of outlets of suflicient area for the discharge of adequate quantities of air upwardly through the spaces separating the cathodes and anodes for acting on the electrolyte and keeping the same in constant upward circulation and moving the impoverished electrolyte from the cathode surfaces and causing the same to pass over to the back thereof, and saidpiping comprising a line of imperforate pipe extending along the lower inner edges of the sides and ends of the tank, air supplying pipes connected therewith and perforated pipes communicating with the pipe system and having the aforesaid outlets through which the air is discharged.
- Apparatus of thei character described for electro-plating comprising a tank for the electrolyte, anode and cathode supports,
- said piping comprising a line of imperforate pipe extending ends of the tank, air supplying pipes connected therewith and perforated pipes communicating with the pipe system and having the aforesaid outlets through which the air is discharged and being disposed closer tothe vertical plane of the front face of the cathodes than to the adjacent faces of the anodes.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Electrolytic Production Of Metals (AREA)
- Hybrid Cells (AREA)
- Electroplating Methods And Accessories (AREA)
Description
A. LEUCHTER. f 1 APPARATUS FOR'ELEBTRODEPOSITION 0F METALS.
I I APPLICATION min 001:5. ms. -1',249,787 1 Patented Dec. 11,1917.
. 1 2 SHEETS-SHEET w.
l t J l T7. I l' I I1 mm ll2r+ Y A. LEUCHTER. APPARATUSFOR ELECTRODEPOSITION 0F METALS.
APPLICATION man ocT. 5. ms. k Patented D00. 11, 1917.
I v 2 gains-shin 2.
AUGUST Lnuunrnn, or
PATENT orricn BROOKLYN, new YORK.
, APPARATUS FOR ELECTRODEPOSITION OF METALS.
Specification of Letters Patent.
Patented Dec. 11, 1917.
Application filed October 5, 1916. Serial No. 123,800.
To all wltom it may concern:
Be it known that I, AUGUST LEUCHTER,
a citizen of the United States, and a resident of Brooklyn, in thecounty of Kings and State of New York, have invented certain new and useful Improvements in Appa-- ratus for Electrodeposition of Metals, of which the followin is a specification.
The invention re ates'more especially to apparatus of the character employed in electroplating and. resides in novel means whereby with great efiiciency and entire success the deposit may be carried on at a much greater speed than has heretofore been usual, without increasing the electro-motive force. With the use of my invention a highly ionized solution or, electrolyte may be employed and a continuous and sound de position of the metal (copper or nickel) efliciently secured at more than the normal rate of speed incident to processes as heretofore practised.
The invention resides more particularly in novel means within the tank of electrolyte and arranged with relation to the cathode and anode rods, whereby an eflicient and special agitation of the electrolytetakes place and the electrolyteis placed in steady circulation immediately adjacent to the cathode surfaces. With my invention I maintain thesolution throughout the tank in substantially uniform condition by constantly moving the electrolyte upwardly along the cathode surfaces and bringing fresh electrolyte to said surfaces, not allowing the electrolyte .tov form into layers of di erent composition. Variousmeans have heretofore been employed to efl'ect a gentle agitation of the electrolyte in the tank, and while they have been more or less beneficial in their use, it has not, I believe, been possible heretofore to secure a continuous and sound deposition of the metal in a highly ionized solution. I
My invention provides within the tankcontaining the electrolyte and having anode and cathode rods in proper distribution for supporting the anodes and cathodes, a series of perforated pipes to which air under pres sure in constant and proper quantity is sup-- moving away from the cathodes the exhausted or impoverished portions of the solution and creating a steady flow of the inexhaustedportions of the solution, at the cathode surfaces.
My invention involves a new construction of apparatus and a novel method of procedure in the usethereof, whereby high eificiency and very beneficial results are attained.
The invention will bev fully understood from the detailed description hereinafter presented, reference being had to the accompanying drawings, in which:
Figure 1 is a top view of a tank embodying the features of In invention;
Fig. 2 is a vertica f longitudinal section 2-2 of Fig. 1, the electrolyte being represented as in the tank and the arrows indicating, as nearly as may be, the-movement-of the electrolyte along the cathode surfaces under the force created by the air issuing from a series of air pi es located at the bottom of the tank with ue regard to the location of the cathodes and anodes;
Fig. 3 is a transverse section through the tank; and
Fig. 4 is a perspective view, partly broken away, of a modified arrangement of piping tncorppra-ting some of the features of my inventlon.
In the drawings, 10 designates a customary lead-lined tank for holding the electrolyte 11. The tank 10 will vary in'size in accordance with the capacity desired for it. Upon the upper longitudinal edges of the sides of the tank 10 are the customary supportmg bars 12, 13 for the cathode and anode rods 14, 15, respectively. The free ends of the rods 14, 15 bear upon the bar 13 and the otherendsof the rods 14, 15 are provided respectively with book members 16,17 which engage upon metallic conducting rods 18, 19, respectively, which carry the current, as usual. The cathodes, diagrammatically indicated in Fig. 2, and numbered 20 are suspended by the usual hook-members 21 from the rods l t; and the anodes 22 are suspended by customary hook-members 23 from the anode rods 15. I do not claim that there is anything new in the specific construction of the bars 12, 13, cathode and anode rods 14, 15 and hook members 21, 23, since these parts are individually of customary characand, as shown in Fig. 2, locate one of the anode rods 15 between each'two of the cathode rods 14, this arrangement being preferred because it brings one anode 22 between the front faces of two cathodes on which it is desired to .deposit. In Fig. 2 I show a series of three units each composed of an anode with one cathode at each side thereof, but of course as many units of this character as may be desired may be employed, in accordance with the size of the tank 10, and further so long as themore essential features ofimy invention are preserved I do not limit myself to the special arrangement of the anodes and cathodes illustrated, since with less advantage it is obvious that one anode may be employed for each cathode, instead of, as I illustrate, one anode for two cathodes. I would call attention to the fact, however, that in the most efficient practice of my invention the oathodes and anodes'must be independent of and separated from each other in series, that they must be suspended vertically, that they must be submerged in the electrolyte and that there must be adequate free spaces at the bottom, top and side edges of the'cathodes and anodes for that character of circulation of the electrolyte which permits of the use of a more highly ionized solution or electrolyte than it has heretofore been thought possible to employ and assures the sound deposition of the metal (copper or nickel) at greater speed than has heretofore been thong t possible or accomplished; and all this without increasing the electro-motive force. It may be seen on reference to Fig. 2, that the cath-' odes and anodes are submerged and vertical and separated from and independent of each other, and on reference to Fig. 3 it may be seen-that abundant free space is provided between the bottom and side edges of the cathodes and anodes and the bottom and sides of the tank.
Upon or adjacent to the bottom of the tank 10 I provide 'a set of piping, preferably lead, comprising pipe sections 24 extending along the inner loweredges of the sides of the tank, pipe sections 25 extending along the lower inner edges of the-ends of the tank and being in communication with the pipe sections 24 and transverse perforated pipe sectiom 26 connecting the aforesaid pipe sections 24. The pipe sections 25 are connected by vertical piping 27 with other piping 28 leadi'n from any suitable source of supply, not s own, of air. under pressure. The pipe sections 24, 25 are not perforated and all of the pi, e sections 26 are perforated and supplied with air under pressure from the pipe sections 24, and it is my purpose that the pipe sections 26 shall be supplied with a substantially constant volume ofair under uniform pressure, so that the air issuing from the perforations in said pipe sections 26 may act with uniformity on the electrolyte 11. The fact that the pipe sections 24, 25, 27 are imperforate, permits me to discharge air under adequate pressure and in sutlicient quantity for the purposes of my invention through the perforations in the pipe sections 26.
An important feature of my invention is that the pipe sections 26 are so disposed with respect to the locations for the anode and cathode rods 14, 15 that, as shown in Fig. 2, the air issuing from the perforations in the pipe sections 26 set up upward currents of the electrolyte between the cathodes and anodes. I preferably locate the pipe sections 26 so that in the arrangement of the anode and cathode rods and the anodes and cathodes suspended by them, said pipe sections 26 shall be slightly offset from the vertical plane of the faces of the cathodes on which the deposit is to take place, said pipe sections 26 thus being nearer to thecathodes than to the anodes, and this arrangement I deem highly desirable so as to obtain a greater agitation or a greater movement of the electrolyte along the cathode surfaces than along the anode surfaces. The more or less impoverished or exhausted electrolyte is naturally ator adjacent to the cathode surfaces, and for this reason I so dispose the pipe sections 26 that the air forcibly issuing from the perforations thereof may act against the electrolyte in close proximity to the cathode surfaces, said air operating to move the more or less impoverished or exhausted electrolyte from the front faces of the cathodes and causing the same to passover the cathodes and to the back thereof or to the spaces holding electrolyte which is in a less impoverished or exhausted state, whereby the electrolyte which has moved along the cathode surfaces becomes renewed and the electrolyte at the back of the cathodes is caused to flow up in between the cathodes and anodes and be efficient in the process being carried out.
My invention, regardless of the special character of the piping at the bottom of the tank, does, in respect to the perforations through which the air is forced, conform to the arrangement of the anode and cathode rods, the feature of the invention, regardless of thespecial piping, being that the air shall issue through a series of perforations directing it upwardly betwen the anodes and cathodes and preferably more closely along the front faces of the cathode than against the adjacent faces of the anodes, so that there may be a constant upward flow of the electrolyte along the front faces of the anodes, this flow or movement carrying away the partly exhausted or impoverished solution and replacing it with those parts of the solution which have not become so nearly exhausted or impoverished, and the constant change in the solution due to its agitation and flow, rendering the-solution substantlally uniform, since as ortions of the the solution become exhauste and move movement of the electrolyte in an upward direction along the front faces'of the cathodes. I have found from practical experience that wlth the use of my invention I am enabled to use a more highly ionized electrolyteor solution than has been possible by the methods heretofore practised, and in consequence thereof I am enabled to effect the deposition of the metal (copper or nickel) more rapidly than hasbeen possible heretofore, and I accomglish the deposition of the metal in a very e cient and satisfactory manner, the deposition being uniform and-of sound formation. I could notemploy my highly ionized solution or electrolyte exce t for my arrangement of piping for the dlscharge of the air under pressure in sufiicient volume and in proper location to effect the constant and adequate circulation of the solution, and this circulation is so efiected as not to disturb the proper deposition of the metal on the cathodes or to cause the ire-distribution of the sludge from the -anodes into those portions of the solution designed for depositing on the cathodes.
In the modification shown in Fig. 4, 30 indicates the supply pipes for air under pressure, 31 a non-perforated pipe to extend along the edges of the bottom of the tank, and 32 longitudinal perforated pipes con- ,necting the end members of .the piping 31. The perforations in the pipes 32 discharge upwardly between the cathodes and anodes and-are arranged to imitate, as far as possible," the.action of the perforated pipes shown in Fig. 1. Piping arranged as shown in Fig. 4 may be utilized to carry out my invention and effect the upward movement of the solution along the front faces of the cathodes by means of sheets of air bubbles, but it will be observed that in the'arrange, ment shown in Fig. 4 a larger number of pipes 32 must beemployed than the pipes 26 required in the arrangement shown in Fig. I.
at I claim as my invention and desire to secure by Letters Patent, is:
1. Apparatus of the character described I tor electroplating, comprising a tank for the' electrolyte, anode and cathode supports,
with their current connections, means for suspendin from said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of theinner walls of said tankand spaced apart, and piping at the bottom of said tank belowsaid anodes and cathodes and affording a series of outlets of suflicient area for the discharge of adequate quantities of air upwardly through the spaces separating the cathodes and anodes for acting on the electrolyte and keeping the same in constant upward circulation and moving the impoverished electrolyte from the cathode surfaces and causing the same to pass over to the back thereof.
2. Apparatus of the character described for electroplating, comprising a tank for the electrolyte, anode and cathode supports, with their current connections, means for suspending from said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of the inner walls of said tank and spaced apart, and piping at the bottom of said tank below said anodes and cathodes and affording a series of outlets .of suflicient area for the discharge of adequate quantities of air upwardly through the spaces separating the cathodes and anodes for acting on .the electrolyte and keeping the same in constant upward circulation and movin the impoverished electrolyte from the catihode surfaces and causin the same. to pass over to the back thereo the vertical plane of the air-outlets being closer to the plane of the front face of the cathodes than to the adjacent face of the piping at the bottom of "said tank below said anodes and cathodes and affording a series of outlets of suflicient area for the discharge of adequate quantities of air upwardly through ,the spaces separating the cathodes and anodes for acting on the electrolyte and. keeping the same in constant upward circulation and moving the impoverished electrolyte from the cathode surfaces'and causing the same to pass over to the back thereof, and said piping comprising a series of transverse perforated pipes disposed between the vertical planes of the cathodes and anodes.
4. An apparatus of the character described for ele'ctro-plating, comprising a tank for the electrolyte, anode and cathode supports, with their current connections, means for suspending from said supports submerged in said electrolyte and free of the inner walls of said tank and spaced apart, and piping at the bottom of said tank below said anodes and cathodes and affording a series of outlets of sufiicient area for the discharge of adequate quantities of air upwardly through the spaces separating the cathodes and anodes for acting on the electrolyte and keeping the same in constant upward circulation and moving the impoverished electrolyte from the cathode surfaces and causing the same to pass over to the back thereof, and said iping comprising a. series of transverse per orated pipes disposed between the vertical planes of the cathodes and anodes and located closer to the plane of the front face of the cathodes than to the adjacent face of the anodes.
5. Apparatus of the character described for electro-plating, comprising a tank for the electrolyte,.anode and cathode supports, with .their current connections, means for suspending from'said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of the inner walls of said tank and spaced apart, and means at the bottom of saidtank below said anodes and cathodes and disposed between the vertical planes of the same forsupplying air under pressure and in adequate quantities for acting on the electrolyte between the anodes and cathodes and keeping said electrolyte inconstant upward circulation and moving the impoverished elec-' trolyte from the cathode surfaces and causing the same to pass over to the back thereof.
6. Apparatus of the character described for electro-plating, comprising a tank for the electrolyte, anode and cathode supports, with their current connections, means for suspending from said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of the inner walls of said. tank and spaced apart, and
means at the bottom of said tank below said I anodes and cathodes and disposed between the vertical planes of the same for supplying air under pressure and in adequate quantities for acting on the electrolyte between the anodes and cathodes and keeping said electrolyte in constant upward circulation and moving the impoverished electrolyte from the cathode surfaces and causing the same to pass over-to the back thereof, said air supplying means being disposed closer to the plane of-the front face bfthe cathodes than to the adjacent face of the anodes.
7, Apparatus of the character described for electro-plating, comprising a tank for the electrolyte, anode and cathode supports, with their current connections, means for suspending from said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of the inner walls of said tank and spaced apart, and piping at the bottom of said tank below said anodes and cathodes and affording a series of outlets of suflicient area for the discharge of adequate quantities of air upwardly through the spaces separating the cathodes and anodes for acting on the electrolyte and keeping the same in constant upward circulation and moving the impoverished electrolyte from the cathode surfaces and causing the same to pass over to the back thereof, and saidpiping comprising a line of imperforate pipe extending along the lower inner edges of the sides and ends of the tank, air supplying pipes connected therewith and perforated pipes communicating with the pipe system and having the aforesaid outlets through which the air is discharged.
8. Apparatus of thei character described for electro-plating, comprising a tank for the electrolyte, anode and cathode supports,
with their current connections, means for suspending from said supports the anodes and cathodes in vertical position submerged in said electrolyte and free of the inner walls of said tank and spaced apart, and piping at the bottom of said tank below said anodes and cathodes and affording a series of outlets of suflicient area for the discharge of adequate quantities of air upwardly through the spaces separating the cathodes and. anodes for acting on the electrolyte and keeping the same in constant upward circulation and moving the impoverished electrolyte from the cathode surfaces and causing the same to pass over to the back thereof, and said piping comprising a line of imperforate pipe extending ends of the tank, air supplying pipes connected therewith and perforated pipes communicating with the pipe system and having the aforesaid outlets through which the air is discharged and being disposed closer tothe vertical plane of the front face of the cathodes than to the adjacent faces of the anodes.
' Signed at New York city, in the county of New York and State of New York, this 26th day of September A. D. 1916.
, AUGUST LEUCHTER.
Witnesses: I
ARTHUR MARION, CHAS. O. Grim.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12380016A US1249787A (en) | 1916-10-05 | 1916-10-05 | Apparatus for electrodeposition of metals. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12380016A US1249787A (en) | 1916-10-05 | 1916-10-05 | Apparatus for electrodeposition of metals. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1249787A true US1249787A (en) | 1917-12-11 |
Family
ID=3317520
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12380016A Expired - Lifetime US1249787A (en) | 1916-10-05 | 1916-10-05 | Apparatus for electrodeposition of metals. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1249787A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2478189A (en) * | 1944-03-08 | 1949-08-09 | Falconbridge Nickel Mines Ltd | Production of malleable and annealable nickel |
| US3412004A (en) * | 1965-09-10 | 1968-11-19 | Enthone | Test plating equipment and method |
| US3503856A (en) * | 1968-01-30 | 1970-03-31 | Rotary Plates Ltd | Process for controlling electrodeposition |
| US4189356A (en) * | 1976-12-17 | 1980-02-19 | Whittaker Corporation | Method for plating copper on steel rods |
-
1916
- 1916-10-05 US US12380016A patent/US1249787A/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2478189A (en) * | 1944-03-08 | 1949-08-09 | Falconbridge Nickel Mines Ltd | Production of malleable and annealable nickel |
| US3412004A (en) * | 1965-09-10 | 1968-11-19 | Enthone | Test plating equipment and method |
| US3503856A (en) * | 1968-01-30 | 1970-03-31 | Rotary Plates Ltd | Process for controlling electrodeposition |
| US4189356A (en) * | 1976-12-17 | 1980-02-19 | Whittaker Corporation | Method for plating copper on steel rods |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104160067B (en) | Method of operating an electrolysis cell and cathode frame | |
| US7431810B2 (en) | Apparatus for controlling flow in an electrodeposition process | |
| US3682809A (en) | Electrolytic cell constructed for high circulation and uniform flow of electrolyte | |
| US1249787A (en) | Apparatus for electrodeposition of metals. | |
| US3558466A (en) | Electrolytic cell | |
| US4263120A (en) | Electrolytic cell for the recovery of nonferrous metals and improved anode therefor | |
| CN102839407A (en) | Piston rapid aluminum oxidation single machine | |
| US4062755A (en) | Electroplating anode plenum | |
| US4517064A (en) | Electrolytic cell | |
| JP4355790B2 (en) | Electrolytic apparatus and electrolytic treatment method | |
| KR20030082447A (en) | Process for the Electrochemical Decomposition of Powders and Eletrolysis Cells Suitable Therefor | |
| JP2009019250A (en) | Method and apparatus for producing metal | |
| CN105734636A (en) | Novel electroplating equipment | |
| JPS646280B2 (en) | ||
| US1535185A (en) | Electrolytic apparatus | |
| US2598228A (en) | Electrolytic apparatus | |
| US2739116A (en) | Electrolytic manganese cell | |
| US2578839A (en) | Nickel liberator cell | |
| US1145593A (en) | Electrolytic cell and method of maintaining the efficiency thereof. | |
| JPH01159400A (en) | Tin electroplating device | |
| US1022561A (en) | Electroplating apparatus. | |
| US1389829A (en) | Method of electrolyzing a solution of nickel salt | |
| US1978356A (en) | Electrolytic apparatus | |
| US2271341A (en) | Electrolytic cell for producing | |
| US1420212A (en) | Method of and apparatus for electrolytic reduction and oxidation |