US1428050A - Electrolytic apparatus and method of depolarizing the same - Google Patents
Electrolytic apparatus and method of depolarizing the same Download PDFInfo
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- US1428050A US1428050A US375502A US37550220A US1428050A US 1428050 A US1428050 A US 1428050A US 375502 A US375502 A US 375502A US 37550220 A US37550220 A US 37550220A US 1428050 A US1428050 A US 1428050A
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- 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
- C25B15/00—Operating or servicing cells
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/007—Current directing devices
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/10—Electrodes, e.g. composition, counter electrode
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/04—Removal of gases or vapours ; Gas or pressure control
Definitions
- This invention relates to apparatus comprising electrolytic means wherein it is desired to maintain a current of substantially uniform strength. It is an improvement on and supplements the invention disclosed-in application Serial No. 275,860, filed February 8th, 1919.
- An important object of the present invention is to avoid and overcome difiiculties which have been found to arise in apparatus of this class by reason of so-called polarization and the formation of an insulating gas film at the circuit controlling electrodes, causing decrease or even. practical cessation of the operating current under conditions at which the current should be maintained at full strength.
- the present invention provides a method of maintaining a constant fiow of low voltage'current between plates or electrodes immersed in water or other electrolyte, by constantly reducing and practically dissipatin the deterrent gas film formed by the electrolysis of the water. This is elfected by taking advantage of the relatively higher voltage inverse and direct currents induced in the secondary winding of inductions coils or transformers when the primary current is varied by polarization or gas film formation to break down the gas film.
- the object of the present invention is not to produce rapid interruptions in the circuit or to prevent electrolysis, but is to increase the flow of the direct current through a circuit, including an electrolytic cell, by reducing. the internal resistance of the cell caused by polarization and insulating gas film formation.
- a current of given minimum value may be indefinitely main- I tained through a circuit (other factors be 105 ing equal) with less E. M. F. than is poss1- ble when polarization and gas film resistance are effective.
- Polarization may be defined as: the production of a secondary current in a cell, contrary in direction to the principle or exciting current, due to the chemical change in the elements composing the cell. Theoretic-ally, this is caused by the liberation of ions which collect and adhere to the respective electrodes according to polarity. An unstable chemical and electrical condition is the result, which in an attempt to neutralize itself, creates the inverse or countercurrent of olarization. The strength and resistance e ect against the original current is proportional to the rapidity and volumes in which the ions are liberated.
- the second effect that of the formation of an insulating gas film on the electrodes may be and probably is a direct result of the action of electrolysis. It is also possible that the counter-current of polarization may have some effect on the formation of the gas film as the nature of these gases depend upon the composition of the electrolyte, as well as that of the electrodes. It will be assumed that the electrolyte is a simple saline or acidulated solution, and that the electrodes are of some element (such as carbon) having practically no chemical reaction with the electrolyte. The gases liberated will then be composed chiefly of oxygen and hydrogen, and will adhere to their respective anode and cathode electrodes and. form a film of high electrical resistance, rapidly increasing the internal resistance of the electrolytic cell to the flow of the original current.
- the gas bubbles thrown off will slowly reduce in volume, but after they have ceased to rise, a number will still remain and adhere with the opaque film to the surface of the electrodes for an indefinite time. Again establishing the current flow, the bubbles immediately rise in maximum quantity and the galvanometer needle will register the minimum current value.
- the bubbles will immediately cease to rise and the opaque film with the bubbles adhering thereto will disappear in a spray or shower of fine bubbles. Removing the short and connecting the battery, the three stages of action will again take place. while the galvanometer will also register the same variations as first noted. Quickly reversing the spring outward from the surface of the electrodes in a fine shower, then begin to rise in increased volume according to voltage.
- the needle When the circuit is disconnected from the battery and short circuited so as to includ'ethe galvanometer, the needle will be sharply deflected in an opposite direction, indicating a decided current flow from the electrolytic cell. After the maximum deflection the needle will not return to zero; but
- the strength of the induced secondary currents. with a given E. M. F. is directly proportional to the increased turn ratio of the secondary winding as compared to the turns in the primary.
- E. M. F. value of the induced secondary currents is greater when the current flowing through the primary is broken or reduced. in strength than when contact is made or the current increased. That complete interruptions of the exciting current through the primary are not necessary, but that any variation of current strength will induce secondary currents of relatively higher E. M. F is illustrated by the well-known example of the telephone transmitter or microphone, when used in connection with an induction coil.
- the electrolytic cell it is not necessary for complete polarization to take place, or the surface of the electrode exposed to the electrolyte to become entirely insulated by the gas film or bubbles.
- the formation of any bubble on-the'surface of the electrode will cause a decrease in the area of the electrode exposed to: the electrolyte, and, therefore, an increase in the internal resistance of the cell with a corresponding decrease in the current flowing through the primary winding of an induction coil included in the circuit.
- An induced current will. therefore, be excited in the secondary winding, having an E. M. F. value in direct proportion to the winding ratio between the two coils.
- Figure -1 is a diagram illustrating the principle involved in overcoming polarization.
- Figure 2 is a diagram showing a modified form of the circuits.
- Electro-magnet 4 is simply typical of a translating device of some kind included in the circuit, and any other translating device may be substituted therefor, according to the specific application of the invention, or in some cases, as hereinafter explained. this translating device may be omitted.
- the electro-magnet 4 may act-asa relay for controlling a signal circuit, for example, the armature 25 of said electromagnet having front contact 26 and backcontact 27, respectively connected by wires 28 and 29 to suitable signal means or other translating devices, such as 30 and 31 from which wires 33 and 34 lead to wires 35 connected to one side of battery 36, and whose other side is connected by wire 37 to armature'25.
- suitable signal means or other translating devices such as 30 and 31 from which wires 33 and 34 lead to wires 35 connected to one side of battery 36, and whose other side is connected by wire 37 to armature'25.
- the armature 25 will 'closeone or the other of the branch circuits through the respective devices 30'an'd 31 according to the condition of energization or de-energization of -the circuit through the electrolytic device comprising the'electrolyte W and the electrodes immersed therein, and in this application of my invention, and referring the invention the main object thereof is to enable continuous energization of this circuit, .without interference by polarization effects.
- the battery A is shown as connected in a circuit including a wire 1 leading from said battery to an impedance or choke coil 2 from which a wire 3 leads to an electromagnet coil 4:, a primary winding 5 of a transformer 6 being also included in this connection by means of the wire 3.
- a wire 7 leads to an electrode 9 immersed in an electrolyte, such as a body W of water, or dilute acid, or alkaline or neutral salt solution contained in a vessel B.
- awire 11 leads to an impedance or choke coil 12 from which a wire 13 leads back to battery A.
- a secondary winding 15 of transformer 6 is connected at one end to wire 7 by wire 23 and at the other end by wire 20 to wire 11.
- the secondary winding 15 of transformer-6 As the secondary winding 15 of transformer-6 is connected in parallel or bridged across the circuit, a portion of the battery current will be shunted through said secondary winding 15, its value depending upon the resistance of the coil.
- the primary 5 and secondary 15 of transformer 6 are connected to the circuit in such an inductive relation that the momentary inducedsecondary current generatedlwhen the current flow is first established will flow in adirection and through that part of the circuit indicated by wire 23, wire 7 electrode 9, solution W, electrode 10, wire 11 and wire 20.
- the condenser current in the cell (as heretofore illustrated) will also have a tendency to flow through the circuit and 1n a direction indicated by electrode 9, wire 7, wire 23, secondary winding 15, wire 20, wire 11, electrode 10, and solution W to electrode 9.
- This condenser current will exalt the secondary current and also dissipate the counter current of polarization. Immediately on the dissipating of the gas film and the counter current of polarization the primary current again rapidly increases in value until checked by polarization and gas film formation, when the operation above described is repeated.
- the winding of the secondary coil 15 must be so proportioned that it will have a resistance equal to or greater than the total resistance of the primary circuit, and the relay coil 4 must be so designed that it will not be sufficiently energized by the small amount of current flowing through the secondary coil 15, to hold the armature 25 thereof when the primary circuit has been opened by removing one or both of the electrode plates 9 and 10 from the solution W, or when the plates have been so removed and the primary circuit disconnected from the battery A that the coil of the relay will not be sufficiently energized to attract its armature when the battery A is again connected, until the total resistance has been reduced by again immersing the electrodes 9 and 10 in the solution W.
- a third electrode plate 17 is immersed in the solution W in vessel B, and in a more or less close relation to electrode 10, said electrode 17 being connec'ted by the wire 16 to secondary winding 15 of transformer 6, The other side of secondary 15 being connected by wire 20 and" wire 11 to electrode 10, as in Figure 1. ⁇ Vith this circuit arrangement the depolarizing and gas film disrupting effects of the induced secondary current will be localized on the electrode plate 10.
- an electrical depolarizing apparatus comprising a circuit including a' source of direct current and electrodes in contact with an electrolyte, means for maintaining the current efiectiveness of said circuit consisting of a transformer having a low tension primary Winding in series with and ener gized by said circuit, and a high tension secondary winding in electrical connection withsaid electrodes and inductively related to said primary winding in such a manner as to cause a reduction of polarization between said electrodes and said electrolytewhen the current in the primary winding is varied by said polarization.
- an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes in contact with an electrolyte, a transformer having a low 3.
- an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes in contact with an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit, and a high tension secondary winding electrically connected to said electrodes, and inductively related to resistance equal to or greater than the resaid primary winding in such a manner as to dissipate a condition of polarization and insulating gas film formation on said electrodes, and impedance coils between said source of current and said transformer secondary coil.
- an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes in contact with an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit, and a high tension secondary winding bridged across said circuit and electrically connected to said electrodes and inductively related to said primary windingin such a manner that induced inverse and direct secondary currents will be generated in said secondary winding during variations in the current in said primary winding produced by a condition of polarization and insulating gas film formation on said electrodes, and directionally applying said inverse and direct induced currents to said electrodes to dissipate the said condition of polarization and to disrupt and repel the said insulating gas film formation from said electrodes.
- an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes in contact with an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit, and a high tension secondary winding bridged across said circuit and electrically connected to said electrodes, and in inductive relation with said primary winding in such a manner as to dissipate a condition of polarization and insulating gas film formation on said electrodes, and impedance coils between said source of current and said secondarywinding, and said secondary winding having a sistance of the circuit through the electrodes and the electrolyte.
- an electrical apparatus comprising a circuit including a source of direct current and circuit controlling electrodes in contact with an electrolyte and positioned to break contact therewith, and an electromagnet relay also included in said circuit and having circuit controlling contacts controlled thereby, and a transformer having a low tension primary winding in series with said circuit and energized thereby, and a high' tension secondary winding electrically connected to said electrodes and inductively relatived to said primary Winding in such a manner as'to maintazn the current effectiveness through said circuit when said electrodes are immersed in said electrolyte by dissipating a condition of polarizatlon and insulating gas film formation produced on said electrodes by said current acting on said electrolyte.
- an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes immersed in an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit, and a high tension secondary winding inductively related to said primary winding and in electrical connection with one of said electrodes and a third electrode also immersed in said electrolyte in such a manner as to reduce a condition of polarization between said electrodes when said primary current is varied or reduced by said polarization.
- an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes immersed in an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit and a high tension secondary winding inductively related to said primary winding and in electrical connection with one of said electrodes and a third electrode also immersed in said electrolyte in such a manner as to localize on one of said first named electrodes the depolarizing and gas film disrupting effects of the inverse and direct induced currents generated in, said secondary Winding when the primary current is varied or reduced by polarization or insulating gas 'film formation produced on said electrodes by said current acting on said electrolyte.
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Description
W. D. NICKUM.
ELECTROLYTIC APPARATUS AND METHOD OF DEPOLARIZING THE SAME APPLICATION FILED APR. 21. 1920. RENEWED NOV-5,1921.
1,428,050. Pa entedsept. 5, 1922.-
Patented Sept. 5, 1922. v
UNITED STATES PATENT OFFICE.
WALTER DANIEL NICKUM, OF GLENDALE, CALIFQR-NIA.
ELECTROLYTIC' APPARATUS AND METHOD OF DEPOLARIZENG THE SAME.
Application filed April 21, 1920, Serial No. 375,502. Renewed November 5, 1921. Serial No. 513,211.
T 0 all whom it may concern:
Be it known that I, WALTER DANIEL NICKUM, a citizen of the United States of America, and a resident of Glendale, in the county of Los Angeles and State of California, have invented or discovered a new and useful Improvement in Electrolytic Apaaratus and Methods of Depolarizing the bame, of which the following is a specification.
This invention relates to apparatus comprising electrolytic means wherein it is desired to maintain a current of substantially uniform strength. It is an improvement on and supplements the invention disclosed-in application Serial No. 275,860, filed February 8th, 1919.
An important object of the present invention is to avoid and overcome difiiculties which have been found to arise in apparatus of this class by reason of so-called polarization and the formation of an insulating gas film at the circuit controlling electrodes, causing decrease or even. practical cessation of the operating current under conditions at which the current should be maintained at full strength.
lVhen plates of two dissimilar metals are partially immersed in a vessel containing an acidulated solution, and their outer ends are connected together by a conducting wire, an electric current is set up, caused by the acid in the solution attacking the metal plates. The water of the solution is also acted upon and free oxygen and hydrogen gases are liberated. The gases collect on the metal plates. partially adhering thereto, and form a film of very high electrical resistance, causing a rapid decrease if not an actual stoppage of the electrical action. This effect of polarization is a well known action in practically all chemical batteries.
It is also well known that when an electric current is caused to pass through an acidulated solution between electrodes immersed therein, a deterrent film of gas if formed on the electrodes due to the electrolysis of the water, and as these gases are poor conductors, the current is practically stopped. If an inductance, consisting of'a coil of wire wound around a soft iron core is included in the circuit between the source of current and one of the electrodes, and if the area of said electrode, or of the electrolyte itself exposed to the action of the current is sufiiciently small, a rapid interruption of the current flowing through the circuit will take place, due to the induced extra current disrupting the gas film formingon the electrode. This forming and disrupting of the gas film is very rapid and has been taken advantage of in designing certain well known types of electrolytic interrupters, but has the disadvantage of being of little Value on currents having a po tential of less than 40 or 50 volts.
The present invention provides a method of maintaining a constant fiow of low voltage'current between plates or electrodes immersed in water or other electrolyte, by constantly reducing and practically dissipatin the deterrent gas film formed by the electrolysis of the water. This is elfected by taking advantage of the relatively higher voltage inverse and direct currents induced in the secondary winding of inductions coils or transformers when the primary current is varied by polarization or gas film formation to break down the gas film.
The object of the present invention is not to produce rapid interruptions in the circuit or to prevent electrolysis, but is to increase the flow of the direct current through a circuit, including an electrolytic cell, by reducing. the internal resistance of the cell caused by polarization and insulating gas film formation.
.With electrodes of appreciable size, it is doubtful if the flow of a current through a circuit containing an electrolytic cell is even entirely stopped. But the resistance of the gas film surrounding the electrodes, and the retarding effect of the inverse current of polarization will quickly reduce the value of the original or primary exciting current through the circuit to a minimum. It is, therefore, evident that with a given E. M. E, if the resistance of thegas film and the retarding effect of polarization can be materially reduced, then a current strength of 100 greater constant value can be maintained.
In other words, by reducing or preventing the'efl'ects of electrolysis, a current of given minimum value may be indefinitely main- I tained through a circuit (other factors be 105 ing equal) with less E. M. F. than is poss1- ble when polarization and gas film resistance are effective.
It isnot thought necessary to enter into a theoretical discussion of what actually takes 110 place in an electrolytic cell when a direct or unidirectional current flows through it, as the action will vary according to the composition of the electrodes and the electrolyte. It will,-therefore, be assumed that the primary effect of a current flowing from one electrode to another through an electrolyte, is to alter the chemical composition of the solution by electrolysis. This, in turn produces the condition known as polarization, and under certain conditions, a gas film of high insulating quality also forms on the electrodes. of polarization and gas film formation, and not the actual phenomenon of electrolysis that is of present interestin this invention;
Polarization may be defined as: the production of a secondary current in a cell, contrary in direction to the principle or exciting current, due to the chemical change in the elements composing the cell. Theoretic-ally, this is caused by the liberation of ions which collect and adhere to the respective electrodes according to polarity. An unstable chemical and electrical condition is the result, which in an attempt to neutralize itself, creates the inverse or countercurrent of olarization. The strength and resistance e ect against the original current is proportional to the rapidity and volumes in which the ions are liberated.
The second effect: that of the formation of an insulating gas film on the electrodes may be and probably is a direct result of the action of electrolysis. It is also possible that the counter-current of polarization may have some effect on the formation of the gas film as the nature of these gases depend upon the composition of the electrolyte, as well as that of the electrodes. It will be assumed that the electrolyte is a simple saline or acidulated solution, and that the electrodes are of some element (such as carbon) having practically no chemical reaction with the electrolyte. The gases liberated will then be composed chiefly of oxygen and hydrogen, and will adhere to their respective anode and cathode electrodes and. form a film of high electrical resistance, rapidly increasing the internal resistance of the electrolytic cell to the flow of the original current.
'The question as to whether the particles forming the gas film are actually the ions of polarization or a separate product of electrolysis, will not be entered into. Either or both conditions create a resistance to, or a retarding action against the flow of the original current, and will, under suitable conditions, apparently stop its flow entirely. That this interruption or stoppage of the current is not limited to cells having electrodes of small surface area exposed to the electrolyte, is illustrated by the action of certain types of electrolytic condensers,
It is only this condition wherein with electrodes of very large surface area and using a potential of nearly 100 volts, the flow of current is almost instantly interrupted.
When an electrolytic cell is connected to a source of direct current and the electrodes are examined with the aid of a magnifying glass, it will be noted that bubbles of gas do not immediately form on the surface of the electrodes in contact with the electrolyte. At first no action can be detected,-then a whitish and more or less opaque: film forms on the electrodes, first on the cathode and then on the anode. After the film appears, bubbles of gas form on the film, usually in groups, and, if the exposed surfaces of the electrodes are vertically inclined, a portion of the bubbles will break away and rise to the surface of the electrolyte. This forming and rising of the bubbles quickly reaches a maximum quantity and volume depending on the voltage employed and the electrode area in contact with the electrolyte. The quantity of bubbles. thrown off increases very rapidily with an increase in voltage and vice versa, but the number adhering to the opaque film (per unit area of electrode surface) remains nearly constant, irrespective of the voltage employed. The time interval between connecting the current to the cell and the maximum rise of the bubbles is very short, seldom exceeding two or three seconds, and is less as the E. M. F. of the exciting current is greater. The needle of a galvanometer included in the circuit, will, during this period, show a very marked decrease deflection, and after a few seconds will indicate a fairly constant minimum current flow.
When the circuit is broken, the gas bubbles thrown off will slowly reduce in volume, but after they have ceased to rise, a number will still remain and adhere with the opaque film to the surface of the electrodes for an indefinite time. Again establishing the current flow, the bubbles immediately rise in maximum quantity and the galvanometer needle will register the minimum current value.
If the battery is disconnected from the cell and the outer terminals of the electrodes connected together or shorted, the bubbles will immediately cease to rise and the opaque film with the bubbles adhering thereto will disappear in a spray or shower of fine bubbles. Removing the short and connecting the battery, the three stages of action will again take place. while the galvanometer will also register the same variations as first noted. Quickly reversing the spring outward from the surface of the electrodes in a fine shower, then begin to rise in increased volume according to voltage.
When the circuit is disconnected from the battery and short circuited so as to includ'ethe galvanometer, the needle will be sharply deflected in an opposite direction, indicating a decided current flow from the electrolytic cell. After the maximum deflection the needle will not return to zero; but
immersing in the electrolyte, the slowlydisslpating current remaining in the cell is destroyed, and the galvanorneter needle will rest at the zero point.
From the foregoing it is evident that a counter current of considerable value is set up within the electrolytic cell, and that the cell acts in the nature of a condenser of large capacity, depending upon the area of the electrodes exposed to the electrolyte. This counter current has considerable effect in retarding the flow of the original or excit ing current, and coupled with the insulating qualities of the gas film, quickly reduces the original current to a minimum value.
In the induction coil, the strength of the induced secondary currents. with a given E. M. F., is directly proportional to the increased turn ratio of the secondary winding as compared to the turns in the primary.
The E. M. F. value of the induced secondary currents is greater when the current flowing through the primary is broken or reduced. in strength than when contact is made or the current increased. That complete interruptions of the exciting current through the primary are not necessary, but that any variation of current strength will induce secondary currents of relatively higher E. M. F is illustrated by the well-known example of the telephone transmitter or microphone, when used in connection with an induction coil.
In the electrolytic cell, it is not necessary for complete polarization to take place, or the surface of the electrode exposed to the electrolyte to become entirely insulated by the gas film or bubbles. Theoretically, the formation of any bubble on-the'surface of the electrode will cause a decrease in the area of the electrode exposed to: the electrolyte, and, therefore, an increase in the internal resistance of the cell with a corresponding decrease in the current flowing through the primary winding of an induction coil included in the circuit. An induced current will. therefore, be excited in the secondary winding, having an E. M. F. value in direct proportion to the winding ratio between the two coils.
As the bubbles of gas do not form slowly and not singly, but spontaneously and in groups covering an appreciable area of the electrode surface, it is evident that current variations of considerable inductive value are produced in the primary winding, and that corresponding currents of comparatively large magnitude are induced in the secondary, and of suificiently high E. M. l., that when properly applied to the polarized electrodes, will disrupt and expell the gas particles. In a condenser, the charge does not localize itself to any one part of the plate, but spreads over the entire area. So also in the electrolytic cell under discussion, the induced current acts over the entire exposed surface area of the electrode, disrupting or repelling any of the gas particles adhering thereto.
The accompanying drawings illustrate embodiments of thereto:
Figure -1 is a diagram illustrating the principle involved in overcoming polarization.
Figure 2 is a diagram showing a modified form of the circuits.
For the purpose of illustration, I have shown in Figs. 1 and 2, the application of .the invention in depolarizing an electrolytic device constituting a circuit controller for ,an electromagnet coil 4 whose armature controls a circuit. such as a signal circuit. Electro-magnet 4 is simply typical of a translating device of some kind included in the circuit, and any other translating device may be substituted therefor, according to the specific application of the invention, or in some cases, as hereinafter explained. this translating device may be omitted. In the specific application of the invention as illustrated in the drawings, the electro-magnet 4 may act-asa relay for controlling a signal circuit, for example, the armature 25 of said electromagnet having front contact 26 and backcontact 27, respectively connected by wires 28 and 29 to suitable signal means or other translating devices, such as 30 and 31 from which wires 33 and 34 lead to wires 35 connected to one side of battery 36, and whose other side is connected by wire 37 to armature'25. With this arrangement the armature 25 will 'closeone or the other of the branch circuits through the respective devices 30'an'd 31 according to the condition of energization or de-energization of -the circuit through the electrolytic device comprising the'electrolyte W and the electrodes immersed therein, and in this application of my invention, and referring the invention the main object thereof is to enable continuous energization of this circuit, .without interference by polarization effects.
A particular application of the invention is claimed specifically in application Serial No. 254,345, filed Sept. 16th, 1918, of which application Serial No. 275,860, filed Feb. 8th, 1919, is a division and of which this application is an improvement. The present application relates to the broad process and improved means for applying the apparatus for depolarization.
Referring'to Figure 1, which illustrates the circuits as far as is required for explaining the depolarizing action, the battery A is shown as connected in a circuit including a wire 1 leading from said battery to an impedance or choke coil 2 from which a wire 3 leads to an electromagnet coil 4:, a primary winding 5 of a transformer 6 being also included in this connection by means of the wire 3. From said primary winding a wire 7 leads to an electrode 9 immersed in an electrolyte, such as a body W of water, or dilute acid, or alkaline or neutral salt solution contained in a vessel B. From another electrode 10 immersed in such a liquid, awire 11 leads to an impedance or choke coil 12 from which a wire 13 leads back to battery A. A secondary winding 15 of transformer 6 is connected at one end to wire 7 by wire 23 and at the other end by wire 20 to wire 11.
If current is allowed to flow from the positive side .of battery A through wire 1, im-
primary winding 5 and wire 7, to electrode 9, through solution W in vessel B to elec-. trode 10 and wire 11, impedance coil 12, and wire 13, back to negative side of battery A, the water in the solution W will be more or less decomposed by the current passing through it and gas will collect on the electrodes, the degree of electrolysis of theawater depending upon the quantity of current flowing through the circuit. The gases liberated by the decomposition of the water and collecting on the electrodes in thesolution W,' as heretofore mentioned, quickly reduce the flow of current.
As the secondary winding 15 of transformer-6 is connected in parallel or bridged across the circuit, a portion of the battery current will be shunted through said secondary winding 15, its value depending upon the resistance of the coil. The primary 5 and secondary 15 of transformer 6 are connected to the circuit in such an inductive relation that the momentary inducedsecondary current generatedlwhen the current flow is first established will flow in adirection and through that part of the circuit indicated by wire 23, wire 7 electrode 9, solution W, electrode 10, wire 11 and wire 20.
But, as the induced current generated in a i primary current immediately follows.
secondary winding at the fmake of a circuit connection is-comparatively feeble, the said induced current generated in secondary to the counter current of polarization and the insulating gas film set up in the electroltic cell by the electrolysis of the solution, a more or less rapid drop in value of tllle s the lines of force generated in the primary winding 5 collapse, a relatively high voltage induced current is generated in the secondary winding 15, and will flow in a direction and through that part of the circuit indicated by wire 20, wire 11, electrode 10,
solution W, electrode 9, wire 7 and Wire 23,
and will disrupt the gas particles adhering to the electrodes and particularly those on electrode 10, and as these gas particles carry an electrical charge opposite in sign to the polarity of. the electrode upon which they collect, and, as the induced secondary current flows in a direction through the cell opposite to the original exciting current, and is of a polarity of like sign to the charged gas particles, said gas particles will be re pelled away from their respective electrodes, as well as disrupted by the said secondary current. The condenser current in the cell (as heretofore illustrated) will also have a tendency to flow through the circuit and 1n a direction indicated by electrode 9, wire 7, wire 23, secondary winding 15, wire 20, wire 11, electrode 10, and solution W to electrode 9. This condenser current will exalt the secondary current and also dissipate the counter current of polarization. Immediately on the dissipating of the gas film and the counter current of polarization the primary current again rapidly increases in value until checked by polarization and gas film formation, when the operation above described is repeated.
It is therefore evident that a more or less complete cycle of oscillations are'set up in that part of the circuit comprising the electrolytic cell and the secondary winding 15, and that these oscillations are sufliciently rapid to materially reduce the retarding effects of polarization and gas film formation is practically bridged across the circuit, and as the induced current generated in said secondary coil becomes practically alternating in character, and to prevent any loss of its efficiency in acting upon the gas film on the electrodes by a certain portion of the secondary current backing up through the battery A, the impedance or choke coils 2 and 12 are introduced in the circuit to impede the transmission of any such alternating 'current through that part of the circuit which includes the battery A.
The winding of the secondary coil 15 must be so proportioned that it will have a resistance equal to or greater than the total resistance of the primary circuit, and the relay coil 4 must be so designed that it will not be sufficiently energized by the small amount of current flowing through the secondary coil 15, to hold the armature 25 thereof when the primary circuit has been opened by removing one or both of the electrode plates 9 and 10 from the solution W, or when the plates have been so removed and the primary circuit disconnected from the battery A that the coil of the relay will not be sufficiently energized to attract its armature when the battery A is again connected, until the total resistance has been reduced by again immersing the electrodes 9 and 10 in the solution W.
It is evident from the foregoing that other electrically operated apparatus could be introduced in the primary circuit besides the relay coil 4, or that said relay can be dispensed with by making direct connection between the wires 3 and 3', as shown in the dotted lines at aa, if it is desired to use the depolarizing effect of the secondary circuit to maintain a flow of low voltage direct current through the solution W for the purpose of electrolysis, For instance, certain applications in chemistry and electro-metallurgy whereby desired actions could be obtained with low voltage that could not be obtained with greater voltages, as for instance, the so-called burning effect of too high voltage in electro-plating, also the purification of water or sewage. In any such application of the invention the electrodes 9 and '10 may constitute the electrodes of the electrolytic cell to which the depolarizing circuit is applied.
An equally effective circuit arrangement for some purposes isshown in Figure 2,
where for mechanical or electrical reasons,
it is not desirable to simplify the construction of apparatus containing the electrodes by reducing their number or the number of wires leading thereto. A third electrode plate 17 is immersed in the solution W in vessel B, and in a more or less close relation to electrode 10, said electrode 17 being connec'ted by the wire 16 to secondary winding 15 of transformer 6, The other side of secondary 15 being connected by wire 20 and" wire 11 to electrode 10, as in Figure 1. \Vith this circuit arrangement the depolarizing and gas film disrupting effects of the induced secondary current will be localized on the electrode plate 10. The circuit arrangement of Fig. 2, is of special value in certain types of electrolytic devices, as for instance the aforementioned electro-plating bath, wherein the depolarizing induced currents could be localized and concentrated on the cathode The operation of the circuit in Figure 2 is substantially the same as described for Fig. 1.
It will be understood that the operation of this invention does not require complete interruption of the current by the depolarizing action, it being required only that there shall be a sufficient decrease or variation of the current to produce the required inductive effect in the secondary circuit to dissipate the condition of polarization and insulating gas film.
What I claim is:
1. In an electrical depolarizing apparatuscomprising a circuit including a' source of direct current and electrodes in contact with an electrolyte, means for maintaining the current efiectiveness of said circuit consisting of a transformer having a low tension primary Winding in series with and ener gized by said circuit, and a high tension secondary winding in electrical connection withsaid electrodes and inductively related to said primary winding in such a manner as to cause a reduction of polarization between said electrodes and said electrolytewhen the current in the primary winding is varied by said polarization.
2. In an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes in contact with an electrolyte, a transformer having a low 3. In an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes in contact with an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit, and a high tension secondary winding electrically connected to said electrodes, and inductively related to resistance equal to or greater than the resaid primary winding in such a manner as to dissipate a condition of polarization and insulating gas film formation on said electrodes, and impedance coils between said source of current and said transformer secondary coil.
4. In an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes in contact with an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit, and a high tension secondary winding bridged across said circuit and electrically connected to said electrodes and inductively related to said primary windingin such a manner that induced inverse and direct secondary currents will be generated in said secondary winding during variations in the current in said primary winding produced by a condition of polarization and insulating gas film formation on said electrodes, and directionally applying said inverse and direct induced currents to said electrodes to dissipate the said condition of polarization and to disrupt and repel the said insulating gas film formation from said electrodes.
5. In an electrical depolarizing apparatus comprising a circuitincluding a source of direct current and electrodes in contact with an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit, and a high tension secondary winding bridged across said circuit and electrically connected to said electrodes, and in inductive relation with said primary winding in such a manner as to dissipate a condition of polarization and insulating gas film formation on said electrodes, and impedance coils between said source of current and said secondarywinding, and said secondary winding having a sistance of the circuit through the electrodes and the electrolyte.
6. In an electrical apparatus comprising a circuit including a source of direct current and circuit controlling electrodes in contact with an electrolyte and positioned to break contact therewith, and an electromagnet relay also included in said circuit and having circuit controlling contacts controlled thereby, and a transformer having a low tension primary winding in series with said circuit and energized thereby, and a high' tension secondary winding electrically connected to said electrodes and inductively relatived to said primary Winding in such a manner as'to maintazn the current effectiveness through said circuit when said electrodes are immersed in said electrolyte by dissipating a condition of polarizatlon and insulating gas film formation produced on said electrodes by said current acting on said electrolyte.
7. In an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes immersed in an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit, and a high tension secondary winding inductively related to said primary winding and in electrical connection with one of said electrodes and a third electrode also immersed in said electrolyte in such a manner as to reduce a condition of polarization between said electrodes when said primary current is varied or reduced by said polarization.
8. In an electrical depolarizing apparatus comprising a circuit including a source of direct current and electrodes immersed in an electrolyte, a transformer having a low tension primary winding in series with and energized by said circuit and a high tension secondary winding inductively related to said primary winding and in electrical connection with one of said electrodes and a third electrode also immersed in said electrolyte in such a manner as to localize on one of said first named electrodes the depolarizing and gas film disrupting effects of the inverse and direct induced currents generated in, said secondary Winding when the primary current is varied or reduced by polarization or insulating gas 'film formation produced on said electrodes by said current acting on said electrolyte.
9. The method of depolarizing surfaces exposed to an electrolyte and included in part of an electric circuit, which consists in causing the current variations in said circuit due to polarization and insulating gas film formation to induce momentary inverse and direct induced currents of relatively high tension and predetermined polarity and applying such high tension and polarized currents to the polarized and gas film i-nsulated surfaces to depolarize the same and disrupt the gas film formation.
WALTER DANIEL NIOKUM.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US375502A US1428050A (en) | 1920-04-21 | 1920-04-21 | Electrolytic apparatus and method of depolarizing the same |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US375502A US1428050A (en) | 1920-04-21 | 1920-04-21 | Electrolytic apparatus and method of depolarizing the same |
| US51321121A | 1921-11-05 | 1921-11-05 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1428050A true US1428050A (en) | 1922-09-05 |
Family
ID=26957637
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US375502A Expired - Lifetime US1428050A (en) | 1920-04-21 | 1920-04-21 | Electrolytic apparatus and method of depolarizing the same |
Country Status (1)
| Country | Link |
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| US (1) | US1428050A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2575712A (en) * | 1945-09-29 | 1951-11-20 | Westinghouse Electric Corp | Electroplating |
| US2860090A (en) * | 1952-02-29 | 1958-11-11 | Paul S Roller | Electrolytic generation of metal hydroxide |
| US3335078A (en) * | 1963-05-16 | 1967-08-08 | Edward L Hendey | Bipolar cell for electrolytically treating water |
| US3481839A (en) * | 1963-10-21 | 1969-12-02 | Inoue K | Method of depositing substances on and diffusing them into conductive bodies under high-frequency electric field |
| US4226695A (en) * | 1978-10-20 | 1980-10-07 | Environmental Sciences Associates, Inc. | Electrochemical processing system |
-
1920
- 1920-04-21 US US375502A patent/US1428050A/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2575712A (en) * | 1945-09-29 | 1951-11-20 | Westinghouse Electric Corp | Electroplating |
| US2860090A (en) * | 1952-02-29 | 1958-11-11 | Paul S Roller | Electrolytic generation of metal hydroxide |
| US3335078A (en) * | 1963-05-16 | 1967-08-08 | Edward L Hendey | Bipolar cell for electrolytically treating water |
| US3481839A (en) * | 1963-10-21 | 1969-12-02 | Inoue K | Method of depositing substances on and diffusing them into conductive bodies under high-frequency electric field |
| US4226695A (en) * | 1978-10-20 | 1980-10-07 | Environmental Sciences Associates, Inc. | Electrochemical processing system |
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