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Method of conducting electrolysis and apparatus for realising said method |
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IPC classes for russian patent Method of conducting electrolysis and apparatus for realising said method (RU 2475569):
Unipolar-bipolar electrolytic cell to make mix of hydrogen with oxygen / 2475343
Invention relates to gas-flame processing of materials with hydrogen-oxygen mix, particularly, to electrolytic cells to this end. Electrolytic cell may be filter-press or box-type device. Note here that some electrodes of the cell are unipolar while some of them are bipolar electrodes. It consists of flat or shaped parallel electrodes with holes of slots making gas and electrolyte passages. Space between electrodes is filled with electrolyte while electric current is supplied to extreme electrodes. Said electrodes are interconnected by current conducting buses to make sets, two extreme of which comprise n+1 electrodes while other include 2n+1 electrodes, where n is natural number. Note here that central electrodes of every said set with 2n+1 electrodes are located between two adjacent sets while other 2n electrodes of this set are arranged at the center of gap between electrodes of adjacent sets with contact with said buses.
Water electrolytic generator gate / 2474624
Proposed device is composed of vertical cylinder divided by two vertical baffles into three chambers. Branch pipes arranged concentrically one in another are attached from below to centre of both baffles. Lower chamber is partially filled with fluid. Note here that end of the branch pipe attached to lower baffle is immersed in lower chamber fluid while branch pipe attached to upper baffle extends through medium chamber and into the branch pipe attached to lower baffle and either does not reach fluid surface in outer branch pipe or terminates several centimetres below fluid surface. Lower and medium chambers are communicated via long tube.
Hydrogen generator / 2473716
Hydrogen generator comprises casing accommodating runs of plates separated by gaps to form impermeable cells. Note here the plate making the first wall of every cell is made from more noble material than plate making second wall of this cell. Note also that fist plate in runs makes anode to be connected to power supply. Note also that last plate in runs makes cathode to be connected to power supply. Inlet of every cell allows electrolyte inflow into cell while outlet of every cell allows electrolyte and hydrogen gas efflux from cell.
Hydrogen generator / 2473716
Hydrogen generator comprises casing accommodating runs of plates separated by gaps to form impermeable cells. Note here the plate making the first wall of every cell is made from more noble material than plate making second wall of this cell. Note also that fist plate in runs makes anode to be connected to power supply. Note also that last plate in runs makes cathode to be connected to power supply. Inlet of every cell allows electrolyte inflow into cell while outlet of every cell allows electrolyte and hydrogen gas efflux from cell.
Novel highly stable aqueous solution, nano-coated electrode for preparing said solution and method of making said electrode / 2472713
Invention relates to disinfectant compositions and specifically to a highly stable acidic aqueous solution, a method and apparatus for production thereof. The solution is prepared using a fluid medium treatment apparatus having at least one chamber (7), at least one anode (4) and at least one cathode (3) inside the chamber (7). The anode (4) and the cathode (3) are at least in part made from a first metallic material. At least one of said at least one cathode (3) and anode (4) have a coating with nanoparticles (5) of one or more metals.
Electrolysis cell for producing chlorine / 2471891
In an electrolysis cell for producing chlorine, bipolar electrode elements are made from a bimetallic sheet (steel+titanium); frames of bipolar chambers are made from shaped tubes; anode and bipolar chambers are made from a bimetallic sheet which is made by welding sheets with insert bimetallic (steel+titanium) elements; the anode and the cathode chambers are equipped with built-in heat exchangers, one part of which is formed by placing shortened metallic separating strips inside the chambers and hermetic sealing of the outer surface of the chambers with a metal sheet; the second part is formed by making supporting frames of the chambers hollow, which enables to use water cooling.
Electrocatalytic method for synthesis of hydrocarbons and alcohols based on plant material / 2471890
Method is realised in a diaphragmless cell which is equipped with an anode and a cathode, in the medium of methyl or ethyl alcohol in the presence of a base, as a result which there is direct electrooxidation of said acids, where the anode used is graphite, pyrographite, Pt-Ir metallurgical alloy, or nanoparticles of a Pt-Ir alloy in amount of 0.1-1.0 mg/cm-2 which are deposited on the surface of glass carbon, and the cathode used is a stainless steel cathode.
Method for obtaining ionic silver solution / 2471018
Metallic silver is diluted in distilled water till electrolyte is formed. After electrolyte is formed as a result of anodic silver oxidation and self-dilution of oxide, dilution process is interrupted, electrolyte is drained and magnetised by passing it through a glass tube going through magnetic field of constant magnet. Then, at weak mixing of the solution, dilution process of metallic silver is continued till hardly transparent black suspension is formed; after that, the process is stopped. Settled concentrate is separated; in addition, clean electrolyte is magnetised and again brought into circulation, and deposit of crystalline hydrate of silver oxide (1) is used in order to obtain water solution of ionic silver, at which crystalline hydrate is diluted in water, magnetised in magnetic field, filtered and drained to glass bottles to be stored.
Method of producing high-purity lithium hydroxide and hydrochloric acid / 2470861
Invention can be used in chemical industry to produce crystalline monohydrate of lithium hydroxide which is used in accumulator batteries, and lithium carbonate. The method of producing crystals of monohydrate of lithium hydroxide and hydrochloric acid involves purifying lithium-containing brine via ion exchange in order to reduce concentration of calcium and magnesium ions. The brine undergoes electrolysis to obtain lithium hydroxide solution containing less than 150 ppb of the total amount of calcium and magnesium to obtain gaseous chlorine and hydrogen as by-products. Hydrochloric acid is obtained by burning the obtained chlorine gas with excess hydrogen. Lithium hydroxide solution is concentrated and crystallised to obtain crystals of a monohydrate of lithium hydroxide.
High-pressure water cell and method of its operation / 2470096
Invention relates to hydrogen power engineering and may be used at hydrogen filling stations for future-technology motor transport running on fuel cells. Proposed cell comprises fuel-cell battery consisting of, at least, two units differing in quantity of fuel cells, each being provided with their separate pipelines with water feed valves and those to discharge from said units. Note here that oxygen is discharged beyond the casing while hydrogen is discharged therein. Said casing is divided into, at least, two different-strength sections by tight partition. Stronger section accommodates units with smaller cells. Method of operation comprises water feed into fuel-cell battery composed of two sections to decompose electrolysis gases, discharging the latter, cutting off supply of cells after reaching maximum tolerable pressure. Note here that hydrogen communication between two sections allows cut off, first, one section with larger quantity of cells in due time and, then, that with smaller quantity of cells.
Method and complex for preparing of bottled oxygen- saturated water / 2246882
Method involves producing oxygen-saturated water by ejection-floatation mixing of water with oxygen-containing gas; bottling oxygen-saturated water and capping, with gas-and-vapor H2O2+O2 mixture synthesized by plasma chemotronical method being used in all above operations. Complex of equipment comprises ejection-floatation unit for oxygen saturation of water and installation for supplying and bottling of oxygen-saturated water.
Method of saturation of water with oxygen and plant for realization of this method / 2247081
Proposed method includes successive ejection-floatation mixing of plasma-chemotronic method of vapor-and-gas mixture H2O2+02 with water. Plant proposed for realization of this method includes two systems interconnected by means of vapor-and-gas pipe line: ejection-floatation system and vapor-and-gas producing system. Ejection-floatation system for saturation of water with oxygen is provided with pump, ejector and pressure floatation column interconnected by circulating pipe line. In its lower part column is connected to starting water pipe line and in upper part it is connected to oxygen-saturated water pipe line. Ejector is mounted in circulating pipe line between lower part of column and pump and is connected to vapor-and-gas mixture producing system by means of vapor-and-gas pipe line. Closed electrolyte circulating system for obtaining the vapor-and-gas mixture includes gas-and-liquid separator, electrolyte reservoir, plasma-chemotronic apparatus whose lower part is connected with air or oxygen supply pipe line through flow regulator.
Electrode, apparatus and method for electrolytic treatment of liquid, system for regenerating soil in situ and unit for performing reduction-oxidation reactions / 2247175
Electrode includes elongated, mainly hollow body made of porous material characterized by comparatively low electric conductivity, connector in the form of elongated electrically conducting member connected to power source. Connector passes along inner cavity of electrode body and it has contact with surface of inner wall of body in large number of places mutually spaced along length of body for distributing electric current supplied from power source practically uniformly along electrode.
Electrode, apparatus and method for electrolytic treatment of liquid, system for regenerating soil in situ and unit for performing reduction-oxidation reactions / 2247175
Electrode includes elongated, mainly hollow body made of porous material characterized by comparatively low electric conductivity, connector in the form of elongated electrically conducting member connected to power source. Connector passes along inner cavity of electrode body and it has contact with surface of inner wall of body in large number of places mutually spaced along length of body for distributing electric current supplied from power source practically uniformly along electrode.
Method of a ferric iron hydroxide hydrosol production / 2250914
The invention is intended for a chemical industry, an agriculture and pedology and may be used at production of solutions for soils reclamation. 0.5 l of a ferric chloride solution with concentration of 0.5 l/mole gram-molecule is poured into a pan. Carbon electrodes are put into the solution. Pass a current of 1А. Each 5-60 seconds polarity of the electrodes is changed. In a result of replacement of anions of the salt for ions of the hydroxyl obtain a stable hydrosol of the ferric iron hydroxide. The invention allows to produce such sols using a simple and a production-friendly method commercially.
Preparation of vanadium electrolyte with aid of asymmetric vanadium-reducing electrolyzer and use of asymmetric vanadium-reducing electrolyzer for reducing electrolyte charge state balance in operating reduction-oxidation vanadium battery / 2251763
Novelty is that acid vanadium electrolyte liquor that has in its composition V+3 and V+4 in desired concentration ratio introduced in electrolyte solution is produced from solid vanadium pentoxide by electrochemical method while at least partially reducing dissolved vanadium in acid electrolyte liquor; for the purpose electrolyte liquor is circulated through plurality of cascaded electrolyzers at least partially to V+3 degree; in this way reduced vanadium incorporating electrolyte liquor leaving the last of mentioned electrolyzers enters in reaction with stoichiometric amount of vanadium pentoxide to produce electrolyte liquor incorporating in effect vanadium in the V+3 form; acid and water are introduced to ensure definite molarity of liquor and the latter is continuously circulated through cascaded electrolyzers; stream of electrolyte liquor produced in the process that incorporates V+3 and V+4 in desired concentrations is discharged at outlet of one of electrolyzers of mentioned cascade. Each electrolyzer is distinguished by high degree of asymmetry and has cathode and anode of relevant surface morphology, geometry, and relative arrangement for setting current density on anode surface exceeding by 5 to 20 times that on projected cathode surface, oxygen being emitted from anode surface. Asymmetric electrolyzer of this type can be used in one of electrolyte circuits, positive or negative, of operating battery (cell) for reducing balance of respective oxidation degrees of their vanadium content.
Hydrogen-oxygen mixture generator / 2252275
The invention is pertaining to technologies of electrochemical productions, in particular, to devices for electrolysis of water. The generator of a hydrogen-oxygen mixture contains at least one cylinder with a jacket of cooling, automatic inlet and outlet gates, a piston and a head of the cylinder forming a self-contained volume of the cylinder, a connecting rod gear linked wit a drive. The electrolyzer is made in a hermetic body with a cooling jacket with a capability of an easy passing through it of an electrolyte water solution. The electrolyzer is made in the form of two electrodes - half-blocks with a positive allowance entering each other. A device of the electrolyte cycle batch feeding into the electrolyzer is made in the form of a high-lift pump kinematically or through a control package is linked with the connecting rod gear and is supplied with the injector. The technical effect consists in an increase of productivity of the generator and its operating safety.
Electrolysis-water gaseous generator / 2252276
The invention is pertaining to the field of welding and may find application in devices of a gas-flame treatment of materials. The electrolysis-water gaseous generator contains a hermetic body made in the form of a rectangular container with a liquid, in the internal grooves of which there are two packages of metal plates shifted in respect to each other. At that the last and the first plates of the two packages are electrically connected. The generator contains a tight cylinder with a volume for automatic feeding of a liquid, a bubbler, a gas-mixer, an outlet connection pipe with a torch and a control circuit with the liquid level and pressure operated magnetic contacts located in a tight pipe, on the outer side of which there are a floater and a magnet. The length of the tight cylinder volume of automatic feeding of a liquid and its diameter are exceeding the length and width of the hermetic rectangular body accordingly. The shape of the upper part of the body is compatible with the cylindrical form of the volume of the automatic feeding, above which there are in series located a tight elastic dielectric spacer and the cylindrical volume of automatic feeding of a liquid. The height of the metal plates of the two packages does not exceed the height of the lower part of the cylindrical volume used for automatic feeding of a liquid, which similarly to the elastic dielectric spacer also has a through groove located in the area of displacement of the two packages of metal plates, which is ensuring formation of a gas cushion above a package of the metal plates and automatic feeding of a liquid. The technical effect is an essential simplification of the design of the device for the gas-flame treatment of materials.
Electrolysis-water gaseous generator / 2252276
The invention is pertaining to the field of welding and may find application in devices of a gas-flame treatment of materials. The electrolysis-water gaseous generator contains a hermetic body made in the form of a rectangular container with a liquid, in the internal grooves of which there are two packages of metal plates shifted in respect to each other. At that the last and the first plates of the two packages are electrically connected. The generator contains a tight cylinder with a volume for automatic feeding of a liquid, a bubbler, a gas-mixer, an outlet connection pipe with a torch and a control circuit with the liquid level and pressure operated magnetic contacts located in a tight pipe, on the outer side of which there are a floater and a magnet. The length of the tight cylinder volume of automatic feeding of a liquid and its diameter are exceeding the length and width of the hermetic rectangular body accordingly. The shape of the upper part of the body is compatible with the cylindrical form of the volume of the automatic feeding, above which there are in series located a tight elastic dielectric spacer and the cylindrical volume of automatic feeding of a liquid. The height of the metal plates of the two packages does not exceed the height of the lower part of the cylindrical volume used for automatic feeding of a liquid, which similarly to the elastic dielectric spacer also has a through groove located in the area of displacement of the two packages of metal plates, which is ensuring formation of a gas cushion above a package of the metal plates and automatic feeding of a liquid. The technical effect is an essential simplification of the design of the device for the gas-flame treatment of materials.
Electrolyzer / 2252921
Electrolyzer includes two electrodes (one electrode of stainless steel and other electrode of carbon); bridge type voltage rectifier; electric circuit plug; membrane; second doubled membrane - cover, for example of tracing paper or canvas; glass vessel; low-resistance voltage divider with taps; array of light emitting diodes with additional resistors whose number corresponds to that of taps; housing of electrolyzer. Plug is connected with inlets of bridge type voltage rectifier; negative outlet of voltage rectifier is connected with electrode of stainless steel. Second positive-polarity outlet of voltage rectifier is connected through low-resistance voltage divider with taps to carbon electrode arranged in second membrane-cover. All cathode ends of light emitting diodes with additional resistors are connected in parallel and they are connected with positive outlet of voltage rectifier; second ends of said diodes are connected with respective taps of low-resistance voltage divider.
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FIELD: chemistry. SUBSTANCE: method of conducting electrolysis employs at least two groups of electrodes which are electrically connected to a power supply, each having at least one pair of oppositely charged electrodes, wherein during electrolysis, an electrical circuit is switched, which enables alternate connection of groups of electrodes to the power supply, wherein during operation of the first group of electrodes, the second group and other groups are disconnected, after which the second group is connected to the power supply and the first and other groups are disconnected. The periodicity of alternate connection of groups of electrodes to the power supply is equal to 0.05-1.0 s. Also disclosed is an apparatus for conducting electrolysis, having an electrolysis cell and switching means, which enables alternate connection of the same groups of electrodes to the power supply while simultaneously disconnecting others. EFFECT: high efficiency of using electric power owing to low heat loss caused by time lag of a specific electrochemical process. 2 cl, 2 dwg
The invention relates to electrochemistry, and in particular to methods and devices for carrying out electrolysis. When carrying out electrolytic processes in an industrial environment with the aim of obtaining a large number of target products use several connected to a power source groups oppositely charged electrodes, connected in serial electrical circuit placed in one or several interconnected electrolytic cells. So, there is a method of conducting electrolysis with the aim of obtaining sodium hypochlorite and device for its implementation, described in [RU 2349682]. In this way the electrolysis is carried out with the use of several groups of oppositely charged electrodes. Each group of electrodes connected with a source of power, while in the process of electrolysis of the group of electrodes include a serial electrical circuit. The device for implementing this method comprises interconnected flow-through electrolytic cells, each of which houses one of the groups of electrodes. While the electrodes of all of the groups are connected with a power source and turned on in a sequential circuit. As for the implementation of this method with the use of the device in question uses multiple groups of electrodes, increased the are stated cost of electricity. This requires a high voltage power supply, because the groups of electrodes included in a serial electrical circuit. There is a method of conducting electrolysis and device for its implementation [EN 2133785], is selected as the nearest analogues of the proposed method and device. In this method, the electrolysis is conducted using two groups of oppositely charged electrodes. Each group of electrodes is connected to the power source. In the process of electrolysis are connecting to a power source first group of electrodes, and shortly after the start of electrolysis is connected to a power source, a second group of electrodes, so that the electrolysis process is carried out with use of two series-connected groups of electrodes. The device for implementing this method includes a cell in which two groups of electrodes, each of which contains at least one pair of oppositely charged electrodes. The device also includes a power source electrically coupled with each of the groups of electrodes, and means for switching, connecting first one and then both groups of electrodes to a power source. Consider the method and the device allow to increase the efficiency of COI is whether energy by reducing heat loss. However, during electrolysis under way a number of groups of electrodes, simultaneously connected to the power source increases, resulting in increase of power consumption. The objective of the proposed method and device is to reduce energy consumption. In respect of the proposed method the invention consists in that in the method of conducting electrolysis using at least two groups of electrodes, electrically connected to the power source, each of which contains at least one pair of oppositely charged electrodes in the electrolysis process carry out switching of the electrical circuit, connecting groups of electrodes to a power source, according to the invention are switching, providing alternate connection to a power source and disconnecting part of the groups of electrodes. In respect of the claimed device, the invention consists in that the device for carrying out electrolysis, comprising at least one cell, at least two groups of electrodes, each of which contains at least one pair of oppositely charged electrodes, a power source, electrically connected to each of the groups of electrodes, and means for switching, providing under the connectivity of the groups of electrodes to a power source, according to the invention the switching means is made to provide alternate connection to a power source and disconnected from the rest of the groups of electrodes. Fundamentally important to the inventive methods and devices is that during electrolysis is one of the groups of electrodes connected to the power source and the other of the groups of electrodes at this time is disconnected from the power source, the connecting and disconnecting part of the groups of electrodes occur alternately. Since the electrochemical processes occurring in the interelectrode space, quite slow, connect the power supply and disconnecting the electrodes does not result in termination of electrochemical reactions in the interelectrode space. This allows to carry out the electrolysis process at lower supply voltages and with less power, because during electrolysis one or the other of the groups of electrodes are disconnected from the power source. As shown by experimental studies, when using the above-described receiving a serial connection to a power source and disconnected from the rest of the groups of electrodes does not reduce the yield of the target product of the electrolysis process in relation to the output achieved in the case of the electrolysis process when p is constant connection to the power source of all groups of electrodes. The frequency of connection to the power source and disconnected from the rest of the groups of electrodes depends on the inertia of the particular electrochemical process. A feature of the inventive device is that it provides a means of switching performed by providing alternate connection to a power source and disconnected from the rest of the groups of electrodes. This allows the above-described reception alternate connection to a power source and disconnected from the rest of the groups of electrodes. Thus, the technical result of the claimed method and the claimed device is to reduce energy consumption. Figure 1 shows the dependence of the concentration of chlorine in the sodium hypochlorite solution from the amount of time spent on carrying out electrolysis of energy for the proposed method curve 1, and the method selected for comparison, curve 2. The method is as follows. Carry out the electrolysis process using at least two groups of electrodes, electrically connected to the power source. In this case a group of electrodes can be placed in the same cell or in different cells. Each group of electrodes includes one or more pairs of oppositely charged electrodes. During electrolysis is connected to the source of feed the first group (or the first part of the groups of electrodes, and the second group (or the second part of the groups of electrodes) at this time disconnected from the power source. Then Vice versa is connected to a power source, a second group (or the second part of the groups of electrodes, and the first group (or the first part of groups) is disconnected from the power source. As shown, for most of electrolysis processes is sufficient to connect the power source and disconnecting any group (part of the group of electrodes) was carried out with a periodicity of from 0.05 to 1.0 sec. An example of the method. Carried out the electrolysis of an aqueous solution of sodium chloride with a concentration of 100 g/l with the aim of obtaining sodium hypochlorite. The volume of the original salt solution was 1.5 L. Used the first, second and third groups of electrodes placed in the cell box type. Each group contained three anode and two cathodes, which formed 4 pairs of oppositely charged electrodes. As the power source electrodes used constant current source providing current to 5 A. During electrolysis to power supply serially connected first, then the second, then the third group of electrodes with a frequency of 0.1 sec. The process is conducted at a voltage of 10-12 B and amperage 5 A. During electrolysis through some periods of time predelli amount spent on electrolysis energy and the concentration of chlorine in the hypochlorite solution at controlled times. The results are presented in figure 1, where the axis A deferred concentration of chlorine in the sodium hypochlorite solution, g/l, and the B-axis is the amount spent on conducting electrolysis electricity, W·min (see curve 1). For comparison, electrolysis was carried out as described above, but with the constant connection of the first, second and third groups of electrodes to a power source. The process of electrolysis was carried out at a voltage of 22-25 B and amperage 5 A. During electrolysis through some intervals determined the amount spent on electrolysis energy and the concentration of chlorine in the sodium hypochlorite solution at controlled times. The results are presented in figure 1 (see curve 2). As shown by the results of the comparison, to obtain the same concentration of chlorine in the sodium hypochlorite solution requires much less energy. So, for example, to achieve a concentration of chlorine in the sodium hypochlorite solution of 2.0 g/l (see figure 1, curves 1 and 2) when carrying out electrolysis by the present method takes an amount of energy approximately 1.7 less than electrolysis according to the method selected for comparison. The device (figure 2) contains several, in particular the first 1, second 2 and third 3 groups of electrodes, each of which includes at least one, in particular, four pairs of oppositely charged electrodes 4 (in the drawing the position indicated two electrodes in the first group). The first 1, second 2 and third 3 groups of electrodes 4 are placed in the electrolytic cell 5. The device also includes a power source 6 and the tool 7 switching, which is in turn connected to the power source 6 and disconnecting the first 1, second 2 and third 3 groups of electrodes 4. As the switching means 7 can be, in particular, used the electronic key with the frequency of switching, which determines the frequency of connection groups 1, 2 and 3, electrodes 4 to the power source 6 and disable them from him. The device operates as follows. Download into the cell 5 of the original electrolyte. Carry out the electrolysis at alternate source connection 6 power supply and disconnecting the first 1, 2, and 3 groups of electrodes 4 by using the switching means 7. Thus, in particular, connect the first 1 group of electrodes 4 to the power source 6, while disconnected from the second 2 and third 3 groups of electrodes 4. Then disable the first 1 group of electrodes 4 from the power source 6 and connects 2 second group of electrodes 4. Next is disconnected from a power source 6 2 second group of electrodes 4 and connects the third group of electrodes 3 and 4. The described process is repeated at a predetermined interval. 1. The method of conducting electrolysis using two groups of electrodes, electrically connected with the United power, each of which contains at least one pair of oppositely charged electrodes in the electrolysis process carry out switching of the electrical circuit, connecting groups of electrodes to a power source, characterized in that perform switching, providing alternate connection to a power source and disconnecting part of the groups of electrodes in such a way that connect to power supply the first group of electrodes and the second group (and others) at this time disconnected from power source, then connect to a power source, a second group of electrodes, and the first group (and others) is disconnected from the power source and so on. 2. The device for carrying out electrolysis, comprising at least one cell, at least two groups of electrodes, each of which contains at least one pair of oppositely charged electrodes, a power source, electrically connected to each of the groups of electrodes, and means for switching, connecting groups of electrodes to a power source, characterized in that the switching means is made to provide alternate connection to a power source and disconnected from the rest of the groups of electrodes in such a way that connect to power supply the first group of electrodes and a second group, etc.) at this time, shut off from the power source, then connect to a power source, a second group of electrodes, and the first group (and others) is disconnected from a power source and so on.
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