CA2573988A1 - Method and device for pickling metals - Google Patents
Method and device for pickling metals Download PDFInfo
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- CA2573988A1 CA2573988A1 CA002573988A CA2573988A CA2573988A1 CA 2573988 A1 CA2573988 A1 CA 2573988A1 CA 002573988 A CA002573988 A CA 002573988A CA 2573988 A CA2573988 A CA 2573988A CA 2573988 A1 CA2573988 A1 CA 2573988A1
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- Prior art keywords
- electrodes
- electrode
- flat product
- strip
- lead
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F1/00—Electrolytic cleaning, degreasing, pickling or descaling
- C25F1/02—Pickling; Descaling
- C25F1/04—Pickling; Descaling in solution
- C25F1/06—Iron or steel
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F7/00—Constructional parts, or assemblies thereof, of cells for electrolytic removal of material from objects; Servicing or operating
Abstract
The invention relates to a method and device for electrolytically descaling flat metal products (2), particularly strips of stainless steel and or C-steel. At least one diamond electrode and /or at least one lead/tin electrode, e.g. a lead 93/tin 7 electrode (15), is used. The specific particularity of the diamond electrode or lead/tin electrodes lies in the form of water decomposition. Normally, water is divided into hydrogen and oxygen during electrolysis. The diamond electrode and/or lead/tin electrode, however, provides a working area in which either ozone or highly reactive hydroxyl radicals are formed instead oxygen. As a result, it is possible to significantly reduce descaling times in comparison with conventional chemical descaling and conventional electrolytic descaling.
Description
- 1._ Method and device for pickling metals The invention relates to a method and a device for the electrolytic pickling of flat metal products, in particular special steel and/or carbon steel strips. The term flat metal products relates primarily to metal strips and plates. However, the invention can also be applied to long metal products (for example, wires, profiles, tubes) or to metal surfaces in general.
In order to obtain a good level of cleanliness in the case of cold-rolled, rust and acid-resistant strips, their surface must undergo further processing to remove adhering oxide layers, or scale, formed during preceding heat treatment. The removal of scale is still done mechanically in the preproduction phase by means of vortex or sand blasters. Any residual scale remaining, such as the annealing scale resulting from intermediate and final annealing in the further course of production, is dissolved and detached by a chemical process, pickling, as the scale-covered strips pass through multiple acid baths. The pickling agent (= pickling solution = electrolytic fluid = electrolyte) used for special steel is generally a preheated acid mixture (mixed acid) of water-diluted nitric acid and hydrofluoric acid. The temperatures prevailing the pickling baths continuously give rise during the pickling process to the very unpleasant and also environmentally pollutant reactions of the NO3 anion forming NOX.
The pickling of cold-rolled special steel strips using the so-called "neutral electrolyte". method is already known. In this the voltage is indirectly impressed on the strip. This means that there are no points of contact between any current rollers and the strip. A
further feature of this method is that the anodes and cathodes are completely covered by electrolyte and are arranged horizontally, that is to say the cells are flooded horizontally.
AT 406385B describes a method of electrolytic pickling, a vertically fed strip being described as variant of the method. Here the electrodes are arranged vertically. In this case the voltage is impressed indirectly on the strip. The electrolytic fluid (Na2SO4) is fed into the gap between the anode and the strip. The advantage of this electrolytic method is that no NOX formation occurs, because no nitric acid is used. The disadvantage of this method stems from the narrow sphere of application. This method with this device is used solely in the pickling of cold-rolled special steel.
The reference manual "Pickling of Metals", by Dr. Rafael Rituper, (published by Eugen G. Leuze Verlag) describes methods which are concerned exclusively with the electrolytic pickling of metal surfaces. Constant reference is made throughout to the generation of oxygen directly on the anode, which permits the pickling.
DE 3937438 Al describes a possible way of pickling metal surfaces, through the combination of Fe3+ salts and/or gaseous or liquid oxygen carriers, such as H202, air and additional oxygen, which is obtained from an anodic oxidation. In this case 0.5 to 1.0 A/dm2 are introduced for the electrolysis.
AT 373922 B furthermore discloses a method for the electrolytic galvanizing of strip. This involves a vertical arrangement of the electrodes. The electrolytic fluid is fed into the gap between the anode and the strip. The voltage is impressed directly onto the strip - the cathodes take the form of current rollers.
In order to obtain a good level of cleanliness in the case of cold-rolled, rust and acid-resistant strips, their surface must undergo further processing to remove adhering oxide layers, or scale, formed during preceding heat treatment. The removal of scale is still done mechanically in the preproduction phase by means of vortex or sand blasters. Any residual scale remaining, such as the annealing scale resulting from intermediate and final annealing in the further course of production, is dissolved and detached by a chemical process, pickling, as the scale-covered strips pass through multiple acid baths. The pickling agent (= pickling solution = electrolytic fluid = electrolyte) used for special steel is generally a preheated acid mixture (mixed acid) of water-diluted nitric acid and hydrofluoric acid. The temperatures prevailing the pickling baths continuously give rise during the pickling process to the very unpleasant and also environmentally pollutant reactions of the NO3 anion forming NOX.
The pickling of cold-rolled special steel strips using the so-called "neutral electrolyte". method is already known. In this the voltage is indirectly impressed on the strip. This means that there are no points of contact between any current rollers and the strip. A
further feature of this method is that the anodes and cathodes are completely covered by electrolyte and are arranged horizontally, that is to say the cells are flooded horizontally.
AT 406385B describes a method of electrolytic pickling, a vertically fed strip being described as variant of the method. Here the electrodes are arranged vertically. In this case the voltage is impressed indirectly on the strip. The electrolytic fluid (Na2SO4) is fed into the gap between the anode and the strip. The advantage of this electrolytic method is that no NOX formation occurs, because no nitric acid is used. The disadvantage of this method stems from the narrow sphere of application. This method with this device is used solely in the pickling of cold-rolled special steel.
The reference manual "Pickling of Metals", by Dr. Rafael Rituper, (published by Eugen G. Leuze Verlag) describes methods which are concerned exclusively with the electrolytic pickling of metal surfaces. Constant reference is made throughout to the generation of oxygen directly on the anode, which permits the pickling.
DE 3937438 Al describes a possible way of pickling metal surfaces, through the combination of Fe3+ salts and/or gaseous or liquid oxygen carriers, such as H202, air and additional oxygen, which is obtained from an anodic oxidation. In this case 0.5 to 1.0 A/dm2 are introduced for the electrolysis.
AT 373922 B furthermore discloses a method for the electrolytic galvanizing of strip. This involves a vertical arrangement of the electrodes. The electrolytic fluid is fed into the gap between the anode and the strip. The voltage is impressed directly onto the strip - the cathodes take the form of current rollers.
The patent US 4,363,709 also disclosed the pickling of special steel strip with higher current densities.
Current densities of 40 to 60 A/dmZ are mentioned without, however, going into the apparatus capable of achieving this within a reasonable range (<40 Volts) in a full-scale plant.
GB 2140036 further describes a device for electrolytic pickling with vertical strip feed, indirect current supply and an electrolyte gravity-flow in the gap between strip and electrodes. In this case the current must cover long distances in the strip, the risk being that it will be diverted at one of the deflection rollers and will be subsequently no longer available for the pickling process.
An object of the present invention is to improve existing electrolytic pickling methods and corresponding devices so that the pickling time can be reduced.
The object is achieved by a method according to claim 1 and by a device according to claim 15. Use is made of at least one diamond electrode and/or at least one lead/tin electrode, for example a lead 93/tin7 electrode. The special characteristic of the diamond electrodes and the lead/tin electrodes is the form of water replacement.
Whereas in electrolysis water is usually split into hydrogen and oxygen, the diamond electrode and/or lead tin electrode provides a working range in which ozone or highly reactive hydroxyl radicals are formed instead of oxygen. One of the outstanding results of this invention is that the pickling times are significantly reduced in comparison to the conventional chemical descaling, and also in comparison to the conventional electrolytic pickling. The reason for this is the formation of highly efficient OH radicals, oxygen in statu nascendi and simultaneous chemical erosion or dissolution of the oxide on the metal surface. Through the use of synthetically produced diamond electrodes and/or lead/tin electrodes, instead of oxygen the extremely efficient OH radicals can be formed here in the electrolysis of the pickling solution. These oxidize all dissolved substances contained in the pickling solution. The diamond electrode and/or lead/tin electrode moreover has a high level of stability in relation to aggressive pickling solutions.
In one possible development of the invention the current is delivered on the one hand directly to the flat product (for example, via current rollers or current brushes) and on the other to a pair of electrodes. The flat product and one electrode can be connected as anode and the other electrode as cathode. Delivering the electrical current directly to the anode (on the flat product) on the one hand generates oxygen in statu nascendi, whilst the use of the diamond electrode and/or lead/tin electrode as anode at the same time forms OH radicals, which permit the pickling of metal surfaces.
The generation of oxygen on the anode (steel strip or steel plate) and/or the formation of OH radicals on the anode (electrode) therefore replace the nitric acid HN03, the pickling solution forming the metal complexes and therefore being able to remove scale from the surface of the special steel and/or carbon steel. The pickling solution (mineral acids such as HF, H2SO4, H3P04i HC1, mixed acid or Na2SO4) here serves as.carrier medium for the direct electrical current, and at the same time as pickling solution for chemical descaling of the steel surface. Through the direct delivery of current on the anode, which may be the metal strip, oxygen in statu nascendi is generated by the anodic oxidation. The anode may also comprise a synthetically produced diamond electrode and/or lead/tin electrode, the diamond being applied to a corresponding substrate material and being made conductive by the doping of suitable elements.
Methods of producing diamond electrodes will be known to the person skilled in the art. The following methods of production will be mentioned as examples:
1) by directly producing boron-doped diamond layers on substrate materials (for example, niobium), in particular by chemical vapour deposition (CVD) processes, 2) by embedding a powder composed of doped, synthetically produced diamonds into the surface of a metal or a metal alloy, in such a way that an electrically conductive connection is produced between the metal or the metal alloy and the diamond particles (see W02004005585 A1), 3) by embedding a powder composed of doped synthetically produced diamonds into an electrically conductive plastic.
One advantageous development of the invention is characterized in that the direct current is intermittently impressed, preferably directly, on the flat product (strip) to be pickled and the diamond electrode and/or the lead/tin electrode. However, the direct current may also be delivered continuously, that is to say constantly.
An advantageous development of this invention is characterized in that the direct current is impressed alternately on the flat product (strip) to be pickled and on the electrode(s), which means that the electrodes can be acted upon by a direct current always changing from a cathodic current to an anodic current, then back to a cathodic current again.
Mineral acids, mixed acid and/or alkaline electrolytes, such as Na2SO4, may be used as electrolyte.
For chemical erosion and/or dissolution of the scale on the surface of the flat metal product (for example, strip) a mixture of mineral acids and water in a concentration of 10 g/l to 250 g/l mineral acid may be used, the concentration of the mineral acids in particular being between 50 to 200 g/l, preferably 150 g/1-In particular the electrolyte fluid may be a mixture of water and Na2SO4 (sodium sulphate), the composition of the electrolyte being purposely adjusted to the flat product to be pickled and the concentration of Na2SO 4 being between 100 and 350 g/l, preferably 150 g/1 Na2SO4.
The electrolyte fluid may also use a mixed acid (mixture of HF and HN03), however, and the composition of the mixed acid may be purposely adjusted to the flat product (strip) to be pickled, the concentration of the mixed acid being between 20 and 100 g/l HF and 50 and 300 g/1 HN03, preferably 50 g/1 HF and 150 g/l HN03. Even where mixed acidis used, only minimal if any NOX is developed, since the oxygen geneirated, or the OH radicals, causes the NOX produced to be immediately oxidized to HNO3 again.
It is also possible, as electrolyte fluid, to use:a mixed acid in which the concentration and composition corresponds to that generally used in conventional chemical pickling.
Current densities of 40 to 60 A/dmZ are mentioned without, however, going into the apparatus capable of achieving this within a reasonable range (<40 Volts) in a full-scale plant.
GB 2140036 further describes a device for electrolytic pickling with vertical strip feed, indirect current supply and an electrolyte gravity-flow in the gap between strip and electrodes. In this case the current must cover long distances in the strip, the risk being that it will be diverted at one of the deflection rollers and will be subsequently no longer available for the pickling process.
An object of the present invention is to improve existing electrolytic pickling methods and corresponding devices so that the pickling time can be reduced.
The object is achieved by a method according to claim 1 and by a device according to claim 15. Use is made of at least one diamond electrode and/or at least one lead/tin electrode, for example a lead 93/tin7 electrode. The special characteristic of the diamond electrodes and the lead/tin electrodes is the form of water replacement.
Whereas in electrolysis water is usually split into hydrogen and oxygen, the diamond electrode and/or lead tin electrode provides a working range in which ozone or highly reactive hydroxyl radicals are formed instead of oxygen. One of the outstanding results of this invention is that the pickling times are significantly reduced in comparison to the conventional chemical descaling, and also in comparison to the conventional electrolytic pickling. The reason for this is the formation of highly efficient OH radicals, oxygen in statu nascendi and simultaneous chemical erosion or dissolution of the oxide on the metal surface. Through the use of synthetically produced diamond electrodes and/or lead/tin electrodes, instead of oxygen the extremely efficient OH radicals can be formed here in the electrolysis of the pickling solution. These oxidize all dissolved substances contained in the pickling solution. The diamond electrode and/or lead/tin electrode moreover has a high level of stability in relation to aggressive pickling solutions.
In one possible development of the invention the current is delivered on the one hand directly to the flat product (for example, via current rollers or current brushes) and on the other to a pair of electrodes. The flat product and one electrode can be connected as anode and the other electrode as cathode. Delivering the electrical current directly to the anode (on the flat product) on the one hand generates oxygen in statu nascendi, whilst the use of the diamond electrode and/or lead/tin electrode as anode at the same time forms OH radicals, which permit the pickling of metal surfaces.
The generation of oxygen on the anode (steel strip or steel plate) and/or the formation of OH radicals on the anode (electrode) therefore replace the nitric acid HN03, the pickling solution forming the metal complexes and therefore being able to remove scale from the surface of the special steel and/or carbon steel. The pickling solution (mineral acids such as HF, H2SO4, H3P04i HC1, mixed acid or Na2SO4) here serves as.carrier medium for the direct electrical current, and at the same time as pickling solution for chemical descaling of the steel surface. Through the direct delivery of current on the anode, which may be the metal strip, oxygen in statu nascendi is generated by the anodic oxidation. The anode may also comprise a synthetically produced diamond electrode and/or lead/tin electrode, the diamond being applied to a corresponding substrate material and being made conductive by the doping of suitable elements.
Methods of producing diamond electrodes will be known to the person skilled in the art. The following methods of production will be mentioned as examples:
1) by directly producing boron-doped diamond layers on substrate materials (for example, niobium), in particular by chemical vapour deposition (CVD) processes, 2) by embedding a powder composed of doped, synthetically produced diamonds into the surface of a metal or a metal alloy, in such a way that an electrically conductive connection is produced between the metal or the metal alloy and the diamond particles (see W02004005585 A1), 3) by embedding a powder composed of doped synthetically produced diamonds into an electrically conductive plastic.
One advantageous development of the invention is characterized in that the direct current is intermittently impressed, preferably directly, on the flat product (strip) to be pickled and the diamond electrode and/or the lead/tin electrode. However, the direct current may also be delivered continuously, that is to say constantly.
An advantageous development of this invention is characterized in that the direct current is impressed alternately on the flat product (strip) to be pickled and on the electrode(s), which means that the electrodes can be acted upon by a direct current always changing from a cathodic current to an anodic current, then back to a cathodic current again.
Mineral acids, mixed acid and/or alkaline electrolytes, such as Na2SO4, may be used as electrolyte.
For chemical erosion and/or dissolution of the scale on the surface of the flat metal product (for example, strip) a mixture of mineral acids and water in a concentration of 10 g/l to 250 g/l mineral acid may be used, the concentration of the mineral acids in particular being between 50 to 200 g/l, preferably 150 g/1-In particular the electrolyte fluid may be a mixture of water and Na2SO4 (sodium sulphate), the composition of the electrolyte being purposely adjusted to the flat product to be pickled and the concentration of Na2SO 4 being between 100 and 350 g/l, preferably 150 g/1 Na2SO4.
The electrolyte fluid may also use a mixed acid (mixture of HF and HN03), however, and the composition of the mixed acid may be purposely adjusted to the flat product (strip) to be pickled, the concentration of the mixed acid being between 20 and 100 g/l HF and 50 and 300 g/1 HN03, preferably 50 g/1 HF and 150 g/l HN03. Even where mixed acidis used, only minimal if any NOX is developed, since the oxygen geneirated, or the OH radicals, causes the NOX produced to be immediately oxidized to HNO3 again.
It is also possible, as electrolyte fluid, to use:a mixed acid in which the concentration and composition corresponds to that generally used in conventional chemical pickling.
The use according to the invention of the direct current, which replaces the HNO3, means that no measures have to be taken to reduce the NOX inevitably produced. The use of urea or hydrogen peroxide can be dispensed with.
It is in any case possible to provide devices which ensure that the concentration of the pickling bath can be precisely adhered to. This makes it possible to improve the surface quality of the flat product, for example the steel strip.
The current densities (amperes per unit area) can be purposely adjusted to the flat product to be pickled, the current densities on the electrodes being between 0.5 and 150 A/dm2. The electrolyte temperature can be purposely adjusted to the strip to be pickled, the electrolyte temperature being between 20 and 90 C, preferably 75 C.
An advantageous development of the invention is characterized in that the electrical voltage can be variably adjusted so that the metal surface of the strip can also, if necessary, be polished.
A beneficial development of the invention is characterized in that the electrolyte feed quantity (quantity of pickling solution) in the gap between the pair of diamond electrodes and/or the pair of lead/tin electrodes and the strip is controlled. The strip-can thereby be hydraulically or mechanically positioned precisely in the centre between the pair of electrodes.
Thus it is possible to reduce the distance between the diamond electrodes and/or lead/tin -electrode and the strip to a minimum.
An advantageous development of the invention is characterized in that the gap between the diamond electrodes and/or lead/tin electrodes can be varied.
This means that the strip can be readily adjusted to the strip undulation.
A beneficial further development of the invention is characterized in that the strip undulation is determined and the diamond electrodes and/or lead/tin electrodes are distanced from the strip, so that any contact between the' strip and the diamond electrodes and/or lead/tin electrodes, which would be bound to lead to short-circuiting, is avoided.
A device for setting and regulating the distance between the strip and the diamond electrodes and/or lead/tin electrodes can furthermore be provided. The adjustable distance between the strip and the diamond electrodes and/or lead/tin electrodes allows the current flow to be adjusted, thereby reducing the power costs.
One possible embodiment of a device according to the invention is a pickling cell, in which the direct electrical current is impressed directly onto an electrically conductive contact between the strip and the electrode (cathode and/or anode). In this case guide devices may be provided, by means of which a strip can be guided at an angle to the horizontal, electrodes being arranged at the same angle and devices being provided, by means of which electrolyte fluid can be introduced between the strip and the electrodes. In particular a..
strip can be led obliquely downwards at an acute angle, in particular an angle of 30 to 45 , and then following at least one deflection roller obliquely upwards -at an angle, in particular an angle of 30 to 45 , so that the strip can be easily and efficiently introduced into the pickling cell. The obliquely inclined arrangement makes the cell space-saving. Substantially less space is required compared to conventional chemical pickling plants. A very effective strip guidance is furthermore achieved in that there is no sagging of the strip.
The position of at least one electrode of a pair of electrodes and the deflection roller may be adjustable perpendicular to the direction of movement of the flat product. The electrodes and the deflection roller can thereby be hydraulically and/or mechanically raised out of the way whilst the strip is being inserted.
Such an inclined pickling cell may be used both in batch-feed pickling and in so-called continuous pickling, since the introduction of the strip is made substantially easier by the folding up of the diamond electrodes and/or lead/tin electrodes and simultaneous raising of the deflection roller.
An advantageous variant of the invention is achieved by the provision of a control device for the electrolyte fluid (pickling solution) feed quantity, a separate control device being provided for each fluid inlet between the strip and the diamond electrodes and/or lead/tin electrodes, so that the flow can be adjusted to the strip width and also set to the optimum for strips of different width. The resulting hydraulic or mechanical guidance of the strip means that the position of the strip can be purposely adjusted between the pair of diamond electrodes and/or pair of lead/tin electrodes.
One advantage of the invention is that the spent pickle, that is to say the used pickling -solution, does not contain any nitrates and can thereby be recovered much more easily and cost effectively. The energy costs for the hydropyrolisis of the spent solutions prove to be substantially less than for conventional techniques.
It is in any case possible to provide devices which ensure that the concentration of the pickling bath can be precisely adhered to. This makes it possible to improve the surface quality of the flat product, for example the steel strip.
The current densities (amperes per unit area) can be purposely adjusted to the flat product to be pickled, the current densities on the electrodes being between 0.5 and 150 A/dm2. The electrolyte temperature can be purposely adjusted to the strip to be pickled, the electrolyte temperature being between 20 and 90 C, preferably 75 C.
An advantageous development of the invention is characterized in that the electrical voltage can be variably adjusted so that the metal surface of the strip can also, if necessary, be polished.
A beneficial development of the invention is characterized in that the electrolyte feed quantity (quantity of pickling solution) in the gap between the pair of diamond electrodes and/or the pair of lead/tin electrodes and the strip is controlled. The strip-can thereby be hydraulically or mechanically positioned precisely in the centre between the pair of electrodes.
Thus it is possible to reduce the distance between the diamond electrodes and/or lead/tin -electrode and the strip to a minimum.
An advantageous development of the invention is characterized in that the gap between the diamond electrodes and/or lead/tin electrodes can be varied.
This means that the strip can be readily adjusted to the strip undulation.
A beneficial further development of the invention is characterized in that the strip undulation is determined and the diamond electrodes and/or lead/tin electrodes are distanced from the strip, so that any contact between the' strip and the diamond electrodes and/or lead/tin electrodes, which would be bound to lead to short-circuiting, is avoided.
A device for setting and regulating the distance between the strip and the diamond electrodes and/or lead/tin electrodes can furthermore be provided. The adjustable distance between the strip and the diamond electrodes and/or lead/tin electrodes allows the current flow to be adjusted, thereby reducing the power costs.
One possible embodiment of a device according to the invention is a pickling cell, in which the direct electrical current is impressed directly onto an electrically conductive contact between the strip and the electrode (cathode and/or anode). In this case guide devices may be provided, by means of which a strip can be guided at an angle to the horizontal, electrodes being arranged at the same angle and devices being provided, by means of which electrolyte fluid can be introduced between the strip and the electrodes. In particular a..
strip can be led obliquely downwards at an acute angle, in particular an angle of 30 to 45 , and then following at least one deflection roller obliquely upwards -at an angle, in particular an angle of 30 to 45 , so that the strip can be easily and efficiently introduced into the pickling cell. The obliquely inclined arrangement makes the cell space-saving. Substantially less space is required compared to conventional chemical pickling plants. A very effective strip guidance is furthermore achieved in that there is no sagging of the strip.
The position of at least one electrode of a pair of electrodes and the deflection roller may be adjustable perpendicular to the direction of movement of the flat product. The electrodes and the deflection roller can thereby be hydraulically and/or mechanically raised out of the way whilst the strip is being inserted.
Such an inclined pickling cell may be used both in batch-feed pickling and in so-called continuous pickling, since the introduction of the strip is made substantially easier by the folding up of the diamond electrodes and/or lead/tin electrodes and simultaneous raising of the deflection roller.
An advantageous variant of the invention is achieved by the provision of a control device for the electrolyte fluid (pickling solution) feed quantity, a separate control device being provided for each fluid inlet between the strip and the diamond electrodes and/or lead/tin electrodes, so that the flow can be adjusted to the strip width and also set to the optimum for strips of different width. The resulting hydraulic or mechanical guidance of the strip means that the position of the strip can be purposely adjusted between the pair of diamond electrodes and/or pair of lead/tin electrodes.
One advantage of the invention is that the spent pickle, that is to say the used pickling -solution, does not contain any nitrates and can thereby be recovered much more easily and cost effectively. The energy costs for the hydropyrolisis of the spent solutions prove to be substantially less than for conventional techniques.
All metering, monitoring and tank units and pumps for HN03 and urea can be dispensed with, resulting in a major cost saving.
Separators arranged in the strip running direction ensure that the strip can be brought to the electrodes as accurately as possible without permitting any contact between the strip and the electrode. This ensures that the strip does not form an electrical short-circuit with the electrode.
An advantageous variant of the invention is characterized in that control of the current flow enables the surface of the strip to be pickled rapidly and efficiently and in a manner consistent with the quality grading, without polluting the environment with harmful gases such as NOX, or nitrate salts in the spent pickling solution.
The invention will now be explained with reference to examples in the drawings, in which Fig. 1 shows a schematic diagram of a conventional pickling plant with chemical removal by means of mixed acid, Fig. 2 shows a plant based on the "neutral electrolyte"
method, Fig. 3 shows a pickling cell based on the method according to the invention, Fig. 4 shows a plant based on the method according to the invention.
Fig. 1 shows a pickling bath 1 according to the prior art. The metal strip 2 is fed over the take-off reel 44 through the degreasing bath 5, and then cleaned with de-ionized water in the rinser 4 before embarking upon the chemical removal of the scale in the pickling bath 1 using the mixed acid 3(HF/HNO3). The mixed acid 3 is fed into the pickling bath 1 by a pump 7 via the pipe 6 and is led off via a pipe 8, for example into an intermediate vessel 9, where the mixed acid 3 is recirculated. The metered addition of a urea solution 10 is performed by a pump 11 directly into the pickling bath 1, and is done for environmental reasons so that the proportion of NOX
is reduced. - After the pickling bath 1, the metal strip 2 has any adhering mixed acid cleaned off by means of de-ionized water in the rinser 12, and the water removed by means of a blower in the drier 16, and is then rolled up on a take-up reel 45.
Fig. 2 shows a pickling bath 1 according to the prior art. The metal strip 2 is fed through the electrolyte 3, for example Na2SO4, between the cathodes 34 and the anodes 35. The distance between the electrodes and the strip is usually approximately 70 to 150 mm, the metal strip 2 having a certain sag, which can be reduced by means of support rollers at the middle of the plant, for example.
The electrolyte 3 is led off by a pipe 8 into an intermediate vessel 9, for example, and is returned by a pump 7 via the pipe 6 into the pickling bath 1, from whence the electrolyte 3 is recirculated.
Fig. 3 shows a pickling cell 13 according to the invention, which fulfils the function of the pickling bath 1. The metal strip 2, for example special steel and/or carbon steel strip, is fed into the gap between the electrodes 15 of a pair of electrodes. One electrode in each pair of electrodes 15 and a current roller 14 (or the metal strip 2) is connected to a rectifier 19 at any time.
Separators arranged in the strip running direction ensure that the strip can be brought to the electrodes as accurately as possible without permitting any contact between the strip and the electrode. This ensures that the strip does not form an electrical short-circuit with the electrode.
An advantageous variant of the invention is characterized in that control of the current flow enables the surface of the strip to be pickled rapidly and efficiently and in a manner consistent with the quality grading, without polluting the environment with harmful gases such as NOX, or nitrate salts in the spent pickling solution.
The invention will now be explained with reference to examples in the drawings, in which Fig. 1 shows a schematic diagram of a conventional pickling plant with chemical removal by means of mixed acid, Fig. 2 shows a plant based on the "neutral electrolyte"
method, Fig. 3 shows a pickling cell based on the method according to the invention, Fig. 4 shows a plant based on the method according to the invention.
Fig. 1 shows a pickling bath 1 according to the prior art. The metal strip 2 is fed over the take-off reel 44 through the degreasing bath 5, and then cleaned with de-ionized water in the rinser 4 before embarking upon the chemical removal of the scale in the pickling bath 1 using the mixed acid 3(HF/HNO3). The mixed acid 3 is fed into the pickling bath 1 by a pump 7 via the pipe 6 and is led off via a pipe 8, for example into an intermediate vessel 9, where the mixed acid 3 is recirculated. The metered addition of a urea solution 10 is performed by a pump 11 directly into the pickling bath 1, and is done for environmental reasons so that the proportion of NOX
is reduced. - After the pickling bath 1, the metal strip 2 has any adhering mixed acid cleaned off by means of de-ionized water in the rinser 12, and the water removed by means of a blower in the drier 16, and is then rolled up on a take-up reel 45.
Fig. 2 shows a pickling bath 1 according to the prior art. The metal strip 2 is fed through the electrolyte 3, for example Na2SO4, between the cathodes 34 and the anodes 35. The distance between the electrodes and the strip is usually approximately 70 to 150 mm, the metal strip 2 having a certain sag, which can be reduced by means of support rollers at the middle of the plant, for example.
The electrolyte 3 is led off by a pipe 8 into an intermediate vessel 9, for example, and is returned by a pump 7 via the pipe 6 into the pickling bath 1, from whence the electrolyte 3 is recirculated.
Fig. 3 shows a pickling cell 13 according to the invention, which fulfils the function of the pickling bath 1. The metal strip 2, for example special steel and/or carbon steel strip, is fed into the gap between the electrodes 15 of a pair of electrodes. One electrode in each pair of electrodes 15 and a current roller 14 (or the metal strip 2) is connected to a rectifier 19 at any time.
The upper electrodes 15 can in each case be moved in the direction 20, and the deflection roller 14' in the direction 20', so that the distance between the metal strip 2 and the electrodes 15 is adjustable. This permits optimum utilization of the current. The electrolyte or pickling solution 3 is in turn delivered by means of a pump 7 via a pipe 6, pipes 21, 21', 21" , 2111, being provided, which feed the electrolyte 3 into the gaps 24, 24', 2411, 24111 between the metal strip 2 and the electrodes 15. The delivery of electrolyte or pickling solution can now be adjusted to the required conditions by the control valves 22, 22', 2211, 221''.
After passing between the metal strip 2 an the electrodes the electrolyte 3 is collected in the lower part 23 of 15 the electrolytic pickling cell 13 and fed back to the pump 7. The separators 25, 25', 2511, 25 "' are arranged in the running direction of the strip.
The lower electrode is in each case connected to the negative output of the rectifier 19, the positive output of the rectifier 19 is connected to the current roller 14. The upper electrode 15 is in each case connected to the negative output of the rectifier 19, the metal strip is connected to the positive output of the rectifier 19.
In order for the electrodes 15, which take the form of diamond electrodes or lead/tin electrodes, to be operated as anode, the direct current would have to be impressed alternately.
A more advantageous development of the invention (which is not limited to the concrete example), is to connect the lower electrode on the inlet side to the positive output of a rectifier, so that it serves as anode. The metal strip is likewise connected to positive potential.
The upper electrode is then connected to the negative output of the rectifier and serves as cathode. On the outlet side the connection of the electrodes is reversed:
the lower electrode there serves as cathode, the upper as anode. In this way both the upper side and the underside of the strip comes into the area of the OH radicals formed on the anode. In this development just one rectifier 19 each could be provided both for the inlet side and for the outlet side.
An alternative to the latter possible embodiment (which is not limited to the concrete example) is to connect no current to the metal strip 2, that is to apply current only to the electrode pair serving as cathode and anode ay any one time.
Fig. 4 shows a plant having a take-off reel 44 and a take-up reel 45, which enable the metal strip 2 to be drawn through the processing at a corresponding speed.
The treatment comprises a chemical and/or electrolytic degreasing 5, in order to be able to clean the oiled strip, and an electrolytic pickling cell 13. The electrolytic pickling cell 13 is connected to the rectifiers. The pairs of electrodes 15 are arranged so that in only one pair of electrodes 15 is connected to a current roller 14 and to a rectifier at any one time. By means of the rectifier setting, variable electrical voltages, intermittent, alternating and/or continuous can be impressed on the electrodes, which where necessary polish the surface of the metal strip 2. The metal strip 2-is deflected over the current rollers 14 and the deflection roller 14'.
After passing between the metal strip 2 an the electrodes the electrolyte 3 is collected in the lower part 23 of 15 the electrolytic pickling cell 13 and fed back to the pump 7. The separators 25, 25', 2511, 25 "' are arranged in the running direction of the strip.
The lower electrode is in each case connected to the negative output of the rectifier 19, the positive output of the rectifier 19 is connected to the current roller 14. The upper electrode 15 is in each case connected to the negative output of the rectifier 19, the metal strip is connected to the positive output of the rectifier 19.
In order for the electrodes 15, which take the form of diamond electrodes or lead/tin electrodes, to be operated as anode, the direct current would have to be impressed alternately.
A more advantageous development of the invention (which is not limited to the concrete example), is to connect the lower electrode on the inlet side to the positive output of a rectifier, so that it serves as anode. The metal strip is likewise connected to positive potential.
The upper electrode is then connected to the negative output of the rectifier and serves as cathode. On the outlet side the connection of the electrodes is reversed:
the lower electrode there serves as cathode, the upper as anode. In this way both the upper side and the underside of the strip comes into the area of the OH radicals formed on the anode. In this development just one rectifier 19 each could be provided both for the inlet side and for the outlet side.
An alternative to the latter possible embodiment (which is not limited to the concrete example) is to connect no current to the metal strip 2, that is to apply current only to the electrode pair serving as cathode and anode ay any one time.
Fig. 4 shows a plant having a take-off reel 44 and a take-up reel 45, which enable the metal strip 2 to be drawn through the processing at a corresponding speed.
The treatment comprises a chemical and/or electrolytic degreasing 5, in order to be able to clean the oiled strip, and an electrolytic pickling cell 13. The electrolytic pickling cell 13 is connected to the rectifiers. The pairs of electrodes 15 are arranged so that in only one pair of electrodes 15 is connected to a current roller 14 and to a rectifier at any one time. By means of the rectifier setting, variable electrical voltages, intermittent, alternating and/or continuous can be impressed on the electrodes, which where necessary polish the surface of the metal strip 2. The metal strip 2-is deflected over the current rollers 14 and the deflection roller 14'.
List of reference numerals 1 Pickling bath 2 Metal strip 3 Electrolyte 4 Rinser Degreasing bath 6 Pipe from pump 6 to pickling bath 1 or pickling cell 13 7 Pump 8 Pipe from pickling bath 1 to intermediate vessel 9 9 Intermediate vessel Urea solution 11 Pump for urea solution 10 12 Rinser 13 Electrolytic pickling cell 14 Current roller 14' Deflection roller Electrodes 16 Drier 19 Rectifier Direction of movement of the electrodes 15 20' Direction of movement of the deflection roller 14' 21, 21', 2111, Electrolyte delivery pipes 21,,, 22, 22', 2211, Electrolyte delivery control valves 22"' 23 Lower part of the pickling cell 13 24, 24', 2411, Gap between metal strip 2 and 24 ,", electrode 15 25, 25', 2511, Separators 25"' Fluid level 34 Cathode 35 Anode 44 Take-off reel 45 Take-up reel
Claims (24)
1. Method for the electrolytic pickling of flat metal products (2), in particular special steel and/or carbon steel strips, characterized in that at least one diamond electrode and/or at least one lead/tin electrode, for example a lead 93/tin7 electrode (15) is used.
2. Method according to Claim 1, characterized in that the current is delivered on the one hand directly to the flat product (2) and on the other to at least one pair of electrodes.
3. Method according to Claim 2, characterized in that one electrode (15) of the pair of electrodes and where necessary the flat product (2) is connected as anode and the other electrode (15) as cathode.
4. Method according to any one of Claims 1 to 3, characterized in that the current is delivered intermittently.
5. Method according to any one of Claims 1 to 4, characterized in that the current is delivered constantly.
6. Method according to any one of Claims 1 to 5, characterized in that direct current is impressed alternately (reverse pulse plating) on the flat product (2) to be pickled and the electrodes (15).
7. Method according to any one of Claims 1 to 6, characterized in that a mixture of mineral acids and water in a concentration of 10 g/l to 250 g/l mineral acid, in particular between 50 to 200 g/l, preferably 150 g/l, is used.
8. Method according to any one of Claims 1 to 7, characterized in that a mixture of water and Na2SO4 (sodium sulphate) is used , the concentration of Na2SO4 being set between 100 and 350 g/l, preferably 150 g/l Na2SO4, as a function of the flat product to be pickled.
9. Method according to any one of Claims 1 to 8, characterized in that mixed acid is used, the concentration being set between 20 and 100 g/l HF
and 50 and 300 g/l HNO3, preferably to 50 g/l HF and 150 g/l HNO3 as a function of the flat product (2) to be pickled.
and 50 and 300 g/l HNO3, preferably to 50 g/l HF and 150 g/l HNO3 as a function of the flat product (2) to be pickled.
10. Method according to any one of Claims 1 to 9, characterized in that the current densities on the electrodes are set between 0.5 and 150 A/dm2 as a function of the flat product (2) to be pickled.
11. Method according to any one of Claims 1 to 10, characterized in that the electrolyte temperature is set between 20 and 90°C, preferably to 75°C, as a function of the flat product (2) to be pickled.
12. Method according to any one of Claims 1 to 11, characterized in that the electrical voltage is variably adjusted.
13. Method according to any one of Claims 1 to 12, characterized in that the distance between the flat product and the electrode is adjusted with the quantity of electrolyte fluid fed between the flat product (2) and the electrode (15).
14. Method according to any one of Claims 2 to 13, characterized in that the distance between the electrodes (15) of a pair of electrodes or between the electrode (15) and the flat product (2) is adjusted to the undulation of the flat product.
15. Device for performing a method according to any one of Claims 1 to 14 for the electrolytic pickling of flat metal products (2), in particular special steel and/or carbon steel strips, characterized in that at least one diamond electrode and/or at least one lead/tin electrode, for example a lead 93/tin7 electrode (15) is used.
16. Device according to Claim 15, characterized in that at least one pair of opposing electrodes (15) is provided, between which a flat product (2) can be fed.
17. Device according to either of Claims 15 or 16, characterized in that a device (19) is provided for delivering current on the one hand directly to the flat product (2) and on the other to the electrodes (15), in particular so that one electrode of a pair of electrodes is connected as cathode and the other electrode as anode, and the flat product can if necessary be connected as anode.
18. Device according to any one of Claims 15 to 17, characterized in that guide devices (14, 14') are provided, by means of which a strip (2) can be guided at an angle to the horizontal, that electrodes (15) are arranged at the same angle, and that devices (21, 21', 211'', 21''', 22, 22', 22'', 22 ''') are provided, by means of which electrolyte fluid can be introduced between the strip (2) and the electrodes (15).
19. Device according to Claim 18, characterized in that a strip can be led obliquely downwards at an angle, in particular an angle of 30 to 45°, and then following at least one deflection roller (14') obliquely upwards at an angle, in particular an angle of 30 to 45°.
20. Device according to any one of Claims 16 to 19, characterized in that the position of at least one electrode (15) of a pair of electrodes and the deflection roller (14') can be adjusted perpendicular to the direction of movement of the flat product.
21. Device according to any one of Claims 16 to 20, characterized in that the gap between the electrodes of a pair of electrodes is adjustable.
22. Device according to any one of Claims 15 to 21, characterized in that a control device is provided for regulating the delivery quantity of the electrolyte fluid.
23. Device according to any one of Claims 15 to 22, characterized in that at least one separator is fitted on at last one electrode.
24. Device according to any one of Claims 15 to 23, characterized in that a control device is provided for controlling the current flow to the electrodes (15).
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT0121804A AT413707B (en) | 2004-07-19 | 2004-07-19 | METHOD AND DEVICE FOR METALING |
| ATA1218/2004 | 2004-07-19 | ||
| PCT/EP2005/007480 WO2006008017A1 (en) | 2004-07-19 | 2005-07-11 | Method and device for descaling metals |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2573988A1 true CA2573988A1 (en) | 2006-01-26 |
Family
ID=34916826
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002573988A Abandoned CA2573988A1 (en) | 2004-07-19 | 2005-07-11 | Method and device for pickling metals |
Country Status (14)
| Country | Link |
|---|---|
| US (1) | US20070289878A1 (en) |
| EP (1) | EP1781842A1 (en) |
| JP (1) | JP2008506847A (en) |
| CN (1) | CN101052752A (en) |
| AT (1) | AT413707B (en) |
| AU (1) | AU2005263476A1 (en) |
| BR (1) | BRPI0513474A2 (en) |
| CA (1) | CA2573988A1 (en) |
| MX (1) | MX2007000707A (en) |
| NO (1) | NO20070938L (en) |
| RU (1) | RU2375506C2 (en) |
| TW (1) | TW200604388A (en) |
| WO (1) | WO2006008017A1 (en) |
| ZA (1) | ZA200701240B (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT1395853B1 (en) * | 2009-09-30 | 2012-10-26 | Tenova Spa | SURFACE PREPARATION GROUP FOR METALLIC TAPE PRODUCTION LINES |
| US20130233702A1 (en) * | 2012-03-09 | 2013-09-12 | Chung-Shan Institute of Science and Technology, Armaments, Bureau, Ministry of National Defense | Multi-Stationed Continuous Electro-Polishing System |
| RU2537488C2 (en) * | 2012-08-22 | 2015-01-10 | Закрытое акционерное общество "Инструменты нанотехнологии" | Device for surface etching for metallographic analysis |
| CN103343381B (en) * | 2013-07-08 | 2016-04-20 | 湖北交投四优钢科技有限公司 | A kind of high-frequency impulse low-temperature quick derusting device and method |
| RU2578623C1 (en) * | 2014-12-30 | 2016-03-27 | Публичное акционерное общество "Ашинский металлургический завод" | Electrolytic method for removing scales from belt of rolled metal |
| ITUB20154984A1 (en) * | 2015-10-16 | 2017-04-16 | Condoroil Stainless Srl | ELECTROLYTIC PICKLING PROCESS FOR STAINLESS STEELS |
| CN105220171B (en) * | 2015-10-24 | 2018-02-16 | 本钢不锈钢冷轧丹东有限责任公司 | One kind mixing descaling bath |
| CN105220213A (en) * | 2015-10-24 | 2016-01-06 | 本钢不锈钢冷轧丹东有限责任公司 | Neutral salt electrolysis groove |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE528202A (en) * | 1953-07-08 | |||
| US4121979A (en) * | 1975-08-28 | 1978-10-24 | Oxy Metal Industries Corporation | Metal treatment |
| US4363709A (en) * | 1981-02-27 | 1982-12-14 | Allegheny Ludlum Steel Corporation | High current density, acid-free electrolytic descaling process |
| IT1173713B (en) * | 1983-05-16 | 1987-06-24 | Centro Speriment Metallurg | DEVICE FOR ELECTROLYTIC TREATMENT OF METAL TAPES |
| DE4425854C1 (en) * | 1994-07-07 | 1995-11-09 | Mannesmann Ag | Electrolytic surface treatment process and plant for carrying out the process |
| US5980935A (en) * | 1996-05-15 | 1999-11-09 | Kirpotin; Dmitri | Cationic lipids and methods of use therefor |
| DE19624436A1 (en) * | 1996-06-19 | 1998-01-02 | Gewerk Keramchemie | Stainless steel strip surface treatment |
| AT406385B (en) * | 1996-10-25 | 2000-04-25 | Andritz Patentverwaltung | METHOD AND DEVICE FOR ELECTROLYTICALLY STICKING METAL STRIPS |
| DE19948184C2 (en) * | 1999-10-06 | 2001-08-09 | Fraunhofer Ges Forschung | Electrochemical production of peroxodisulfuric acid using diamond coated electrodes |
| US6569308B2 (en) * | 1999-10-14 | 2003-05-27 | The United States Of America As Represented By The Secretary Of The Navy | Fabrication of a high surface area diamond-like carbon or dirty diamond coated metal mesh for electrochemical applications |
| JP2002173799A (en) * | 2000-12-04 | 2002-06-21 | Zenken:Kk | Oxidation decomposition method and oxidation decomposition equipment of organic substance using hydroxyl radical |
| ITRM20010747A1 (en) * | 2001-12-19 | 2003-06-19 | Ct Sviluppo Materiali Spa | PROCEDURE WITH REDUCED ENVIRONMENTAL IMPACT AND RELATED PLANT FOR DESCALING, PICKLING AND FINISHING / PASSIVATING, IN A CONTINUOUS, INTEGRATED AND FL |
| DE10219688A1 (en) * | 2002-05-02 | 2003-11-20 | Condias Gmbh | Process for the oxidative treatment of surfaces using an electrolyte fluid containing an oxidant used in the microelectronics industry comprises pumping the electrolyte in a cycle |
| AT412002B (en) * | 2002-07-08 | 2004-08-26 | Wolfgang Dipl Ing Mag Wesner | DIAMOND ELECTRODE AND METHOD FOR THEIR PRODUCTION |
| EP1468965B1 (en) * | 2003-04-15 | 2006-09-13 | Permelec Electrode Ltd. | Diamond electrode for electrolysis |
| DE10324558A1 (en) * | 2003-05-30 | 2004-12-23 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Diamond electrode for electrochemical applications and process for their manufacture and use |
-
2004
- 2004-07-19 AT AT0121804A patent/AT413707B/en not_active IP Right Cessation
-
2005
- 2005-07-08 TW TW094123142A patent/TW200604388A/en unknown
- 2005-07-11 AU AU2005263476A patent/AU2005263476A1/en not_active Abandoned
- 2005-07-11 ZA ZA200701240A patent/ZA200701240B/en unknown
- 2005-07-11 US US11/632,757 patent/US20070289878A1/en not_active Abandoned
- 2005-07-11 CN CNA2005800311654A patent/CN101052752A/en active Pending
- 2005-07-11 WO PCT/EP2005/007480 patent/WO2006008017A1/en active Application Filing
- 2005-07-11 BR BRPI0513474-9A patent/BRPI0513474A2/en not_active IP Right Cessation
- 2005-07-11 EP EP05759974A patent/EP1781842A1/en not_active Withdrawn
- 2005-07-11 CA CA002573988A patent/CA2573988A1/en not_active Abandoned
- 2005-07-11 RU RU2007105890/02A patent/RU2375506C2/en not_active IP Right Cessation
- 2005-07-11 MX MX2007000707A patent/MX2007000707A/en not_active Application Discontinuation
- 2005-07-11 JP JP2007521848A patent/JP2008506847A/en not_active Withdrawn
-
2007
- 2007-02-19 NO NO20070938A patent/NO20070938L/en not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| AT413707B (en) | 2006-05-15 |
| WO2006008017A1 (en) | 2006-01-26 |
| ZA200701240B (en) | 2008-09-25 |
| RU2375506C2 (en) | 2009-12-10 |
| TW200604388A (en) | 2006-02-01 |
| AU2005263476A1 (en) | 2006-01-26 |
| RU2007105890A (en) | 2008-08-27 |
| EP1781842A1 (en) | 2007-05-09 |
| CN101052752A (en) | 2007-10-10 |
| US20070289878A1 (en) | 2007-12-20 |
| MX2007000707A (en) | 2007-07-13 |
| ATA12182004A (en) | 2005-09-15 |
| JP2008506847A (en) | 2008-03-06 |
| NO20070938L (en) | 2007-04-17 |
| BRPI0513474A2 (en) | 2011-11-16 |
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