WO2001019755A1 - Kombinationselektrode für die elektrochemische sanierung von korrosionsgeschädigtem stahlbeton und verfahren zu deren ansteuerung - Google Patents
Kombinationselektrode für die elektrochemische sanierung von korrosionsgeschädigtem stahlbeton und verfahren zu deren ansteuerung Download PDFInfo
- Publication number
- WO2001019755A1 WO2001019755A1 PCT/DE2000/003192 DE0003192W WO0119755A1 WO 2001019755 A1 WO2001019755 A1 WO 2001019755A1 DE 0003192 W DE0003192 W DE 0003192W WO 0119755 A1 WO0119755 A1 WO 0119755A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- electrode
- combination electrode
- ion exchange
- voltage
- concrete
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 64
- 239000011150 reinforced concrete Substances 0.000 title claims abstract description 13
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims abstract description 33
- 239000002131 composite material Substances 0.000 claims abstract description 20
- 239000003792 electrolyte Substances 0.000 claims abstract description 18
- 238000005342 ion exchange Methods 0.000 claims abstract description 16
- 238000005259 measurement Methods 0.000 claims abstract description 10
- 238000001704 evaporation Methods 0.000 claims abstract description 7
- 230000008020 evaporation Effects 0.000 claims abstract description 7
- 125000000129 anionic group Chemical group 0.000 claims abstract description 5
- 230000001105 regulatory effect Effects 0.000 claims abstract description 4
- 230000001276 controlling effect Effects 0.000 claims abstract description 3
- 230000002787 reinforcement Effects 0.000 claims description 23
- 230000008569 process Effects 0.000 claims description 22
- 150000002500 ions Chemical class 0.000 claims description 21
- 239000000463 material Substances 0.000 claims description 18
- 238000009418 renovation Methods 0.000 claims description 17
- 238000010276 construction Methods 0.000 claims description 5
- 238000012937 correction Methods 0.000 claims description 5
- 150000001805 chlorine compounds Chemical group 0.000 claims description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 4
- 239000011707 mineral Substances 0.000 claims description 4
- 229920006395 saturated elastomer Polymers 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 2
- 229910052715 tantalum Inorganic materials 0.000 claims description 2
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 claims description 2
- 150000003608 titanium Chemical class 0.000 claims description 2
- 239000012876 carrier material Substances 0.000 claims 1
- 125000004122 cyclic group Chemical group 0.000 claims 1
- 230000011664 signaling Effects 0.000 claims 1
- 239000004567 concrete Substances 0.000 abstract description 49
- 238000012544 monitoring process Methods 0.000 abstract description 4
- 239000000460 chlorine Substances 0.000 description 10
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 7
- 239000000853 adhesive Substances 0.000 description 7
- 230000008859 change Effects 0.000 description 7
- 229910052801 chlorine Inorganic materials 0.000 description 7
- 230000007797 corrosion Effects 0.000 description 7
- 238000005260 corrosion Methods 0.000 description 7
- 239000010959 steel Substances 0.000 description 7
- 230000001070 adhesive effect Effects 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- 239000011248 coating agent Substances 0.000 description 5
- 238000000576 coating method Methods 0.000 description 5
- 238000011161 development Methods 0.000 description 5
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 4
- 239000004568 cement Substances 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 241000053208 Porcellio laevis Species 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- -1 anionic ion Chemical class 0.000 description 2
- 239000004566 building material Substances 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 239000011244 liquid electrolyte Substances 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- 238000013021 overheating Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000004886 process control Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000009419 refurbishment Methods 0.000 description 2
- 238000005067 remediation Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000009172 bursting Effects 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000009532 heart rate measurement Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000007420 reactivation Effects 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000012976 tarts Nutrition 0.000 description 1
- 230000002123 temporal effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003079 width control Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/009—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone characterised by the material treated
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/45—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
- C04B41/4505—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements characterised by the method of application
- C04B41/4564—Electrolytic or electrophoretic processes, e.g. electrochemical re-alkalisation of reinforced concrete
- C04B41/4566—Electrochemical re-alcalisation
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/53—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone involving the removal of at least part of the materials of the treated article, e.g. etching, drying of hardened concrete
- C04B41/5369—Desalination, e.g. of reinforced concrete
- C04B41/5376—Electrochemical desalination
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/60—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone of only artificial stone
- C04B41/61—Coating or impregnation
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/60—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone of only artificial stone
- C04B41/72—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone of only artificial stone involving the removal of part of the materials of the treated articles, e.g. etching
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F2201/00—Type of materials to be protected by cathodic protection
- C23F2201/02—Concrete, e.g. reinforced
Definitions
- the invention relates to a combination electrode for the electrochemical renovation of corrosion-damaged reinforced concrete and a method for its control.
- the mineral building materials used in construction technology such as concrete, cement or mortar, are usually reinforced with steel elements that are embedded in the mineral building material.
- these steel elements are coated with such a thick layer of concrete that the steel element is usually permanently protected against corrosion.
- the corrosion protection of the concrete layer is based on the alkalinity of the water that is in the pores of the concrete and has a pH value that is greater than 12.5. Under these conditions, a thin, firmly adhering oxide layer forms on the steel surface, which practically completely prevents corrosion of the steel element. For this reason, reinforced concrete can be used for exterior parts that are exposed to the weather.
- the corrosion protection of the reinforcement can be impaired.
- carbon dioxide from the air reacts with the alkaline components of the cement, the concrete is carbonated. This lowers the pH so that there is no longer any protection against corrosion.
- Another, frequently occurring cause of corrosion is the penetration of chlorides into the concrete, for example when using the concrete components as a carriageway or near a carriageway when using de-icing salt. Both processes begin at the concrete surface and continue inside the concrete to the steel parts concreted in there, whereby their oxide layer dissolves.
- the chloride-containing concrete must be replaced or the chloride itself removed from the concrete.
- a method has therefore been proposed in which the chlorides are removed from the concrete electrochemically by ion migration. In this way, the chloride concentration in the concrete is drastically reduced, so that replacement of the concrete is no longer necessary.
- the method described by JE Slater in Materials Performance, 1976, 21-26 involves the application of an electrical potential between the internal reinforcement and a surface electrode immersed in a liquid electrolyte located on the surface of the concrete.
- the surface electrode forms the positive pole of the electric field, causing the negatively charged chloride ions contained in the concrete to migrate through the concrete, exit from it and enter the electrolyte.
- the chloride ions on the positive electrode are oxidized to gaseous chlorine or react chemically with components contained in the electrolyte.
- the method proposed by Slater has several disadvantages: On the one hand, this method requires the use of voltages between 100 and 120 V. Such high voltages, which have to be applied over a period of 24 hours, around 90% of the chlorides in the concrete are not acceptable for safety reasons. In addition, the costs involved can even exceed conventional techniques. On the other hand, the liquid electrolyte used is retained by dams that have to be created on the concrete surface. The method can therefore only be used for horizontal concrete surfaces. this means a lot of effort to prepare for chlorine deprivation and also severely limits the applicability of the method.
- DE 4 229 072 A1 proposes an electrolyte store with a resistance R »0, so that partial overheating, e.g. B. in the above individual reinforcement with the resulting small R concrete can be compensated by the R E ⁇ ektr0 ⁇ yt .
- the disadvantage of this solution is that the process peaks are only cut off automatically, without a regulation update with partial subfunction (R concrete large).
- US 5,228,959 proposes as the electrolyte an adhesive coating that can be applied to vertical surfaces or even on the undersides of concrete elements and adheres to them.
- An electrode is embedded in the adhesive coating, which forms the positive pole of the electrical system.
- the method comprises applying a removable, adhesive electrolytic coating to the surface of the concrete; applying a DC voltage between the reinforcement and the electrode to cause the negative ions to migrate; Interrupting the applied voltage and removing the adhesive coating when the desired level of ion migration has been reached; periodically measuring the potential difference between the reinforcement and the reference electrode and temporarily interrupting the DC voltage if the potential difference indicates the development of hydrogen.
- EP 0 398 117 A1 proposes a material for the adhesive electrolyte layer in the form of cellulose pulp, which is premixed with water or another solution such as calcium hydroxide in a nozzle and sprayed onto the surface of the area to be treated.
- This application also proposes an iron-containing material for the electrode that is reactive towards chlorine in order to minimize the release of free chlorine gas into the environment. This offers the advantage that less chlorine is released into the environment, but has the disadvantage that the formation of chlorine is not completely suppressed.
- the electrode is decomposed in the course of the application of the method, so that the method can only be used once for this reason.
- the object of the present invention to propose a means for the electrochemical remediation of corrosion-damaged reinforced concrete which overcomes the disadvantages of the prior art methods described above.
- the task here is to propose a cost-effective solution which is associated with little technical effort, can be used not only once but can be used several times and is optimally adapted to inhomogeneities in the component to be renovated.
- a combination electrode consisting of a dimensionally stable electrode as an anode; a pre-made, reusable electrolyte storage; an evaporation protection; a prefabricated termed, exchangeable, anionic ion exchange element; a central fastening with dowels, anchor rod and eccentric quick release device; a reference electrode on the dowel head; a humidifier; a power switching part for anodic control; a measuring system for determining the state of the ion exchanger element and electrical connections for the reference electrode, etc.
- the dimensionally stable electrode, the evaporation protection, the electrolyte storage and the ion exchanger can be connected to one another in the form of a sandwich construction.
- the combination electrode has a small area (approx. 0.6 x 0.6 m).
- the combination electrode according to the invention has the advantage that it can be prefabricated industrially. It also contains all the components that are necessary for active process control.
- the multi-part combination electrode allows the reactivation of the ion exchange material for reprocessing.
- a major advantage of the invention is that no active chlorine is formed. The chloride ions extracted from the concrete are bound to the ion exchange material, from which they can be removed by reactivating this material. The combination electrode is therefore reusable. The electrode is not self-adhesive.
- the dimensionally stable electrode is preferably made of surface-modified titanium, tantalum or similar materials.
- the electrolyte storage consists of fibrous mineral material, preferably of glass fleece. It therefore behaves chemically neutral under extremely acidic or basic loads, discoloration on the concrete surface is avoided; it is also geometrically stable and has a good water storage capacity.
- the ion exchanger is designed in such a way that anionic ion exchanger material is attached to a perforated carrier and can be pre-assembled in this way as a layer in the combination electrode, preferably between the electrolyte storage device and the electrode. This means that the electrode can be used in all installation positions and can be serviced quickly and easily when the ion exchanger is used up.
- the sensor system for on-line status control of the ion exchange material is characterized in that a measuring system for monitoring the consumption status is installed between the ion exchange layer and the dimensionally stable electrode, which is cyclically scanned by a computer system. An auxiliary electrode or a chloride sensor is integrated into the combination electrode. A measurable signal is generated when chloride ions strike the auxiliary electrode.
- Fastening, quick clamping device and reference electrode are designed so that a reference cell with a water-holding, slightly flexible diaphragm (for example MnO 2 and water-soaked felt) is attached to a plastic dowel.
- the dowel is brought with the reference electrode first into a borehole that is preferably centrally located within the electrode surface and that is located at a defined distance from the relevant reinforcement.
- the sandwich part of the combination electrode is pushed onto the anchor rod, which is hollow to accommodate the reference electrode lead and has a setting depth limit, and is fastened with a sleeve pushed over it, to which an eccentric shaft with a lever is attached.
- 1 is a schematic cross-sectional view of the combination electrode. 2 shows an oblique top view of the use of the combination electrode according to the invention.
- the multi-part and prefabricated combination electrode shown in FIG. 1 consists of the dimensionally stable electrode 1; the prefabricated, reusable electrolyte storage 2; the evaporation protection 3 and the prefabricated, exchangeable, anionic ion exchanger element 4, which are connected to one another as a sandwich construction.
- the reference electrode 6 is located on the dowel head of the central fastening with dowels, anchor rod and eccentric quick-action clamping device 5.
- the combination electrode is equipped with a humidification device 7, a power switching part for anodic control 8, a measuring system 9 for determining the state on the ion exchanger element and (not shown) electrical connections for equipped the reference cell.
- the dowel with the reference electrode 6 is introduced into a borehole in the concrete 11.
- the borehole is preferably located centrally within the electrode surface and at a defined lateral distance from the decisive reinforcement 12.
- the concrete part surface is divided into small partial areas.
- Such a partial area is preferably 60 x 60 cm.
- the method for controlling an electrode system is aimed at the short-term electrochemical renovation of corrosion-damaged reinforced concrete and comprises (1) the subdivision of the two-dimensional surface of a reinforced concrete structure to be renovated into any number of grid areas of equal size; (2) the electrochemical, physical and chemical characterization, consisting of measuring the resting potential, galvanic pulse measurement, recording the course of the reinforcement of the deck reinforcement, the concrete cover, the pore space, the moisture, the chloride content and the depth of carbonation; (3) the assembly of the composite electrodes on the grid surfaces; (4) performing control measurements on each grid area to determine the rest potential (E ref ), the control of the electrical contacts and to determine the change in current over time as a result of the external voltage ( ⁇ I AK ); (5) the determination of the start values, the clamping voltage between anode and cathode (E AK ), the minimum clamping voltage without external voltage (E AK m ⁇ n ), the frequency of the pulse width modulation (f PWR ), the switch-on time of the external voltage (t An ) , include
- step (1) the two-dimensional surfaces of a reinforced concrete building to be renovated are preferably divided into 0.6 x 0.6 m grid areas.
- the monitoring of the voltage change at the chloride sensor in step (7) comprises the permanent interrogation of an auxiliary electrode in order to determine the saturation of the ion exchanger.
- the termination criteria which are monitored at each grid area during the entire duration of the renovation, are selected from the group that contains the total amount of chloride contained in the ion exchanger, which is the difference between the chloride content at the beginning of the renovation (Cs tart ) and the target chloride content (CI End ) in the concrete; the 100 mV criterion used to estimate the reserve of alkalinity; and includes the amount of charge registered.
- the saturation of the ion exchanger in the composite electrode can be precisely determined.
- the renovation process is automatically interrupted for the grid area in question, so that no chlorine gas development can occur at the anode.
- the amount of chloride, which corresponds to the absorption capacity of the ion exchanger is included in the process as a calculated value.
- a reduction in the direct current power at an electrode is achieved by pulse width modulation.
- the pulse width modulation comprises a two-point control with the states on and off. By varying the temporal ratio of the on and off phases, an effective output on the consumer, that is to say the grid areas, is achieved.
- a reduction of the direct current requirement by reducing the direct current power is not possible via conventional series regulators, since the unused energy is converted into heat in the regulator. This is prevented by using pulse width modulation according to the invention.
- pulse width modulation With the help of pulse width modulation and due to the modular structure, which enables the individual control of each grid area, the energy requirement of each grid area is optimally recorded so that the power fed in can be adapted to the needs.
- the DC voltage available for all electrodes of the renovation area is from Control computer switched, fed into the electrodes and regulated according to the energy requirement with minimal power losses as pulse-width-modulated square-wave voltage, so that there is an individual effective voltage or an individual effective current between the anode and cathode, which is measured anew with each control cycle and optimally to the kinetic Ratios on each electrode is adjusted. Furthermore, the cathodic potential measured on the reference electrode and falsified by the ohmic resistance of the concrete between the reinforcement and the reference electrode can be corrected by measuring and evaluating the slope of the switch-off edge on the pulse width control module on each electrode via the control computer (IR compensation).
- each grid area or group of grid areas can be treated as required by the actual degree of damage due to the modular structure of the device used.
- Each grid area or group of grid areas can be individually processed by the runtime control depending on the progress of the renovation.
- pulse width modulation low-loss power supply and power control is achieved individually for each grid area depending on its needs, so that an optimal renovation is made possible.
- no large-scale security provisions are necessary to avoid process overheating, since each grid area is treated as a function of the respective cathodic reference potential. Process reserves are thus used and also guaranteed that no damage to the structure occurs.
- the invention is characterized by a better reinforcement analysis in connection with small-area electrodes, whereby the method relates to the outer surface of the effective reinforcement and not, like the methods of the prior art, to the simplifying and incorrect assumption that the reinforcement surface and the concrete surface are the same is.
- the method can be individually adapted and optimized on the basis of known electrode areas and current density distributions.
- the pulse width modulation used according to the invention enables individual and dynamic process control of each individual composite electrode (0.6 x 0.6 m) without major power losses compared to the otherwise usual constant or regulated current sources.
- the method achieves an increase in efficiency by shifting the active times of different composite electrodes from one another in such a way that the maximum output of the system can be dimensioned below the total output of all composite electrodes.
- the pulse width modulation realizes an effective voltage for each composite electrode in accordance with the thermodynamic conditions within the reinforcement area covered by the composite electrode. Parameters of the pulse width modulation are frequency and duty cycle, which are continuously adjusted in the process based on the set start values. By using pulse width modulation, no current limitation is required for the connected composite electrode; For safety reasons, the DC voltage provided is set to 40 V.
- an essential starting parameter is the developed outer surface of the covering reinforcement; the electrode area of the working electrode (reinforcement, cathode) has been determined beforehand non-destructively.
- the current distribution is dimensioned and optimized much better than in the current view, which sets the electrode area equal to the concrete surface and can lead to completely wrong reference values.
- the chloride sensor used according to the invention indicates as a threshold switch that no further chloride ions can be absorbed by the ion exchanger. In this way, reliable conclusions can be drawn about the chloride removal rate achieved.
- an unintentional development of chlorine gas at the anode is prevented by the threshold signal described leading to the shutdown of the composite electrode in question; the shutdown state is maintained until the exhausted ion exchanger is replaced.
- pulse width modulation shown makes the function of a switch-off edge of the pulse-width-modulated DC voltage for permanent IR correction only applicable in that the switch-off edges of this type are available for evaluation in a very short sequence. Due to the significantly increased point layer of the IR waste measurements (location and time-resolved), safety limits of the process (avoidance of H 2 development) can be exploited much better, which leads to a sustainably higher effectiveness.
- an apparatus structure which consists of a composite electrode, which is on an approximately 0.6 x 0.6 m grid area of the two-dimensional reinforced concrete surface to be renovated is attached.
- the steel reinforcement contained in the concrete is connected to the ground line.
- the composite electrode which has a sensor output and a control input, is connected to sensor electronics via a sensor line for recording measured values and to control electronics via a control line for power regulation, and is connected to a direct current bus.
- Two electronic modules are connected to a control computer via network electronics and an Ethernet network.
- the method according to the invention illustrated in FIG. 3 consists of the following steps: after completion of the necessary preparations, which include an assessment of the state of the building, for example with regard to the spacing of the reinforcement elements, the division of the concrete surface into individual grid areas, the assembly of the composite electrodes and sufficient moistening of the concrete , control measurements are carried out to check the electrical contacts, determine the rest potential and the change in current as a result of the external voltage ( ⁇ ) AK ), that is to say the extraction current.
- the current change ⁇ I AK is a function of the clamping voltage between the anode and cathode (E AK ) and the time. If these values meet the specifications, the further process steps can be carried out, otherwise the values have to be adjusted again.
- the control computer continuously checks whether the reference potential at the cathode (E ref ) is greater than the cathodic reference potential (E ref min ) defined as the threshold value (for example -1070 mV vs. Cu / CuSO 4 ). If this is the case, the correction value of the switch-on time ( An . Orr ) is set greater than the defined switch-on time (t An ) of the external voltage so that the direct current supply can be continued.
- E ref m ⁇ n If E ref m ⁇ n is reached or undershot, it can be switched off and it is checked whether the off clamping voltage between anode and cathode (E AK Aus ) is less than the minimum specified clamping voltage without extreme voltage (E AK m ⁇ n ). If this is the case before T off , the correction value of the switch-off time (t Aus corr ) is set smaller than the switch-off time (t Aus ) of the external voltage, so that the direct current supply can be continued.
- E AK Aus is greater than E AK and the reference potential at the cathode (E ref ) is equal to the minimum specified cathodic reference potential (E ref min ), then it is then checked whether a voltage change at the chloride sensor (dE CL ), the so-called “breakdown potential” , which is in the millivolt range, is not equal to 0.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Electrochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Water Supply & Treatment (AREA)
- Prevention Of Electric Corrosion (AREA)
- Working Measures On Existing Buildindgs (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP00965848A EP1216214B1 (de) | 1999-09-15 | 2000-09-14 | Kombinationselektrode für die elektrochemische sanierung von korrosionsgeschädigtem stahlbeton und verfahren zu deren ansteuerung |
AT00965848T ATE238978T1 (de) | 1999-09-15 | 2000-09-14 | Kombinationselektrode für die elektrochemische sanierung von korrosionsgeschädigtem stahlbeton und verfahren zu deren ansteuerung |
AU76449/00A AU7644900A (en) | 1999-09-15 | 2000-09-14 | Combination electrode for the electrochemical restoration of corrosion-damaged reinforced concrete and corresponding method for controlling the same |
JP2001523338A JP2003509587A (ja) | 1999-09-15 | 2000-09-14 | 腐食損傷した鉄筋コンクリート構造の電気化学的な改修のための複合電極及びその制御方法 |
DK00965848T DK1216214T3 (da) | 1999-09-15 | 2000-09-14 | Kombinationselektrode til den elektrokemiske sanering af korrosionsskadet armeret beton og metode til kontrol heraf |
CA002384913A CA2384913C (en) | 1999-09-15 | 2000-09-14 | Combination electrode for the electrochemical restoration of corrosion-damaged reinforced concrete and corresponding method for controlling the same |
DE50002005T DE50002005D1 (de) | 1999-09-15 | 2000-09-14 | Kombinationselektrode für die elektrochemische sanierung von korrosionsgeschädigtem stahlbeton und verfahren zu deren ansteuerung |
NO20021280A NO20021280L (no) | 1999-09-15 | 2002-03-14 | Kombinasjonselektrode for elektrokjemisk sanering av korrosjonsskadet armert betong og fremgangsmåte for styring avsamme |
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19944974.0 | 1999-09-15 | ||
DE19944974A DE19944974C1 (de) | 1999-09-15 | 1999-09-15 | Kombinationselektrode für die elektrochemische Sanierung von korrosionsgeschädigtem Stahlbeton |
DE10001706.1 | 2000-01-18 | ||
DE10001706A DE10001706C2 (de) | 2000-01-18 | 2000-01-18 | Verfahren zur Ansteuerung eines Elektrodensystems für die elektrochemische Sanierung von korrosionsgeschädigtem Stahlbeton |
US10/098,267 US6881306B2 (en) | 1999-09-15 | 2002-03-15 | Combination electrode for electrochemical restoration of corrosion-damaged reinforced concrete and method of controlling same |
Publications (1)
Publication Number | Publication Date |
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WO2001019755A1 true WO2001019755A1 (de) | 2001-03-22 |
Family
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Family Applications (1)
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PCT/DE2000/003192 WO2001019755A1 (de) | 1999-09-15 | 2000-09-14 | Kombinationselektrode für die elektrochemische sanierung von korrosionsgeschädigtem stahlbeton und verfahren zu deren ansteuerung |
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Country | Link |
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US (1) | US6881306B2 (de) |
JP (1) | JP2003509587A (de) |
AU (1) | AU7644900A (de) |
CA (1) | CA2384913C (de) |
DE (1) | DE50002005D1 (de) |
WO (1) | WO2001019755A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3088376A1 (de) * | 2015-04-30 | 2016-11-02 | CITec Concrete Improvement Technologies GmbH | Anordnung zur durchführung eines verfahrens zum elektrochemischen chloridentzug an einer korrosionsgeschädigten stahlbetonfläche |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006302677A (ja) * | 2005-04-21 | 2006-11-02 | Sankosha Corp | 接地装置及び該接地装置の施工方法 |
EP1777322A1 (de) * | 2005-10-18 | 2007-04-25 | Technische Universiteit Delft | Vorrichtung und Verfahren für kathodischen Korrosionsschutz für eine stahlarmierte Betonstruktur |
EP1942085B1 (de) * | 2007-01-05 | 2011-06-08 | M Lefevre | Vorrichtung zur Sanierung einer Betonstruktur und entsprechendes Verfahren |
GB0715494D0 (en) * | 2007-08-10 | 2007-09-19 | Cell Ltd G | Monitoring system and method |
CN104619884A (zh) * | 2012-04-17 | 2015-05-13 | 索列丹斯-弗莱西奈公司 | 钢筋混凝土结构的电防腐方法 |
CN102627473B (zh) * | 2012-04-27 | 2013-07-24 | 浙江大学宁波理工学院 | 一种两步法修复盐害混凝土结构的装置与方法 |
US9353446B2 (en) | 2013-04-29 | 2016-05-31 | Transistor Devices, Inc. | Systems and methods for impressed current cathodic protection |
CN112981414B (zh) * | 2019-12-17 | 2023-03-14 | 江苏苏博特新材料股份有限公司 | 一种分阶段电化学修复盐侵蚀钢筋混凝土的系统及方法 |
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WO1990010767A1 (en) * | 1989-03-10 | 1990-09-20 | Elcraft A/S | Method and apparatus for controlling the relative humidity in concrete and masonry structures |
EP0398117A2 (de) | 1989-05-16 | 1990-11-22 | Oystein Vennesland | Verfahren zum Sanieren von innen bewehrtem Beton durch Chloridentfernung |
US5228959A (en) | 1987-09-25 | 1993-07-20 | Miller John B | Process for rehabilitating internally reinforced concrete by removal of chlorides |
DE4229072A1 (de) | 1992-09-01 | 1994-03-03 | Zueblin Ag | Verfahren zum regulierten elektrochemischen Chloridentzug |
WO1994004474A1 (en) * | 1992-08-26 | 1994-03-03 | John Philip Broomfield | Electrochemical stabilisation of mineral masses such as concrete, and electrode arrangements therefor |
Family Cites Families (6)
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JPS63163266A (ja) * | 1986-12-26 | 1988-07-06 | Nippon Steel Corp | コンクリート中鋼材の腐食検出プローブ |
CA2040610A1 (en) * | 1990-05-21 | 1991-11-22 | John E. Bennett | Apparatus for the removal of chloride from reinforced concrete structures |
GB9714047D0 (en) * | 1997-07-03 | 1997-09-10 | Fosroc International Ltd | A process for the electrochemical treatment of concrete |
US5968339A (en) * | 1997-08-28 | 1999-10-19 | Clear; Kenneth C. | Cathodic protection system for reinforced concrete |
WO2001007683A1 (en) * | 1999-07-22 | 2001-02-01 | Infrastructure Repair Technologies, Inc. | Method of treating corrosion in reinforced concrete structures by providing a uniform surface potential |
US6358397B1 (en) * | 2000-09-19 | 2002-03-19 | Cor/Sci, Llc. | Doubly-protected reinforcing members in concrete |
-
2000
- 2000-09-14 JP JP2001523338A patent/JP2003509587A/ja active Pending
- 2000-09-14 AU AU76449/00A patent/AU7644900A/en not_active Abandoned
- 2000-09-14 WO PCT/DE2000/003192 patent/WO2001019755A1/de active IP Right Grant
- 2000-09-14 DE DE50002005T patent/DE50002005D1/de not_active Expired - Lifetime
- 2000-09-14 CA CA002384913A patent/CA2384913C/en not_active Expired - Fee Related
-
2002
- 2002-03-15 US US10/098,267 patent/US6881306B2/en not_active Expired - Fee Related
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US5228959A (en) | 1987-09-25 | 1993-07-20 | Miller John B | Process for rehabilitating internally reinforced concrete by removal of chlorides |
WO1990010767A1 (en) * | 1989-03-10 | 1990-09-20 | Elcraft A/S | Method and apparatus for controlling the relative humidity in concrete and masonry structures |
EP0398117A2 (de) | 1989-05-16 | 1990-11-22 | Oystein Vennesland | Verfahren zum Sanieren von innen bewehrtem Beton durch Chloridentfernung |
WO1994004474A1 (en) * | 1992-08-26 | 1994-03-03 | John Philip Broomfield | Electrochemical stabilisation of mineral masses such as concrete, and electrode arrangements therefor |
DE4229072A1 (de) | 1992-09-01 | 1994-03-03 | Zueblin Ag | Verfahren zum regulierten elektrochemischen Chloridentzug |
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J.E. SLATER, MATERIALS PERFORMANCE, 1976, pages 21 - 26 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3088376A1 (de) * | 2015-04-30 | 2016-11-02 | CITec Concrete Improvement Technologies GmbH | Anordnung zur durchführung eines verfahrens zum elektrochemischen chloridentzug an einer korrosionsgeschädigten stahlbetonfläche |
Also Published As
Publication number | Publication date |
---|---|
JP2003509587A (ja) | 2003-03-11 |
CA2384913A1 (en) | 2001-03-22 |
US6881306B2 (en) | 2005-04-19 |
US20030173231A1 (en) | 2003-09-18 |
DE50002005D1 (de) | 2003-06-05 |
CA2384913C (en) | 2009-12-29 |
AU7644900A (en) | 2001-04-17 |
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