EP0427840B1 - Vorrichtung zur elektrokinetischen entsalzung von mauerwerken - Google Patents
Vorrichtung zur elektrokinetischen entsalzung von mauerwerken Download PDFInfo
- Publication number
- EP0427840B1 EP0427840B1 EP90908410A EP90908410A EP0427840B1 EP 0427840 B1 EP0427840 B1 EP 0427840B1 EP 90908410 A EP90908410 A EP 90908410A EP 90908410 A EP90908410 A EP 90908410A EP 0427840 B1 EP0427840 B1 EP 0427840B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- buffer material
- separator layer
- layer
- electrode
- buffer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 28
- 150000002500 ions Chemical class 0.000 claims abstract description 15
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 16
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 14
- 239000004033 plastic Substances 0.000 claims description 13
- 229920003023 plastic Polymers 0.000 claims description 13
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 8
- 239000000292 calcium oxide Substances 0.000 claims description 8
- 239000012528 membrane Substances 0.000 claims description 8
- 239000001913 cellulose Substances 0.000 claims description 5
- 229920002678 cellulose Polymers 0.000 claims description 5
- 239000003349 gelling agent Substances 0.000 claims description 5
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 4
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 4
- 229920000298 Cellophane Polymers 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims description 3
- 239000004743 Polypropylene Substances 0.000 claims description 3
- 239000010425 asbestos Substances 0.000 claims description 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 3
- 239000000920 calcium hydroxide Substances 0.000 claims description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 3
- 239000011888 foil Substances 0.000 claims description 3
- 239000003365 glass fiber Substances 0.000 claims description 3
- 239000004800 polyvinyl chloride Substances 0.000 claims description 3
- 239000004627 regenerated cellulose Substances 0.000 claims description 3
- 229910052895 riebeckite Inorganic materials 0.000 claims description 3
- 238000004804 winding Methods 0.000 claims description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims 2
- 238000010276 construction Methods 0.000 claims 1
- 150000003839 salts Chemical class 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 8
- 239000002184 metal Substances 0.000 description 8
- 239000007795 chemical reaction product Substances 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 235000010216 calcium carbonate Nutrition 0.000 description 6
- 235000012255 calcium oxide Nutrition 0.000 description 6
- 239000004020 conductor Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 150000001450 anions Chemical class 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 238000005370 electroosmosis Methods 0.000 description 3
- 230000003100 immobilizing effect Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000013508 migration Methods 0.000 description 3
- 230000005012 migration Effects 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 230000032258 transport Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 239000004566 building material Substances 0.000 description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 description 2
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 2
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 2
- 239000004567 concrete Substances 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 230000037427 ion transport Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- -1 sheets Substances 0.000 description 2
- 229920001817 Agar Polymers 0.000 description 1
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- 241000206672 Gelidium Species 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 235000010419 agar Nutrition 0.000 description 1
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000002800 charge carrier Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000003841 chloride salts Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000002999 depolarising effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000012982 microporous membrane Substances 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04B—GENERAL BUILDING CONSTRUCTIONS; WALLS, e.g. PARTITIONS; ROOFS; FLOORS; CEILINGS; INSULATION OR OTHER PROTECTION OF BUILDINGS
- E04B1/00—Constructions in general; Structures which are not restricted either to walls, e.g. partitions, or floors or ceilings or roofs
- E04B1/62—Insulation or other protection; Elements or use of specified material therefor
- E04B1/70—Drying or keeping dry, e.g. by air vents
- E04B1/7007—Drying or keeping dry, e.g. by air vents by using electricity, e.g. electro-osmosis
Definitions
- the invention relates to a device and an anode arrangement for the electrokinetic desalination of masonry according to the preambles of claims 1 and 6.
- Wall salts are mostly hygroscopic and therefore absorb water from the air depending on the air humidity. This increase in volume of the salt crystals causes high hydration pressures, which in turn destroy the porous building material.
- Electrophysical drying processes based on the principle of electroosmosis in porous masonry can only work if a sufficient zeta potential can form between the pore wall and the electrolyte. Excessive concentrations of soluble salts hinder the formation of this zeta potential and drainage by electroosmosis becomes impossible. For this reason, the walls must be largely desalinated before using electroosmosis.
- the principle of salt removal from the masonry is based on the use of electrokinetic charge separation.
- Ion transport in masonry is considerably slower, but is still sufficient to desalinate masonry in an acceptable period of time.
- the known methods for electrokinetic desalination of masonry mostly use metal anodes, which are broken down corrosively and whose liquid corrosion products are removed from the masonry by a plastic channel.
- FR-A-2 552 797 discloses a device for such electrokinetic desalination of masonry using a combined electrode consisting of a plastic shell, steel rod, cover plate, outflow opening and burnt lime, which are in predrilled, outwardly inclined holes in the Masonry.
- the shell or the trough is arranged in the hole, the hole is filled with the burnt lime and the electrode rod, which is preferably made of steel, is pushed through the cover plate into the masonry so that it is surrounded by the burnt lime all around.
- the saline solution can drain off through the trough.
- the electrode consists of an iron electrode, on which there is a dimensionally stable layer of a bound mixture of calcium hydroxide and calcium carbonate, a plastic channel for the removal of the salt solutions formed being connected directly to the electrode via a sleeve.
- US-A-3 856 646 describes an arrangement for the electroosmotic dewatering of damp structures, the positive electrode being designed as a cylinder with a conductive electrode embedded in a depolarizing material.
- FR-A-2 346 511 (3) discloses an arrangement for drying and keeping buildings water-free, consisting of electrical metal conductors, optionally insulated from the masonry, in the form of thin foils, sheets, metal wire nets, grids or bars.
- the object of the invention is to provide a device for the electrokinetic desalination of masonry, the operation of which eliminates the disadvantages inherent in the known desalination processes.
- the handling and installation of such a device should be simple and inexpensive, and in particular, prefabricated electrodes or electrode arrangements should also be able to be used in a manner known per se.
- the separator layer consists of a microporous and possibly ion-selective membrane.
- the main advantage of this design is that the arrangement of the separator layer creates a barrier against the diffusion of the reaction products back into the masonry.
- the separator layer should lie against the immobilizing buffer material layer at least wherever the masonry is directly adjacent, so that the migration of the ions to the electrode also takes place exclusively via the separator layer.
- the electrode is optimally protected from excessive corrosion by the buffer material layer as far as possible.
- the invention further relates to an anode arrangement with an electrode completely surrounded by a buffer material, apart from the connection ends, for use in such a device for the electrokinetic desalination of masonry, wherein there is a separator layer on the buffer material layer, and the anode arrangement is characterized in that the separator layer consists of a microporous and possibly ion-selective membrane.
- Fig. 1 shows a desalination device with a plurality of anodes 2 laid in boreholes in the wall 1, which are wired together.
- the anodes 2 are each completely surrounded by an ion-immobilizing buffer material layer except for their connection ends; this, in turn, is enclosed by a separator layer which directly adjoins the borehole walls.
- a DC voltage is applied to a cathode, in this case an earth rod 4, via a current source 3.
- a desalination device is shown schematically in FIG. 2, in which flat anodes 5 are arranged on the wall 1.
- the anodes each of which is completely embedded in ion-immobilizing buffer material, are in turn wired together and connected to a current source 3, a direct voltage being applied to an earth rod 4.
- the separator layer lying against the buffer material layer is arranged only on the surface facing the wall.
- FIG. 3 shows a cartridge-shaped anode arrangement 6 which is particularly suitable for laying in drilled holes in the masonry to be desalinated.
- the core of the anode arrangement is formed by a metal, preferably copper, conductor 7, which is coated with conductive plastic 8.
- a layer 9 of a buffer material is arranged around this core, which chemically and physically binds the reaction products.
- the buffer material essentially comprises water, Ca (OH) 2, CaCO3 and / or CaO or mixtures thereof, an addition of a gelling agent being advantageous. This has an immobilizing effect and is moisture-retaining, so that there is no risk of the area around the anode drying out.
- the layer of the buffer material is completely enclosed by a separator layer 10 formed from a microporous membrane, which in the installed state of the anode arrangement adjoins the wall of the borehole in a borehole in the masonry.
- the anode assembly 11 is rod-shaped. This arrangement is particularly suitable for laying in wall slots.
- the electrode 12, which in turn consists of a metal conductor covered with conductive plastic, is enclosed all around except for its two connection ends by the buffer material layer 13, which is covered on the outside by the separator layer 14. This then adjoins the walls of the anode arrangement in a wall slot in the assembled state.
- the electrode 17 which is formed from a metal conductor coated with conductive plastic, is embedded in the buffer material layer 18 in the form of serpentine windings which extend over the entire surface of the anode arrangement.
- the separator layer 19 is arranged on the side of the buffer material layer facing the wall.
- the anodes can be designed as rod, strip or surface electrodes and consist of metal, graphite, conductive plastic or of metal conductors or graphite fiber conductors coated with such an electrode.
- the buffer material essentially comprises Water, Ca (OH) 2, CaCO3 and / or CaO or mixtures thereof, an addition of a gelling agent being advantageous. This has an immobilizing effect and is moisture-retaining, so that there is no risk of the area around the anode drying out.
- all commercially available, but preferably agar-agar or carboxymethyl cellulose can be used as the gelling agent.
- the Coulombsche The efficiency of the anion (wall salt) conversion at the anode was between 40 and 50%, depending on the degree of salinization and the moisture content of the masonry. After a period of 60 days, the 40 grams of CaCO3 had been consumed and the electrodes could be removed from the wall with the reaction products. Analysis showed that over 90% of the reaction products were bound to the electrode.
Landscapes
- Engineering & Computer Science (AREA)
- Architecture (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Water Supply & Treatment (AREA)
- Physics & Mathematics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electromagnetism (AREA)
- Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Prevention Of Electric Corrosion (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Processing Of Solid Wastes (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Filtration Of Liquid (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Treating Waste Gases (AREA)
- Electrolytic Production Of Metals (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Fire-Extinguishing Compositions (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Insulators (AREA)
- Other Surface Treatments For Metallic Materials (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
- Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
- Manufacture Of Alloys Or Alloy Compounds (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Processing Of Stones Or Stones Resemblance Materials (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT1307/89 | 1989-05-30 | ||
AT0130789A AT394409B (de) | 1989-05-30 | 1989-05-30 | Vorrichtung zur elektrokinetischen entsalzung von mauerwerken |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0427840A1 EP0427840A1 (de) | 1991-05-22 |
EP0427840B1 true EP0427840B1 (de) | 1993-08-18 |
Family
ID=3511056
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP90908410A Expired - Lifetime EP0427840B1 (de) | 1989-05-30 | 1990-05-30 | Vorrichtung zur elektrokinetischen entsalzung von mauerwerken |
Country Status (19)
Country | Link |
---|---|
EP (1) | EP0427840B1 (lt) |
AT (2) | AT394409B (lt) |
CA (1) | CA2033167A1 (lt) |
CZ (1) | CZ285180B6 (lt) |
DD (1) | DD294750A5 (lt) |
DE (1) | DE59002386D1 (lt) |
DK (1) | DK0427840T3 (lt) |
ES (1) | ES2044595T3 (lt) |
HR (1) | HRP921231B1 (lt) |
HU (1) | HU209897B (lt) |
LT (1) | LT3290B (lt) |
LV (1) | LV5314A3 (lt) |
PL (1) | PL163847B1 (lt) |
RU (1) | RU1834960C (lt) |
SI (1) | SI9011062A (lt) |
SK (1) | SK280162B6 (lt) |
UA (1) | UA13472A (lt) |
WO (1) | WO1990015203A1 (lt) |
YU (1) | YU106290A (lt) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9208921D0 (en) * | 1992-04-24 | 1992-06-10 | Isis Innovation | Electrochemical treatment of surfaces |
EP0612365B1 (fr) * | 1992-06-15 | 2001-02-28 | ORTLIEB, Mathieu | Procede et dispositif pour eliminer l'humidite des murs d'une construction |
DE4235583A1 (de) * | 1992-10-22 | 1994-05-05 | Tridelta Ag | Anode für die elektroosmotische Sanierung von Bauwerken und Verfahren zum Betrieb solcher Anoden |
US5451677A (en) * | 1993-02-09 | 1995-09-19 | Merck & Co., Inc. | Substituted phenyl sulfonamides as selective β 3 agonists for the treatment of diabetes and obesity |
DE10202764A1 (de) * | 2002-01-25 | 2003-08-07 | Fischer Christel | Verfahren und Anordnung zum Entfeuchten eines Mauerwerks |
FR2846571B1 (fr) * | 2002-11-06 | 2006-05-26 | Francois Chasteau | Procede d'assechement par electro-osmose d'un milieu poreux et electrodes pour sa mise en oeuvre |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3856646A (en) * | 1967-09-19 | 1974-12-24 | D Morarau | Methods and electrodes for the drying of damp buildings |
NL7603539A (nl) * | 1976-04-03 | 1977-10-04 | Halle Hoch & Montagebau Veb | Werkwijze voor het van vocht bevrijden en droog houden van bouwkundige constructies. |
DD231236A3 (de) * | 1983-10-04 | 1985-12-24 | Bauakademie Ddr | Vorrichtung zur trocknung von naessegeschaedigtem mauerwerk |
DD234997A3 (de) * | 1983-10-04 | 1986-04-23 | Adw Ddr | Elektrodenanordnung zur elektrochemischen entsalzung undtrocknung von mauerwerk |
-
1989
- 1989-05-30 AT AT0130789A patent/AT394409B/de not_active IP Right Cessation
-
1990
- 1990-05-29 CZ CS902643A patent/CZ285180B6/cs not_active IP Right Cessation
- 1990-05-29 SK SK2643-90A patent/SK280162B6/sk unknown
- 1990-05-30 WO PCT/AT1990/000051 patent/WO1990015203A1/de active IP Right Grant
- 1990-05-30 YU YU106290A patent/YU106290A/sh unknown
- 1990-05-30 UA UA4894405A patent/UA13472A/uk unknown
- 1990-05-30 EP EP90908410A patent/EP0427840B1/de not_active Expired - Lifetime
- 1990-05-30 DD DD90341133A patent/DD294750A5/de not_active IP Right Cessation
- 1990-05-30 PL PL90285402A patent/PL163847B1/pl unknown
- 1990-05-30 DE DE9090908410T patent/DE59002386D1/de not_active Expired - Fee Related
- 1990-05-30 ES ES90908410T patent/ES2044595T3/es not_active Expired - Lifetime
- 1990-05-30 HU HU905208A patent/HU209897B/hu not_active IP Right Cessation
- 1990-05-30 SI SI9011062A patent/SI9011062A/sl unknown
- 1990-05-30 CA CA002033167A patent/CA2033167A1/en not_active Abandoned
- 1990-05-30 AT AT90908410T patent/ATE93291T1/de not_active IP Right Cessation
- 1990-05-30 DK DK90908410.5T patent/DK0427840T3/da active
-
1991
- 1991-01-29 RU SU914894405A patent/RU1834960C/ru active
-
1992
- 1992-11-11 HR HRP-1062/90A patent/HRP921231B1/xx not_active IP Right Cessation
-
1993
- 1993-04-08 LV LV930235A patent/LV5314A3/xx unknown
- 1993-05-06 LT LTIP513A patent/LT3290B/lt not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
UA13472A (uk) | 1997-02-28 |
EP0427840A1 (de) | 1991-05-22 |
DK0427840T3 (da) | 1993-10-11 |
DE59002386D1 (de) | 1993-09-23 |
ATA130789A (de) | 1991-09-15 |
CZ285180B6 (cs) | 1999-06-16 |
ATE93291T1 (de) | 1993-09-15 |
PL163847B1 (pl) | 1994-05-31 |
DD294750A5 (de) | 1991-10-10 |
CZ264390A3 (cs) | 1999-01-13 |
RU1834960C (ru) | 1993-08-15 |
WO1990015203A1 (de) | 1990-12-13 |
SK280162B6 (sk) | 1999-09-10 |
CA2033167A1 (en) | 1990-12-01 |
LV5314A3 (lv) | 1993-10-10 |
HRP921231B1 (en) | 1999-04-30 |
HRP921231A2 (en) | 1995-08-31 |
ES2044595T3 (es) | 1994-01-01 |
SI9011062A (en) | 1997-08-31 |
HU905208D0 (en) | 1992-08-28 |
HU209897B (en) | 1994-11-28 |
SK264390A3 (en) | 1994-04-06 |
LT3290B (en) | 1995-06-26 |
LTIP513A (en) | 1994-11-25 |
HUT62357A (en) | 1993-04-28 |
AT394409B (de) | 1992-03-25 |
YU106290A (sh) | 1994-04-05 |
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Legal Events
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---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
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17P | Request for examination filed |
Effective date: 19901227 |
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AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB IT LI LU NL SE |
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