EP0265451A1 - Electrostatic separation device. - Google Patents
Electrostatic separation device.Info
- Publication number
- EP0265451A1 EP0265451A1 EP87902057A EP87902057A EP0265451A1 EP 0265451 A1 EP0265451 A1 EP 0265451A1 EP 87902057 A EP87902057 A EP 87902057A EP 87902057 A EP87902057 A EP 87902057A EP 0265451 A1 EP0265451 A1 EP 0265451A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- filter cartridge
- electrostatic filter
- separating device
- electrodes
- electrostatic
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/04—Plant or installations having external electricity supply dry type
- B03C3/14—Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
- B03C3/155—Filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/60—Use of special materials other than liquids
- B03C3/64—Use of special materials other than liquids synthetic resins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/74—Cleaning the electrodes
- B03C3/78—Cleaning the electrodes by washing
Definitions
- the prior art includes two-stage electrostatic precipitators. They have been known for around 45 years and were developed for the purpose of achieving high degrees of separation for solid particles, aerosols or under iconic drops from the gas stream.
- the solid particles are charged by ions of one polarity with the aid of a so-called ionizer stage.
- the ionizer consists of electrodes, also called spray electrodes, in the form of wires or tips on which the electrical field lines are concentrated. These electrodes are arranged between the counter electrodes, consisting of parallel plates. A plasma layer forms around the spray electrodes. The ions of the plasma layer with the same polarity as the spray electrodes migrate to the counter electrodes. The solid particles that flow through this ion rain are electrically charged because the ions are fixed on their surface.
- the solid particles are pulled out of the gas flow and fixed on the plates of a collector.
- the collector consists of separating plates which are at different potentials under high voltage and between which an electric field is generated.
- the electrically charged solid particles are eliminated from the gas flow thanks to the electrostatic forces which act on the charged solid particles in the electrical field of the collector and are deposited on the collector plates.
- the object of the present invention is to improve the current state of the art and is intended to manufacture electrostatic filters for the filtration of solid particles or droplets from gas or air with a higher degree of separation, in particular for submicron particles, ie in the range of 0.01 / um to l, um particle sizes.
- An advantage is that such an electrostatic filter is, for example, much cheaper to manufacture, about 10-20 times cheaper than a classic two-stage electrostatic precipitator for the same amount of gas flow to be filtered.
- the embodiment of the present invention allows the distances between collector electrodes to be reduced to the smallest distances, on the order of approximately 1 mm. In this way the highest degrees of separation are achieved.
- the realization of such small distances between the electrodes and the collector plates is impossible with the previously existing electrostatic filters with metal plates.
- the described electrostatic filter can be operated with only a single high voltage supply.
- the electrostatic filter described in the invention has a minimal weight. It can be about 20 times lighter than a classic electrostatic filter because conductive foils with a low weight and a small thickness, for example 0.03 mm, are used as electrodes.
- the separating device according to the invention can be inserted into any tubular system, whether or not already on site.
- the pluses and minusions generated by the electrodes at the outlet of the gas flow from the electrostatic filter cartridge neutralize the electrical charge in the room air.
- the degree of separation of the filter can be increased in a very simple manner.
- This measure i.e. Extension of the cylindrical filter cartridge, separation levels from the area of HEPA filters with 99.99% separation rate for the smallest particles are achieved.
- An increase in the degree of separation can also be produced by increasing the diameter of the spiral or cylindrical electrostatic filter cartridge and by increasing the high voltage.
- the electrostatic filter cartridge because it is inexpensive to manufacture, like any mechanical filter made of porous or fibrous medium when loaded with dust, can be fitted with a new cartridge and replaced like any other mechanical filter. In this way, the filter cartridge can be replaced as "hazardous waste" when the filtered aerosol is dangerous or toxic to the environment. As a result, the current existing situation can be eliminated, in which electrostatic precipitators are cleaned and the toxic dust that is washed out of the electrostatic precipitator gets into the waste water.
- this new type of electrostatic precipitator can be used wherever radioactive particles have to be filtered.
- this new electrostatic filter is an ideal air filter for the nuclear industry, where radioactive particles or aerosols have to be filtered.
- a further advantage of this invention is that the price of the separating device can be reduced even further by using insulating foils which have a conductive layer on one of their sides, or by the foils having special electrical polarization properties or magnetic properties exhibit.
- a further increase in the degree of separation can also be achieved if a centrifugal movement is impressed on the gas flow before it enters the collector, so that the adhesion of the particles to the foils is favored.
- FIG. 1 shows an electrostatic separating device with a UV light source 2, with a grid electrode 4 and an electrostatic filter cartridge 6, consisting of spiral-shaped insulating foils 8 and foil electrodes 7, applied to a high-voltage source 9, and which in a tubular housing 1 is mounted.
- FIG. 2 shows a sectional view of a spiral-shaped electrostatic filter cartridge 6 in the housing 1.
- FIG. 3 shows a zigzag-shaped insulating film 8 between the film electrodes 7 and the housing 1.
- FIG. 4 shows a smooth insulating film 8 with zigzag-shaped film electrodes 7, installed in the housing 1.
- the insulating foils 8 have a zigzag shape and the foil electrodes 7 have been placed one on top of the other, whereby one rectangular electrostatic filter cartridge 6 is formed.
- FIG. 6 shows a possibility of the invention, in which the insulating foils 8 are laid flat and the foil electrodes 7 are placed on top of one another in a zigzag shape, whereby a rectangular electrostatic filter cartridge 6 is created.
- FIG. 7 shows a further possibility of folding the insulating film 8 between the film electrodes 7 and the housing 1.
- FIG. 8 shows a reversal of FIG. 7, the insulating foils 8 being smooth and the foil electrodes 7 being folded.
- FIG. 10 shows an embodiment of an electrostatic precipitator, in which the insulating foils 8 and the foil electrodes 7 arranged in a cylindrical, coaxial manner form an electrostatic filter cartridge 6 which has been installed in a housing 1.
- FIG. 11 shows an embodiment of the invention in which the electrostatic filter cartridge 6 can be cleaned by an automatic washing device with an ultrasound generator 16, by means of a filler tube 11, a cleaning liquid 10 flows in, which can flow out of the drain valve 12 after use.
- FIG. 12 shows an embodiment of the invention in which the gas flow in the core area and in the edge area of the electrostatic filter cartridge 6 is passed through a gas flow guide 13.
- FIG. 13 shows an embodiment of the invention in which a liquid 15 is sprayed onto the electrostatic filter cartridge 6 by means of a nozzle 14, whereby a wet separator is created.
- the electrostatic filter cartridge 6 is formed from two spiral-shaped insulating foils 18, 19, each of which has a conductive layer on one of its sides.
- FIG. 15 shows an embodiment of the invention in which the ionization stage is separated from the collector stage and a spiral-shaped spray electrode 20 discharges corona in the direction of one or two grid electrodes 4.
- a gas stream to be cleaned flows through a housing 1 in the direction of the arrow and is irradiated by the UV rays 3 of a UV source 2. After that, he is through a grid electrode 4 is conducted and ionized in the ionizer zone 5 by an ion rain. Positive or negative ions are generated in the ionizer zone 5. They arise from a corona discharge from the spiral edge, which is located under high voltage potential 9.
- the particles in the gas stream flow into a third zone, the so-called electrostatic filter cartridge 6.
- insulating foils 8 extend beyond the foil electrodes 7 in their length, producing the so-called insulation spacing.
- the particles in the gas stream which are electrically charged after the ionization stage are pulled out of the gas stream thanks to the electrostatic forces in the space between the film electrodes 7 and deposited on the surface of the grounded film electrode and also on the surface of the strongly polarized insulating films 8 .
- a so-called fourth stage is formed by a neutralizer 17.
- the neutralizer zone 17 is on the gas outlet side of the electrostatic filter cartridge 6 formed.
- the fourth stage is formed by the edges of the spiral foil electrodes 7, which generate a corona discharge between them by concentrating the field lines. As a result, ions of both polarities are generated, which in this way bring about an electrical neutralization of both the gas flow and the objects possibly located in the space into which the gas flow flows.
- insulating foils 8 protrude from the foil electrodes 7 and that a necessary insulating distance is achieved. 1 that a spiral-shaped insulating film 8 is inserted between the grounded housing 1 and the film electrode 7 connected to the high-voltage potential 9, which isolates the electrostatic filter cartridge 6 from the housing 1.
- the particles can also be charged on the gas inlet side in that the corona discharge does not take place between the edge of a foil electrode and the grid electrode, but between the edges of two foil electrodes lying at different potential.
- the grid electrode can then be omitted.
- Fig. 2 the spiral design of the electrostatic precipitator is shown.
- the sectional view shows the top view of the electrostatic filter cartridge 6. It can clearly be seen that the ends of the insulating film 8 protrude beyond the ends of the film electrodes 7, so that there is a safe insulation distance. It can also be seen that an insulating film 8 is inserted between the housing 1 and the film electrode 7, which has been applied to a positive high-voltage potential 9.
- Fig. 3 the layered structure of an electrostatic filter cartridge 6 is shown in a sectional view.
- the zigzag films are insulating films 8.
- the film electrodes 7 are smooth films. It can also be clearly seen here that an insulating film 8 is inserted between the outer film electrode 7 and the housing 1.
- FIG. 4 shows the sectional structure of an electrostatic filter cartridge 6 in a sectional view, in which case the foil electrodes 7 are folded in a zigzag shape and the insulating foils 8 are smooth foils.
- an insulating film 8 is inserted between the housing 1 and the outer film electrode 7.
- FIG. 8 A further possibility of the invention is shown in FIG. In this case, zig-zag insulating foils 8 are placed on top of one another in layers with flat foil electrodes 7. In this way, rectangular electrostatic filter cartridges 6 can also be produced.
- FIG. 6 shows a possibility corresponding to that already described in FIG. 5.
- zigzag-shaped foil electrodes 7 are inserted between flat insulating foils 8, so that, for example, rectangular electrostatic filter cartridges 6 are created. 13
- FIG. 7 A further embodiment of the folded insulating films 8 is shown in FIG. 7.
- the film was folded round and, as already described in FIG. 3, wrapped between the film electrodes 7.
- FIG. 8 similar to FIG. 4, a film electrode, which is folded round, is processed into an electrostatic filter cartridge 6.
- the foil electrodes 7 and the insulating foils 8 represent cylindrical bodies which, when placed coaxially one inside the other, form an electrostatic filter cartridge 6. In this case too, an insulating film 8 is inserted between the outer film electrode 7 and the housing 1.
- the U-shaped housing 1 can be 14
- the filtered material can sink down, collect in the lower part of the U-shaped housing 1 and be drained from there, so that the filtered liquid aerosols can be recovered.
- FIG. 12 shows an embodiment in which the gas stream flowing into the housing is passed through gas flow guides 13 which are arranged directly in front of the electrostatic filter cartridge 6. This makes it possible to direct the gas flow in such a way that it cannot flow through the intermediate space between the housing 1 and the electrostatic filter cartridge 6. The same also applies to the core area of the electrostatic filter cartridge 6.
- the gas flow guides 13 15 are arranged directly in front of the electrostatic filter cartridge 6.
- the core area and the edge area are zones with a lower degree of separation.
- FIG. 13 shows an electrostatic filter device in which a liquid 15 is sprayed onto the electrostatic filter cartridge 6 by means of a nozzle 14. This creates a wet electrostatic precipitator with a high degree of separation.
- the electrostatic cartridge 6 is formed only from two foils, one of which is smooth and the other is zigzag-shaped. Each of these foils is conductive on one side, so that when it is wound up, the two conductive layers, which are at different potential, are separated throughout the cartridge by an insulating layer.
- FIG. 15 An embodiment is shown in FIG. 15 in which the ionizer is separated from the collector.
- the ionizer is formed from a spiral spray electrode 20, which can be the edge of a foil, a fine metal wire or a plurality of tips, which discharges the corona with respect to one or two grid electrodes 4 and thereby forms one or two ionization zones 5.
- This ionizer is designed such that it can be supplied with current of one polarity, thereby generating ions of this polarity, or with alternating current, thereby generating ions of both polarities.
Landscapes
- Electrostatic Separation (AREA)
Abstract
Dispositif de séparation électrostatique à deux niveaux se présentant sous la forme d'une cartouche filtrante électrostatique (6) incorporant un agent de neutralisation et pouvant être logée dans un boîtier (1) tubulaire ou rectangulaire. Le dispositif est formé d'électrodes en forme de lamelles (7) auxquelles on applique des potentiels différents et qui sont séparées par des films isolants (8). L'ionisation des particules à séparer s'effectue via une source d'UV et/ou dans l'espace entre une électrode de grille (4) mise à la terre et le bord de l'électrode en lamelles (7), à laquelle on applique une forte tension, une densité ionique élevée étant créée dans ledit espace. Les particules ionisées sont séparées dans la cartouche filtrante (6) électrostatique formant le collecteur. Au niveau de la sortie du gaz de la cartouche filtrante (6) électrostatique, une décharge par effet de couronne présentant les deux polarités ioniques se produit entre les électrodes mises à la terre et les électrodes en lamelles (7) qui sont soumises à une tension élevée (9), ce qui permet d'assurer le fonctionnement d'une zone de neutralisation (17) pour le courant de gaz filtré.Two-level electrostatic separation device in the form of an electrostatic filter cartridge (6) incorporating a neutralizing agent and which can be housed in a tubular or rectangular housing (1). The device consists of lamellar electrodes (7) to which different potentials are applied and which are separated by insulating films (8). The ionization of the particles to be separated is carried out via a UV source and / or in the space between a grounded gate electrode (4) and the edge of the strip electrode (7), to which a high voltage is applied, a high ion density being created in said space. The ionized particles are separated in the electrostatic filter cartridge (6) forming the collector. At the gas outlet of the electrostatic filter cartridge (6), a corona discharge with two ionic polarities occurs between the grounded electrodes and the strip electrodes (7) which are subjected to a voltage high (9), which ensures the operation of a neutralization zone (17) for the filtered gas stream.
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19863611019 DE3611019A1 (en) | 1986-03-27 | 1986-03-27 | ELECTROSTATIC SEPARATOR |
DE3611019 | 1986-03-27 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0265451A1 true EP0265451A1 (en) | 1988-05-04 |
EP0265451B1 EP0265451B1 (en) | 1990-05-23 |
Family
ID=6297744
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP87902057A Expired - Lifetime EP0265451B1 (en) | 1986-03-27 | 1987-03-26 | Electrostatic separation device |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0265451B1 (en) |
DE (2) | DE3611019A1 (en) |
WO (1) | WO1987005830A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5837035A (en) * | 1994-01-10 | 1998-11-17 | Maxs Ag | Method and apparatus for electrostatically precipitating impurities, such as suspended matter or the like, from a gas flow |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3744167A1 (en) * | 1987-12-24 | 1989-07-06 | Krupp Gmbh | Magnetic separator |
JPH0796216A (en) * | 1993-09-28 | 1995-04-11 | Kuriintetsuku Kogyo:Kk | Cylindrical electrostatic oil cleaner |
US6187271B1 (en) * | 1997-08-21 | 2001-02-13 | Lg Electronics, Inc. | Electrostatic precipitator |
DE102009042113A1 (en) * | 2009-09-18 | 2011-04-21 | Kma Umwelttechnik Gmbh | Electrostatic precipitators and methods for separating particles from gases |
ES2714366T3 (en) | 2015-12-21 | 2019-05-28 | Fydec Holding Sa | Dosing device for minimum quantities, in particular for pharmaceutical applications, as well as the dosing process for minimum amounts of powder |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1440887A (en) * | 1916-10-11 | 1923-01-02 | Arthur F Nesbit | Art of electrical precipitation |
DE577049C (en) * | 1931-05-23 | 1933-05-30 | Metallgesellschaft Akt Ges | Process for the electrical separation of floating bodies from gases or gas mixtures |
FR1302701A (en) * | 1961-10-02 | 1962-08-31 | Engelhard Hanovia Inc | Electrostatic precipitator |
DE1557120A1 (en) * | 1966-12-02 | 1970-06-25 | Hilarius Link | Filler electric deduster |
SE7707503L (en) * | 1976-10-12 | 1978-04-13 | American Air Filter Co | ELECTROSTATIC GAS FILTER |
DE3587609T2 (en) * | 1985-05-30 | 1994-05-11 | Ishimori & Co | Electrostatic dust collector. |
-
1986
- 1986-03-27 DE DE19863611019 patent/DE3611019A1/en not_active Withdrawn
-
1987
- 1987-03-26 WO PCT/DE1987/000133 patent/WO1987005830A1/en active IP Right Grant
- 1987-03-26 DE DE8787902057T patent/DE3762810D1/en not_active Expired - Lifetime
- 1987-03-26 EP EP87902057A patent/EP0265451B1/en not_active Expired - Lifetime
Non-Patent Citations (1)
Title |
---|
See references of WO8705830A1 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5837035A (en) * | 1994-01-10 | 1998-11-17 | Maxs Ag | Method and apparatus for electrostatically precipitating impurities, such as suspended matter or the like, from a gas flow |
Also Published As
Publication number | Publication date |
---|---|
DE3762810D1 (en) | 1990-06-28 |
WO1987005830A1 (en) | 1987-10-08 |
DE3611019A1 (en) | 1987-10-01 |
EP0265451B1 (en) | 1990-05-23 |
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