EP1266693A2 - Measures for avoiding of electrical field densities with locally destructive effect on a rotationally symmetric electrode assembly - Google Patents
Measures for avoiding of electrical field densities with locally destructive effect on a rotationally symmetric electrode assembly Download PDFInfo
- Publication number
- EP1266693A2 EP1266693A2 EP02009524A EP02009524A EP1266693A2 EP 1266693 A2 EP1266693 A2 EP 1266693A2 EP 02009524 A EP02009524 A EP 02009524A EP 02009524 A EP02009524 A EP 02009524A EP 1266693 A2 EP1266693 A2 EP 1266693A2
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- European Patent Office
- Prior art keywords
- electrode
- reaction vessel
- process liquid
- measures
- insulator
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/18—Use of auxiliary physical effects, e.g. ultrasonics, irradiation, for disintegrating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/18—Use of auxiliary physical effects, e.g. ultrasonics, irradiation, for disintegrating
- B02C2019/183—Crushing by discharge of high electrical energy
Definitions
- the invention relates to a measure or measures to avoid of locally destructive electric field densities on a rotationally symmetrical electrode arrangement.
- Such an electrode arrangement is part of a Fragmentation. It consists of one with high voltage actable, rod-shaped electrode, the high-voltage electrode and one always at a fixed electrical potential lying counter electrode. Both have a predetermined distance to each other.
- the rod longitudinal axis of the high voltage electrode lies on the axis of rotation.
- the counter electrode is a component the bottom of a reaction vessel. It is with process fluid is filled and is loaded with process goods that via pulsed and powerful electrical discharge in the Electrode gap to a required grain size range is fractionated.
- the high voltage electrode is with a Insulator leaving a bare end area exposed given length encased. This bare end area is completely immersed in the process liquid.
- the electrode arrangement is connected to an electrical energy store, a Marx generator z. B., connected when reached a predetermined charging voltage over a spark gap is discharged into the two-electrode system.
- a Marx generator z. B. connected when reached a predetermined charging voltage over a spark gap is discharged into the two-electrode system.
- reaction liquid often water but also others suitable liquids, process material in the form of debris, any conglomerate baked tightly together Solid, tilted.
- the discharge is controlled by setting the electrical parameters controlled so that there are high-current discharge channels between form the two electrodes and thereby the same blow up by electrical influence and mechanically over Shatter shock waves.
- the grain size of the fragments can be can be controlled within limits by the number of discharges. At the deepest area of the reaction vessel are the finely smashed Parts removed (see DE 195 34 232).
- Central but highly stressed component of such a fragmentation system is that in the process liquid in the reaction vessel protruding electrode, especially the place where the three media: bare electrode, insulating jacket end and process liquid - This is a ring area - meet each other at the same time.
- the high voltage electrode is from the high voltage connection to the bare tip area taking into account the pulsed operation with tough insulator material immediately encased around the bare electrode surface, that has direct contact with the process liquid to keep small. Loss currents before the ignition of the fragmentation Discharge channel between the electrode tip and the counter electrode in the bottom of the reaction vessel the electrolytic conductivity of the process liquid flow should be prevented, but at least on a tolerable Be limited. So that will be none or at least consumes less energy in the pre-discharge phase. In order to there is more energy in the fragmentation effective per discharge Discharge phase available.
- Discharge channels start from the free electrode surface outgoing, at the joint process liquid insulator electrode and preferably run along the insulator surface especially if there is little fragmentation material in the reaction vessel located, the isolator is due to the high current Discharge destroyed.
- the invention is based, with the electrode their encasing insulator made of tough material in their geometry in the border area insulator-electrode tip process liquid to be designed so that the tangential to the insulator surface directed field strength at the isolator forehead at the transition to Electrode is as small as possible.
- the rotationally symmetrical structure is: insulator electrode shown in sections.
- the arrangement is here only half of the axis of rotation due to the nature of the symmetry, the left edge of the picture.
- insulator, electrode and process liquid here water, all three mutually meet (three-media interface / area), exists, field-related seen the field relief.
- the electrode has where them from the encasing insulator into the process liquid an annular bulge occurs around the circumference, facing outwards has no edges, i.e. with a radius equal to half Bead thickness is rounded.
- the curve can also be used with others Measurements must be carried out, this is only manufacturing technology very easy.
- the density of the equipotential lines is in this three-media impact area low, hence very likely to start from there no discharge channels. They are most likely to form or preferably in areas of high equipotential line density off, i.e. on the area facing the counter electrode the forehead of the bead or just the tip of the electrode, like the arrangement of the line array shows.
- the discharges are in the Start the front area of the bare electrode preferably.
- the frustoconical shape, indicated in Figure 2 here is a grid made of dielectric, tough material like PE or nylon or the like. That is already sufficiently fragmented Well can trickle through in the area. This Depending on the dielectric property, the grating tightens the potential lines in addition to themselves and thus sets the Density of the same further down in the electrode area. The condition, that discharge channels can start there through these measures also very considerably and therefore effectively reduced.
- the comparison shows the effectiveness of the measure the design (Figure 3) according to the prior art with the ( Figure 1 and / or 2) of the invention.
- the density of the equipotential lines is in the conventional design in the three media zone incomparably higher and thus the electrical load the insulator in its forehead zone much larger.
- FIG. 4 shows the meaning of the electrode and their stress in operation are highlighted.
- the whole Fragmentation system is schematic with its essential components outlined.
- the Marx generator is the fragmentation device via the im simplest case in the case of self-breakthrough spark gap connected to the output. It couples to the spark gap Reaction tube protruding immediately.
- the electrode is covered with the insulator.
- the insulator protrudes above the level of the process liquid, here water, out, so that in this area in operation safely Isolation exists, it leaves the end area in the process liquid the electrode is free, since only from there are the discharge channels in series through the fragmentation material and the process liquid should train.
- the design of the counter electrode is process dependent and here e.g. only the bottom of the reaction bucket from which it is electrical goes straight back to the Marx generator.
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- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Disintegrating Or Milling (AREA)
- Ceramic Capacitors (AREA)
Abstract
Description
Die Erfindung betrifft eine Maßnahme oder Maßnahmen zur Vermeidung von lokal zerstörerisch wirkenden elektrischen Felddichten an einer rotationssymmetrischen Elektrodenanordung.The invention relates to a measure or measures to avoid of locally destructive electric field densities on a rotationally symmetrical electrode arrangement.
Eine solche Elektrodenanordnung ist hier Bestandteil einer Fragmentieranlage. Sie besteht aus einer mit Hochspannung beaufschlagbaren, stabförmigen Elektrode, der Hochspannungselektrode und einer stets auf festem elektrischen Potential liegenden Gegenelektrode. Beide haben einen vorgegebenen Abstand zueinander. Die Stablängsachse der Hochspannungselektrode liegt auf der Rotationsachse. Die Gegenelektrode ist Bestandteil des Bodens eines Reaktionsgefäßes. Es ist mit Prozessflüssigkeit gefüllt und wird mit Prozessgut beschickt, das über impulsartige und leistungsstarke elektrische Entladung im Elektrodenzwischenraum auf einen geforderten Körnungsbereich fraktioniert wird. Die Hochspannungselektrode ist mit einem Isolator unter Freilassung eines blankliegenden Endbereichs vorgegebener Länge ummantelt. Dieser blanke Endbereich ist völlig in die Prozessflüssigkeit eingetaucht.Such an electrode arrangement is part of a Fragmentation. It consists of one with high voltage actable, rod-shaped electrode, the high-voltage electrode and one always at a fixed electrical potential lying counter electrode. Both have a predetermined distance to each other. The rod longitudinal axis of the high voltage electrode lies on the axis of rotation. The counter electrode is a component the bottom of a reaction vessel. It is with process fluid is filled and is loaded with process goods that via pulsed and powerful electrical discharge in the Electrode gap to a required grain size range is fractionated. The high voltage electrode is with a Insulator leaving a bare end area exposed given length encased. This bare end area is completely immersed in the process liquid.
Die Elektrodenanordnung ist an einen elektrischen Energiespeicher, einen Marxgenerator z. B., angeschlossen, der bei Erreichen einer vorgegebenen Ladespannung über eine Funkenstrecke in das Zweielektrodensystem entladen wird. In die Prozessoder auch Reaktionsflüssigkeit, häufig Wasser aber auch andere geeignete Flüssigkeiten, wird Prozessgut in Form von Schuttstücken, irgendwelche fest zusammen gebackene konglomerierte Festkörper, gekippt.The electrode arrangement is connected to an electrical energy store, a Marx generator z. B., connected when reached a predetermined charging voltage over a spark gap is discharged into the two-electrode system. In the process or also reaction liquid, often water but also others suitable liquids, process material in the form of debris, any conglomerate baked tightly together Solid, tilted.
Die Entladung wird über die Einstellung der elektrischen Parameter so gesteuert, daß sich stromstarke Entladungskanäle zwischen den beiden Elektroden ausbilden und dadurch dieselben durch elektrische Einwirkung sprengen und mechanisch über Schockwellen zertrümmern. Die Korngröße der Fragmente kann durch die Anzahl Entladungen in Grenzen gesteuert werden. Am tiefsten Bereich des Reaktionsgefäßes werden die fein zertrümmerten Teile entnommen (siehe hierzu DE 195 34 232).The discharge is controlled by setting the electrical parameters controlled so that there are high-current discharge channels between form the two electrodes and thereby the same blow up by electrical influence and mechanically over Shatter shock waves. The grain size of the fragments can be can be controlled within limits by the number of discharges. At the deepest area of the reaction vessel are the finely smashed Parts removed (see DE 195 34 232).
Zentrales aber hoch belastetes Bauteil einer solchen Fragmentieranlage ist die in die Prozeßflüssigkeit im Reaktionsgefäß ragende Elektrode, insbesondere die Stelle, wo die drei Medien: blanke Elektrode, Isoliermantelende und Prozessflüssigkeit - das ist ein Ringbereich - gleichzeitig gegenseitig aufeinandertreffen.Central but highly stressed component of such a fragmentation system is that in the process liquid in the reaction vessel protruding electrode, especially the place where the three media: bare electrode, insulating jacket end and process liquid - This is a ring area - meet each other at the same time.
Die Hochspannungselektrode ist ab dem Hochspannungsanschluß bis zum blankliegenden Spitzenbereich unter Berücksichtigung des impulsartigen Betriebs mit zähem Isolatormaterial unmittelbar ummantelt, um die blankliegende Elektrodenoberfläche, die direkten Kontakt mit der Prozessflüssigkeit hat, gezielt klein zu halten. Verlustströme, die vor dem Zünden des fragmentierwirksamen Entladungskanals zwischen Elektrodenspitze und der Gegenelektrode im Boden des Reaktionsgefäßes aufgrund der elektrolytischen Leitfähigkeit der Prozessflüssigkeit fließen, sollen unterbunden, zumindest aber auf ein tolerables Maß beschränkt werden. Damit wird keine oder zumindest aber weniger Energie in der Vorentladungsphase verbraucht. Damit steht pro Entladung mehr Energie in der fragmentierwirksamen Entladungsphase zur Verfügung.The high voltage electrode is from the high voltage connection to the bare tip area taking into account the pulsed operation with tough insulator material immediately encased around the bare electrode surface, that has direct contact with the process liquid to keep small. Loss currents before the ignition of the fragmentation Discharge channel between the electrode tip and the counter electrode in the bottom of the reaction vessel the electrolytic conductivity of the process liquid flow should be prevented, but at least on a tolerable Be limited. So that will be none or at least consumes less energy in the pre-discharge phase. In order to there is more energy in the fragmentation effective per discharge Discharge phase available.
Wesentlich für die Wirksamkeit der Fragmentieranlage ist, daß der elektrische Durchschlag durch das Fragmentiergut hindurch früher erfolgt als nur durch die Prozeßflüssigkeit, dem Wasser beispielsweise. It is essential for the effectiveness of the fragmentation system that the electrical breakdown through the fragmented material takes place earlier than only through the process liquid, the water for example.
Im praktischen Betrieb hat sich gezeigt, dass die Standzeit des Isolators gemäß der Ausführung nach dem Stand der Technik durch Gleitentladungen entlang seiner Oberfläche zur Prozessflüssigkeit stark begrenzt ist.Practical operation has shown that the service life of the isolator according to the design according to the prior art through sliding discharges along its surface to the process liquid is severely limited.
Entladungskanäle starten, von der freien Elektrodenoberfläche ausgehend, an der Stoßstelle Prozeßflüssigkeit-Isolator-Elektrode und verlaufen bevorzugt entlang der Isolatoroberfläche insbesondere, wenn sich wenig Fragmentiergut im Reaktionsgefäß befindet, dabei wird der Isolator infolge der stromstarken Entladung zerstört.Discharge channels start from the free electrode surface outgoing, at the joint process liquid insulator electrode and preferably run along the insulator surface especially if there is little fragmentation material in the reaction vessel located, the isolator is due to the high current Discharge destroyed.
Der Erfindung liegt die Aufgabe zugrunde, die Elektrode mit ihrem ummantelnden Isolator aus zähem Material in ihrer Geometrie im Grenzgebiet Isolator-Elektrodenspitze-Prozeßflüssigkeit so zu gestalten, daß die tangential zur Isolatoroberfläche gerichtete Feldstärke an der Isolatorstirn am Übergang zur Elektrode möglichst gering ist.The invention is based, with the electrode their encasing insulator made of tough material in their geometry in the border area insulator-electrode tip process liquid to be designed so that the tangential to the insulator surface directed field strength at the isolator forehead at the transition to Electrode is as small as possible.
Die Aufgabe wird durch die im Anspruch 1 beiden aufgeführten
kennzeichnenden Merkmale oder durch eines der beiden Merkmale
alleine gelöst. Im einzelnen ist das:
Die andere oder weitere Maßnahme ist:
Er ist gemäß Anspruch 2 nicht durchlässig ist und hat damit für das gesamte drauffallende Prozessgut Sammelwirkung zur Mitte hin, oder er ist nach Anspruch 3 perforiert und hat entsprechend der Lochweite für das drauffallende Prozessgut Sieboder Separationswirkung, indem, gemessen an der Lochweite, großkörniges Prozessgut zur Mitte durch die kleine Kegelstumpfmantelöffnung und, daran gemessen, kleinkörniges Prozessgut hindurchfällt und absinkt.According to claim 2, it is not permeable and thus has for the entire falling process goods Middle out, or it is perforated according to claim 3 and has accordingly of the hole width for the process material sieve or Separation effect by, measured by the hole width, large-grained process material to the middle through the small truncated cone opening and, measured against this, small-grain process material falls through and sinks.
Die Schonung des problematische Drei-Medien-Gebiets, blanke Elektrode, Isolatorstirn und Prozessflüssigkeit, durch die geeignete Feldsteuerung entlastet dasselbe dadurch, dass es nahezu feldfrei bzw. feldschwach gehalten wird. Dadurch ist dort die Ausbildung eines Entladungskanals oder von Entladungskanälen entlang der Isolatoroberfläche sehr unwahrscheinlich. Zur Folge hat das eine beträchtliche Erhöhung der Lebensdauer der gesamten Hochspannungselektrode oder gleichbedeutend: ihre elektrischen Eigenschaften bleiben langzeitstabil.The protection of the problematic three-media area, bare Electrode, insulator face and process liquid, through the appropriate Field control relieves the same in that it is almost is kept field-free or weak in the field. Because of that is there the formation of a discharge channel or channels very unlikely along the insulator surface. to As a result, the lifespan of the entire high voltage electrode or equivalent: their electrical properties remain stable over the long term.
Die in Anspruch 1 aufgeführten Maßnahmen werden in der Zeichnung
mit den Figuren 1 bis 3 näher erläutert. Es zeigt:
In Figur 1 ist das rotationssymmetrische Gebilde: Isolator-Elektrode ausschnittsweise dargestellt. Die Anordnung ist hier wegen der Art der Symmetrie nur hälftig zur Rotationsachse, dem linken Bildrand, dargestellt. Dort, wo Isolator, Elektrode und Prozeßflüssigkeit, hier Wasser, alle drei sich gegenseitig treffen (Drei-Medien-Stoßstelle/Gebiet), besteht, feldtechnisch gesehen, die Feldentlastung. Die Elektrode hat dort, wo sie aus dem ummantelnden Isolator in die Prozeßflüssigkeit tritt einen ringförmigen Wulst um den Umfang, der nach außen hin keine Kanten aufweist, also mit dem Radius gleich der halben Wulstdicke abgerundet ist. Die Rundung kann auch mit anderen Maßen durchgeführt sein, diese hier ist nur fertigungstechnisch sehr einfach.In Figure 1, the rotationally symmetrical structure is: insulator electrode shown in sections. The arrangement is here only half of the axis of rotation due to the nature of the symmetry, the left edge of the picture. Where insulator, electrode and process liquid, here water, all three mutually meet (three-media interface / area), exists, field-related seen the field relief. The electrode has where them from the encasing insulator into the process liquid an annular bulge occurs around the circumference, facing outwards has no edges, i.e. with a radius equal to half Bead thickness is rounded. The curve can also be used with others Measurements must be carried out, this is only manufacturing technology very easy.
Die Dichte der Äquipotentiallinien ist in diesem Drei-Medien-Stoßgebiet gering, folglich starten von dort aus sehr wahrscheinlich keine Entladungskanäle. Die bilden sich höchstwahrscheinlich bzw. vorzugsweise in Gebieten hoher Äquipotentialliniendichte aus, also an dem zur Gegenelektrode weisenden Gebiet der Stirn des Wulstes oder eben der Elektrodenspitze, wie die Anordnung der Linienschar zeigt. Die Entladungen werden im Stirnbereich der blanken Elektrode bevorzugt starten.The density of the equipotential lines is in this three-media impact area low, hence very likely to start from there no discharge channels. They are most likely to form or preferably in areas of high equipotential line density off, i.e. on the area facing the counter electrode the forehead of the bead or just the tip of the electrode, like the arrangement of the line array shows. The discharges are in the Start the front area of the bare electrode preferably.
Das kegelstumpfmantelförmige, in Figur 2 angedeutete Gebilde ist hier ein Gitter aus dielektrischem, zähem Material wie PE bzw. Nylon oder dergleichen. Das schon hinreichend fragmentierte Gut kann im dortigen Bereich hindurch rieseln. Dieses Gitter zerrt je nach dielektrischer Eigenschaft gewissermaßen die Potentiallinen noch zusätzlich zu sich und setzt damit die Dichte derselben im Elektrodenbereich weiter herab. Die Voraussetzung, daß dort Entladungskanäle starten können, ist durch diese Maßnahmen auch ganz erheblich und damit wirksam abgebaut.The frustoconical shape, indicated in Figure 2 here is a grid made of dielectric, tough material like PE or nylon or the like. That is already sufficiently fragmented Well can trickle through in the area. This Depending on the dielectric property, the grating tightens the potential lines in addition to themselves and thus sets the Density of the same further down in the electrode area. The condition, that discharge channels can start there through these measures also very considerably and therefore effectively reduced.
Die Wirksamkeit der Maßnahme zeigt sich durch den Vergleich der Gestaltung (Figur 3) nach dem Stand der Technik mit dem (Figur 1 und/oder 2) der Erfindung. Die Dichte der Äquipotentiallinien ist in der herkömmlichen Gestaltung in der Drei-Medien-Zone ungleich höher und damit die elektrische Belastung des Isolator in seiner Stirnzone ungleich größer.The comparison shows the effectiveness of the measure the design (Figure 3) according to the prior art with the (Figure 1 and / or 2) of the invention. The density of the equipotential lines is in the conventional design in the three media zone incomparably higher and thus the electrical load the insulator in its forehead zone much larger.
In Figur 4 ist der Übersicht halber die Bedeutung der Elektrode und deren Belastung im Betrieb hervorgehoben. Die gesamte Fragmentieranlage ist schematisch mit ihren wesentlichen Baugruppen skizziert. An den elektrischen Energiespeicher, den Marx-Generator, ist die Fragmentiereinrichtung über die im einfachsten Fall im Selbstdurchbruch arbeitende Funkenstrecke am Ausgang angeschlossen. An die Funkenstrecke koppelt die ins Reaktionsgefäß ragende Elektrode unmittelbar an. Im Bereich des Reaktionsgefäßes ist die Elektrode mit dem Isolator ummantelt. Der Isolator ragt über den Pegel der Prozeßflüssigkeit, hier Wasser, hinaus, so daß in diesem Gebiet im Betrieb sicher Isolation besteht, er läßt in der Prozeßflüssigkeit den Endbereich der Elektrode frei, da nur von dort sich die Entladungskanäle in Reihe durch das Fragmentiergut und die Prozeßflüssigkeit ausbilden sollen.For the sake of clarity, FIG. 4 shows the meaning of the electrode and their stress in operation are highlighted. The whole Fragmentation system is schematic with its essential components outlined. To the electrical energy storage, the Marx generator, is the fragmentation device via the im simplest case in the case of self-breakthrough spark gap connected to the output. It couples to the spark gap Reaction tube protruding immediately. In the area of the reaction vessel, the electrode is covered with the insulator. The insulator protrudes above the level of the process liquid, here water, out, so that in this area in operation safely Isolation exists, it leaves the end area in the process liquid the electrode is free, since only from there are the discharge channels in series through the fragmentation material and the process liquid should train.
Die Gestaltung der Gegenelektrode ist prozeßabhängig und hier z.B. nur der Boden des Reaktionskübels, von dem aus es elektrisch unmittelbar zurück zum Marx-Generator geht.The design of the counter electrode is process dependent and here e.g. only the bottom of the reaction bucket from which it is electrical goes straight back to the Marx generator.
Claims (3)
wobei:
ein zur Elektrodenachse rotationsförmiger dielektrischer Einsatz mit zentralem Durchgang im Elektrodenzwischenraum zur Verdrängung des elektrischen Feldes auf dem Boden des Reaktionsgefäßes mit seiner Öffnung aufliegt. Measures to avoid locally destructive electrical field densities on a rotationally symmetrical electrode arrangement comprising a rod-shaped electrode that can be subjected to high voltage and a counterelectrode that is at a fixed electrical potential and have a predeterminable distance from one another.
in which:
a dielectric insert which is rotationally shaped in relation to the electrode axis and has a central passage in the gap between the electrodes for displacing the electric field rests on the bottom of the reaction vessel with its opening.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10126646A DE10126646C2 (en) | 2001-06-01 | 2001-06-01 | Rotation-symmetrical electrode arrangement made of a rod-shaped electrode that can be subjected to high voltage |
DE10126646 | 2001-06-01 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1266693A2 true EP1266693A2 (en) | 2002-12-18 |
EP1266693A3 EP1266693A3 (en) | 2004-10-20 |
EP1266693B1 EP1266693B1 (en) | 2005-10-05 |
Family
ID=7686836
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP02009524A Expired - Lifetime EP1266693B1 (en) | 2001-06-01 | 2002-04-26 | Apparatus for reducing and crushing comprising a rotationally symmetric electrode assembly |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP1266693B1 (en) |
AT (1) | ATE305820T1 (en) |
DE (2) | DE10126646C2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008017172A1 (en) * | 2006-08-11 | 2008-02-14 | Selfrag Ag | Method for fragmenting material by means of high-voltage discharges |
WO2008113189A1 (en) * | 2007-03-16 | 2008-09-25 | Selfrag Ag | Sample holder and assembly for the electrodynamic fragmentation of samples |
CN112169965A (en) * | 2020-09-22 | 2021-01-05 | 东北大学 | Ore high-voltage pulse discharge pretreatment system and application method thereof |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19534232A1 (en) | 1995-09-15 | 1997-03-20 | Karlsruhe Forschzent | Process for comminuting and crushing solids conglomerated from non-metallic or partially metallic components and for comminuting homogeneous non-metallic solids |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU1719075A1 (en) * | 1990-04-06 | 1992-03-15 | Экспериментальный кооператив "ЭГИДА-А" | Apparatus for electrohydraulically crushing and milling solid materials |
DE19545580C2 (en) * | 1995-12-07 | 2003-02-13 | Rheinmetall W & M Gmbh | Method and arrangement for the disintegration of elastic materials in connection with metallic materials |
DE19736027C2 (en) * | 1997-08-20 | 2000-11-02 | Tzn Forschung & Entwicklung | Method and device for breaking concrete, in particular reinforced concrete slabs |
-
2001
- 2001-06-01 DE DE10126646A patent/DE10126646C2/en not_active Expired - Fee Related
-
2002
- 2002-04-26 EP EP02009524A patent/EP1266693B1/en not_active Expired - Lifetime
- 2002-04-26 AT AT02009524T patent/ATE305820T1/en active
- 2002-04-26 DE DE50204434T patent/DE50204434D1/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19534232A1 (en) | 1995-09-15 | 1997-03-20 | Karlsruhe Forschzent | Process for comminuting and crushing solids conglomerated from non-metallic or partially metallic components and for comminuting homogeneous non-metallic solids |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008017172A1 (en) * | 2006-08-11 | 2008-02-14 | Selfrag Ag | Method for fragmenting material by means of high-voltage discharges |
WO2008113189A1 (en) * | 2007-03-16 | 2008-09-25 | Selfrag Ag | Sample holder and assembly for the electrodynamic fragmentation of samples |
AU2007349730B2 (en) * | 2007-03-16 | 2011-08-25 | Selfrag Ag | Sample holder and assembly for the electrodynamic fragmentation of samples |
US8138952B2 (en) | 2007-03-16 | 2012-03-20 | Selfrag Ag | Sample holder and assembly for the electrodynamic fragmentation of samples |
CN112169965A (en) * | 2020-09-22 | 2021-01-05 | 东北大学 | Ore high-voltage pulse discharge pretreatment system and application method thereof |
Also Published As
Publication number | Publication date |
---|---|
ATE305820T1 (en) | 2005-10-15 |
EP1266693A3 (en) | 2004-10-20 |
DE10126646C2 (en) | 2003-04-10 |
EP1266693B1 (en) | 2005-10-05 |
DE50204434D1 (en) | 2005-11-10 |
DE10126646A1 (en) | 2002-12-12 |
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