EP2154371A1 - Pumping device - Google Patents
Pumping device Download PDFInfo
- Publication number
- EP2154371A1 EP2154371A1 EP08014528A EP08014528A EP2154371A1 EP 2154371 A1 EP2154371 A1 EP 2154371A1 EP 08014528 A EP08014528 A EP 08014528A EP 08014528 A EP08014528 A EP 08014528A EP 2154371 A1 EP2154371 A1 EP 2154371A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pulsator
- pumping device
- line
- pump head
- main pump
- 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
- 238000005086 pumping Methods 0.000 title claims abstract description 17
- 238000013022 venting Methods 0.000 claims abstract description 5
- 239000012528 membrane Substances 0.000 claims description 13
- 239000002245 particle Substances 0.000 claims description 11
- 238000012546 transfer Methods 0.000 claims description 9
- 239000007787 solid Substances 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 4
- 238000010276 construction Methods 0.000 claims description 3
- 238000013461 design Methods 0.000 claims description 2
- 230000003247 decreasing effect Effects 0.000 claims 1
- 238000011084 recovery Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 7
- 239000012530 fluid Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000002028 Biomass Substances 0.000 description 2
- 239000002551 biofuel Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B53/00—Component parts, details or accessories not provided for in, or of interest apart from, groups F04B1/00 - F04B23/00 or F04B39/00 - F04B47/00
- F04B53/06—Venting
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B43/00—Machines, pumps, or pumping installations having flexible working members
- F04B43/02—Machines, pumps, or pumping installations having flexible working members having plate-like flexible members, e.g. diaphragms
- F04B43/06—Pumps having fluid drive
- F04B43/067—Pumps having fluid drive the fluid being actuated directly by a piston
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B53/00—Component parts, details or accessories not provided for in, or of interest apart from, groups F04B1/00 - F04B23/00 or F04B39/00 - F04B47/00
- F04B53/08—Cooling; Heating; Preventing freezing
Definitions
- the invention relates to a pump device with a pulsator as a drive element for a main pump head, which is located in a feed line and the working space is provided on the suction side with a check valve and the pressure side with a pressure valve.
- the invention has for its object to provide a pump device of the type mentioned, which can be used for pumping aggressive fluids at high temperature, and yet operates at low cost with high reliability.
- This object is achieved in that the working space of the pulsator is directly connected to the working space of the main pump head via a suspension line filled with conveying medium in such a way that the pulsator sucks oscillating conveying medium from the delivery line into the working space of the main pump head or pushes it out of the working space, and that the working space of the pulsator is connected via a vent valve with the suction side of the delivery line.
- a basic idea of the invention thus lies in the fact that the pulsator acts on a main pump head, which in principle is designed like a piston pump head, but without a piston being required.
- a pump head suitable for high temperatures and pressures standard component can be used, which represents an overall cost-effective alternative to the known solutions by the combination with a standard diaphragm pump, the principle of a "remote head" - pump is maintained.
- the wear is further reduced by the fact that any particles present in the pumped medium do not come into contact with the workspace of the pulsator, since the liquid in the pendulum line is moved back and forth only in the scope of the pump stroke, and mixes only slightly with freshly sucked liquid.
- the pulsator can be designed in membrane or tubular membrane construction as well as in piston or plunger construction. If the pulsator is a diaphragm pump, particles will not get to the membrane. Since high temperatures in the pumped medium decrease in the course of the transfer line, diaphragm pumps can be used with inexpensive plastic membranes, such as PTFE, even at high pressures and high temperatures in the delivery line. Therefore, pumping devices according to the invention are particularly well suited for the conveyance of biomass in the production of biofuel.
- the inlet into the suction-side delivery line is preferably located above the ventilation valve, so that the gases escape from the working space automatically.
- a forced ventilation for example with a time and / or pressure-controlled valve, be present.
- the pendulum line is provided with a cooling.
- the pendulum line is aligned by the diaphragm pump to the main pump head falling down. The particles thus remain in the region of the main pump head and are returned to the delivery line.
- the pendulum line is provided with a sink as a receiving space for solid particles in the pumped medium. It is thus provided in the pendulum line, an area which is below the working space of the diaphragm pump, so that the particles accumulate there due to gravity and do not get into the working space of the pulsator.
- the working chamber of the pulsator is acted upon by a compensating medium to compensate for leakage fade, so that a flow through the pendulum line and a migration of solid particles to the pulsator can be prevented.
- a further advantageous embodiment of the invention is to arrange a separating piston in the pendulum line.
- a low drive power is achieved in that a double-acting pulsator and two oppositely driven pump circuits are present, which is particularly advantageous when used in recirculation processes.
- a pump device 1 has a diaphragm pump 10 serving as a pulsator, a main pump head 11 and a transfer line 12.
- the main pump head 11 has an inlet 13 and an outlet 14 for installation in a delivery line whose pressure side is denoted by 5 and the suction side by 15.
- On the inlet side (suction side) is a check valve 16 and the output side (pressure side) a pressure valve 17 is present.
- the conveying direction is marked with arrow 6.
- the main pump head 11 corresponds constructively to a pump head of a piston pump. However, he has no piston. His working space 18 is rather directly connected via the pendulum line 12 with a working space 20 of the diaphragm pump 10.
- the diaphragm pump 10 is provided only with a single connection 7 for the shuttle 12. It has no pump valves. It is only a connection 8 for a vent with a vent valve 9 ( Fig. 2 ) and a connection 4 for a refill reservoir 30 (FIG. Fig. 2 ) available.
- the hub causes the diaphragm pump 10 via the liquid column in the transfer line 12, the promotion in the main pump head 11th
- the pendulum line 12 is filled with delivery fluid 21. It leads via a control input 22 of the main pump head 11 to the working space 20 of the diaphragm pump 10.
- the pendulum line 12 is provided with a cooling, which is formed by a cooling liquid applied to the cooling jacket 23. In this way, a temperature reduction of, for example, about 360 ° C at the main pump head 11, as it typically has to be promoted bio-mass in the bio-fuel production, be made to about 100 ° C at the diaphragm pump 10.
- the transfer line 12 contains the delivery liquid 21, which may also have solid particles 24, a portion 25 is present in the transfer line 12, which drops from the diaphragm pump 10 to the main pump head 11, and which opens directly into the working chamber 18 of the main pump head 11. At its lowest point the pendulum line 12 is thus at the level of the working space 18 of the main pump head 11. The solid particles 24 remain due to gravity in the working space 18 of the main pump head 11 and do not reach the working space 20 of the diaphragm pump 10. They are the pressure-side delivery line 5 supplied.
- the membrane pump 10 has a membrane 26, which is hydraulically controlled via a diaphragm control chamber 27.
- the membrane material is preferably PTFE. Alternatively, elastomers, metallic materials or composite materials can be used.
- the diaphragm control chamber 27 is acted upon by a piston 28 which is driven by a motor 29 (FIG. Fig. 2 ) is driven.
- a refilling reservoir 30 filled with a compensating medium is present, which is supplied via a controlled valve 31 (FIG. Fig. 2 ) Emits compensation medium in the working space 20 of the diaphragm pump 10.
- the feeder is in Fig. 2 denoted by 32.
- Fig. 2 illustrated configuration has a double-acting pulsator with two pump devices, as shown in Fig. 1 illustrated up.
- the pump devices are connected in parallel in two counteracted branches A, B.
- a pumping operation will be described with reference to a branch.
- the pendulum line 12 and the working space 18 of the main pump head 11 are completely filled with pumped liquid.
- the check valve 16 and the pressure valve 17 are closed.
- each main pump head 11 with a single-acting pulsator equal or opposite directions can be controlled.
- FIG. 3 is shown as a detail of a second embodiment, a portion of a pendulum line 12 '.
- a separating piston 32 mounted longitudinally displaceably according to a double arrow 34 is arranged in the transfer line 12'. Any existing solid particles 24 thereby remain in a region 32 on the side of the main pump head 11 and can not reach a region 33 on the side of the diaphragm pump.
Abstract
Description
Die Erfindung betrifft eine Pumpenvorrichtung mit einem Pulsator als Antriebselement für einen Hauptpumpenkopf, der in einer Förderleitung liegt und dessen Arbeitsraum saugseitig mit einem Rückschlagventil und druckseitig mit einem Druckventil versehen ist.The invention relates to a pump device with a pulsator as a drive element for a main pump head, which is located in a feed line and the working space is provided on the suction side with a check valve and the pressure side with a pressure valve.
Pumpen dieser Art sind aus
Der Erfindung liegt die Aufgabe zugrunde, eine Pumpenvorrichtung der eingangs genannten Art anzugeben, die zum Pumpen von aggressiven Fördermedien mit hoher Temperatur eingesetzt werden kann, und die dennoch bei geringen Kosten mit hoher Zuverlässigkeit arbeitet.The invention has for its object to provide a pump device of the type mentioned, which can be used for pumping aggressive fluids at high temperature, and yet operates at low cost with high reliability.
Diese Aufgabe wird dadurch gelöst, dass der Arbeitsraum des Pulsators über eine mit Fördermedium gefüllte Pendelleitung unmittelbar mit dem Arbeitsraum des Hauptpumpenkopfes in der Weise in Verbindung steht, dass der Pulsator oszillierend Fördermedium aus der Förderleitung in den Arbeitsraum des Hauptpumpenkopfes ansaugt oder aus dem Arbeitsraum drückt, und dass der Arbeitsraum des Pulsators über ein Entlüftungsventil mit der Saugseite der Förderleitung verbunden ist.This object is achieved in that the working space of the pulsator is directly connected to the working space of the main pump head via a suspension line filled with conveying medium in such a way that the pulsator sucks oscillating conveying medium from the delivery line into the working space of the main pump head or pushes it out of the working space, and that the working space of the pulsator is connected via a vent valve with the suction side of the delivery line.
Ein Grundgedanke der Erfindung liegt somit darin, dass der Pulsator einen Hauptpumpenkopf beaufschlagt, der prinzipiell wie ein Kolbenpumpenkopf ausgebildet ist, ohne dass jedoch ein Kolben erforderlich ist. Auf diese Weise kann als Pumpenkopf ein für hohe Temperaturen und Drücke geeignetes Standardbauteil verwendet werden, welches durch die Kombination mit einer Standard-Membranpumpe insgesamt eine kostengünstige Alternative zu den bekannten Lösungen darstellt, wobei das Prinzip einer "Remote Head"- Pumpe beibehalten wird. Der Verschleiß wird ferner dadurch verringert, dass eventuell im Fördermedium vorhandene Partikel nicht mit dem Arbeitsraum des Pulsators in Berührung kommen, da die Flüssigkeit in der Pendelleitung nur im Umfang des Pumpenhubs hin und her bewegt wird, und sich nur geringfügig mit frisch angesaugter Flüssigkeit mischt. Der Pulsator kann in Membran- oder Schlauchmembranbauweise sowie in Kolben- oder Plungerbauweise ausgeführt sein. Wenn es sich bei dem Pulsator um eine Membranpumpe handelt, gelangen Partikel nicht zur Membran. Da auch hohe Temperaturen im Fördermedium im Verlauf der Pendelleitung abnehmen, können Membranpumpen mit kostengünstigen Kunststoff-Membranen, beispielsweise aus PTFE, auch bei hohen Drücken und hohen Temperaturen in der Förderleitung eingesetzt werden. Daher sind erfindungsgemäße Pumpenvorrichtungen besonders gut zum Fördern von Biomasse bei der Herstellung von Biokraftstoff geeignet.A basic idea of the invention thus lies in the fact that the pulsator acts on a main pump head, which in principle is designed like a piston pump head, but without a piston being required. In this way, as a pump head suitable for high temperatures and pressures standard component can be used, which represents an overall cost-effective alternative to the known solutions by the combination with a standard diaphragm pump, the principle of a "remote head" - pump is maintained. The wear is further reduced by the fact that any particles present in the pumped medium do not come into contact with the workspace of the pulsator, since the liquid in the pendulum line is moved back and forth only in the scope of the pump stroke, and mixes only slightly with freshly sucked liquid. The pulsator can be designed in membrane or tubular membrane construction as well as in piston or plunger construction. If the pulsator is a diaphragm pump, particles will not get to the membrane. Since high temperatures in the pumped medium decrease in the course of the transfer line, diaphragm pumps can be used with inexpensive plastic membranes, such as PTFE, even at high pressures and high temperatures in the delivery line. Therefore, pumping devices according to the invention are particularly well suited for the conveyance of biomass in the production of biofuel.
Ein weiterer Vorteil liegt darin, dass sich aufgrund der Entlüftung Gase aus dem Fördermedium oder Lufteinschlüsse nicht in dem Pumpenraum des Pulsators ansammeln können, sondern in den Prozess zurück geführt werden. Bevorzugt liegt der Eintritt in die saugseitige Förderleitung zu diesem Zweck oberhalb des Entlüftungsventils, so dass die Gase selbsttätig aus dem Arbeitsraum austreten. Alternativ kann eine Zwangsbelüftung, beispielsweise mit einem zeit- und/ oder druckgesteuerten Ventil, vorhanden sein.Another advantage is that due to the venting gases from the fluid or air bubbles can not accumulate in the pump chamber of the pulsator, but are fed back into the process. For this purpose, the inlet into the suction-side delivery line is preferably located above the ventilation valve, so that the gases escape from the working space automatically. Alternatively, a forced ventilation, for example with a time and / or pressure-controlled valve, be present.
Um die Membranpumpe noch weiter temperaturmäßig zu entlasten, besteht eine bevorzugte Weiterbildung der Erfindung darin, dass die Pendelleitung mit einer Kühlung versehen ist.To further relieve the diaphragm pump in terms of temperature, a preferred development of the invention is that the pendulum line is provided with a cooling.
Es erweist sich ferner als vorteilhaft, dass die Pendelleitung von der Membranpumpe zum Hauptpumpenkopf hin fallend ausgerichtet ist. Die Partikel verbleiben somit im Bereich des Hauptpumpenkopfes und werden in die Förderleitung zurückgeführt.It also proves to be advantageous that the pendulum line is aligned by the diaphragm pump to the main pump head falling down. The particles thus remain in the region of the main pump head and are returned to the delivery line.
Alternativ kann es vorteilhaft sein, dass die Pendelleitung mit einer Senke als Aufnahmeraum für Feststoffteilchen im Fördermedium versehen ist. Es wird also in der Pendelleitung ein Bereich vorgesehen, der unterhalb des Arbeitsraums der Membranpumpe liegt, so dass die Partikel sich aufgrund der Schwerkraft dort ansammeln und nicht in den Arbeitsraum des Pulsators gelangen.Alternatively, it may be advantageous that the pendulum line is provided with a sink as a receiving space for solid particles in the pumped medium. It is thus provided in the pendulum line, an area which is below the working space of the diaphragm pump, so that the particles accumulate there due to gravity and do not get into the working space of the pulsator.
Es ist zweckmäßig, dass der Arbeitsraum des Pulsators mit einem Ausgleichsmedium zum Ausgleich von Leckageschwund beaufschlagt ist, so dass ein Durchströmen der Pendelleitung und ein Wandern von Feststoffteilchen zum Pulsator verhindert werden.It is expedient that the working chamber of the pulsator is acted upon by a compensating medium to compensate for leakage fade, so that a flow through the pendulum line and a migration of solid particles to the pulsator can be prevented.
Um den Pulsator noch weiter gegen Feststoffteilchen aus dem Fördermedium zu schützen, besteht eine weitere vorteilhafte Ausgestaltung der Erfindung darin, in der Pendelleitung einen Trennkolben anzuordnen. Durch diese Maßnahme wird der dem Pulsator zugeordnete Teil der Pendelleitung von dem Teil getrennt, welcher dem Hauptpumpenkopf zugeordnet ist.In order to protect the pulsator even further against solid particles from the pumped medium, a further advantageous embodiment of the invention is to arrange a separating piston in the pendulum line. By this measure, the pulsator associated part of the shuttle line is separated from the part which is associated with the main pump head.
Eine geringe Antriebsleistung wird dadurch erreicht, dass ein doppelt wirkender Pulsator und zwei gegensinnig angesteuerte Pumpenkreise vorhanden sind, was besonders beim Einsatz bei Rezirkulationsprozessen vorteilhaft ist.A low drive power is achieved in that a double-acting pulsator and two oppositely driven pump circuits are present, which is particularly advantageous when used in recirculation processes.
Nachfolgend wird die Erfindung anhand von zwei Ausführungsbeispielen weiter erläutert. Es zeigen schematisch:
- Fig. 1
- einen Vertikalschnitt durch eine erste Ausführung einer Pumpenvorrichtung;
- Fig. 2
- ein Schaltbild einer aus zwei Pumpenvorrichtungen nach
Fig. 1 zusammengesetzten Pumpenkonfiguration; und - Fig. 3
- eine Einzelheit einer zweiten Ausführung einer Pumpenvorrichtung.
- Fig. 1
- a vertical section through a first embodiment of a pump device;
- Fig. 2
- a circuit diagram of one of two pump devices after
Fig. 1 composite pump configuration; and - Fig. 3
- a detail of a second embodiment of a pump device.
Gemäß
Konstruktiv entspricht der Hauptpumpenkopf 11 zwar einem Pumpenkopf einer Kolbenpumpe. Er weist jedoch keinen Kolben auf. Sein Arbeitsraum 18 ist vielmehr unmittelbar über die Pendelleitung 12 mit einem Arbeitsraum 20 der Membranpumpe 10 verbunden. Die Membranpumpe 10 ist nur mit einem einzigen Anschluss 7 für die Pendelleitung 12 versehen. Sie weist keine Pumpenventile auf. Es ist lediglich ein Anschluss 8 für eine Entlüftung mit einem Entlüftungsventil 9 (
Die Pendelleitung 12 ist mit Förderflüssigkeit 21 gefüllt. Sie führt über einen Steuereingang 22 des Hauptpumpenkopfes 11 zum Arbeitsraum 20 der Membranpumpe 10. Die Pendelleitung 12 ist mit einer Kühlung versehen, die von einem mit Kühlflüssigkeit beaufschlagten Kühlmantel 23 gebildet wird. Auf diese Weise kann eine Temperaturabsenkung von beispielsweise ca. 360°C am Hauptpumpenkopf 11, wie sie typischerweise die zu fördernde Bio-Masse bei der Bio-Kraftstoffherstellung aufweist, auf ca. 100°C an der Membranpumpe 10 vorgenommen werden.The
Da die Pendelleitung 12 die Förderflüssigkeit 21 enthält, welche auch Feststoffteilchen 24 aufweisen kann, ist ein Abschnitt 25 in der Pendelleitung 12 vorhanden, der von der Membranpumpe 10 zum Hauptpumpenkopf 11 hin abfällt, und der unmittelbar in den Arbeitsraum 18 des Hauptpumpenkopfes 11 mündet. An ihrer tiefsten Stelle liegt die Pendelleitung 12 somit auf dem Niveau des Arbeitsraums 18 des Hauptpumpenkopfes 11. Die Feststoffteilchen 24 verbleiben dadurch aufgrund der Schwerkraft im Arbeitsraum 18 des Hauptpumpenkopfes 11 und gelangen nicht in den Arbeitsraum 20 der Membranpumpe 10. Sie werden vielmehr der druckseitigen Förderleitung 5 zugeführt.Since the
Die Membranpumpe 10 weist eine Membran 26 auf, die hydraulisch über einen Membransteuerraum 27 angesteuert wird. Als Membranwerkstoff eignet sich vorzugsweise PTFE. Alternativ können auch Elastomere, metallische Werkstoffe oder Verbundwerkstoffe eingesetzt werden. Der Membransteuerraum 27 wird mit einem Kolben 28 beaufschlagt, der von einem Motor 29 (
Unter Bezugnahme auf die
Wird der Kolben 28 ausgefahren, bewirkt dies ein Abflachen der Membran 26 und einen Unterdruck im Arbeitsraum 20 der Membranpumpe 10. Der Unterdruck wirkt über die Pendelleitung 12 im Arbeitsraum 18 des Hauptpumpenkopfes, so dass das Rückschlagventil 16 öffnet und Förderflüssigkeit von der Saugseite der Förderleitung 15 angesaugt wird. Beim folgenden entgegengesetzten Hub des Kolbens 28 wird beim Ausbauchen der Membran 26 Druck im Arbeitsraum 20 der Membranpumpe 10 erzeugt, der über die Pendelleitung 12 auf den Arbeitsraum 18 des Hauptpumpenkopfes 11 wirkt. Der Druck bewirkt ein Schließen des Rückschlagventils 16 und ein Öffnen des Druckventils 17, so dass Förderflüssigkeit 21 in die druckseitige Förderleitung 5 gepumpt wird. Durch oszillierende Bewegung des Kolbens 28 erfolgt auf diese Weise eine kontinuierliche Förderung.If the
Durch die gegensinnige Ansteuerung zweier Hauptpumpenköpfe 11 mittels doppelt wirkendem Pulsator 10, der vorzugsweise in Membranbauart ausgeführt ist, überlagern sich die Pump- und Saugvorgänge mit den zwei Kreisen A und B derart, dass insbesondere bei Rezirkulationsprozessen mit hohem Systemdruck und relativ niedrigem Differenzdruck zwischen Saug- und Druckleitung nur eine geringe Leistung für den antreibenden Motor erforderlich ist. Alternativ kann jeder Hauptpumpenkopf 11 mit einem einfach wirkenden Pulsator gleich- oder gegensinnig angesteuert werden.By opposing control of two main pump heads 11 by means of double-acting
In
Claims (11)
dadurch gekennzeichnet, dass der Arbeitsraum (20) des Pulsators über eine mit Fördermedium (21) gefüllte Pendelleitung (12) unmittelbar mit dem Arbeitsraum (18) des Hauptpumpenkopfes (11) in der Weise in Verbindung steht, dass der Pulsator oszillierend Fördermedium (21) aus der Förderleitung (15) in den Arbeitsraum (18) des Hauptpumpenkopfes (11) ansaugt oder aus dem Arbeitsraum (18) drückt, und
dass der Arbeitsraum (20) des Pulsators über ein Entlüftungsventil (9) mit der Saugseite der Förderleitung (15) verbunden ist.Pump device with a pulsator as a drive element for a main pump head (11), which lies in a delivery line (15) and whose working space (18) is provided on the suction side with a check valve (16) and on the pressure side with a pressure valve (17),
characterized in that the working chamber (20) of the pulsator via a pumped with conveying medium (21) shuttle line (12) directly to the working space (18) of the main pump head (11) in such a way that the pulsator oscillating conveying medium (21) from the delivery line (15) in the working space (18) of the main pump head (11) sucks or pushes out of the working space (18), and
the working chamber (20) of the pulsator is connected to the suction side of the delivery line (15) via a venting valve (9).
dadurch gekennzeichnet,
dass die Saugseite der Förderleitung (15) zur selbsttätigen Entlüftung oberhalb des Entlüftungsventils (9) angeordnet ist.Pumping device according to claim 1,
characterized,
that the suction side of the conveying line (15) for automatic venting above the vent valve (9) is arranged.
dadurch gekennzeichnet,
dass das Entlüftungsventil (9) in Verbindung mit einer Rückführungspumpe zwangsgesteuert, insbesondere zeitlich gesteuert, ist.Pumping device according to claim 1,
characterized,
in that the venting valve (9) is positively controlled, in particular time-controlled, in connection with a return pump.
dadurch gekennzeichnet,
dass die Pendelleitung (12) mit einer Kühlung versehen ist.Pumping device according to one of the preceding claims,
characterized,
that the pendulum line (12) is provided with a cooling.
dadurch gekennzeichnet,
dass die Pendelleitung (12) vom Pulsator zum Hauptpumpenkopf (11) hin fallend ausgerichtet ist.Pumping device according to one of the preceding claims,
characterized,
that the transfer line (12) from the pulsator to the main pump head (11) toward decreasing aligned.
dadurch gekennzeichnet,
dass die Pendelleitung (12) mit einer Senke (25) als Aufnahmeraum für Feststoffteilchen (24) im Fördermedium (21) versehen ist.Pumping device according to one of claims 1 to 4,
characterized,
that the transfer line (12) having a depression (25) as a receiving space for solid particles (24) in the medium (21) is provided.
dadurch gekennzeichnet,
dass der Arbeitsraum (20) des Pulsators mit einem Ausgleichsmedium zum Ausgleich von Leckageschwund beaufschlagt ist.Pumping device according to one of the preceding claims,
characterized,
that the working chamber (20) of the pulsator is supplied with a compensation medium for compensating for leakage fade.
dadurch gekennzeichnet,
dass in der Pendelleitung (12') ein Trennkolben (32) angeordnet ist.Pumping device according to one of the preceding claims,
characterized,
that in the pendulum line (12 '), a separating piston (32) is arranged.
dadurch gekennzeichnet,
dass sie mit einem doppelt wirkenden Pulsator und zwei gegensinnig angesteuerten Pumpenkreisen (A, B) ausgebildet ist.Pumping device according to one of the preceding claims,
characterized,
that it is formed with a double-acting pulsator and two oppositely controlled pump circuits (A, B).
dadurch gekennzeichnet,
dass der Pulsator in Membran- oder Schlauchmembranbauweise ausgeführt ist.Pumping device according to one of the preceding claims,
characterized,
that the pulsator is designed in membrane or tubular membrane design.
dadurch gekennzeichnet,
dass der Pulsator in Kolben- oder Plungerbauweise ausgeführt ist.Pumping device according to one of the preceding claims 1 to 9,
characterized,
that the pulsator is designed in piston or plunger construction.
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08014528.7A EP2154371B1 (en) | 2008-08-14 | 2008-08-14 | Pumping device |
DK200800165U DK200800165U3 (en) | 2008-08-14 | 2008-08-27 | pumping device |
US13/058,904 US20110135514A1 (en) | 2008-08-14 | 2009-08-14 | Pump Device |
ES09777900T ES2773043T3 (en) | 2008-08-14 | 2009-08-14 | Pump device |
EP09777900.3A EP2329147B1 (en) | 2008-08-14 | 2009-08-14 | Pumping device |
PCT/EP2009/005928 WO2010017997A2 (en) | 2008-08-14 | 2009-08-14 | Pump device |
BRPI0917663A BRPI0917663A2 (en) | 2008-08-14 | 2009-08-14 | pump device |
PL09777900T PL2329147T3 (en) | 2008-08-14 | 2009-08-14 | Pumping device |
CN200980131732.1A CN102124226B (en) | 2008-08-14 | 2009-08-14 | Pump device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08014528.7A EP2154371B1 (en) | 2008-08-14 | 2008-08-14 | Pumping device |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2154371A1 true EP2154371A1 (en) | 2010-02-17 |
EP2154371B1 EP2154371B1 (en) | 2018-09-19 |
Family
ID=39883770
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08014528.7A Active EP2154371B1 (en) | 2008-08-14 | 2008-08-14 | Pumping device |
EP09777900.3A Active EP2329147B1 (en) | 2008-08-14 | 2009-08-14 | Pumping device |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP09777900.3A Active EP2329147B1 (en) | 2008-08-14 | 2009-08-14 | Pumping device |
Country Status (8)
Country | Link |
---|---|
US (1) | US20110135514A1 (en) |
EP (2) | EP2154371B1 (en) |
CN (1) | CN102124226B (en) |
BR (1) | BRPI0917663A2 (en) |
DK (1) | DK200800165U3 (en) |
ES (1) | ES2773043T3 (en) |
PL (1) | PL2329147T3 (en) |
WO (1) | WO2010017997A2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013045598A3 (en) * | 2011-09-30 | 2013-05-30 | Aker Wirth Gmbh | Positive displacement pump and operating method thereof |
WO2013135681A1 (en) * | 2012-03-13 | 2013-09-19 | Prominent Dosiertechnik Gmbh | Displacement pump with forced venting |
WO2015090928A1 (en) * | 2013-12-18 | 2015-06-25 | Mhwirth Gmbh | Hot slurry pump |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101374048B1 (en) * | 2012-06-14 | 2014-03-13 | 한국과학기술연구원 | Fluid pumping device, fuel cell device and fuel gas recirculation method using the same |
EP3167029A1 (en) * | 2014-07-11 | 2017-05-17 | JOHANNSEN, Ib | A method and apparatus for producing biofuel in an oscillating flow production line under supercritical fluid conditions |
DE102016015110A1 (en) * | 2016-12-20 | 2018-06-21 | Fresenius Medical Care Deutschland Gmbh | Positive displacement pump for medical fluids and blood treatment device with a positive displacement pump for medical fluids and method for controlling a positive displacement pump for medical fluids |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3216360A (en) * | 1963-06-10 | 1965-11-09 | Lapp Insulator Company Inc | Fluid transport device |
FR1426416A (en) * | 1964-01-08 | 1966-01-28 | Panther Pumps & Equipment Comp | Fluid actuated transfer apparatus |
EP0036945A2 (en) * | 1980-03-28 | 1981-10-07 | Josef Emmerich Pumpenfabrik GmbH | Device for delivering fluid materials |
DE19903061A1 (en) * | 1999-01-26 | 2000-08-03 | Emmerich Josef Pumpenfab | Displacement pump with adjoining hydraulic piping which incorporates a cooling system and accommodates a freely movable separation piston reducing heat transferred to the pump membrane |
US20040062662A1 (en) * | 2002-09-27 | 2004-04-01 | Claude Cordell E. | Effervescent gas bleeder apparatus |
EP0919724B1 (en) | 1997-11-28 | 2005-07-06 | Ente per le Nuove Tecnologie, l'Energia e l'Ambiente - ENEA | Hydraulically driven double acting diaphragm pump |
EP1898093A1 (en) | 2006-09-04 | 2008-03-12 | BRAN + LUEBBE GmbH | Pumping device |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2444586A (en) * | 1944-03-20 | 1948-07-06 | Wuensch Charles Erb | Pump |
US2445127A (en) * | 1946-05-15 | 1948-07-13 | Earl B Schwenk | Hot liquid pump |
US3661167A (en) * | 1970-05-25 | 1972-05-09 | A & D Fabricating Co | Chemical feed pump with improved valve means |
JPS5018604B1 (en) * | 1971-06-24 | 1975-07-01 | ||
US3802807A (en) * | 1972-06-02 | 1974-04-09 | Precision Control Prod Corp | Pump |
DE2553794A1 (en) * | 1975-11-29 | 1977-06-02 | Bayer Ag | Continuous delivery of hot aggressive fluids - uses sealing liquid arranged to produce temperature drop to safe level |
US4247266A (en) * | 1979-02-16 | 1981-01-27 | Vapor Corporation | Fluid pump drive system |
DE3021851C2 (en) * | 1980-06-11 | 1984-04-12 | Pumpenfabrik Urach, 7432 Urach | High pressure piston pump |
US4378183A (en) * | 1980-09-18 | 1983-03-29 | The Pittsburgh & Midway Coal Mining Co. | Apparatus and method for pumping hot, erosive slurry of coal solids in coal derived, water immiscible liquid |
US4386888A (en) * | 1980-09-29 | 1983-06-07 | Mccann's Engineering And Manufacturing Company | Double diaphragm operated reversing valve pump |
DE3040478C2 (en) * | 1980-10-28 | 1986-07-10 | Uraca Pumpenfabrik GmbH & Co KG, 7432 Bad Urach | Pump or the like. hydraulic working machine |
ATE10670T1 (en) * | 1980-12-29 | 1984-12-15 | Lewa Herbert Ott Gmbh + Co. | DIAPHRAGM PUMP WITH RELIEVED CLAMPED DIAPHRAGM. |
EP0085725B1 (en) * | 1982-02-05 | 1984-11-28 | Bran & Lübbe GmbH | Piston-driven diaphragm pump |
US5310321A (en) * | 1990-07-24 | 1994-05-10 | Baker Hughes Incorporated | Pump system |
US5249932A (en) * | 1991-10-07 | 1993-10-05 | Erik Van Bork | Apparatus for controlling diaphragm extension in a diaphragm metering pump |
NL1004890C2 (en) * | 1996-12-24 | 1998-06-25 | Envirotech Pumpsystems Netherl | Pump system particularly suitable for pumping hot media. |
-
2008
- 2008-08-14 EP EP08014528.7A patent/EP2154371B1/en active Active
- 2008-08-27 DK DK200800165U patent/DK200800165U3/en not_active IP Right Cessation
-
2009
- 2009-08-14 ES ES09777900T patent/ES2773043T3/en active Active
- 2009-08-14 CN CN200980131732.1A patent/CN102124226B/en active Active
- 2009-08-14 PL PL09777900T patent/PL2329147T3/en unknown
- 2009-08-14 EP EP09777900.3A patent/EP2329147B1/en active Active
- 2009-08-14 BR BRPI0917663A patent/BRPI0917663A2/en not_active Application Discontinuation
- 2009-08-14 US US13/058,904 patent/US20110135514A1/en not_active Abandoned
- 2009-08-14 WO PCT/EP2009/005928 patent/WO2010017997A2/en active Application Filing
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3216360A (en) * | 1963-06-10 | 1965-11-09 | Lapp Insulator Company Inc | Fluid transport device |
FR1426416A (en) * | 1964-01-08 | 1966-01-28 | Panther Pumps & Equipment Comp | Fluid actuated transfer apparatus |
EP0036945A2 (en) * | 1980-03-28 | 1981-10-07 | Josef Emmerich Pumpenfabrik GmbH | Device for delivering fluid materials |
EP0919724B1 (en) | 1997-11-28 | 2005-07-06 | Ente per le Nuove Tecnologie, l'Energia e l'Ambiente - ENEA | Hydraulically driven double acting diaphragm pump |
DE19903061A1 (en) * | 1999-01-26 | 2000-08-03 | Emmerich Josef Pumpenfab | Displacement pump with adjoining hydraulic piping which incorporates a cooling system and accommodates a freely movable separation piston reducing heat transferred to the pump membrane |
US20040062662A1 (en) * | 2002-09-27 | 2004-04-01 | Claude Cordell E. | Effervescent gas bleeder apparatus |
EP1898093A1 (en) | 2006-09-04 | 2008-03-12 | BRAN + LUEBBE GmbH | Pumping device |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013045598A3 (en) * | 2011-09-30 | 2013-05-30 | Aker Wirth Gmbh | Positive displacement pump and operating method thereof |
US9695808B2 (en) | 2011-09-30 | 2017-07-04 | Mhwirth Gmbh | Positive displacement pump and operating method thereof |
WO2013135681A1 (en) * | 2012-03-13 | 2013-09-19 | Prominent Dosiertechnik Gmbh | Displacement pump with forced venting |
WO2015090928A1 (en) * | 2013-12-18 | 2015-06-25 | Mhwirth Gmbh | Hot slurry pump |
AU2014365435B2 (en) * | 2013-12-18 | 2018-05-10 | Mhwirth Gmbh | Hot slurry pump |
Also Published As
Publication number | Publication date |
---|---|
CN102124226A (en) | 2011-07-13 |
DK200800165U3 (en) | 2009-12-11 |
EP2329147A2 (en) | 2011-06-08 |
WO2010017997A3 (en) | 2010-04-08 |
CN102124226B (en) | 2014-09-17 |
WO2010017997A2 (en) | 2010-02-18 |
PL2329147T3 (en) | 2020-06-29 |
ES2773043T3 (en) | 2020-07-09 |
BRPI0917663A2 (en) | 2015-12-01 |
EP2329147B1 (en) | 2019-12-18 |
EP2154371B1 (en) | 2018-09-19 |
US20110135514A1 (en) | 2011-06-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1898093B1 (en) | Pumping device | |
DE112017000240T5 (en) | OVERPRESSURE RELIEF SYSTEM FOR FLUID OUTPUT SIDE | |
EP2154371B1 (en) | Pumping device | |
EP1712796A1 (en) | Diaphragm pump | |
DE102014010108B4 (en) | Hydraulically driven diaphragm pump | |
EP2825774B1 (en) | Displacement pump with forced ventilation system | |
WO2018091306A1 (en) | Method for operating a piston pump, and piston pump | |
DE102011089399A1 (en) | Pump, in particular high-pressure fuel pump for a fuel injection device | |
DE202013105650U1 (en) | piston pump | |
DE3631408A1 (en) | AXIAL PISTON PUMP | |
DE102017117983A1 (en) | Pump unit, bearing device equipped therewith and method of operating the bearing device | |
EP0007109A1 (en) | Apparatus for metering a solution of chemicals to a stream of liquid | |
DE202008010872U1 (en) | pump device | |
DE102006055845A1 (en) | Multi-stage pump arrangement, has three pumps whose pressure sides are connected with common load line for adjusting high volume flow, where two of pumps are parallely connected for adjusting high pressurizing medium volume flow | |
DE102020108235A1 (en) | Hydraulic element and positive displacement pump with one such | |
DE102009028609A1 (en) | Manually operated pump device for exhaustion of fuel injection system of internal-combustion engine, has housing that is adjusted besides annular piston | |
DE3928411C2 (en) | ||
EP2342118B1 (en) | Hydraulic power steering system | |
DE102006062960B3 (en) | pump device | |
DE102013105072A1 (en) | Diaphragm pump with position control | |
DE2710428A1 (en) | Self lubricating high pressure plunger pump - has chambers along plunger, supplied with high viscosity sealing fluid | |
EP2877745B1 (en) | Metering system and metering pump therefor | |
DE2441570A1 (en) | Device for venting of injection pumps etc. - has narrow connecting pipe between evacuation chamber and return flow pipe | |
DE102016220610A1 (en) | High pressure pump for a fuel injection system | |
EP3167191B1 (en) | Diaphragm pump with reduced leak extension in the event of overload |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
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 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
|
AX | Request for extension of the european patent |
Extension state: AL BA MK RS |
|
17P | Request for examination filed |
Effective date: 20100813 |
|
AKX | Designation fees paid |
Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
|
17Q | First examination report despatched |
Effective date: 20100929 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R079 Ref document number: 502008016348 Country of ref document: DE Free format text: PREVIOUS MAIN CLASS: F04B0043067000 Ipc: F04B0053060000 |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: F04B 53/08 20060101ALI20180315BHEP Ipc: F04B 43/067 20060101ALI20180315BHEP Ipc: F04B 43/06 20060101ALI20180315BHEP Ipc: F04B 53/06 20060101AFI20180315BHEP |
|
INTG | Intention to grant announced |
Effective date: 20180409 |
|
RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: LADIGES, HENNING Inventor name: HUHNKE, CHRISTIAN |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D Free format text: NOT ENGLISH |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 502008016348 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 1043569 Country of ref document: AT Kind code of ref document: T Effective date: 20181015 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D Free format text: LANGUAGE OF EP DOCUMENT: GERMAN |
|
RAP2 | Party data changed (patent owner data changed or rights of a patent transferred) |
Owner name: SPX FLOW TECHNOLOGY NORDERSTEDT GMBH |
|
RAP2 | Party data changed (patent owner data changed or rights of a patent transferred) |
Owner name: SPX FLOW TECHNOLOGY GERMANY GMBH |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20180919 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20181219 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20181219 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20181220 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190119 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190119 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 502008016348 Country of ref document: DE |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 |
|
26N | No opposition filed |
Effective date: 20190620 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R082 Ref document number: 502008016348 Country of ref document: DE Representative=s name: GROSSE, SCHUMACHER, KNAUER, VON HIRSCHHAUSEN, DE Ref country code: DE Ref legal event code: R081 Ref document number: 502008016348 Country of ref document: DE Owner name: SPX FLOW TECHNOLOGY GERMANY GMBH, DE Free format text: FORMER OWNER: BRAN + LUEBBE GMBH, 22844 NORDERSTEDT, DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190831 Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190831 Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190814 |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20190831 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190814 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190831 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MM01 Ref document number: 1043569 Country of ref document: AT Kind code of ref document: T Effective date: 20190814 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190814 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20180919 Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20080814 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20230822 Year of fee payment: 16 Ref country code: GB Payment date: 20230828 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20230825 Year of fee payment: 16 Ref country code: DE Payment date: 20230829 Year of fee payment: 16 |