EP2594795B1 - Device for compressing a gas or a fluid comprising gaseous and liquid components, and a submarine boat containing such a device - Google Patents
Device for compressing a gas or a fluid comprising gaseous and liquid components, and a submarine boat containing such a device Download PDFInfo
- Publication number
- EP2594795B1 EP2594795B1 EP12190384.3A EP12190384A EP2594795B1 EP 2594795 B1 EP2594795 B1 EP 2594795B1 EP 12190384 A EP12190384 A EP 12190384A EP 2594795 B1 EP2594795 B1 EP 2594795B1
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- Prior art keywords
- fluid
- piston
- compression
- submarine
- liquid
- Prior art date
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- 239000012530 fluid Substances 0.000 title claims description 47
- 239000007788 liquid Substances 0.000 title description 38
- 230000033001 locomotion Effects 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 6
- 238000007906 compression Methods 0.000 description 74
- 230000006835 compression Effects 0.000 description 73
- 239000007789 gas Substances 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 239000011230 binding agent Substances 0.000 description 9
- 239000000203 mixture Substances 0.000 description 6
- 238000005056 compaction Methods 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 239000000110 cooling liquid Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Images
Classifications
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- 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
- F04B35/00—Piston pumps specially adapted for elastic fluids and characterised by the driving means to their working members, or by combination with, or adaptation to, specific driving engines or motors, not otherwise provided for
- F04B35/04—Piston pumps specially adapted for elastic fluids and characterised by the driving means to their working members, or by combination with, or adaptation to, specific driving engines or motors, not otherwise provided for the means being electric
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63G—OFFENSIVE OR DEFENSIVE ARRANGEMENTS ON VESSELS; MINE-LAYING; MINE-SWEEPING; SUBMARINES; AIRCRAFT CARRIERS
- B63G8/00—Underwater vessels, e.g. submarines; Equipment specially adapted therefor
- B63G8/36—Adaptations of ventilation, e.g. schnorkels, cooling, heating, or air-conditioning
-
- 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
- F04B37/00—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00
- F04B37/10—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use
- F04B37/18—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use for specific elastic fluids
- F04B37/20—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use for specific elastic fluids for wet gases, e.g. wet air
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- 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
- F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
- F04B39/06—Cooling; Heating; Prevention of freezing
- F04B39/062—Cooling by injecting a liquid in the gas to be compressed
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- 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
- F04B41/00—Pumping installations or systems specially adapted for elastic fluids
- F04B41/06—Combinations of two or more pumps
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62B—DEVICES, APPARATUS OR METHODS FOR LIFE-SAVING
- A62B11/00—Devices for reconditioning breathing air in sealed rooms
Definitions
- the invention relates to a device for compressing a gaseous or consisting of gaseous and liquid components fluid having the features specified in the preamble of claim 1 and a submarine.
- reciprocating compressors For compressing gases piston compressors are often used.
- reciprocating compressors generally have a dead space, also referred to as a harmful space, in which compressed gas is present after the compression stroke, which expands during the intake stroke of the reciprocating compressor and thus initially prevents aspiration of new gas.
- a dead space also referred to as a harmful space
- the efficiency of reciprocating compressors is significantly reduced, and this effect increases with increasing compression pressure.
- the compression of gases is polytropic, so that the temperature in compressors increases with the ratio of final pressure / initial pressure. As the temperature increases, the compression work to be performed increases.
- This and the above-mentioned dead space of reciprocating compressors mean that it is generally not possible to compress gases which are to be compressed to a comparatively high pressure in a single-stage process in a reciprocating compressor. Therefore, it is often necessary to gradually increase the pressure of a gas in a plurality of reciprocating piston compressors, wherein the gas is cooled in each case between the compression steps.
- DE 296 367 A and US 2,404,660 are known devices for compressing gases which have a reciprocating drive driven piston compressor, the gas sucks in a compression space and compacted there. In order to avoid dead space in the compression space and to cool the gas in the compression space, water is introduced into the compression space.
- An apparatus for compressing gas which comprises a pressure vessel having a gas inlet, a gas outlet and a liquid inlet, wherein gas in the pressure vessel is compressed by the admission of liquid into the pressure vessel.
- A1 known piston working machine has a piston compressor and means for introducing a cooling liquid in a compression chamber of the reciprocating compressor.
- a piston rod of the reciprocating compressor is motion-coupled with a crank mechanism.
- a known device for compressing a fluid which is intended for use in the field of brewing, is introduced into the compression chamber of a reciprocating compressor by means of a piston pump cooling liquid.
- the reciprocating compressor and the piston pump have a common drive.
- the present invention seeks to provide a device for compressing a gaseous or consisting of gaseous and liquid components fluid, the compression of a gaseous or gaseous and liquid constituents fluid to a relatively high pressure in a single-stage litigation in one Piston compressor allows, with a reciprocating compressor of the device can be adapted quickly to different or changing compaction tasks.
- the inventive device for compressing a gaseous or consisting of gaseous and liquid components fluid has a reciprocating compressor.
- the device has means for introducing a fluid into a compression chamber of the piston compressor during the compression and a piston pump for conveying the fluid.
- conveying means are provided with which a liquid is conveyed from a liquid reservoir into the compression space of the reciprocating compressor.
- control means are provided which actuate the device such that the liquid is introduced during the compression of the fluid in the compression space of the reciprocating compressor.
- the aim of this embodiment of the device according to the invention is, during the compression of the fluid in the compression space of the reciprocating compressor Initiate liquid.
- the fluid in the compression chamber is cooled during the compression process.
- the dead space present in the compression chamber is completely filled with the incompressible liquid with appropriate metering of the quantity of liquid introduced into the compression chamber, so that then there is no more gas in the compression chamber and the dead space is virtually eliminated.
- the adverse effects otherwise associated with the dead space can therefore not occur in the method according to the invention.
- the piston rod of the reciprocating compressor is preferably coupled for movement with a continuously adjustable linear drive.
- a continuously adjustable linear drive is such a linear drive to understand, in which the movement path and the speed of movement of a translationally movable component of the linear drive, which is coupled to the piston rod, can be changed without transition.
- the path traveled by the piston of the reciprocating compressor and its speed are infinitely adjustable on the piston compressor during the suction and compression of the fluid, so that the reciprocating compressor can be adapted quickly to different or changing compaction tasks.
- the compression space of the reciprocating compressor expediently has, in addition to a first inlet for the fluid to be compressed, also a second inlet for introducing the liquid.
- a valve On the input side of the first inlet of the compression chamber, a valve is arranged in the usual way, which prevents the fluid during the compression stroke of the piston compressor can flow out of the compression space.
- a valve with the same task is arranged on the input side of the second inlet of the compression chamber expediently.
- These valves may advantageously be check valves.
- the piston pump for conveying the liquid is connected to the second inlet of the piston compressor.
- This piston pump which allows a very accurate fluid metering, so that exactly the amount of liquid required to fill the dead space and to cool the fluid can be pumped into the compression chamber of the reciprocating compressor is expediently designed to counteract the compression pressure prevailing in the compression chamber of the reciprocating compressor can.
- the working cycles of the reciprocating compressor and the piston pump are synchronized.
- the reciprocating compressor and / or the piston pump are preferably activated in such a way that when the reciprocating compressor performs a compression stroke, the piston pump simultaneously executes an expulsion cycle and pumps liquid into the compression chamber of the reciprocating compressor and the piston pump then, when the reciprocating compressor sucks the fluid to be compressed, at the same time also performs an intake stroke and sucks in the liquid to be introduced in the compression chamber of the piston compressor from a liquid reservoir.
- an electrically driven screw drive forms the linear drive.
- a threaded spindle of the screw drive is translationally coupled in motion with the piston rod of the reciprocating compressor.
- a screwed on the threaded spindle, axially non-movable component is rotatably coupled to an electric drive motor.
- the screw drive is particularly advantageous a planetary roller screw, which allows the transmission of relatively high forces and high positioning accuracy of the threaded spindle.
- a screw drive can be provided with a translationally movable threaded spindle, wherein the threaded spindle at one end with the piston rod of the reciprocating compressor and at the other End is motion coupled with a piston rod of the piston pump.
- the piston compressor and the piston pump are designed and / or arranged such that in a translational movement of the threaded spindle of the piston compressor performs a compression stroke, while the piston pump performs an exhaust stroke and the piston compressor and the piston pump in a movement of the threaded spindle in the opposite direction in each case one intake stroke To run.
- the invention is particularly suitable for delivering CO 2 from a submarine.
- CO 2 contained in the inner air of the submarine or CO 2 , which accumulates in particular in the exhaled air of the crew of the submarine to bind in a suitable manner and then store in the submarine in designated storage or from the submarine to its external environment dissipate.
- the steam required to separate the CO 2 from the CO 2 binder is typically generated in an evaporator where the water is boiled.
- Advantageously condensate obtained in the evaporator is sucked by a pump and introduced into the compression chamber of the reciprocating compressor during the compression of the fluid from CO 2 and water vapor as the cooling liquid.
- the invention also relates to a submarine comprising at least one device according to one of claims 4 - 10.
- This device is used in the submarine to divert the resulting in the exhaled air of the crew of the submarine inside the submarine CO 2 in the outer environment of the submarine.
- the apparatus shown has a reciprocating compressor 2, in which a piston 4 for sucking and compressing a gaseous or liquid and gaseous components fluid is linearly displaceable in a cylinder 6.
- a supply line 10 opens into a compression chamber 12 of the reciprocating compressor 2. Via the feed line 10 and the inlet 8, a fluid in an intake stroke of the reciprocating compressor 2 can be sucked into its compression chamber 12 and then compressed there.
- FIG. 1 apparatus shown a piston pump 14 with a cylinder 16 in a linearly movable piston 18 arranged on.
- liquid 22 stored in a reservoir 20 is sucked into an abutment space 28 of the piston pump 14 via a supply line 24, which opens at an inlet 26 of the piston pump 14, and then discharged via an outlet 30 into a line 32.
- the line 32 opens at a formed on the compression chamber 12 of the reciprocating compressor 2 inlet 14. D. h., By means of the piston pump 14, liquid 22 is conveyed from the reservoir 20 into the compression chamber 12 of the reciprocating compressor 2, the manner and purpose This measure will be explained in more detail below.
- the reciprocating compressor 2 and the piston pump 14 are driven by a common drive. This is a driven by an electric motor 36 screw drive with a threaded spindle 38.
- the threaded spindle 38 is coupled at a first end with a piston rod 40 of the reciprocating compressor 2 and at the other end with a piston rod 42 of the piston pump 14 coupled in motion.
- the piston rod 42 of the piston pump 14 is guided through the discharge space 28 of the piston pump 14 to the piston 18.
- the volume of the discharge space 28 reduces to an annular gap around the piston rod 42 around.
- the threaded spindle 38 is movable by means of the electric motor 36 in a direction A and a direction B opposite thereto. Accordingly, the piston rod 40 with the piston 4 and the piston rod 42 with the piston 18 can be moved together in the directions A and B.
- the reciprocating compressor 2 and the piston pump 14 are designed and arranged such that they each perform an intake stroke when the threaded spindle 38 moves in the direction A, whereas during a movement of the threaded spindle 38 in the direction B the reciprocating compressor 2 performs a compression stroke and the piston pump 14 Run exhaust stroke.
- the electric motor 36 is controlled by a control device not shown in the drawing such that the threaded spindle 38 is moved in the direction B.
- the piston compressor 2 then performs a compression stroke, in which the previously sucked fluid is compressed in the compression chamber 12. In this case prevent the check valve 44 and disposed in the line 10 check valve 46, an outflow of the fluid from the compression chamber 12.
- the fluid is discharged via an outlet 48 formed on the compression chamber 12, to which a conduit 50 is connected, wherein a pretensioned check valve 52 is arranged in the conduit 50 only opens at the desired compression pressure.
- the piston pump 14 executes an exhaust stroke at the same time as the compression stroke of the reciprocating compressor 2, the liquid 22 contained in the ejection space 28 of the piston pump 14 is delivered to the compression space 12 of the reciprocating compressor 2 during the compression of the fluid.
- a check valve 54 arranged in the supply line 24 prevents a backflow of the liquid 22 into the supply line 24.
- the fluid in the compression chamber 12 is cooled by the liquid 22, so that the temperature rise during the compression with respect to a piston pump without supply of liquid is considerably lower.
- the liquid 22 fills the entire dead space in the compression space 12 of the reciprocating compressor 2. This and the cooling of the fluid in the compression chamber 12 allow the compression of the fluid to higher compression pressures than would be possible without the introduction of fluid into the compression chamber 12.
- a submarine 56 is shown.
- This submarine 56 has the in Fig. 1 illustrated device for compressing a gaseous or gaseous and liquid constituents fluid.
- a CO 2 binding device 58 is arranged. Via a line 60, the interior air of the submarine is directed into the CO 2 binding device 58.
- the CO 2 contained in the air is bound by a CO 2 binder 62 and the freed from the CO 2 air via a line 64 again directed into the interior of the submarine 56.
- the CO 2 binder 62 is regenerated by means of steam which dissolves the CO 2 from the CO 2 binder 62.
- the water vapor is provided by an evaporator 66 disposed in the submarine 56. Water is introduced into the evaporator 66 via a water inlet 68 and evaporated there. Subsequently, the steam is passed via a line 70 into the CO 2 binding device 58.
- the mixture of CO 2 and water vapor in the reciprocating compressor 2 must be compressed to a pressure which is greater than the ambient pressure of the submarine.
- the generation of such a pressure is made possible by introducing liquid into the compression chamber 12 of the piston compressor 2 during the compression of the mixture of CO 2 and water vapor.
- This condensate is fed to the piston pump 14.
- To drain the condensate from the evaporator 66 in the piston pump 14 which opens into the discharge chamber 28 of the piston pump 14 supply line 24 is connected to the evaporator 66.
- the condensate is sucked from the evaporator 66 and pumped in an exhaust stroke of the piston pump 14 via the line 32 into the compression chamber 12 of the reciprocating compressor 2.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Aviation & Aerospace Engineering (AREA)
- Compressor (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
Description
Die Erfindung betrifft eine Vorrichtung zum Verdichten eines gasförmigen oder aus gasförmigen und flüssigen Bestandteilen bestehenden Fluids mit den im Oberbegriff von Anspruch 1 angegebenen Merkmalen sowie ein Unterseeboot.The invention relates to a device for compressing a gaseous or consisting of gaseous and liquid components fluid having the features specified in the preamble of claim 1 and a submarine.
Zum Verdichten von Gasen werden häufig Kolbenverdichter eingesetzt. Allerdings weisen Kolbenverdichter in der Regel einen auch als schädlicher Raum bezeichneten Totraum auf, in dem sich nach dem Verdichtungstakt komprimiertes Gas befindet, das während des Ansaugtaktes des Kolbenverdichters expandiert und so zunächst ein Ansaugen von neuem Gas verhindert. Hierdurch wird der Wirkungsgrad von Kolbenverdichtern in erheblichem Maße verringert, wobei dieser Effekt mit steigendem Kompressionsdruck zunimmt.For compressing gases piston compressors are often used. However, reciprocating compressors generally have a dead space, also referred to as a harmful space, in which compressed gas is present after the compression stroke, which expands during the intake stroke of the reciprocating compressor and thus initially prevents aspiration of new gas. As a result, the efficiency of reciprocating compressors is significantly reduced, and this effect increases with increasing compression pressure.
Zudem verläuft die Verdichtung von Gasen polytrop, so dass die Temperatur in Verdichtern mit dem Verhältnis von Enddruck / Anfangsdruck steigt. Mit steigender Temperatur erhöht sich die zu leistende Verdichtungsarbeit. Dies und der zuvor angesprochene Totraum von Kolbenverdichtern führen dazu, dass es in der Regel nicht möglich ist, Gase, die auf einen vergleichsweise hohen Druck komprimiert werden sollen, in einem einstufigen Prozess in einem Kolbenverdichter zu verdichten. Daher ist es häufig erforderlich, den Druck eines Gases in mehreren hintereinander angeordneten Kolbenverdichtern schrittweise zu erhöhen, wobei das Gas zwischen den Verdichtungsschritten jeweils gekühlt wird.In addition, the compression of gases is polytropic, so that the temperature in compressors increases with the ratio of final pressure / initial pressure. As the temperature increases, the compression work to be performed increases. This and the above-mentioned dead space of reciprocating compressors mean that it is generally not possible to compress gases which are to be compressed to a comparatively high pressure in a single-stage process in a reciprocating compressor. Therefore, it is often necessary to gradually increase the pressure of a gas in a plurality of reciprocating piston compressors, wherein the gas is cooled in each case between the compression steps.
Diese Vorgehensweise ist zeitaufwändig und anlagentechnisch aufwöndig.This procedure is time-consuming and complex.
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Vor diesem Hintergrund liegt der Erfindung die Aufgabe zugrunde, eine Vorrichtung zum Verdichten eines gasförmigen oder aus gasförmigen und flüssigen Bestandteilen bestehenden Fluids zu schaffen, die die Verdichtung eines gasförmigen oder aus gasförmigen und flüssigen Bestandteilen bestehenden Fluids auf einen vergleichsweise hohen Druck bei einstufiger Prozessführung in einem Kolbenverdichter ermöglicht, wobei ein Kolbenverdichter der Vorrichtung schnell an unterschiedliche oder sich ändernde Verdichtungsaufgaben angepasst werden kann.Against this background, the present invention seeks to provide a device for compressing a gaseous or consisting of gaseous and liquid components fluid, the compression of a gaseous or gaseous and liquid constituents fluid to a relatively high pressure in a single-stage litigation in one Piston compressor allows, with a reciprocating compressor of the device can be adapted quickly to different or changing compaction tasks.
Diese Aufgabe wird durch eine Vorrichtung mit den in Anspruch 1 angegebenen Merkmalen gelöst wird. Vorteilhafte Weiterbildungen der Vorrichtung ergeben sich aus den Unteransprüchen, der nachfolgenden Beschreibung sowie der Zeichnung. Hierbei können gemäß der Erfindung die in den Unteransprüchen angegebenen Merkmale jeweils für sich oder in geeigneter Kombination die Vorrichtung nach Anspruch 1 weiter ausgestalten.This object is achieved by a device having the features specified in claim 1. Advantageous developments of the device will become apparent from the dependent claims, the following description and the drawings. In this case, according to the invention, the features specified in the dependent claims in each case by itself or in a suitable combination, the device of claim 1 further.
Die erfindungsgemäße Vorrichtung zum Verdichten eines gasförmigen oder aus gasförmigen und flüssigen Bestandteilen bestehenden Fluids weist einen Kolbenverdichter auf. Um das Fluid in dem Kolbenverdichter einstufig auf einen vergleichsweise hohen Druck verdichten zu können, weist die Vorrichtung Mittel zum Einleiten einer Flüssigkeit in einen Verdichtungsraum des Kolbenverdichters während des Verdichtens und eine Kolbenpumpe zum Fördern der Flüssigkeit auf. Demnach sind Fördermittel vorgesehen, mit der eine Flüssigkeit von einem Flüssigkeitsreservoir in den Verdichtungsraum des Kolbenverdichters gefördert wird. Darüber hinaus sind Steuermittel vorgesehen, die die Vorrichtung derart ansteuern, dass die Flüssigkeit während des Verdichtens des Fluids in den Verdichtungsraum des Kolbenverdichters eingeleitet wird.The inventive device for compressing a gaseous or consisting of gaseous and liquid components fluid has a reciprocating compressor. In order to be able to compress the fluid in the piston compressor in one stage to a comparatively high pressure, the device has means for introducing a fluid into a compression chamber of the piston compressor during the compression and a piston pump for conveying the fluid. Accordingly, conveying means are provided with which a liquid is conveyed from a liquid reservoir into the compression space of the reciprocating compressor. In addition, control means are provided which actuate the device such that the liquid is introduced during the compression of the fluid in the compression space of the reciprocating compressor.
Ziel dieser Ausgestaltung der erfindungsgemäßen Vorrichtung ist es, während des Verdichtens des Fluids in den Verdichtungsraum des Kolbenverdichters Flüssigkeit einzuleiten. Durch diese Maßnahme wird das in dem Verdichtungsraum befindliche Fluid während des Verdichtungsvorgangs gekühlt. Gleichzeitig wird nach dem Ende der Fluidverdichtung der in dem Verdichtungsraum vorhandene Totraum bei entsprechender Dosierung der in den Verdichtungsraum eingeleiteten Flüssigkeitsmenge vollständig mit der inkompressiblen Flüssigkeit gefüllt, so dass sich dann kein Gas mehr in dem Verdichtungsraum befindet und der Totraum quasi eliminiert ist. Die mit dem Totraum ansonsten verbundenen nachteiligen Effekte können daher bei dem erfindungsgemäßen Verfahren nicht auftreten. Durch die mit dem Einleiten der Flüssigkeit in den Verdichtungsraum bedingte Kühlung und die Eliminierung des Totraums ist es möglich, Gase in dem Kolbenverdichter in einem einstufigen Prozess auf einen vergleichsweise hohen Druck zu verdichten.The aim of this embodiment of the device according to the invention is, during the compression of the fluid in the compression space of the reciprocating compressor Initiate liquid. By this measure, the fluid in the compression chamber is cooled during the compression process. At the same time, after the end of the fluid compression, the dead space present in the compression chamber is completely filled with the incompressible liquid with appropriate metering of the quantity of liquid introduced into the compression chamber, so that then there is no more gas in the compression chamber and the dead space is virtually eliminated. The adverse effects otherwise associated with the dead space can therefore not occur in the method according to the invention. By cooling with the introduction of the liquid into the compression chamber and the elimination of the dead space, it is possible to compress gases in the reciprocating compressor in a one-stage process to a relatively high pressure.
Gemäß der Erfindung ist die Kolbenstange des Kolbenverdichters vorzugsweise mit einem stufenlos einstellbaren Linearantrieb bewegungsgekoppelt. Unter einem stufenlos einstellbaren Linearantrieb ist ein solcher Linearantrieb zu verstehen, bei dem der Bewegungsweg und die Bewegungsgeschwindigkeit eines translatorisch bewegbaren Bauteils des Linearantriebs, welches mit der Kolbenstange gekoppelt ist, übergangslos verändert werden können. Demzufolge sind an dem Kolbenverdichter während des Ansaugens und Verdichtens des Fluids auch der von dem Kolben des Kolbenverdichters zurückgelegte Weg und dessen Geschwindigkeit stufenlos einstellbar, so dass der Kolbenverdichter schnell an unterschiedliche oder sich ändernde Verdichtungsaufgaben angepasst werden kann.According to the invention, the piston rod of the reciprocating compressor is preferably coupled for movement with a continuously adjustable linear drive. Under a continuously adjustable linear drive is such a linear drive to understand, in which the movement path and the speed of movement of a translationally movable component of the linear drive, which is coupled to the piston rod, can be changed without transition. As a result, the path traveled by the piston of the reciprocating compressor and its speed are infinitely adjustable on the piston compressor during the suction and compression of the fluid, so that the reciprocating compressor can be adapted quickly to different or changing compaction tasks.
Der Verdichtungsraum des Kolbenverdichters weist zweckmäßigerweise neben einem ersten Einlass für das zu verdichtende Fluid auch einen zweiten Einlass zum Einleiten der Flüssigkeit auf. Eingangsseitig des ersten Einlasses des Verdichtungsraumes ist in üblicher Weise ein Ventil angeordnet, welches verhindert, dass das Fluid während des Verdichtungstaktes des Kolbenverdichters aus dessen Verdichtungsraum ausströmen kann. In ähnlicher Weise ist eingangsseitig des zweiten Einlasses des Verdichtungsraumes zweckmäßigerweise ein Ventil mit der gleichen Aufgabe angeordnet. Bei diesen Ventilen kann es sich vorteilhaft um Rückschlagventile handeln.The compression space of the reciprocating compressor expediently has, in addition to a first inlet for the fluid to be compressed, also a second inlet for introducing the liquid. On the input side of the first inlet of the compression chamber, a valve is arranged in the usual way, which prevents the fluid during the compression stroke of the piston compressor can flow out of the compression space. Similarly, a valve with the same task is arranged on the input side of the second inlet of the compression chamber expediently. These valves may advantageously be check valves.
Vorteilhaft ist an dem zweiten Einlass des Kolbenverdichters die Kolbenpumpe zum Fördern der Flüssigkeit angeschlossen. Diese Kolbenpumpe, die eine sehr genaue Flüssigkeitsdosierung ermöglicht, so dass in den Verdichtungsraum des Kolbenverdichters exakt die zum Auffüllen des Totraums und zur Kühlung des Fluids geforderte Flüssigkeitsmenge gepumpt werden kann, ist zweckmäßigerweise so ausgelegt, dass sie dem in dem Verdichtungsraum des Kolbenverdichters herrschenden Verdichtungsdruck entgegenwirken kann.Advantageously, the piston pump for conveying the liquid is connected to the second inlet of the piston compressor. This piston pump, which allows a very accurate fluid metering, so that exactly the amount of liquid required to fill the dead space and to cool the fluid can be pumped into the compression chamber of the reciprocating compressor is expediently designed to counteract the compression pressure prevailing in the compression chamber of the reciprocating compressor can.
Vorteilhaft sind die Arbeitstakte des Kolbenverdichters und der Kolbenpumpe synchronisiert. D. h. der Kolbenverdichter und/oder die Kolbenpumpe werden vorzugsweise derart angesteuert, dass die Kolbenpumpe dann, wenn der Kolbenverdichter einen Verdichtungstakt ausführt, zeitgleich einen Ausstoßtakt ausführt und Flüssigkeit in den Verdichtungsraum des Kolbenverdichters pumpt und die Kolbenpumpe dann, wenn der Kolbenverdichter das zu verdichtende Fluid ansaugt, zeitgleich ebenfalls einen Ansaugtakt ausführt und die in dem Verdichtungsraum des Kolbenverdichters einzuführende Flüssigkeit aus einem Flüssigkeitsreservoir ansaugt.Advantageously, the working cycles of the reciprocating compressor and the piston pump are synchronized. Ie. the reciprocating compressor and / or the piston pump are preferably activated in such a way that when the reciprocating compressor performs a compression stroke, the piston pump simultaneously executes an expulsion cycle and pumps liquid into the compression chamber of the reciprocating compressor and the piston pump then, when the reciprocating compressor sucks the fluid to be compressed, at the same time also performs an intake stroke and sucks in the liquid to be introduced in the compression chamber of the piston compressor from a liquid reservoir.
Vorzugsweise bildet ein elektrisch angetriebener Gewindetrieb den Linearantrieb. Hierbei ist eine Gewindespindel des Gewindetriebs translatorisch mit der Kolbenstange des Kolbenverdichters bewegungsgekoppelt. Ein auf der Gewindespindel aufgeschraubtes, axial nicht bewegbares Bauteil ist drehbeweglich mit einem elektrischen Antriebsmotor gekoppelt. Besonders vorteilhaft handelt es sich bei dem Gewindetrieb um einen Planetenrollengewindetrieb, der die Übertragung vergleichsweise hoher Kräfte und eine hohe Positioniergenauigkeit der Gewindespindel ermöglicht.Preferably, an electrically driven screw drive forms the linear drive. Here, a threaded spindle of the screw drive is translationally coupled in motion with the piston rod of the reciprocating compressor. A screwed on the threaded spindle, axially non-movable component is rotatably coupled to an electric drive motor. The screw drive is particularly advantageous a planetary roller screw, which allows the transmission of relatively high forces and high positioning accuracy of the threaded spindle.
Erfindungsgemäß weisen der Kolbenverdichter und die Kolbenpumpe einen gemeinsamen Antrieb auf. So kann beispielsweise ein Gewindetrieb mit einer translatorisch bewegbaren Gewindespindel vorgesehen sein, wobei die Gewindespindel an einem Ende mit der Kolbenstange des Kolbenverdichters und an dem anderen Ende mit einer Kolbenstange der Kolbenpumpe bewegungsgekoppelt ist. Hierbei sind der Kolbenverdichter und die Kolbenpumpe so ausgebildet und/oder angeordnet, dass bei einer translatorischen Bewegung der Gewindespindel der Kolbenverdichter einen Verdichtungstakt ausführt, während die Kolbenpumpe einen Ausstoßtakt ausführt und der Kolbenverdichter und die Kolbenpumpe bei einer Bewegung der Gewindespindel in entgegengesetzter Richtung jeweils einen Ansaugtakt ausführen.According to the piston compressor and the piston pump to a common drive. For example, a screw drive can be provided with a translationally movable threaded spindle, wherein the threaded spindle at one end with the piston rod of the reciprocating compressor and at the other End is motion coupled with a piston rod of the piston pump. In this case, the piston compressor and the piston pump are designed and / or arranged such that in a translational movement of the threaded spindle of the piston compressor performs a compression stroke, while the piston pump performs an exhaust stroke and the piston compressor and the piston pump in a movement of the threaded spindle in the opposite direction in each case one intake stroke To run.
Die Erfindung eignet sich besonders zum Ausbringen von CO2 aus einem Unterseeboot. In Unterseebooten ist es erforderlich, während einer Tauchfahrt das in der Innenluft des Unterseeboots enthaltene Kohlendioxid bzw. CO2, das insbesondere in der Ausatemluft der Mannschaft des Unterseeboots anfällt, in geeigneter Weise zu binden und dann in dem Unterseeboot in hierfür vorgesehenen Speichern zu speichern oder aus dem Unterseeboot an dessen Außenumgebung abzuführen.The invention is particularly suitable for delivering CO 2 from a submarine. In submarines it is necessary during a dive trip the carbon dioxide contained in the inner air of the submarine or CO 2 , which accumulates in particular in the exhaled air of the crew of the submarine to bind in a suitable manner and then store in the submarine in designated storage or from the submarine to its external environment dissipate.
Aus
Der zum Trennen des CO2 von dem CO2-Bindemittel erforderliche Wasserdampf wird in der Regel in einem Verdampfer erzeugt, in dem das Wasser zum Sieden gebracht wird. Vorteilhaft wird in dem Verdampfer anfallendes Kondensat von einer Pumpe angesaugt und in den Verdichtungsraum des Kolbenverdichters während des Verdichtens des Fluids aus CO2 und Wasserdampf als Kühlflüssigkeit eingeleitet.The steam required to separate the CO 2 from the CO 2 binder is typically generated in an evaporator where the water is boiled. Advantageously condensate obtained in the evaporator is sucked by a pump and introduced into the compression chamber of the reciprocating compressor during the compression of the fluid from CO 2 and water vapor as the cooling liquid.
Insofern betrifft die Erfindung auch ein Unterseeboot, das mindestens eine Vorrichtung nach einem der Ansprüche 4 - 10 aufweist. Diese Vorrichtung dient in dem Unterseeboot dazu, das in der Ausatemluft der Mannschaft des Unterseeboots im Inneren des Unterseeboots entstehende CO2 in die Außenumgebung des Unterseeboots abzuleiten.In this respect, the invention also relates to a submarine comprising at least one device according to one of claims 4 - 10. This device is used in the submarine to divert the resulting in the exhaled air of the crew of the submarine inside the submarine CO 2 in the outer environment of the submarine.
Nachfolgend ist die Erfindung anhand von in der Zeichnung dargestellten Ausführungsbeispielen näher erläutert. In der Zeichnung zeigt:
- Fig. 1
- eine Vorrichtung zum Verdichten eines gasförmigen oder aus gasförmigen und flüssigen Bestandteilen bestehenden Fluids in einer schematisch stark vereinfachten Prinzipskizze und
- Fig. 2
- ein Unterseeboot mit der Vorrichtung nach
Fig. 1 in einer schematisch stark vereinfachten Prinzipskizze.
- Fig. 1
- a device for compressing a gaseous or gaseous and liquid constituents fluid in a schematically simplified schematic diagram and
- Fig. 2
- a submarine with the device behind
Fig. 1 in a schematically simplified schematic diagram.
Die in
Des Weiteren weist die in
Die Leitung 32 mündet an einem an dem Verdichtungsraum 12 des Kolbenverdichters 2 ausgebildeten Einlass 14. D. h., mittels der Kolbenpumpe 14 wird Flüssigkeit 22 aus dem Reservoir 20 in den Verdichtungsraum 12 des Kolbenverdichters 2 gefördert, wobei die Art und Weise sowie der Zweck dieser Maßnahme im weiteren Verlauf näher erläutert wird.The
Der Kolbenverdichter 2 und die Kolbenpumpe 14 werden von einem gemeinsamen Antrieb angetrieben. Hierbei handelt es sich um einen von einem Elektromotor 36 angetriebenen Gewindetrieb mit einer Gewindespindel 38. Die Gewindespindel 38 ist an einem ersten Ende mit einer Kolbenstange 40 des Kolbenverdichters 2 bewegungsgekoppelt und an dem anderen Ende mit einer Kolbenstange 42 der Kolbenpumpe 14 bewegungsgekoppelt.The
Die Kolbenstange 42 der Kolbenpumpe 14 wird durch den Ausstoßraum 28 der Kolbenpumpe 14 zu dem Kolben 18 geführt. Hierdurch und aufgrund des vergleichsweise großen Durchmessers der Kolbenstange 14 verringert sich das Volumen des Ausstoßraumes 28 auf einen Ringspalt um die Kolbenstange 42 herum.The
Die Gewindespindel 38 ist mittels des Elektromotors 36 in eine Richtung A und eine hierzu entgegengesetzte Richtung B verfahrbar. Entsprechend sind die Kolbenstange 40 mit dem Kolben 4 und die Kolbenstange 42 mit dem Kolben 18 gemeinsam in die Richtungen A und B verfahrbar. Der Kolbenverdichter 2 und die Kolbenpumpe 14 sind derart ausgebildet und angeordnet, dass sie bei einer Bewegung der Gewindespindel 38 in Richtung A beide jeweils einen Ansaugtakt ausführen, während bei einer Bewegung der Gewindespindel 38 in Richtung B der Kolbenverdichter 2 einen Verdichtungstakt und die Kolbenpumpe 14 einen Ausstoßtakt ausführen.The threaded
Die Funktionsweise der in
Wird die Gewindespindel 38von dem Elektromotor 36 in Richtung A angetrieben, führt der Kolbenverdichter 2 einen Ansaugtakt aus, bei dem ein gasförmiges oder aus gasförmigen und flüssigen Bestandteilen bestehendes Fluid inden Verdichtungsraum 12der Kolbenpumpe 14 über die Leitung 10 angesaugt wird. Hierbei wird der andem Verdichtungsraum 12 ausgebildete zweite Einlass 34 von einem inder Leitung 30 angeordneten Rückschlagventil 44 verschlossen. Gleichzeitig führt dieKolbenpumpe 14 einen Ansaugtakt aus, bei dem die indem Reservoir 20befindliche Flüssigkeit 22 inden Ausstoßraum 28 der Kolbenpumpe gesaugt wird.
- If the threaded
spindle 38 is driven by theelectric motor 36 in the direction A, thereciprocating compressor 2 performs an intake stroke in which a gaseous or gaseous and liquid components existing fluid is sucked into thecompression chamber 12 of thepiston pump 14 via theline 10. In this case, thesecond inlet 34 formed on thecompression chamber 12 is closed by acheck valve 44 arranged in theline 30. At the same time, thepiston pump 14 performs an intake stroke in which the liquid 22 in thereservoir 20 is sucked into thedischarge space 28 of the piston pump.
Anschließend wird der Elektromotor 36 von einer in der Zeichnung nicht dargestellten Steuerungsvorrichtung derart angesteuert, dass die Gewindespindel 38 in Richtung B bewegt wird. Der Kolbenverdichter 2 führt dann einen Verdichtungstakt aus, bei dem das zuvor angesaugte Fluid in dem Verdichtungsraum 12 verdichtet wird. Hierbei verhindern das Rückschlagventil 44 und ein in der Leitung 10 angeordnetes Rückschlagventil 46 ein Ausströmen des Fluids aus dem Verdichtungsraum 12. Sobald sich in dem Verdichtungsraum 12 ein gewünschter Verdichtungsdruck eingestellt hat, wird das Fluid über einen an dem Verdichtungsraum 12 ausgebildeten Auslass 48, an dem eine Leitung 50 angeschlossen ist, abgelassen, wobei in der Leitung 50 ein vorgespanntes Rückschlagventil 52 angeordnet ist, das erst bei dem gewünschten Verdichtungsdruck öffnet.Subsequently, the
Da die Kolbenpumpe 14 zeitgleich mit dem Verdichtungstakt des Kolbenverdichters 2 einen Ausstoßtakt ausführt, wird die in dem Ausstoßraum 28 der Kolbenpumpe 14 befindliche Flüssigkeit 22 während des Verdichtens des Fluids in den Verdichtungsraum 12 des Kolbenverdichters 2 gefördert. Hierbei verhindert ein in der Zuführleitung 24 angeordnetes Rückschlagventil 54 ein Zurückströmen der Flüssigkeit 22 in die Zuführleitung 24.Since the
Indem dem Verdichtungsraum 12 des Kolbenverdichters 2 während des Verdichtungstaktes die Flüssigkeit 22 zugeführt wird, wird das in dem Verdichtungsraum 12 befindliche Fluid von der Flüssigkeit 22 gekühlt, so dass der Temperaturanstieg während des Verdichtens gegenüber einer Kolbenpumpe ohne Zuführung von Flüssigkeit erheblich geringer ausfällt. Darüber hinaus füllt die Flüssigkeit 22 nach dem Öffnen des Rückschlagventils 52, wenn sich der Kolben 4 in seinem Totpunkt befindet, den gesamten Totraum in dem Verdichtungsraum 12 des Kolbenverdichters 2 auf. Dies und die Kühlung des in dem Verdichtungsraum 12 befindlichen Fluids ermöglichen die Verdichtung des Fluids auf höhere Verdichtungsdrücke, als es ohne die Einleitung von Flüssigkeit in den Verdichtungsraum 12 möglich wäre.By supplying the liquid 22 to the
In
Das CO2-Bindemittel 62 wird mittels Wasserdampf, der das CO2 von dem CO2-Bindemittel 62 löst, regeneriert. Der Wasserdampf wird von einem in dem Unterseeboot 56 angeordneten Verdampfer 66 bereitgestellt. Über einen Wassereinlass 68 wird Wasser in den Verdampfer 66 eingeleitet und dort verdampft. Anschließend wird der Wasserdampf über eine Leitung 70 in die CO2-Bindeeinrichtung 58 geleitet.The CO 2 binder 62 is regenerated by means of steam which dissolves the CO 2 from the CO 2 binder 62. The water vapor is provided by an
Nach dem Regenerieren des CO2-Bindemittels 62 befindet sich in der CO2-Bindeeinrichtung 58 ein Gemisch aus CO2 und Wasserdampf. Dieses Gemisch wird über die an der CO2-Bindeeinrichtung 58 angeschlossene Zuführleitung 10 bei einem Ansaugtakt des Kolbenverdichters 2 in dessen Verdichtungsraum 12 geleitet, dort verdichtet und über die Leitung 50 in eine seewasserdurchflutete Leitung 72 geleitet. Von dort gelangt das Gemisch aus CO2 und Wasserdampf in die Außenumgebung des Unterseebootes 56.After the regeneration of the CO 2 binder 62 is in the CO 2 binder 58, a mixture of CO 2 and water vapor. This mixture is passed through the connected to the CO 2 binding device 58
Um das Gemisch aus CO2 und Wasserdampf bei Tauchfahrt des Unterseebootes 56 aus diesem auslassen zu können, muss das Gemisch aus CO2 und Wasserdampf in dem Kolbenverdichter 2 auf einen Druck verdichtet werden, der größer als der Umgebungsdruck des Unterseebootes ist. Die Erzeugung eines solchen Druckes wird dadurch möglich, dass während des Verdichtens des Gemisches aus CO2 und Wasserdampf Flüssigkeit in den Verdichtungsraum 12 des Kolbenverdichters 2 eingeführt wird. Als Flüssigkeit wird ein Kondensat verwendet, das sich am Boden des Verdampfers 66 sammelt. Dieses Kondensat wird der Kolbenpumpe 14 zugeführt. Zum Ableiten des Kondensats aus dem Verdampfer 66 in die Kolbenpumpe 14 ist die in den Ausstoßraum 28 der Kolbenpumpe 14 mündende Zuführleitung 24 an den Verdampfer 66 angeschlossen. Mittels der Kolbenpumpe 14 wird das Kondensat aus dem Verdampfer 66 angesaugt und in einem Ausstoßtakt der Kolbenpumpe 14 über die Leitung 32 in den Verdichtungsraum 12 des Kolbenverdichters 2 gepumpt.In order to be able to discharge the mixture of CO 2 and water vapor during
- 22
- - Kolbenverdichter- Piston compressor
- 44
- - Kolben- Piston
- 66
- - Zylinder- Cylinder
- 88th
- - Einlass- inlet
- 1010
- - Zuführleitung- Feed line
- 1212
- - Verdichtungsraum- Compaction space
- 1414
- - Kolbenpumpe- Piston pump
- 1616
- - Zylinder- Cylinder
- 1818
- - Kolben- Piston
- 2020
- - Reservoir- Reservoir
- 2222
- - Flüssigkeit- Liquid
- 2424
- - Zuführleitung- Feed line
- 2626
- - Einlass- inlet
- 2828
- - Ausstoßraum- discharge space
- 3030
- - Auslass- outlet
- 3232
- - Leitung- Management
- 3434
- - Einlass- inlet
- 3636
- - Elektromotor- electric motor
- 3838
- - Gewindespindel- threaded spindle
- 4040
- - Kolbenstange- piston rod
- 4242
- - Kolbenstange- piston rod
- 4444
- - Rückschlagventil- Check valve
- 4646
- - Rückschlagventil- Check valve
- 4848
- - Auslass- outlet
- 5050
- - Leitung- Management
- 5252
- - Rückschlagventil- Check valve
- 5454
- - Rückschlagventil- Check valve
- 5656
- - Unterseeboot- Submarine
- 5858
- - CO2-Bindeeinrichtung- CO 2 binding device
- 6060
- - Leitung- Management
- 6262
- - CO2-Bindemittel- CO 2 binders
- 6464
- - Leitung- Management
- 6666
- - Verdampfer- Evaporator
- 6868
- - Wassereinlass- Water intake
- 7070
- - Leitung- Management
- 7272
- - Leitung- Management
- AA
- - Richtung- Direction
- BB
- - Richtung- Direction
Claims (5)
- A device for compressing a gaseous fluid or a fluid consisting of gaseous and fluid components, with a piston compressor (2), with means for introducing a fluid (22) into a compressing space (12) of the piston compressor (2) during the compressing, and with a piston pump (14) for delivering fluid, characterised in that a piston rod (40) of the piston compressor (2) is coupled in movement to an infinitely settable linear drive, wherein the linear drive drives the piston compressor (2) together with the piston pump (14).
- A method according to claim 1, characterised in that the compressor space (12) comprises a first inlet (8) for the fluid to be compressed and a second inlet (34) for introducing the fluid (22).
- A device according to claim 2, characterised in that the piston pump (14) for delivering the fluid is connected on the second inlet (34) of the piston compressor (2).
- A device according to one of the preceding claims, characterised in that an electrically driven screw drive forms the linear drive.
- A submarine (54), characterised in that the submarine (56) comprises at least one device according to one of the claims 1 to 4, for leading a gaseous fluid out of the submarine (56).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL12190384T PL2594795T3 (en) | 2011-11-16 | 2012-10-29 | Device for compressing a gas or a fluid comprising gaseous and liquid components, and a submarine boat containing such a device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102011086441A DE102011086441A1 (en) | 2011-11-16 | 2011-11-16 | Method for compressing a gaseous or gaseous and liquid constituent fluid and device for compressing a gaseous or gaseous and liquid constituent fluid |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2594795A1 EP2594795A1 (en) | 2013-05-22 |
EP2594795B1 true EP2594795B1 (en) | 2015-06-03 |
Family
ID=47143601
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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EP12190384.3A Active EP2594795B1 (en) | 2011-11-16 | 2012-10-29 | Device for compressing a gas or a fluid comprising gaseous and liquid components, and a submarine boat containing such a device |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP2594795B1 (en) |
DE (1) | DE102011086441A1 (en) |
ES (1) | ES2544536T3 (en) |
PL (1) | PL2594795T3 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
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DE102014212584A1 (en) * | 2014-06-30 | 2015-12-31 | Thyssenkrupp Ag | Device for discharging gas from a submarine |
DE102019217200A1 (en) * | 2019-05-26 | 2020-11-26 | Robert Bosch Gmbh | Method for operating a fuel system, prefeed pump and fuel system |
DE102022001448A1 (en) | 2022-04-14 | 2023-10-19 | Borsig Zm Compression Gmbh | Piston compressor |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE296367C (en) * | ||||
DE357858C (en) * | 1915-02-20 | 1922-09-01 | Handel Mij Rohta | Method and device for cooling air and gas compressors |
GB455829A (en) * | 1935-12-20 | 1936-10-28 | Edward Zahm | Cooling means for gas compressors |
US2404660A (en) * | 1943-08-26 | 1946-07-23 | Wilfred J Rouleau | Air compressor |
DE2404810A1 (en) * | 1974-02-01 | 1975-08-21 | Worthington Gmbh Deutsche | Electrical linear motor driven displacement pump - has rotor coupled directly to piston |
US20050042111A1 (en) * | 2003-02-05 | 2005-02-24 | Zaiser Lenoir E. | Fluid pump |
DE102004052168A1 (en) * | 2004-10-27 | 2006-05-04 | Compart Compressor Technology Gmbh & Co. Kg | Reciprocating engine for compressing gas, has linear motor utilized as linear drive, where reciprocating engine is driven by linear drive and not by crank drive or fluid, and can be operated with or without lubrication |
DE102006053923B4 (en) * | 2005-10-11 | 2008-09-11 | Neander Motors Ag | Piston machine |
DE102006048716B3 (en) | 2006-10-14 | 2008-02-21 | Howaldswerke Deutsche Werft Ag | Submarine boat comprises carbon dioxide binding unit for binding carbon dioxide contained in air inside submarine, where binding unit has carbon dioxide binding medium, and steam generator is provided for producing water vapors |
DE102008003982B3 (en) * | 2008-01-11 | 2009-07-02 | Gabler Maschinenbau Gmbh | Pressure-bodyless submarine vehicle, has cylinder with gas-filled cylinder chamber containing gas-filled volume that is changeable by controlling of piston, where volume is limited by piston movably guided in cylinder |
DE102009040379B3 (en) * | 2009-09-07 | 2011-07-28 | Howaldtswerke-Deutsche Werft GmbH, 24143 | Submarine with a compressor |
-
2011
- 2011-11-16 DE DE102011086441A patent/DE102011086441A1/en not_active Withdrawn
-
2012
- 2012-10-29 ES ES12190384.3T patent/ES2544536T3/en active Active
- 2012-10-29 EP EP12190384.3A patent/EP2594795B1/en active Active
- 2012-10-29 PL PL12190384T patent/PL2594795T3/en unknown
Also Published As
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PL2594795T3 (en) | 2015-11-30 |
ES2544536T3 (en) | 2015-09-01 |
EP2594795A1 (en) | 2013-05-22 |
DE102011086441A1 (en) | 2013-05-16 |
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