EP3091203B1 - Speicher zur aufnahme eines kondensierten arbeitsfluids eines organischen rankine kreislaufsystems - Google Patents

Speicher zur aufnahme eines kondensierten arbeitsfluids eines organischen rankine kreislaufsystems Download PDF

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Publication number
EP3091203B1
EP3091203B1 EP16167519.4A EP16167519A EP3091203B1 EP 3091203 B1 EP3091203 B1 EP 3091203B1 EP 16167519 A EP16167519 A EP 16167519A EP 3091203 B1 EP3091203 B1 EP 3091203B1
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Prior art keywords
reservoir
port
working fluid
rankine cycle
distribution
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English (en)
French (fr)
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EP3091203A1 (de
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Marco Giuseppe Francesco FLORIS
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Kaymacor Srl
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Kaymacor Srl
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K9/00—Plants characterised by condensers arranged or modified to co-operate with the engines
    • F01K9/02—Arrangements or modifications of condensate or air pumps

Definitions

  • the present invention relates to organic Rankine cycle (ORC) systems, in particular to reservoirs for receiving a condensed working fluid, which are commonly known as "receivers".
  • ORC organic Rankine cycle
  • An organic Rankine cycle uses a working fluid of an organic nature, unlike a common Rankine cycle with superheated steam.
  • Document CN102230401B discloses for example an organic Rankine cycle.
  • the reference number 1* designates as a whole an example of organic Rankine cycle system of a known type.
  • the system 1* includes a receiver 2*, a pump 4*, a heat exchanger 6, an evaporator 8, an expander 10, an electric generator 12 mechanically connected to the expander 10, and a condenser unit 14.
  • the receiver 2* includes an inlet port 2IN* configured for receiving condensed working fluid from the condenser unit 14, and a discharge port 2OUT* in fluid communication with the intake port of the pump 4*.
  • a delivery port of the pump 4* is, instead, in fluid communication with a first inlet port 6LIN of the heat exchanger 6, whereas a first outlet port 6LOUT of the heat exchanger 6 is in fluid communication with a first inlet port 8LIN of the evaporator 8.
  • a first outlet port of the evaporator 8, designated by the reference 8LOUT, is in turn in fluid communication with an intake port 10IN of the expander 10, whereas a discharge port 10OUT of the expander 10 is in fluid communication with a second inlet port 6GIN of the heat exchanger 6.
  • a second outlet port 6GOUT of the heat exchanger 6 is in turn in fluid communication with an inlet port 14IN of the condenser unit 14, whereas a discharge port 14OUT of the unit 14 is in fluid communication with the inlet port 2IN*.
  • the two pairs of inlet and outlet ports of the heat exchanger 6 and of the evaporator 8 constitute the ends of two flow paths.
  • the first flow path develops between the ports 6LIN and 6LOUT
  • the second flow path develops between the ports 6GIN and 6GOUT.
  • the two flow paths are in relation of heat exchange with one another.
  • the first flow path within the evaporator 8 is defined between the ports 8LIN and 8LOUT, whereas the second flow path is defined between a second inlet port 8HSIN and a second outlet port 8HSOUT, which are traversed by a thermovector fluid HS.
  • the two flow paths are in relation of heat exchange with one another.
  • the working fluid in the liquid phase processed by the pump 4* enters the first flow path of the heat exchanger 6 through the port 6LIN, where it is pre-heated thanks to the heat exchange with the fluid that flows in the second flow path of the heat exchanger 6.
  • the pre-heated fluid then exits from the heat exchanger 6 in the liquid phase through the outlet port 6LOUT and enters the first flow path of the evaporator 8 through the port 8IN.
  • the working fluid passes into the gaseous phase, and exits through the port 8OUT.
  • the reference L identifies the stretches of the system 1* in which working fluid in the liquid phase flows
  • the reference G identifies the stretches of the system 1* in which working fluid in gaseous phase flows.
  • the letters G and L appearing in the references that designate the working ports of the components of the system in which biphasic fluid flows or two monophasic fluids flow indicate the physical state of the fluid at the port in question.
  • the working fluid in the gaseous phase is sent through the port 8OUT to the inlet 10IN of the expander 10 for conversion of the thermal energy of the fluid into mechanical energy, and hence into electrical energy via the generator 12.
  • the flow rate of gaseous working fluid discharged by the expander 10 through the port 10 OUT then enters the second flow path of the heat exchanger 6 through the port 6GIN, pre-heats the working fluid in the liquid phase in the first flow path of the heat exchanger 6, and exits through the port 6GOUT. From here, the working fluid (still in the gaseous phase) enters the condenser unit 14, by which it is condensed and brought back into the liquid phase, after which, at outlet from the unit 14, the condensed working fluid, which is hence in the liquid phase, is accumulated within the receiver 2, which constitutes a safe intake environment for the pump 4 in so far as the accumulation of fluid therein prevents phenomena of cavitation at intake.
  • the configuration of the system 1* presents, however, a drawback that cannot be eliminates and consists in leakage of working fluid in the liquid phase through the pump 4*.
  • the organic fluids used as working fluid in systems of this type are generally characterized by very low values of viscosity, and are hence very liable to infiltrate through the gaps that are inevitably present in the pump 4*.
  • the object of the present invention is to solve the technical problems mentioned previously.
  • the object of the present invention is to simplify production of the pump that takes in the condensed working fluid of the receiver, at the same time eliminating the problem of leakage of working fluid.
  • a reservoir, or receiver for the reception of a condensed working fluid of an organic Rankine cycle system, the reservoir including an internal volume, an inlet port for the intake of condensed working fluid into the internal volume, and an outlet port for the condensed working fluid, the reservoir being characterized in that it includes a pump housed in said internal volume, said pump having an intake port for the withdrawal of said condensed working fluid from said internal volume and a delivery port for the delivery of said working fluid through said outlet port of the reservoir.
  • an organic Rankine cycle system including a reservoir according to the invention like the one just been described.
  • the system 1 differs from the system 1* in that it comprises a reservoir (receiver) 2 for receiving a condensed working fluid, which includes an internal volume, an inlet port 2IN for entry of the condensed working fluid into the internal volume and an outlet port for exit of the condensed working fluid, and houses a pump 4 within the internal volume.
  • the pump 4 includes an intake port 4IN configured for intake of condensed working fluid from the internal volume of the reservoir and a delivery port 4OUT, which is configured for sending condensed working fluid through the outlet port 2OUT of the reservoir 2.
  • the reservoir 2 includes a first end plate 16, a second end plate 18, and a wall 20, the latter having a cylindrical shape and preferably being made integral with the second end plate 18 (this hence means that the end plates 16, 18 are circular and that the shape of the reservoir 2 is as a whole cylindrical).
  • the internal volume of the reservoir 2 is delimited by the end plates 16, 18 and by the wall 20.
  • the inlet port 2IN is provided in the end plate 18, whereas the outlet port 2OUT is provided in the end plate 16.
  • the end plate 16 includes a central relief 22 having a circular shape and preferably provided with radial lobes 24A, which have a respective threaded hole configured for receiving a corresponding fixing screw, as will be described hereinafter.
  • central relief 22 Provided moreover in the central relief 22 are two distribution ports of the pump 4, in particular an intake port I22 (not visible in the cross-sectional view of Figure 6 ) in communication with the internal volume of the reservoir 2, and a delivery port D22, which is in direct fluid communication with the outlet port 2OUT.
  • the intake and delivery ports I22, D22 on the central relief 22 of the end plate 18 form part of a distribution assembly of the pump 4, as will be described hereinafter.
  • a manifold 28 from which there departs a tube 30 ( Figure 6 ), which functionally prolongs the outlet port 2 beyond the top of the end plate 18. It should be noted in fact that the orientation of the reservoir 2 as installed within the system 1 is the one illustrated in Figure 6 .
  • the pump 4 includes an electric motor 32 having a rotor that turns about an axis of rotation X4 and is connected in rotation to an output shaft 33, which also is coaxial to the axis X4.
  • the pump 4 moreover includes a plurality of distribution plates, which, together with the end plate 16 (in particular, at the central relief 22) define a distribution assembly of the pump 4, which enables management of intake and delivery of the condensed working fluid coming from the internal volume of the reservoir 2.
  • the plurality of distribution plates includes a first distribution plate 34, a second distribution plate 36, and a third distribution plate 38.
  • the distribution plate 34 is received in a seat having a complementary shape provided on the plate 34 and designated by the reference 39.
  • an eccentric annular plate 40 that includes a hole 40A, which is coaxial to the axis X4 and with respect to which the plate is positioned eccentrically.
  • the hole 40A houses inside it a rotor assembly 42 of the pump 4.
  • the rotor assembly 42 is of the internal-gear type and includes an external rotor 44, which has a diameter that is substantially the same as that of the hole 40A (except for the clearance necessary for assembly and operation) and is set in an eccentric position with respect to the axis X4, an internal rotor 46, which is set sharing the axis X4, and a crescent-shaped element 48 between the (internal and external) toothings of the two rotors 44, 46.
  • the internal rotor 46 is connected in rotation to the shaft 33 of the motor 32.
  • a closing cup 50 (possibly provided with radial openings) is coupled to the plate 34 so as to enclose the motor 32 and secure it on the plate 34.
  • the cup 50 is preferentially secured to the plate 34 by means of a threaded joint between the two or a plurality of radial threaded grub-screws that engage in coinciding radial holes on the two plates.
  • Each of the distribution plates 34, 36, 38 carries a respective intake port I34, I36, I38, and a respective delivery port D34, D36, D38.
  • both of the intake and delivery ports I34 and D34 are "false ports", i.e., they are blind ports.
  • the plate 34 moreover includes a ring of radial holes 34IN configured for establishing a fluid communication between the internal volume of the reservoir and the inside of the plate 34 itself so as to carry the organic working fluid in an optimal way towards the motor 32.
  • all the distribution plates have a hole, which is coaxial tos the axis X4, for receiving the shaft 33.
  • FIG. 5 and Figure 6 illustrate the set of distribution plates in the assembled condition.
  • the shaft 33 traverses all the distribution plates, and all the distribution ports I34, I36, I38 and D34, D36, D38 are aligned (and collimated) with respect to one another.
  • the ensemble constituted by the distribution plates 34, 36, 38, the rotor assembly 42 (and plate 40), and the electric motor 32 packed between the plate 34 and the cup 50 is then fixed to the central relief 22 of the end plate 16 by means of screws 52 that engage in radial grooves on a flange F34 of the plate 34 and within the threaded holes provided in the lobes 24.
  • the intake ports I34 (which is blind), I36, and I38 are to be aligned and collimated with the intake port I22, whereas the delivery ports D34 (which is blind), D36, and D38 are aligned and collimated with the delivery port D22: in this way, as anticipated, it is the end plate 16 itself that forms part of the pump 4; in particular, it forms part of the distribution assembly thereof by means of the central relief 22.
  • the integration of the pump 4 with the reservoir 2 is not limited to the mere insertion of the former into the latter, but there is a true functional integration.
  • the organic working fluid in the liquid phase at outlet from the condenser unit 14 through the port 14OUT is received within the reservoir 2 through the inlet port 2IN.
  • the working fluid in the liquid phase flows into the internal volume of the reservoir 2 and submerges the ensemble constituted by the distribution plates and the electric motor 32 to an extent variable as a function of the accumulation of fluid in the internal volume.
  • the working fluid penetrates into the plate 34 through the holes 34IN, thus lapping the motor 32, guaranteeing optimal cooling thereof.
  • the holes 34IN co-operate only for the purposes of cooling of the motor 32 and do not co-operate with the distribution ports of the pump 4.
  • the working fluid laps the relief 22 and flows into the intake environment of the pump, i.e., the set of intake ports I22, I36, I38, I34, through the intake port I22, and likewise flows into the volume of the compartments of the rotors 44, 46 that faces the set of intake ports and is not occupied by teeth of one or other of the rotors.
  • the modalities with which the working fluid in the liquid phase is sent from the intake environment to the delivery environment are those common to operation of any internal-gear pump.
  • driving of the internal rotor 46 in rotation via the electric motor 32 also causes the external rotor 44 to be driven in rotation with respect to the hole 40A.
  • the working fluid that occupies the intake environment is moved by means of rotation of the rotors 44 and 46, occupying a free volume of the compartments of the rotors 44, 46 that faces the set of intake ports (which functionally constitutes the intake port 4IN), this free volume progressively increasing in the direction of rotation.
  • the working fluid is hence confined between the crescent-shaped element 48, the compartments between the teeth of the rotors 46 and 44 that are located in a position corresponding to the crescent-shaped element 48, and the plates 36, 38.
  • the volume of fluid moved by the rotors 44, 46 exceeds the crescent-shaped element 48, it is sent towards the delivery environment, i.e., the set of delivery ports D34, D36, D38, D22 and the volume of the compartments of the rotors 44, 46 that faces the set of delivery ports and is not occupied by teeth of one or other of the rotors.
  • the fluid is then sent on to the outlet port 2OUT of the reservoir 2, in particular through the port D22.
  • Provision of the blind delivery port D34 enables equalization of the pressure at the opposite faces of the rotors 44, 46 that face the delivery environment.
  • the delivery pressure (imposed by the circuit of the system 1) is applied on both faces of the rotors 44, 46, hydraulically balancing the system.
  • blind intake port I34 it mainly has the function of rendering uniform distribution of the fluid at the intake of the pump 4 straddling the rotors 44, 46 so as to prevent as much as possible onset of cavitation phenomena.
  • the working fluid in the liquid phase follows the same cycle that has already been described with reference to Figure 1A : in particular, it enters, in the liquid phase, the first flow path of the heat exchanger 6 (entry at 6LIN), exits therefrom in pre-heated conditions (but still in the liquid phase) from the port 6LOUT, and enters the first flow path of the evaporator 8 (entry at 8LIN). From here, the fluid exits in the gaseous phase through the port 8LOUT thanks to the heat exchange with the thermovector fluid HS that flows in the second flow path (entry at 8HSIN, exit at 8HSOUT).
  • the working fluid in the gaseous phase proceeds towards the inlet 10IN of the expander 10, exits through the discharge port 10OUT, and enters the second flow path of the heat exchanger 6 (entry at 6GIN, exit at 6GOUT) yielding heat to the fluid that flows in the first flow path, so pre-heating it.
  • Expansion of the working fluid in the expander 10 enables conversion of the mechanical energy transferred to the shaft of the expander 10 into electrical energy by means of the generator 12.
  • the fluid still in the gaseous phase, is then sent to the condenser unit 14 (entry at 14IN), by which it is condensed in the liquid phase and sent on, through the port 14OUT, to the reservoir 2 through the port 2IN.
  • the reservoir 2 according to the present invention hence enables solution of the technical problems of the systems and pumps of a known type, even introducing further advantages.
  • the electric motor 32 that drives in rotation the rotor assembly of the pump 4 is free from problems of cooling, even in conditions of high power absorbed by the pump 4, in so far as the condensed fluid within the reservoir 2 functions as coolant for the motor 32, which is itself immersed in the fluid in the liquid phase.
  • cooling of the motor 32 by means of the working fluid in the liquid phase enables recovery of thermal energy, which would otherwise be dissipated, and reduction of the workload of the heat exchanger 6 in so far as the fluid that laps the motor 32 is already to a certain extent pre-heated.
  • the inventors have advantageously noted that, for some systems, there may exist a particular convenience in arranging both the inlet port 2IN and the discharge port 2OUT at the end plate 16 of the reservoir 2', which, in addition to performing the functions of distribution plate for the pump 4, also functions as intake manifold for the condensed working fluid at inlet to the reservoir 2'.
  • the end plate 16 by means of a common commercially available disk element or cup-shaped element welded to the wall 20.
  • the relief 22 would be absent, and the delivery and intake ports of the pump obtained thereon would be provided on the distribution plate 38 (ports 4IN and 4OUT).
  • the latter may be in turn fixed (for example with O-rings) on an internal flange welded on the end plate of a commercial type. On the flange there must of course be provided at least one hole for delivery of the working fluid.
  • the pump 4 is in effect completely independent; i.e., it could hypothetically function also taken by itself, without having any need of the end plate 16 for defining the distribution ports.
  • the only integration between the pump and the end plate envisaged in this case is fixing of the former to the latter.
  • the distribution plate of the pump 4 is in this case single (only the plate 38 is present) in so far as the plates 36 and 40 are integrated and perform the function that was performed by the plate 40 alone, whereas the plate 34, as described, becomes a pure and simple receptacle. Consequently, all the distribution ports on the plate 38 are functional; i.e., there is no blind port as on the plate 34 of the embodiments illustrated in Figures 1 to 7 .
  • the reservoir 2" includes a first end plate 16", a second end plate 18", and a wall 20", the latter having a cylindrical shape and being provided integral with the second end plate 18 or else carried thereon (this hence means that the end plates 16, 18 are circular and the shape of the reservoir 2" is as overall cylindrical).
  • the internal volume of the reservoir 2" is delimited by the end plates 16", 18" and by the wall 20".
  • the distribution assembly of the pump 4" is here provided entirely in the end plate 16".
  • the first end plate 16" includes the following, all obtained therein:
  • the intake port 116" is moreover in communication with the internal volume of the reservoir 2, whereas the delivery port D16" is in direct fluid communication with the delivery environment of the pump 4".
  • the intake port 4IN is provided by means of a first hole 4IN_1, which develops preferably in an axial direction within the end plate 16, without traversing it completely, and then intersects a second hole 4IN_2 with radial orientation, which finally intersects an axial hole 4IN_3, which in turn gives out into the intake port 116".
  • the intake port is provided by means of a U-shaped channel within the end plate 16" that sets the intake port 116" in fluid communication with the internal volume of the reservoir 2".
  • the intake port 4IN of the pump 4" is in fluid communication with the inlet port 2IN of the reservoir 2, here provided by means of an external channel obtained on the end plate 16.
  • the inlet port 2IN of the reservoir 2" is in effect provided in the end plate 16.
  • the port 2IN is functionally connected to a bifurcation that departs both in the direction of the intake port I16" and in the direction of the internal volume of the reservoir 2".
  • Fluid communication between the port 2OUT and the delivery port D16" of the pump 4" is ensured, instead, by means of a single radial hole 2OUT_1 that gives out, at one end, into the port 2OUT and intersects, at the opposite end, an axial hole corresponding to the delivery port 4OUT, which in turn gives out into the port D16".
  • the pump 4" includes an electric motor 32 having a rotor that turns about an axis of rotation X4" and is connected in rotation to an output shaft 33", which also is coaxial to the axis X4".
  • the output shaft 33" is connected in rotation to a bushing H" (for example, by means of a shape coupling with a spline), which is in turn connected in rotation - once again preferably by means of a shape coupling - to an output shaft S42" of a rotor assembly 42" of the pump 4.
  • the rotor assembly 42" is of the type with internal lobed rotors, commonly designated by the term "gerotor".
  • the rotor assembly 42" is housed within a bushing B42", in particular within a cylindrical seat thereof, which develops about an axis X42" parallel to the axis X4". Moreover fixed to the bushing B42" is a double hollow flange F" that is coaxial to the axis X4", which receives the shaft 33" and located in which is the bushing H".
  • the rotor assembly 42" includes an external rotor 44", which has a diameter substantially similar to that of the cylindrical seat on the bushing B42" and turns with respect thereto about the axis X42"; i.e., it is eccentric with respect to the axis X4".
  • the rotor assembly 42" moreover includes an internal rotor 46" sharing the axis X4", which is connected in rotation to the shaft S42". In this way, the rotor 46" is eccentric with respect to the rotor 44".
  • the internal rotor 46" and the external rotor 44" both present a trocoidal geometry, and the internal rotor 46" has a number of external lobes that is smaller by one than the number of internal lobes of the external rotor 44".
  • the external lobes of the internal rotor 46" mesh with the internal lobes of the external rotor 44": driving of the rotors of the pump in rotation is thus obtained by the electric motor 32", which drives the rotor 46" in rotation about the axis X4" (shafts 33" and S42"), which in turn drives the rotor 44" in rotation about the axis X42" by meshing therewith.
  • integration of the pump 4" with the reservoir 2" is not limited to a mere juxtaposition, i.e., to the mere insertion of the former into the latter, but there is a real functional integration between the two.
  • the reservoir 2" functions also as steam separator: since the inlet port 2IN and the outlet port 2OUT are provided on the end plate 16, which is set in a lower position, and hence, since it is at a lower geometrical height than, for example, the port 2IN on the reservoir 2, the pump 4" is prevented from drawing in working fluid in the vapour phase. This is a problem frequently encountered in this type of systems in so far as a mere widening of cross section of a duct for passage of the fluid is sufficient for the latter to evaporate.
  • the working fluid in the vapour phase remains confined in the top part of the internal volume of the reservoir, in the proximity of the end plate 18", whereas on the bottom (end plate 16") only the working fluid in the liquid phase remains thanks to the higher density.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Details And Applications Of Rotary Liquid Pumps (AREA)
  • Applications Or Details Of Rotary Compressors (AREA)

Claims (9)

  1. System für organische Rankine-Kreisprozesse (1) mit einem Behälter (2; 2') zur Aufnahme eines kondensierten Arbeitsfluids, wobei der Behälter ein Innenvolumen, einen Einlasskanal (2IN) zum Aufnehmen von kondensiertem Arbeitsfluid in das Innenvolumen und einen Auslasskanal (2OUT) für das kondensierte Arbeitsfluid aufweist, wobei das System mit organischem Rankine-Kreisprozess (1) dadurch gekennzeichnet ist, dass der Behälter (2; 2') eine Pumpe (4) aufweist, die im Innenvolumen aufgenommen ist, wobei die Pumpe (4) einen Eingangskanal (4IN, I34, I36, I38, I22) für das Absaugen des kondensierten Arbeitsfluids aus dem Innenvolumen und einen Abgabekanal (4OUT, D34, D36, D38, D22) für die Abgabe des Arbeitsfluids durch den Auslasskanal (2OUT) des Behälters aufweist.
  2. System für organische Rankine-Kreisprozesse (1) nach Anspruch 1, wobei die Pumpe (4) einen Elektromotor (32), eine Rotoranordnung (42), die durch den Elektromotor (32) in Drehbewegung betrieben werden kann, und eine Verteilungsanordnung (34, 36, 38, 16, 22, I34, I36, I38, I22, D34, D36, D38, D22) zum Steuern der Aufnahme und der Abgabe des kondensierten Arbeitsfluids aufweist.
  3. System für organische Rankine-Kreisprozesse nach Anspruch 1 oder 2, wobei der Behälter (2; 2') eine erste Endplatte (16), eine zweite Endplatte (18) und ein Gehäuse (20) aufweist, wobei das Innenvolumen des Behälters (2; 2') durch die erste und die zweite Endplatte (16, 18) und das Gehäuse (20) begrenzt ist.
  4. System für organische Rankine-Kreisprozesse (1) nach Anspruch 3, wobei die erste Endplatte (16) Teil der Verteilungsanordnung (34, 36, 38, 16, 22, I34, I36, I38, I22, D34, D36, D38, D22) der Pumpe (4) ist.
  5. System für organische Rankine-Kreisprozesse (1) nach Anspruch 4, wobei die Verteilungsanordnung (34, 36, 38, 16, 22, I34, I36, 138,122, D34, D36, D38, D22) aufweist:
    - eine erste Verteilungsplatte (34), die dafür ausgelegt ist, den Elektromotor (32) aufzunehmen,
    - eine zweite Verteilungsplatte (36),
    - eine dritte Verteilungsplatte (38),
    - eine ringförmige exzentrische Platte (40), die die Rotoranordnung (42) aufnimmt,
    - eine zentrale Entlastungseinheit (22) der ersten Endplatte (16),
    wobei die ringförmige exzentrische Platte (40) zwischen der zweiten (34) und der dritten (38) Verteilungsplatte montiert ist, wobei die Rotoranordnung (42) darin aufgenommen ist, und
    wobei die zweite (36) und die dritte (38) Verteilungsplatte zwischen der ersten Verteilungsplatte (34) und der zentralen Entlastungseinheit (22) montiert sind.
  6. System für organische Rankine-Kreisprozesse (1) nach Anspruch 5, wobei die zweite Verteilungsplatte (36) in einem Sitz (39) auf der ersten Verteilungsplatte (34) aufgenommen ist und die dritte Verteilungsplatte (38) in einem Sitz auf der zentralen Entlastungseinheit (22) aufgenommen ist.
  7. System für organische Rankine-Kreisprozesse (1) nach einem der Ansprüche 5 bis 6,
    wobei die erste, zweite und dritte Verteilungsplatte (34, 36, 38) und die zentrale Entlastungseinheit (22) jeweils eine Einlassöffnung (I34, I36, I38, I22) und eine Abgabeöffnung (D34, D36, D38, D22) aufweisen, wobei alle Einlassöffnungen (I34, I36, I38, I22) fluchtend und parallel zueinander angeordnet sind und alle Abgabeöffnungen fluchtend und parallel zueinander angeordnet sind (D34, D36, D38, D22).
  8. System für organische Rankine-Kreisprozesse (1) nach einem der Ansprüche 5 bis 7,
    wobei die erste Verteilungsplatte (34) mehrere radiale Bohrungen (34IN) aufweist, die dafür ausgelegt sind, ein Durchdringen des Arbeitsfluids zu ermöglichen, das sich im Innenvolumen des Behälters (2, 2') befindet, sodass es auf den Elektromotor (32) auftrifft, der in der ersten Verteilungsplatte (34) aufgenommen ist.
  9. System für organische Rankine-Kreisprozesse (1) nach Anspruch 1, das ferner aufweist:
    - einen Wärmetauscher (6),
    - einen Verdampfer (8),
    - einen Expander (10), der mechanisch mit einem Stromgenerator (12) gekoppelt ist,
    - eine Kondensatoreinheit (14), wobei:
    - der Auslasskanal (2OUT) des Behälters (2; 2') in Fluidverbindung mit einem ersten Einlasskanal (6LIN) des Wärmetauschers (6) steht,
    - ein erster Auslasskanal (6LOUT) des Wärmetauschers (6) in Fluidverbindung mit einem ersten Einlasskanal (8LIN) des Verdampfers (8) steht,
    - ein erster Auslasskanal (8GOUT) des Verdampfers (8) in Fluidverbindung mit einem Einlasskanal (10IN) des Expanders (10) steht,
    - ein Ausströmkanal (10OUT) des Expanders (10) in Fluidverbindung mit einem zweiten Einlasskanal (6GIN) des Wärmetauschers (6) steht,
    - ein zweiter Auslasskanal (6GOUT) des Wärmetauschers (6) in Fluidverbindung mit einem Einlasskanal (14IN) der Kondensatoreinheit (14) steht,
    - ein Auslasskanal (14OUT) der Kondensatoreinheit (14) in Fluidverbindung mit dem Einlasskanal (2IN) des Behälters (2, 2') steht.
EP16167519.4A 2015-04-29 2016-04-28 Speicher zur aufnahme eines kondensierten arbeitsfluids eines organischen rankine kreislaufsystems Active EP3091203B1 (de)

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FR3059355B1 (fr) * 2016-11-28 2019-07-19 Energy Solar Drill Installation de production d'energie electrique, d'energie mecanique et/ou de froid

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GB2401396A (en) * 2003-05-08 2004-11-10 Automotive Motion Tech Ltd Pump assembly
DE102010042068A1 (de) * 2010-10-06 2012-04-12 Behr Gmbh & Co. Kg Wärmeübertrager
JP6376492B2 (ja) * 2013-09-10 2018-08-22 パナソニックＩｐマネジメント株式会社 空冷ユニット

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