WO2005061858A1 - Verfahren zur umwandlung von wärmeenergie in mechanische energie mit einer niederdruck-entspannungsvorrichtung - Google Patents
Verfahren zur umwandlung von wärmeenergie in mechanische energie mit einer niederdruck-entspannungsvorrichtung Download PDFInfo
- Publication number
- WO2005061858A1 WO2005061858A1 PCT/EP2004/053654 EP2004053654W WO2005061858A1 WO 2005061858 A1 WO2005061858 A1 WO 2005061858A1 EP 2004053654 W EP2004053654 W EP 2004053654W WO 2005061858 A1 WO2005061858 A1 WO 2005061858A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- roots blower
- expansion device
- working fluid
- working medium
- pressure
- Prior art date
Links
Classifications
-
- 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
- F01K25/06—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 mixtures of different fluids
- F01K25/065—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 mixtures of different fluids with an absorption fluid remaining at least partly in the liquid state, e.g. water for ammonia
-
- 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
- F01K25/06—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 mixtures of different fluids
Definitions
- the invention relates to a method for converting heat energy generated in an evaporator into mechanical energy by expanding a vaporous working medium which evaporates in the evaporator and is expanded in a expansion device. Furthermore, the invention relates to a relaxation device for converting thermal energy into mechanical energy.
- Wäi ⁇ iekraftaölagen are known, for example, in which a working medium at a high in a boiler Isobaric pressure is heated to the boiling point, evaporated and then overheated in a superheater. The steam is then adiabatically expanded in a turbine, performing work, and liquefied in a condenser, giving off heat. The liquid, usually water, is brought to a pressure by the feed water pump and pumped back into the boiler.
- One of the disadvantages of these devices is that high pressures of over 15 bar to 200 bar must be generated in the expansion processes in turbines, in which case the realized pressure ratio of the expansion is decisive for the efficiency achieved for turbines.
- the invention has for its object to provide a method and an apparatus for converting thermal energy into mechanical energy, which avoid the disadvantages mentioned, in particular have an improved efficiency.
- the expansion device is designed as a low-pressure expansion device, which is designed as a Roots blower, in which the working medium is expanded and thermal energy is converted into mechanical energy.
- the Roots blower as a low-pressure expansion device, however, has the advantage according to the invention that it can work with low gas friction and at the same time is insensitive to liquid drops. Furthermore, it achieves this Roots blowers at rotational speed at which the sealing edge on the outer radius reaches speeds of more than about 1/10 of the speed of sound have a particularly high volumetric efficiency, since the gap acts as a dynamic seal at these speeds.
- the Roots blower which can be in the form of an oval gear pump, can operate at full efficiency at a pressure difference of 500 mbar and can be used in a closed system at pressures of 10 to 0.5 bar.
- Another advantage is that in the relaxation devices mentioned, only the pressure difference and not the mass or the relaxation ratio is decisive for the efficiency. With already small pressure differences of less than two bar, full efficiency can be achieved. The physical reason for this lies in the high operating time of almost 95% in the pump, since it is actually not a conventional expansion in the sense of a compressor, but the expansion takes place through the discharge of the gas into the pressure port.
- the inflow and outflow with an increase or decrease in the scooping volume does not take place in the Roots blower, but the inflow of the gas takes place parallel to the transport of the gas via the rotary movement at a constant volume and thus with full efficiency.
- the Roots blower and other comparable low-pressure expansion devices according to the invention are distinguished here from other expansion devices in which the pressure change itself takes place by changing the scoop volume. As a result, the working time of this device is much shorter.
- the thermal energy of the vaporous working medium is at least partially converted into mechanical energy.
- the Roots blower is advantageously connected to a generator which converts the mechanical energy into electrical energy.
- the relaxed working fluid can be condensed in a heat exchanger.
- at least some of the condensed working fluid can be injected into the Roots blower during the expansion process, for example up to 16% of the mass fraction, whereby according to the invention the injected working fluid in the Roots blower partially condenses in the blower in the heat exchange with the steam and thereby the acting pressure difference of relaxation increases.
- a separator is connected downstream of the heat exchanger, which removes part of the condensed working fluid for injection into the Roots blower.
- a pump which is in turn connected downstream of the separator, expediently asks the condensed working medium back into the evaporator.
- a pressure-controlled injection takes place in a further embodiment of the invention.
- the method preferably has a first component of the working medium, which is formed by a mixture, is absorbed in and / or after the low-pressure expansion device by means of an absorption medium, heat being transferred to the remaining, vaporous second component, which is traceable.
- the mixture is an azeotr ⁇ p with a boiling point minimum at a specific mixing ratio of the components.
- the evaporation temperatures can be lowered so that they are below the condensation temperatures of the individual components. If the first component is absorbed adiabatically from the steam mixture, the corresponding heat is transferred to the second component remaining in vapor form.
- the heat of condensation can thus be withdrawn at an elevated temperature level.
- the second vapor-like component can be condensed in the evaporator of the working medium itself, giving off the heat of condensation, so that the corresponding proportion of the thermal energy can be returned to the process.
- the first component to be absorbed is water, an alkaline silicate solution, for example, can be used as the absorbent.
- the working medium for example an azeotropic mixture of water with perchlorethylene or silicone
- the working medium can be evaporated, for example, by heat exchange with primary energy from process vapors or heated process liquids and / or heat stores.
- the absorption in which, according to the invention, the heat of absorption obtained is transferred to the second component remaining in vapor form, as a result of which this component heats up to a temperature level above the boiling point of the azeotropic mixture, can take place in and / or after the expansion device.
- One of the main advantages here is that mechanical energy can be "gained” by the relaxation of the azeotropic mixture in the Roots blower and at the same time the relaxed working medium, which has already done “work” in the relaxation process, by separating (absorption) the first from the second component heats up due to the released heat of absorption.
- it can remaining work equipment can be returned after relaxation, for example, to give off its heat in the heat exchanger.
- the remaining working fluid only second component
- the remaining working fluid condenses and, due to the heat of condensation that arises, the liquid working fluid with the first and second components evaporated and then returned to the expansion device.
- the efficiency of the method for converting thermal energy into mechanical energy can be significantly improved.
- the working medium is preferably formed by an azeotropic mixture with a boiling point or an almost azeotropic mixture.
- the invention is described below with an azeotropic mixture; of course, the invention can also be applied to almost azeotropic mixtures or to non-azeotropic mixtures. High efficiencies can be achieved particularly with an azeotropic or an almost azeotropic mixture.
- the evaporation temperatures can be lowered so that they are below the evaporation temperatures of the individual components.
- the working medium has a low volume-specific or low molar enthalpy of vaporization. This ensures that a large amount of motive steam is generated with a predetermined amount of thermal energy.
- the working medium is preferably a solvent mixture which has organic and / or inorganic solvent components. Examples of this are mixtures of water and selected silicones.
- at least one component can also be a protic solvent.
- the absorbent is a reversible immobilizable solvent, which is the first component of the working medium in the non-immobilized physical state.
- the reversible solvent in the boiling agent can advantageously change through physico-chemical changes in such a way that it can be changed from the non-immobilized state to the reversibly immobilized state by ionization or complex formation from the vapor phase and in the non-immobilized form as an absorbent works for the work equipment.
- the vaporous working medium thus already contains the absorbent (in the non-immobilized state) before the expansion.
- the reversibly immobilized solvent is in a vaporous state and changes to the liquid state due to physico-chemical changes - such as pH shift, change in mole fraction and temperature in its volatility and / or vapor pressure (comparable to steam as a solvent in non-immobilized form and water as a reversibly immobilizable solvent).
- the advantage here is that the working fluid consists of two components, with one component simultaneously acting as an absorbent for the other component in the reversibly immobilized state.
- Cyclic nitrogen compounds such as pyridines, for example, can be used as pH-dependent, reversibly immobilizable solvents.
- the object of the invention is also achieved by a relaxation device for converting thermal energy into mechanical energy by relaxing a vaporous working medium with the features of claim 15.
- a relaxation device for converting thermal energy into mechanical energy by relaxing a vaporous working medium with the features of claim 15.
- the expansion device is designed as a low-pressure expansion device, which is designed as a Roots blower.
- a Roots blower two rotors run on one another on elliptical or oval-shaped pitch curves.
- Well-known examples are the oval wheel pump or the Roots blower.
- With multi-bladed rotors higher order elliptical pitch curves can be realized.
- One advantage of Roots blowers with multi-bladed rotors is a reduction in the pulsations that occur, since the chamber volume, based on the scooping volume, is smaller and the frequency of gas discharge increases.
- the Roots blower expediently has a gas-tight seal between the pump chamber and the gear chamber in order to prevent oil from entering the vaporous working medium.
- the Roots blower also has a shaft that can be connected to the generator, whereby the mechanical energy can be converted into electrical energy.
- the use of a Roots blower as a low-pressure expansion device opens up the possibility, on the one hand, of the process by injecting absorption agents, in particular when using waste heat with a temperature of less than approximately 100 ° C. for driving pumps or generators support, and on the other hand to "raise the condensation energy of the working fluid, for example with a heat pump," to an increased temperature level due to the small pressure and temperature differences.
- FIG. 1 shows a method for converting thermal energy accumulating in an evaporator 6 into mechanical energy by expanding a vaporous working medium which evaporates in the evaporator 6 and is expanded in a low-pressure expansion device 2.
- the working medium in this exemplary embodiment is water, which is conveyed in the vapor state to the expansion device 2, which is designed as a Roots blower 2.
- the expansion device 2 which is designed as a Roots blower 2.
- the Roots blower 2 is connected to a generator 1 and drives it, so that mechanical energy is converted into electrical energy.
- the expanded motive steam is condensed in a heat exchanger 7.
- the evaporator 6 is preferably connected to the heat exchanger 7, the condensate being conveyed back into the evaporator 6 by means of the pump 9.
- the heat exchanger 7 is followed by a separator 3, which removes part of the condensed working fluid for injection into the Roots blower 2.
- the Roots blower 2 has a plurality of injection openings (not shown) through which the condensed working fluid is injected into the scooping space of the Roots blower 2, a portion of the vaporous working fluid condensing in the Roots blower 2, thereby reducing the outlet pressure and thus improving the efficiency. Due to the pressure difference compared to the heat exchanger 7 connected to the outlet of the Roots blower 2, the rotors arranged in the Roots blower 2 are set in motion by the relaxing working medium, and those that come with the relaxation Change in entropy is given off as mechanical energy.
- a pump 9 is connected downstream of the separator 3, which conveys the condensed working fluid back into the evaporator 6.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Applications Or Details Of Rotary Compressors (AREA)
- Sorption Type Refrigeration Machines (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP04816348A EP1702140B1 (de) | 2003-12-22 | 2004-12-22 | Verfahren zur umwandlung von wärmeenergie in mechanische energie mit einer niederdruck-entspannungsvorrichtung |
US10/583,925 US8132413B2 (en) | 2003-12-22 | 2004-12-22 | Method of transforming heat energy to mechanical energy in a low-pressure expansion device |
DE502004004776.9T DE502004004776C5 (de) | 2003-12-22 | 2004-12-22 | Verfahren zur umwandlung von wärmeenergie in mechanische energie mit einer niederdruck-entspannungsvorrichtung |
ES04816348T ES2293384T3 (es) | 2003-12-22 | 2004-12-22 | Procedimiento para la conversion de energia termina en energia mecaniza con un dispositivo de expansion a baja presion. |
Applications Claiming Priority (10)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10360380.8 | 2003-12-22 | ||
DE10360379.4 | 2003-12-22 | ||
DE2003160380 DE10360380A1 (de) | 2003-12-22 | 2003-12-22 | Extraktions-Wärmepumpe mit reversibel immobilisierbarem Lösemittel |
DE10360364.6 | 2003-12-22 | ||
DE2003160364 DE10360364A1 (de) | 2003-12-22 | 2003-12-22 | Offene Wärmepumpe unter Verwendung von flüssigkeitsüberlagerten Verdichtersystemen |
DE2003160379 DE10360379A1 (de) | 2003-12-22 | 2003-12-22 | Niederdruck-Entspannungsmotor auf der Basis von Rootsgebläsen |
DE2003161203 DE10361203A1 (de) | 2003-12-24 | 2003-12-24 | Niederdruck-Entspannungsmotor mit Energierückführung |
DE10361203.3 | 2003-12-24 | ||
DE2003161223 DE10361223A1 (de) | 2003-12-24 | 2003-12-24 | Niederdruck-Entspannungsmotor mit Treibdampftrennung mittels extraktiver Rektifikation |
DE10361223.8 | 2003-12-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2005061858A1 true WO2005061858A1 (de) | 2005-07-07 |
Family
ID=34714591
Family Applications (5)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2004/053655 WO2005066466A1 (de) | 2003-12-22 | 2004-12-22 | Verfahren und anlage zur umwandlung von anfallender wärmeenergie in mechanische energie |
PCT/EP2004/053651 WO2005061973A1 (de) | 2003-12-22 | 2004-12-22 | Verfahren und anlage zur temperaturerhöhung eines dampfförmigen arbeitsmittels |
PCT/EP2004/053654 WO2005061858A1 (de) | 2003-12-22 | 2004-12-22 | Verfahren zur umwandlung von wärmeenergie in mechanische energie mit einer niederdruck-entspannungsvorrichtung |
PCT/EP2004/053650 WO2005061857A1 (de) | 2003-12-22 | 2004-12-22 | Vorrichtung und verfahren zur umwandlung von wärmeenergie in mechanische energie |
PCT/EP2004/053649 WO2005066465A1 (de) | 2003-12-22 | 2004-12-22 | Verfahren und anlage zur umwandlung von wärmeenergie aus kältemaschinen |
Family Applications Before (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2004/053655 WO2005066466A1 (de) | 2003-12-22 | 2004-12-22 | Verfahren und anlage zur umwandlung von anfallender wärmeenergie in mechanische energie |
PCT/EP2004/053651 WO2005061973A1 (de) | 2003-12-22 | 2004-12-22 | Verfahren und anlage zur temperaturerhöhung eines dampfförmigen arbeitsmittels |
Family Applications After (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2004/053650 WO2005061857A1 (de) | 2003-12-22 | 2004-12-22 | Vorrichtung und verfahren zur umwandlung von wärmeenergie in mechanische energie |
PCT/EP2004/053649 WO2005066465A1 (de) | 2003-12-22 | 2004-12-22 | Verfahren und anlage zur umwandlung von wärmeenergie aus kältemaschinen |
Country Status (6)
Country | Link |
---|---|
US (2) | US8132413B2 (de) |
EP (5) | EP1706599B1 (de) |
AT (1) | ATE371101T1 (de) |
DE (1) | DE502004004776C5 (de) |
ES (2) | ES2293384T3 (de) |
WO (5) | WO2005066466A1 (de) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006128423A2 (de) * | 2005-06-02 | 2006-12-07 | Lutz Giechau | Verfahren und vorrichtung zur erzeugung mechanischer energie |
WO2007131943A3 (de) * | 2006-05-16 | 2008-09-18 | Ecoenergy Patent Gmbh | Umwandlung von wärme in mechanische energie mit verwendung eines strahlverdichters |
WO2009030283A2 (de) * | 2007-08-31 | 2009-03-12 | Siemens Aktiengesellschaft | Verfahren und vorrichtung zur umwandlung der wärmeenergie einer niedertemperatur-wärmequelle in mechanische energie |
WO2009140944A2 (de) * | 2008-05-17 | 2009-11-26 | Hamm & Dr. Oser Gbr | Umwandlung der druckenergie von gasen und dämpfen bei niedrigen ausgangsdrücken in mechanische energie |
DE102012016991A1 (de) | 2012-08-25 | 2014-02-27 | Erwin Oser | Energieeffizientes Entspannungsaggregat |
DE102013112024A1 (de) * | 2013-10-31 | 2015-04-30 | ENVA Systems GmbH | Drehkolbengebläse mit einem Dichtsystem |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102008013737A1 (de) | 2008-03-06 | 2009-09-10 | Heinz Manfred Bauer | Verfahren zur Wandlung thermischer Energie in mechanische und weiter in elektrische Energie |
DE102008036917A1 (de) | 2008-08-05 | 2010-02-11 | Heinz Manfred Bauer | Verfahren zur Wandlung thermischer Energie in mechanische und weiter in elektrische Energie |
US20110314805A1 (en) * | 2009-03-12 | 2011-12-29 | Seale Joseph B | Heat engine with regenerator and timed gas exchange |
US20130174552A1 (en) * | 2012-01-06 | 2013-07-11 | United Technologies Corporation | Non-azeotropic working fluid mixtures for rankine cycle systems |
EP2820257A1 (de) * | 2012-02-29 | 2015-01-07 | Eaton Corporation | Volumetrische energierückgewinnungsvorrichtung und systeme |
US10648745B2 (en) | 2016-09-21 | 2020-05-12 | Thermal Corp. | Azeotropic working fluids and thermal management systems utilizing the same |
DE102019135820A1 (de) | 2019-12-27 | 2021-07-01 | Corinna Ebel | Verfahren zur Dampferzeugung, Dampferzeuger und Verwendung eines Wälzkolbengebläses |
CN112412560A (zh) * | 2020-10-28 | 2021-02-26 | 北京工业大学 | 一种基于单螺杆膨胀机的卡琳娜循环*** |
DE202021100874U1 (de) | 2021-02-23 | 2022-05-30 | Marlina Hamm | Wälzkolbengebläse zur Entspannung eines dampfförmigen Mediums bei hohem Druck und guter Dichtigkeit |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1301214A (en) * | 1970-05-26 | 1972-12-29 | Wallace Louis Minto | Prime mover system |
WO1985002881A1 (en) * | 1983-12-22 | 1985-07-04 | Lipovetz Ivan | System for converting heat energy, particularly for utilizing heat energy of the environment |
DE3619547A1 (de) * | 1984-12-13 | 1987-12-17 | Peter Koch | Verfahren und einrichtung zur erzeugung einer kraft aus einer temperaturdifferenz zweier medien |
US20030172654A1 (en) * | 2002-03-14 | 2003-09-18 | Paul Lawheed | Rankine cycle generation of electricity |
Family Cites Families (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1546326A (fr) * | 1966-12-02 | 1968-11-15 | Générateur d'énergie perfectionné, particulièrement pour créer une énergie enutilisant un réfrigérant | |
DE1601003A1 (de) * | 1966-12-02 | 1970-07-16 | Gohee Mamiya | Energieerzeugungssystem |
US3972195A (en) * | 1973-12-14 | 1976-08-03 | Biphase Engines, Inc. | Two-phase engine |
US4009575A (en) * | 1975-05-12 | 1977-03-01 | said Thomas L. Hartman, Jr. | Multi-use absorption/regeneration power cycle |
FR2374539A1 (fr) * | 1976-12-15 | 1978-07-13 | Air Ind | Procede de compression de vapeur d'eau, et circuits thermiques pour sa mise en oeuvre |
US4295335A (en) * | 1978-01-09 | 1981-10-20 | Brinkerhoff Verdon C | Regenative absorption engine apparatus and method |
DE2803118B2 (de) * | 1978-01-25 | 1980-07-31 | Stiebel Eltron Gmbh & Co Kg, 3450 Holzminden | Verfahren zur Beheizung mit einer Absorptionswärmepumpenanlage und Vorrichtung zur Durchführung des Verfahrens |
US4195485A (en) * | 1978-03-23 | 1980-04-01 | Brinkerhoff Verdon C | Distillation/absorption engine |
US4307572A (en) * | 1978-05-15 | 1981-12-29 | New Energy Dimension Corporation | Externally cooled absorption engine |
US4429661A (en) * | 1981-11-27 | 1984-02-07 | Mcclure Michael C | Heat recovery apparatus and method |
US4534175A (en) * | 1982-03-11 | 1985-08-13 | Gason Energy Engineering Ltd. | Method and apparatus for the absorption of a gas in a liquid and their use in energy conversion cycles |
DE3219680A1 (de) * | 1982-05-21 | 1983-11-24 | Siemens AG, 1000 Berlin und 8000 München | Waermepumpenanlage |
DE3417833A1 (de) * | 1984-05-14 | 1985-11-14 | VEB Wärmeanlagenbau "DSF" im VE Kombinat Verbundnetze Energie, DDR 1020 Berlin | Anordnung fuer eine resorptionswaermepumpenanlage zur erzeugung von heizwaerme aus industrie- und umweltwaerme |
JPS61171811A (ja) | 1985-01-28 | 1986-08-02 | Sanyo Electric Co Ltd | 動力取出し用吸収ヒ−トポンプ装置 |
US4622820A (en) * | 1985-09-27 | 1986-11-18 | Sundquist Charles T | Absorption power generator |
JPH0696978B2 (ja) | 1985-12-03 | 1994-11-30 | トヨタ自動車株式会社 | 過給機付内燃機関 |
US4848088A (en) * | 1987-12-03 | 1989-07-18 | Lazarevich Milan P M | Heat recycling process |
US5027602A (en) * | 1989-08-18 | 1991-07-02 | Atomic Energy Of Canada, Ltd. | Heat engine, refrigeration and heat pump cycles approximating the Carnot cycle and apparatus therefor |
US5791157A (en) * | 1996-01-16 | 1998-08-11 | Ebara Corporation | Heat pump device and desiccant assisted air conditioning system |
DE19712325A1 (de) | 1997-03-24 | 1998-10-15 | Wilhelm Holzapfel | Anlage zur Umwandlung thermischer Energie niedrigen Niveaus in mechanische Energie |
KR20010002901A (ko) * | 1999-06-18 | 2001-01-15 | 김창선 | 물질 열팽창에너지 재활용 방법 |
GB0007917D0 (en) * | 2000-03-31 | 2000-05-17 | Npower | An engine |
HU0100463D0 (en) * | 2001-01-29 | 2001-03-28 | Szopko Mihaly | Method and device for absorption heat pumping |
DE10214183C1 (de) * | 2002-03-28 | 2003-05-08 | Siemens Ag | Kraftwerk zur Kälteerzeugung |
US7019412B2 (en) * | 2002-04-16 | 2006-03-28 | Research Sciences, L.L.C. | Power generation methods and systems |
DE10221145A1 (de) * | 2002-05-11 | 2003-11-20 | Juergen Uehlin | Wärmekraftmaschine mit interner Wärmesenke |
US7028476B2 (en) * | 2004-05-22 | 2006-04-18 | Proe Power Systems, Llc | Afterburning, recuperated, positive displacement engine |
-
2004
- 2004-12-22 US US10/583,925 patent/US8132413B2/en not_active Expired - Fee Related
- 2004-12-22 EP EP04804988.6A patent/EP1706599B1/de active Active
- 2004-12-22 DE DE502004004776.9T patent/DE502004004776C5/de active Active
- 2004-12-22 EP EP04804983.7A patent/EP1706598B1/de active Active
- 2004-12-22 WO PCT/EP2004/053655 patent/WO2005066466A1/de active Application Filing
- 2004-12-22 EP EP04804984A patent/EP1702139A1/de not_active Withdrawn
- 2004-12-22 WO PCT/EP2004/053651 patent/WO2005061973A1/de active Application Filing
- 2004-12-22 EP EP04816348A patent/EP1702140B1/de active Active
- 2004-12-22 WO PCT/EP2004/053654 patent/WO2005061858A1/de active IP Right Grant
- 2004-12-22 WO PCT/EP2004/053650 patent/WO2005061857A1/de active Application Filing
- 2004-12-22 EP EP04804985A patent/EP1706681A1/de not_active Withdrawn
- 2004-12-22 US US10/583,936 patent/US7726128B2/en not_active Expired - Fee Related
- 2004-12-22 ES ES04816348T patent/ES2293384T3/es active Active
- 2004-12-22 AT AT04816348T patent/ATE371101T1/de active
- 2004-12-22 ES ES04804988.6T patent/ES2624638T3/es active Active
- 2004-12-22 WO PCT/EP2004/053649 patent/WO2005066465A1/de active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1301214A (en) * | 1970-05-26 | 1972-12-29 | Wallace Louis Minto | Prime mover system |
WO1985002881A1 (en) * | 1983-12-22 | 1985-07-04 | Lipovetz Ivan | System for converting heat energy, particularly for utilizing heat energy of the environment |
DE3619547A1 (de) * | 1984-12-13 | 1987-12-17 | Peter Koch | Verfahren und einrichtung zur erzeugung einer kraft aus einer temperaturdifferenz zweier medien |
US20030172654A1 (en) * | 2002-03-14 | 2003-09-18 | Paul Lawheed | Rankine cycle generation of electricity |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006128423A2 (de) * | 2005-06-02 | 2006-12-07 | Lutz Giechau | Verfahren und vorrichtung zur erzeugung mechanischer energie |
WO2006128423A3 (de) * | 2005-06-02 | 2008-04-10 | Lutz Giechau | Verfahren und vorrichtung zur erzeugung mechanischer energie |
WO2007131943A3 (de) * | 2006-05-16 | 2008-09-18 | Ecoenergy Patent Gmbh | Umwandlung von wärme in mechanische energie mit verwendung eines strahlverdichters |
US8196406B2 (en) | 2006-05-16 | 2012-06-12 | Ecoenergy Patent Gmbh | Conversion of heat into mechanical energy by means of a jet compressor |
AU2007251575B2 (en) * | 2006-05-16 | 2012-12-13 | Ecoenergy Patent Gmbh | Conversion of heat into mechanical energy by means of a jet compressor |
WO2009030283A2 (de) * | 2007-08-31 | 2009-03-12 | Siemens Aktiengesellschaft | Verfahren und vorrichtung zur umwandlung der wärmeenergie einer niedertemperatur-wärmequelle in mechanische energie |
WO2009030283A3 (de) * | 2007-08-31 | 2010-03-18 | Siemens Aktiengesellschaft | Verfahren und vorrichtung zur umwandlung der wärmeenergie einer niedertemperatur-wärmequelle in mechanische energie |
WO2009140944A2 (de) * | 2008-05-17 | 2009-11-26 | Hamm & Dr. Oser Gbr | Umwandlung der druckenergie von gasen und dämpfen bei niedrigen ausgangsdrücken in mechanische energie |
WO2009140944A3 (de) * | 2008-05-17 | 2012-08-09 | Hamm & Dr. Oser Gbr | Umwandlung der druckenergie von gasen und dämpfen bei niedrigen ausgangsdrücken in mechanische energie |
DE102012016991A1 (de) | 2012-08-25 | 2014-02-27 | Erwin Oser | Energieeffizientes Entspannungsaggregat |
DE102013112024A1 (de) * | 2013-10-31 | 2015-04-30 | ENVA Systems GmbH | Drehkolbengebläse mit einem Dichtsystem |
Also Published As
Publication number | Publication date |
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WO2005061973A1 (de) | 2005-07-07 |
ATE371101T1 (de) | 2007-09-15 |
US20080289336A1 (en) | 2008-11-27 |
WO2005061857A1 (de) | 2005-07-07 |
EP1702139A1 (de) | 2006-09-20 |
ES2293384T3 (es) | 2008-03-16 |
EP1706599A1 (de) | 2006-10-04 |
EP1702140B1 (de) | 2007-08-22 |
US20080134680A1 (en) | 2008-06-12 |
DE502004004776D1 (de) | 2007-10-04 |
EP1706598B1 (de) | 2013-10-16 |
DE502004004776C5 (de) | 2020-01-16 |
ES2624638T3 (es) | 2017-07-17 |
WO2005066465A1 (de) | 2005-07-21 |
EP1706681A1 (de) | 2006-10-04 |
WO2005066466A1 (de) | 2005-07-21 |
EP1706599B1 (de) | 2017-02-15 |
EP1706598A1 (de) | 2006-10-04 |
EP1702140A1 (de) | 2006-09-20 |
US8132413B2 (en) | 2012-03-13 |
US7726128B2 (en) | 2010-06-01 |
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