EP2655813A2 - Waste heat recovery installation - Google Patents
Waste heat recovery installationInfo
- Publication number
- EP2655813A2 EP2655813A2 EP11802103.9A EP11802103A EP2655813A2 EP 2655813 A2 EP2655813 A2 EP 2655813A2 EP 11802103 A EP11802103 A EP 11802103A EP 2655813 A2 EP2655813 A2 EP 2655813A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- waste heat
- orc
- heat recovery
- generator
- recovery system
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
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
- F01K25/08—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
- 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
- F01K25/10—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 the vapours being cold, e.g. ammonia, carbon dioxide, ether
Definitions
- Waste heat utilization system The invention relates to a waste heat utilization system according to the preamble of claim 1.
- An ORC Organic Rankine Cycle
- a working medium passes through various thermodynamic states in order to be finally returned to the liquid initial state.
- the working medium is brought to a higher pressure level with a pump. Thereafter, the working medium is preheated to the evaporation temperature and then evaporated. It is thus a steam process in which instead of water, an organic medium is evaporated.
- the resulting steam drives an expansion machine, such as a turbine, a piston or screw motor, which in turn is coupled to an electrical generator to generate power.
- the process medium enters a condenser and is cooled down there with heat being released. Since water evaporates at 100 ° C under atmospheric conditions, heat at a low temperature level, such as industrial waste heat or geothermal heat, often can not be used to generate electricity. However, using organic media with lower boiling temperatures, low-temperature steam can be produced.
- ORC plants for example, in the utilization of biomass in connection with combined heat and power, especially at relatively low power, so if the conventional biomass combustion technology seems relatively expensive.
- Biomass plants often have a fermenter for biogas production, which usually has to be heated.
- Combined heat and power plants as plants for combined heat and power are well known. These are decentralized, usually powered by internal combustion engines power generation systems with simultaneous waste heat recovery. The discharged during the combustion of the cooling media heat is used as completely as possible for the heating of suitable objects.
- the engine manufacturers prescribe a cooling water inlet temperature of only approx. 40 to 50 ° C for the mixture cooling so that the mixture can be sufficiently cooled. Since this temperature level is relatively low, the heat extracted from the fuel gas mixture in the previously known combined heat and power plants is released to the environment, for example with a table cooler.
- DE 10 2005 048 795 B3 also discloses the preheating of the working medium in the ORC in two steps in a heating device, namely that the process medium in the ORC is connected via two heat exchangers arranged downstream of a feed pump is heated, wherein the first heat exchanger is provided after the feed pump as a first stage for coupling low-temperature heat and the subsequent heat exchanger as a second stage for coupling high-temperature heat.
- the mixture cooling of the internal combustion engine is connected via a circuit to the first heat exchanger after the feed pump, wherein the heat from the cooling of the fuel gas mixture drawn in by the internal combustion engine serves to preheat the process medium in ORC and is coupled in as a low-temperature heat in the first heat exchanger.
- a second heating circuit draws heat from engine cooling water and exhaust gas of the internal combustion engine and is connected to the second heat exchanger after the feed pump, the heat from the cooling circuit and the exhaust gas for overheating and evaporation of the process medium in ORC and coupled as high temperature heat in the second heat exchanger after the feed pump becomes.
- the invention is therefore based on the object to optimize an existing from a waste heat source downstream ORC waste heat recovery system in terms of design and safe performance.
- the waste heat recovery system consists inter alia of an expansion machine for steam expansion in ORC, which has a magnetic bearing with an associated control device and a power supply via a DC intermediate circuit of a generator-frequency converter.
- the waste heat recovery system is characterized by a unit of expander, generator and frequency converter cooled with the refrigerant from the ORC circuit.
- cool, liquid refrigerant is removed after the feed pump and supplied for cooling the unit from the expansion machine, generator and frequency converter.
- the cool, liquid refrigerant is taken after the feed pump and fed directly to the expansion machine for storage cooling.
- heated refrigerant exiting from the unit of expansion machine, generator and frequency converter and / or the storage area of the expansion machine is supplied to the condenser on the inlet side.
- the refrigerant used for cooling of about 15 ° C to 50 ° C on the inlet side and about 30 ° C to 80 ° C on the outlet side, the respective temperatures of the current operating condition to be cooled components and / or assemblies and the entire waste heat recovery system.
- a temperature monitoring device associated with a higher-level control device is provided with temperature measuring points in the components and / or assemblies to be cooled. This compares actual temperature measured values with predefinable setpoint values, evaluates them and / or regulates accordingly optimized refrigerant flow rate.
- separate control loops with separate cooling channels or corresponding lines are preferably provided for the components to be cooled and / or assemblies. These individual, each to be cooled components and / or assemblies associated control circuits, valves, preferably solenoid valves, to control the refrigerant flow rate to optimally meet the respective local temperature situation.
- Off-heat sources can be, for example, combined heat and power plants, industrial plants or boiler plants.
- the waste heat recovery system in particular the unit of expansion machine, generator and frequency converter, is optimally and si tuationsNF cooled with the inventive measures.
- this is a prerequisite for safe, robust plant operation, but on the other hand also for effective and gentle operation of the individual components, all of which have special requirements with regard to cooling.
- This not only applies to the stationary operation of the waste heat recovery system, but also the modulating of the system according to it waste heat attack and the startup and shutdown. In particular, these states pose a challenge to the refrigeration system and, in accordance with the invention, provide safe control.
- the drawing illustrates an embodiment of the invention and shows in a single figure the schematic structure of a waste heat recovery system, consisting of one of these downstream ORC.
- the essential components for the ORC are an ORC circuit 1, a feed pump 2, an evaporator 3, a steam expansion expansion machine 4, which is coupled to a generator 5, a condenser 6 for re-cooling via a heat sink 7, and the heat exchangers 9, 10 for preheating the working medium in ORC circuit 1.
- the two heat exchangers 8, 9 are connected downstream of the feed pump 2 in series.
- the first heat exchanger 8 after the feed pump 2 serves as a first stage for coupling low-temperature heat and the subsequent heat exchanger 9 as a second stage for coupling high-temperature heat from a waste heat source 10th
- a second heating circuit 1 1 is connected to its flow area with the evaporator 3 of the ORC, because the temperature level is initially high enough for its direct heating. Thereafter, the second heating circuit 1 1 opens the return side in the second heat exchanger 9 and there are still residual heat from the ORC.
- a liquid refrigerant partial stream 12 for cooling the expansion machine 4 is branched off and initially passed through the generator 5. Thereafter, the cooling medium flows through the housing of the expansion machine 4, there in the starting phase for preheating initially for heat and ensures there in normal operation for sufficient heat dissipation. Only a simplified, schematic cable routing without the necessary branches to individual components or subassemblies, subcircuits, temperature measuring points, valves and control devices is distinguished.
- a steam valve 13 is opened at the inlet of the steam expansion expansion machine 4 in the ORC and during the rest Opening the steam valve 13 is carried out a further ramping up the speed, so that the generator 5 passes from the engine operation in the normal generator operation.
- a controlled bypass 14 with at least one throttle valve 15 is provided around the expansion machine 4.
- This bypass 14 is initially open in the starting phase, ie at a still relatively low temperature of the working medium.
- the working medium is passed around the expansion machine 4 around.
- the throttle valve 15 in the bypass 14 is closed and the steam engine 13 connected upstream of the expansion engine 4 is opened.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Motor Or Generator Cooling System (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102010056299A DE102010056299A1 (en) | 2010-12-24 | 2010-12-24 | Waste heat utilization system |
PCT/EP2011/073920 WO2012085264A2 (en) | 2010-12-24 | 2011-12-23 | Waste heat recovery installation |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2655813A2 true EP2655813A2 (en) | 2013-10-30 |
EP2655813B1 EP2655813B1 (en) | 2017-04-19 |
Family
ID=45418691
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP11802103.9A Not-in-force EP2655813B1 (en) | 2010-12-24 | 2011-12-23 | Waste heat recovery installation |
Country Status (6)
Country | Link |
---|---|
US (1) | US20140013749A1 (en) |
EP (1) | EP2655813B1 (en) |
CN (1) | CN103620167A (en) |
DE (1) | DE102010056299A1 (en) |
RU (1) | RU2013134398A (en) |
WO (1) | WO2012085264A2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102014202487A1 (en) * | 2014-02-12 | 2015-08-13 | Robert Bosch Gmbh | Control unit, heat coupling circuit and method for operating such a heat coupling circuit |
DE202017107002U1 (en) * | 2017-11-18 | 2019-02-19 | Bdr Thermea Group B.V. | CHP |
CN109401954A (en) * | 2018-12-07 | 2019-03-01 | 黑龙江省能源环境研究院 | Heat-exchange system and working method are heated outside biogas fermentation reactor |
CN109337798A (en) * | 2018-12-07 | 2019-02-15 | 黑龙江省能源环境研究院 | Biogas slurry waste heat recycling system and working method |
US11015846B2 (en) | 2018-12-20 | 2021-05-25 | AG Equipment Company | Heat of compression energy recovery system using a high speed generator converter system |
CN110173313A (en) * | 2019-05-28 | 2019-08-27 | 上海慕帆动力科技有限公司 | High parameter ORC turbine power generation equipment and ORC device applied to engine exhaust heat recycling |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3035557A (en) * | 1959-07-23 | 1962-05-22 | Sulzer Ag | Method of cooling resuperheaters of a steam plant |
FR2449780A1 (en) | 1979-02-22 | 1980-09-19 | Semt | METHOD AND APPARATUS FOR RECOVERING THERMAL ENERGY IN A SUPERFUELED INTERNAL COMBUSTION ENGINE |
US4901531A (en) | 1988-01-29 | 1990-02-20 | Cummins Engine Company, Inc. | Rankine-diesel integrated system |
DE59205446D1 (en) * | 1991-07-17 | 1996-04-04 | Siemens Ag | Process for operating a gas and steam turbine plant and plant for carrying out the process |
NZ248729A (en) * | 1992-10-02 | 1996-03-26 | Ormat Ind Ltd | High pressure geothermal power plant with secondary low pressure turbogenerator |
DE19541521A1 (en) | 1995-11-08 | 1997-07-31 | Schmeink & Cofreth En Manageme | Electrical efficiency improver for flow of special gases |
JP2007503546A (en) * | 2003-08-27 | 2007-02-22 | ティーティーエル ダイナミクス リミッテッド | Energy recovery system |
JP4427364B2 (en) * | 2004-03-19 | 2010-03-03 | 株式会社荏原製作所 | Power generator |
DE102005048795B3 (en) | 2005-10-12 | 2006-12-28 | Köhler & Ziegler Anlagentechnik GmbH | Combined heat and power generation plant, has heat exchanger provided next to feed pumps as stage for coupling low temperature heat, and another heat exchanger provided as another stage for coupling high temperature heat |
EP1984602B1 (en) * | 2006-02-02 | 2015-10-21 | Frank Eckert | Organic rankine cycle (orc) turbogenerator |
US8839622B2 (en) * | 2007-04-16 | 2014-09-23 | General Electric Company | Fluid flow in a fluid expansion system |
US7841306B2 (en) * | 2007-04-16 | 2010-11-30 | Calnetix Power Solutions, Inc. | Recovering heat energy |
US7638892B2 (en) * | 2007-04-16 | 2009-12-29 | Calnetix, Inc. | Generating energy from fluid expansion |
DE202007016668U1 (en) * | 2007-12-04 | 2008-02-28 | GMK-Gesellschaft für Motoren und Kraftanlagen mbH | Power generation plant according to the ORC principle |
US20090277400A1 (en) * | 2008-05-06 | 2009-11-12 | Ronald David Conry | Rankine cycle heat recovery methods and devices |
CN101806232A (en) * | 2010-03-17 | 2010-08-18 | 昆明理工大学 | Multistage evaporation organic Rankine cycle waste heat recovery generation system and method thereof |
US8400005B2 (en) * | 2010-05-19 | 2013-03-19 | General Electric Company | Generating energy from fluid expansion |
US8739538B2 (en) * | 2010-05-28 | 2014-06-03 | General Electric Company | Generating energy from fluid expansion |
-
2010
- 2010-12-24 DE DE102010056299A patent/DE102010056299A1/en not_active Ceased
-
2011
- 2011-12-23 EP EP11802103.9A patent/EP2655813B1/en not_active Not-in-force
- 2011-12-23 US US13/996,220 patent/US20140013749A1/en not_active Abandoned
- 2011-12-23 CN CN201180062001.3A patent/CN103620167A/en active Pending
- 2011-12-23 RU RU2013134398/06A patent/RU2013134398A/en unknown
- 2011-12-23 WO PCT/EP2011/073920 patent/WO2012085264A2/en active Application Filing
Non-Patent Citations (1)
Title |
---|
See references of WO2012085264A3 * |
Also Published As
Publication number | Publication date |
---|---|
DE102010056299A1 (en) | 2012-06-28 |
EP2655813B1 (en) | 2017-04-19 |
WO2012085264A2 (en) | 2012-06-28 |
CN103620167A (en) | 2014-03-05 |
US20140013749A1 (en) | 2014-01-16 |
RU2013134398A (en) | 2015-01-27 |
WO2012085264A3 (en) | 2013-12-19 |
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