US20100236261A1 - Method for utilizing heat of compression - Google Patents
Method for utilizing heat of compression Download PDFInfo
- Publication number
- US20100236261A1 US20100236261A1 US12/695,572 US69557210A US2010236261A1 US 20100236261 A1 US20100236261 A1 US 20100236261A1 US 69557210 A US69557210 A US 69557210A US 2010236261 A1 US2010236261 A1 US 2010236261A1
- Authority
- US
- United States
- Prior art keywords
- compression
- heat
- heating
- medium
- air
- 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.)
- Abandoned
Links
- 238000007906 compression Methods 0.000 title claims abstract description 42
- 230000006835 compression Effects 0.000 title claims abstract description 28
- 238000000034 method Methods 0.000 title claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000003507 refrigerant Substances 0.000 claims abstract description 11
- 238000004378 air conditioning Methods 0.000 claims abstract description 9
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 12
- 239000001257 hydrogen Substances 0.000 claims description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- 239000003345 natural gas Substances 0.000 claims description 6
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims description 2
- 238000001816 cooling Methods 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D3/00—Hot-water central heating systems
- F24D3/18—Hot-water central heating systems using heat pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2200/00—Heat sources or energy sources
- F24D2200/16—Waste heat
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/12—Hot water central heating systems using heat pumps
Definitions
- the invention pertains to a method for utilizing the heat of compression accumulating during a compression process.
- Energy is required for heating and air-conditioning buildings, as well as for heating service water, and therefore needs to be supplied and/or generated directly on-site. In order to lower the energy requirement, excess energy is already utilized for the aforementioned purposes in a number of applications. In many applications, however, energy is needed for heating or cooling buildings while energy simultaneously is or must be wastefully dissipated because it could not be “recycled” so far.
- Natural gas and hydrogen fueling stations feature a number of buildings that need to be at least temporarily heated or cooled. If such fueling stations also feature a car wash, the service water required for this car wash also needs to be heated. The natural gas or hydrogen sold at such a fueling station needs to be compressed before a vehicle is refueled. Until now, the heat of compression released during the compression of these mediums was wastefully dissipated by means of a suitable cooling system—in which water or ambient air is used as cooling medium. The compression of the aforementioned mediums to pressures up to 1000 bar requires an expenditure of energy between 15 and 300 kW, wherein the same amount of energy is generated in the form of heat and had to be transferred to the surroundings so far with the aid of corresponding heat exchangers.
- the present invention is based on the objective of disclosing a method of the initially cited type for utilizing the heat of compression accumulating during a compression process, wherein said method eliminates the above-described disadvantages and makes it possible, in particular, to utilize the heat of compression accumulating during a compression process for air-conditioning buildings, for heating buildings and/or for heating service water.
- the invention proposes a method of the initially cited type for utilizing the heat of compression accumulating during a compression process, wherein said method is characterized in that the heat of compression accumulating during the compression process is at least temporarily transferred to at least one consumer that serves for air-conditioning and/or heating a building and/or for heating service water by means of at least one refrigerant circuit.
- a gaseous medium to be compressed is fed to a pre-compressor V 1 via a line 1 and compressed to a desired intermediate pressure therein.
- this intermediate pressure lies in the range between 12 and 27 bar.
- the pre-compressed medium can either be intermediately stored in a storage device that is not illustrated in the FIGURE and/or directly fed to the main compressor V 2 via a line 1 ′.
- the medium is compressed to the desired ultimate pressure in this main compressor. In the compression of natural gas or hydrogen, this ultimate pressure usually lies between 250 and 1000 bar.
- the compressed medium is subsequently fed to a vehicle to be refueled—if applicable after a corresponding intermediate storage—via a line 1 ′′.
- the compression of the gaseous medium to be compressed may also be realized in only one compression stage or in more than two compression stages.
- the pre-compressor V 1 and the main compressor V 2 are respectively provided with a heat exchanger E 1 and E 2 —that is illustrated in the form of the broken lines connecting the respective compressor and the assigned heat exchanger.
- the heat exchangers E 1 /E 2 serve for dissipating the heat of compression created during the compression in the two compression stages V 1 /V 2 .
- the temperature usually increases by 50 to 150 K per compression stage.
- the two heat exchangers E 1 and E 2 are connected by a refrigerant circuit 2 - 5 .
- a refrigerant that is suitable for the respective application circulates in this refrigerant circuit, wherein the refrigerant may consist, in principle, of a one-component or multi-component refrigerant. In many applications, it is sufficient and practical to use water as the refrigerant.
- a consumer E 3 that receives a medium via a line 6 and discharges a medium heated or cooled therein via a line 6 ′ is illustrated in the FIGURE in a purely exemplary fashion.
- the consumer E 3 may consist, for example, of a heater, an air-conditioner or a device for heating service water that is preferably realized in the form of an adsorption system, an absorption system or a DEC-system (Desiccant and Evaporative Cooling).
- the medium fed to the consumer E 3 via the line 6 would respectively consist of air or service water.
- Several consumers will exist in many applications, but these consumers do not necessarily have to always operate simultaneously.
- the inventive method for utilizing the heat of compression accumulating during a compression process now makes it possible to cost-efficiently provide the energy or the majority of the energy required for heating or air-conditioning buildings.
- the inventive method for utilizing the heat of compression accumulating during a compression process can also be subsequently implemented in existing processes or systems, in which a compression process is realized.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Other Air-Conditioning Systems (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Steam Or Hot-Water Central Heating Systems (AREA)
Abstract
Described is a method for utilizing the heat of compression accumulating during a compression process for air-conditioning and/or heating buildings and/or for heating service water. According to the invention, the heat of compression accumulating during the compression process is at least temporarily transferred to at least one consumer that serves for air-conditioning and/or heating a building and/or for heating service water by means of at least one refrigerant circuit.
Description
- This application claims priority from German Patent Application Serial No. DE 102009013755.6 filed Mar. 17, 2009.
- The invention pertains to a method for utilizing the heat of compression accumulating during a compression process.
- Energy is required for heating and air-conditioning buildings, as well as for heating service water, and therefore needs to be supplied and/or generated directly on-site. In order to lower the energy requirement, excess energy is already utilized for the aforementioned purposes in a number of applications. In many applications, however, energy is needed for heating or cooling buildings while energy simultaneously is or must be wastefully dissipated because it could not be “recycled” so far.
- Natural gas and hydrogen fueling stations feature a number of buildings that need to be at least temporarily heated or cooled. If such fueling stations also feature a car wash, the service water required for this car wash also needs to be heated. The natural gas or hydrogen sold at such a fueling station needs to be compressed before a vehicle is refueled. Until now, the heat of compression released during the compression of these mediums was wastefully dissipated by means of a suitable cooling system—in which water or ambient air is used as cooling medium. The compression of the aforementioned mediums to pressures up to 1000 bar requires an expenditure of energy between 15 and 300 kW, wherein the same amount of energy is generated in the form of heat and had to be transferred to the surroundings so far with the aid of corresponding heat exchangers.
- The present invention is based on the objective of disclosing a method of the initially cited type for utilizing the heat of compression accumulating during a compression process, wherein said method eliminates the above-described disadvantages and makes it possible, in particular, to utilize the heat of compression accumulating during a compression process for air-conditioning buildings, for heating buildings and/or for heating service water.
- In order to attain this objective, the invention proposes a method of the initially cited type for utilizing the heat of compression accumulating during a compression process, wherein said method is characterized in that the heat of compression accumulating during the compression process is at least temporarily transferred to at least one consumer that serves for air-conditioning and/or heating a building and/or for heating service water by means of at least one refrigerant circuit.
- Other advantageous variations of the inventive method for utilizing the heat of compression accumulating during a compression process form the objects of the dependent claims and are characterized in that
-
- the inventive method is implemented in a gas fueling system, in which a one-stage or multi-stage compression of a medium, preferably natural gas or hydrogen, is realized and
- the medium circulating in the refrigerant circuit consists of water and/or glycol.
- The inventive method for utilizing the heat of compression accumulating during the compression process for air-conditioning buildings, for heating buildings and/or for heating service water, as well as other variations thereof, are described in greater detail below with reference to the exemplary embodiment illustrated in the FIGURE. However, this FIGURE merely shows a schematic representation of the inventive method.
- A gaseous medium to be compressed is fed to a pre-compressor V1 via a
line 1 and compressed to a desired intermediate pressure therein. In the case of a natural gas or hydrogen fueling station, this intermediate pressure lies in the range between 12 and 27 bar. The pre-compressed medium can either be intermediately stored in a storage device that is not illustrated in the FIGURE and/or directly fed to the main compressor V2 via aline 1′. The medium is compressed to the desired ultimate pressure in this main compressor. In the compression of natural gas or hydrogen, this ultimate pressure usually lies between 250 and 1000 bar. The compressed medium is subsequently fed to a vehicle to be refueled—if applicable after a corresponding intermediate storage—via aline 1″. The compression of the gaseous medium to be compressed may also be realized in only one compression stage or in more than two compression stages. - The pre-compressor V1 and the main compressor V2 are respectively provided with a heat exchanger E1 and E2—that is illustrated in the form of the broken lines connecting the respective compressor and the assigned heat exchanger. The heat exchangers E1/E2 serve for dissipating the heat of compression created during the compression in the two compression stages V1/V2. The temperature usually increases by 50 to 150 K per compression stage.
- The two heat exchangers E1 and E2 are connected by a refrigerant circuit 2-5. A refrigerant that is suitable for the respective application circulates in this refrigerant circuit, wherein the refrigerant may consist, in principle, of a one-component or multi-component refrigerant. In many applications, it is sufficient and practical to use water as the refrigerant.
- A consumer E3 that receives a medium via a
line 6 and discharges a medium heated or cooled therein via aline 6′ is illustrated in the FIGURE in a purely exemplary fashion. The consumer E3 may consist, for example, of a heater, an air-conditioner or a device for heating service water that is preferably realized in the form of an adsorption system, an absorption system or a DEC-system (Desiccant and Evaporative Cooling). In this case, the medium fed to the consumer E3 via theline 6 would respectively consist of air or service water. Several consumers will exist in many applications, but these consumers do not necessarily have to always operate simultaneously. - It is advantageous to provide an additional heat exchanger E4 that makes it possible to realize a degradation or dissipation of the energy released during the compression—for example in the form of a heat transfer to cooling water or ambient air—when an “energy consumption” by the or at least one of several consumers E3 is impossible or undesirable.
- The inventive method for utilizing the heat of compression accumulating during a compression process now makes it possible to cost-efficiently provide the energy or the majority of the energy required for heating or air-conditioning buildings.
- The inventive method for utilizing the heat of compression accumulating during a compression process can also be subsequently implemented in existing processes or systems, in which a compression process is realized.
Claims (5)
1. A method for utilizing the heat of compression accumulating during a compression process selected from the group consisting of air-conditioning, heating buildings, and heating service water, characterized in that the heat of compression accumulating during the compression process is at least temporarily transferred to at least one consumer selected from the group consisting of air-conditioning, heating a building, and heating service water by means of at least one refrigerant circuit.
2. The method according to claim 1 , wherein the method is implemented in a gas fueling system, in which a compression of a medium is realized.
3. The method according to claim 1 , wherein said compression of a medium is selected from the group consisting of one-stage and multi-stage.
4. The method as claimed in claim 2 , wherein said medium is selected from the group consisting of natural gas and hydrogen.
5. The method according to claim 1 , characterized in that the medium circulating in the refrigerant circuit is selected from the group consisting of water and glycol.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102009013755A DE102009013755A1 (en) | 2009-03-17 | 2009-03-17 | Method for using heat of compression |
DE102009013755.6 | 2009-03-17 |
Publications (1)
Publication Number | Publication Date |
---|---|
US20100236261A1 true US20100236261A1 (en) | 2010-09-23 |
Family
ID=42153934
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US12/695,572 Abandoned US20100236261A1 (en) | 2009-03-17 | 2010-01-28 | Method for utilizing heat of compression |
Country Status (4)
Country | Link |
---|---|
US (1) | US20100236261A1 (en) |
EP (1) | EP2236945A3 (en) |
JP (1) | JP2010216800A (en) |
DE (1) | DE102009013755A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112815427A (en) * | 2021-02-04 | 2021-05-18 | 钟学能 | Energy-efficient air source heat pump system |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3922876A (en) * | 1974-11-21 | 1975-12-02 | Energy Conservation Unlimited | Energy conservation unit |
US4254630A (en) * | 1979-06-01 | 1981-03-10 | Carrier Corporation | Heat reclaiming method and apparatus |
US4342201A (en) * | 1980-02-19 | 1982-08-03 | Kawasaki Jukogyo Kabushiki Kaisha | Energy recovery apparatus for a gas compressor plant |
US6557535B2 (en) * | 2001-05-08 | 2003-05-06 | Ise Research Corporation | System and method for transferring heat from exhaust gasses to compressed gas fuel |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2721564A1 (en) * | 1976-08-12 | 1978-03-02 | Calorcal Ag | Refrigerator waste heat utilising system - is connected to water heater by heat exchanger in water tank |
JPS6022097A (en) * | 1983-07-18 | 1985-02-04 | Sumitomo Metal Ind Ltd | Gas compressing device |
DE3407438A1 (en) * | 1984-02-29 | 1985-09-12 | Hans-Jürgen 8391 Tittling Dietrich | Heating installation with fossil fuels combined with heat pump operated by heat |
JPH01170788A (en) * | 1987-12-25 | 1989-07-05 | Hitachi Ltd | Dry-type screw compressor having exhaust heat recovery device |
DE4111319A1 (en) * | 1991-04-08 | 1992-10-15 | Siemens Ag | Air-conditioning installation powered by buffered solar battery - includes forced draught heat exchanger fans and coolant compressor driven by motors independent of mains electricity |
DE20103351U1 (en) * | 2001-02-26 | 2001-05-23 | Fgn Ferngas Nordbayern Gmbh | Gas refueling system for motor vehicles |
JP2002346330A (en) * | 2001-05-23 | 2002-12-03 | Nippon Sanso Corp | Method and apparatus for manufacturing clean/dry air |
JP2005273958A (en) * | 2004-03-23 | 2005-10-06 | Sanyo Electric Co Ltd | Hot-water supply and heating apparatus |
JP4932525B2 (en) * | 2007-02-16 | 2012-05-16 | 株式会社日立プラントテクノロジー | Hydrogen station |
-
2009
- 2009-03-17 DE DE102009013755A patent/DE102009013755A1/en not_active Withdrawn
-
2010
- 2010-01-28 US US12/695,572 patent/US20100236261A1/en not_active Abandoned
- 2010-03-09 EP EP10002438.9A patent/EP2236945A3/en not_active Withdrawn
- 2010-03-17 JP JP2010060873A patent/JP2010216800A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3922876A (en) * | 1974-11-21 | 1975-12-02 | Energy Conservation Unlimited | Energy conservation unit |
US4254630A (en) * | 1979-06-01 | 1981-03-10 | Carrier Corporation | Heat reclaiming method and apparatus |
US4342201A (en) * | 1980-02-19 | 1982-08-03 | Kawasaki Jukogyo Kabushiki Kaisha | Energy recovery apparatus for a gas compressor plant |
US6557535B2 (en) * | 2001-05-08 | 2003-05-06 | Ise Research Corporation | System and method for transferring heat from exhaust gasses to compressed gas fuel |
Non-Patent Citations (1)
Title |
---|
Kilicarslan, A. and Müller, N. (2005), A comparative study of water as a refrigerant with some current refrigerants. Int. J. Energy Res., 29: 947-959. doi: 10.1002/er.1084 * |
Also Published As
Publication number | Publication date |
---|---|
JP2010216800A (en) | 2010-09-30 |
DE102009013755A1 (en) | 2010-09-23 |
EP2236945A3 (en) | 2014-03-26 |
EP2236945A2 (en) | 2010-10-06 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: LINDE AKTIENGESELLSCHAFT, GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:ADLER, ROBERT;DORNER, SASCHA;KLEIN, EKKEHARDT;REEL/FRAME:024070/0505 Effective date: 20100204 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |