专利摘要:
The high-pressure gas-liquid drive unit contains two high-pressure heat exchangers (A) (B), in which gas (1) (2) and liquid (3) (4) are located and in the initial state the same high pressure prevails. In the first heat exchanger (A), the gas pressure is increased by supplying heat via register (5) and double jacket (16). In the second heat exchanger (B), the gas pressure is reduced by cooling via register (6) and double jacket (16). The liquid in heat exchanger (A) is passed through the pressure difference in the two heat exchangers when opening the valves (11,15,12,14) via the compressor (7) in the heat exchanger (B) at a lower pressure, which is a displacement of the piston (8) causes and via separate gas chambers (9,10) for driving a turbine and for heat-cooling generation, until the pressure equalization takes place in both high-pressure heat exchangers (A, B). The increased liquid level in the high-pressure heat exchanger (B) is compensated by opening the valve (13) via the connecting line of the two high-pressure heat exchangers (A) (B). The continuous operation of the piston (8) takes place by connecting several stations (I) (II) in series from two high-pressure heat exchangers (A) (B).
公开号:AT511077A4
申请号:T11842011
申请日:2011-08-16
公开日:2012-09-15
发明作者:
申请人:Innova Gebaeudetechnik Gmbh;
IPC主号:
专利说明:

• t · »·
description
The invention relates to a high-pressure gas drive unit with which gas is compressed on the basis of temperature and pressure differences in high-pressure heat exchangers, which gas is used in conjunction with a fluid to drive a turbine.
From US 5 259 363 a plant for solar production is known, as well as patent AT 410 966 B. It describes a device for compressing a gas by solar energy and / or ambient heat, wherein a first heat exchanger at a high temperature level and a second heat exchanger at a low temperature level and in between a turbine is provided for the delivery of mechanical energy.
The invention aims at the fact that in the high-pressure heat exchange partly gas, partly liquid, wherein the liquid is passed through the compressed gas via the compressor in the second high-pressure heat exchanger. The advantage is that, when pressure equalization has taken place in the two high-pressure heat exchangers, the liquid which has risen in the second high-pressure heat exchanger is restored by opening a valve via a connecting line of the two high-pressure heat exchangers in the two high-pressure heat exchangers, whereby the gas does not described in Patent AT 410 966 B, after pressure equalization by a pump - which consumes additional energy - must be returned (see features in claim 1 and 2). Furthermore, the respective temperature of the two high-pressure heat exchangers is not changed, the first high pressure heat exchanger remains in the high temperature range, the second high pressure heat exchanger in the low temperature range, which brings additional energy savings (see feature in claim 3).
The invention will be further explained with reference to the accompanying drawings. Fig. 1 shows a schematic representation of the system. 1 · · · «· · ·« «« * »· * * * * * t I ·
* i * * * * * * a «a
The drive unit consists of two high-temperature chambers A and B in station I, in which gas and liquid are located and in the initial state the pressure is the same. In the first heat exchanger A, the gas 1 and the liquid 3, for example, by solar energy, geothermal, industrial waste heat and the like, heated via register 5 and double jacket 16, which leads to pressure increase in this heat exchanger A. In the second heat exchanger B, the gas 2 and the liquid 4 are e.g. due to lower ambient temperature, cooling water, industrial cooling, wind influence, etc., cooled via register 6 and double jacket 16, which causes pressure drop in this heat exchanger B.
The two high-pressure heat exchangers A and B are connected to lines and valves 11, 12 and 14, 15. The liquid in high-pressure heat exchanger A is passed through the gas in the overpressure opening of the valves 11 and 15 via the compressor 7 in the lower pressure located high-pressure heat exchanger ß and acts on the piston 8. After the operation of the piston 8, the valves are 12th and 14, whereby the piston 8 moves in the opposite direction. These piston movements are used in a secondary gas circulation 9 and 10 for driving a turbine and also serve by pressing and relaxing the gas for heat generation and cooling. This effect persists until the pressure equalization in both high-pressure heat exchangers A and B occurs.
Since now the liquid in the high-pressure heat exchanger B is at a higher level than in the high-pressure heat exchanger A, the level compensation of the liquids is restored when the valve 13 is opened via the high-pressure heat exchanger connecting line.
The cycle may begin anew after heating of high pressure heat exchanger A and cooling of high pressure heat exchanger B.
The continuous continuation of the operation of the piston 8 is ensured in the meantime by station II or more downstream stations. 2
权利要求:
Claims (3)
[1]
«* * · • · · · · ······················································································································································································································· is compressed on the basis of temperature and pressure differences in high pressure heat exchangers (A) (B) via a compressor (7) gas (9) (10), which is used to drive a turbine and for heat and cold generation, characterized in that in the high-pressure heat exchangers (A) (B) partially gas (1) (2) and liquid (3) (4) and the compressed gas (1) acts on the liquid (3), the piston (8) from the compressor (8) 7) drives.
[2]
2. High-pressure gas drive unit according to claim 1, characterized in that the standing at the same level high-pressure heat exchanger (A) (B) are connected by a line with valve (13), which at opening a pressure and level compensation of gas (1 ) (2) and liquid (3) (4).
[3]
3. High-pressure gas drive unit according to claim 1 and 2, characterized in that the temperatures of the two high pressure heat exchanger (A) (B) do not alternate, the first high pressure heat exchanger (A) remains in the high temperature range, the second high pressure heat exchanger (B) in the N I retire in peruvium. 1
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同族专利:
公开号 | 公开日
WO2013023231A2|2013-02-21|
WO2013023231A3|2014-04-10|
AT511077B1|2012-09-15|
EP2744985A2|2014-06-25|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题
AT410966B|2001-03-16|2003-09-25|Bammer Peter|DEVICE FOR COMPRESSING A GAS BY MEANS OF SOLAR ENERGY AND / OR AMBIENT HEAT|
WO2003081011A1|2002-03-27|2003-10-02|Richard Laurance Lewellin|Engine for converting thermal energy to stored energy|
US20050198960A1|2004-03-12|2005-09-15|Marnoch Ian A.|Thermal conversion device and process|
AT502402A4|2006-01-10|2007-03-15|Int Innovations Ltd|METHOD FOR CONVERTING THERMAL ENERGY TO MECHANICAL WORK|AT519851A1|2017-03-14|2018-10-15|Daniel Erwin|High pressure energy generator|AT210966B|1959-04-20|1960-09-10|Medek & Schoerner|Arrangement for supplying energy to AC synchronous motors from DC sources, in particular chemical elements|
DE4127135A1|1991-08-15|1993-02-18|Gunther Guenter Schlicht|Electrical energy generation process - uses explosion of inflammable material to drive turbine|
US5259363A|1991-12-23|1993-11-09|Lolar Logistics, Inc.|Solar roofing system|
DE102007045888B4|2007-09-25|2010-04-15|Ea Energiearchitektur Gmbh|Process for conversion and storage of regenerative energy|AT514222A1|2013-04-30|2014-11-15|Seyfried Andrea Mag|drive unit|
DE102013009351B8|2013-06-04|2014-05-28|Maschinenwerk Misselhorn Mwm Gmbh|Plant and method for recovering energy from heat in a thermodynamic cycle|
CN104061029B|2014-05-16|2015-12-30|张中和|A kind of solar energy heating fluid temperature difference supercharging air power generating equipment|
CN107939622A|2017-10-30|2018-04-20|黄丽贤|A kind of solar energy turns mechanical energy structure|
PL424234A1|2018-01-09|2019-07-15|Dobriański Jurij|Steam engine|
法律状态:
2017-04-15| MM01| Lapse because of not paying annual fees|Effective date: 20160816 |
优先权:
申请号 | 申请日 | 专利标题
AT11842011A|AT511077B1|2011-08-16|2011-08-16|HIGH PRESSURE GAS DRIVE UNIT|AT11842011A| AT511077B1|2011-08-16|2011-08-16|HIGH PRESSURE GAS DRIVE UNIT|
PCT/AT2012/000213| WO2013023231A2|2011-08-16|2012-08-16|High-pressure gas drive unit|
EP12759620.3A| EP2744985A2|2011-08-16|2012-08-16|High-pressure gas drive unit|
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