CN102269141A - Ambient temperature engine - Google Patents

Ambient temperature engine Download PDF

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Publication number
CN102269141A
CN102269141A CN2011102232175A CN201110223217A CN102269141A CN 102269141 A CN102269141 A CN 102269141A CN 2011102232175 A CN2011102232175 A CN 2011102232175A CN 201110223217 A CN201110223217 A CN 201110223217A CN 102269141 A CN102269141 A CN 102269141A
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liquid phase
phase
vapour
pressure
valve
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CN102269141B (en
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文会桥
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Abstract

The invention relates to an ambient temperature engine which is composed of a sound-velocity-changing self-pressurizing energy-saving heat exchanger, a main device, a start device, a liquid phase supplement device and a vapor phase supplement device; motive power output is generated by the main device and the sound-velocity-changing self-pressurizing energy-saving heat exchanger; the engine is started by the start device; during the start process, the normal start is ensured through the liquid phase supplement device and the vapor phase supplement device; during the operation process, heat energy in the environment is absorbed by a heat absorption sheet; and the heat energy is converted into kinetic energy through the sound-velocity-changing self-pressurizing energy-saving heat exchanger, thus the motive power is output continuously. According to the invention, the functions of the novel sound-velocity-changing self-pressurizing energy-saving heat exchanger are utilized fully, the perfect structure supporting is realized, and the engine has the advantages of energy conservation, and energy sources can be developed and utilized preferably.

Description

The ambient temperature motor
Technical field
The present invention relates to a kind of motor, is a kind of heat energy that utilizes ambient temperature, through the fast effect from the boosting energy-saving heat exchanger of changing voice, produces the power plant of power.
Background technique
For the people of the present earth, the energy beyond doubt that is short of most.The human energy that be unable to do without has had fuel-engined vehicle to run, and has had the electric energy electric light just can be bright, and fan could change, none too busy to get away electric energy of various electrical equipment, or the like.And, all consuming the tellurian energy in large quantities every day along with expanding economy, make that the tellurian energy is more and more in short supply.Therefore, the new energy of exploitation is human very urgent task.Solar energy, wind energy or the like all are the very valuable energy, and people have also proposed the technology of various this respects.The mankind are aerial, and air has temperature, and air has temperature to be because the molecule of air is ceaselessly vibrating promptly small motion.Though this motion is not have the direction of determining, irregular, we can not directly extract its energy, but utilize a kind of suitable device, utilizing the principle of heat exchange and the mechanical structure of speed change supercharging, is that heat energy changes into kinetic energy with the temperature of air, is a kind of very significant trial.
Summary of the invention
To the objective of the invention is in order solving the problems of the technologies described above, to propose a kind of ambient temperature motor, utilize the principle of heat exchange and the supercharging of vapour-liquid speed change, convert the temperature thermal energy of air to kinetic energy, thus the energy utilization patterns that exploitation makes new advances.
The objective of the invention is to be achieved through the following technical solutions: a kind of ambient temperature motor, be provided with the speed of changing voice from the boosting energy-saving heat exchanger, it is characterized in that: be provided with main device, starting drive, liquid phase supplementary device and vapour phase supplementary device;
Described main device, be provided with the speed of changing voice from the boosting energy-saving heat exchanger, the liquid entering hole of this heat exchanger is communicated with the liquid phase outlet of a stored in liquid phase case by the liquid phase inlet passage of a band liquid phase import barrier valve, be provided with a vapour phase slow release device in this stored in liquid phase case, the vapor phase exit of this vapour phase slow release device is communicated with steamer chamber (19) steam inlet of steam turbine by a vapor phase channel that has vapour phase slowly-releasing valve, the indoor steamer of this steamer is in transmission connection through clutch (18) and power output wheel (17), the steam ouput of this steamer chamber is communicated with from the vapour phase import of boosting energy-saving heat exchanger with the described speed of changing voice by a vapor phase channel (26), on this vapor phase channel, be provided with endothermic plate (27), controlled electric heating apparatus (271), steam gauge (28) and vapour phase import barrier valve (29) are provided with pressure gauge (30) on described stored in liquid phase case; The speed of changing voice is with the liquid channel (6) of liquid phase control of export valve (7) to be communicated with the liquid phase import of described stored in liquid phase case from the liquid phase outlet of boosting energy-saving heat exchanger by one;
Described starting drive (B), be provided with startup capacity case (10), this startup capacity case is provided with the liquid phase import, and this liquid phase import is communicated with from the liquid phase outlet passage (6) of boosting energy-saving heat exchanger with the described speed of changing voice by autocontrol valve (9) and liquid phase delivery gauge (8);
Described liquid phase supplementary device (C), be provided with liquid phase pressure and replenish capacity case (11), this capacity case is provided with the liquid phase outlet, and this liquid phase outlet is communicated with the liquid phase pressurization passageway (16) of described stored in liquid phase case by liquid phase pressurized control valve (12) and liquid phase compression pump (13); The outlet of this liquid phase also is communicated with the bottom of stored in liquid phase case by described liquid phase pressurized control valve (12) and liquid phase compression pump (13) and a liquid phase pressurize one-way valve (14);
Described vapour phase supplementary device (D), be provided with vapour phase pressure and replenish capacity case (20), this capacity case is provided with vapor phase exit, this vapor phase exit is communicated with the steam ouput vapor phase channel of described steamer chamber by the passage (25) that has vapour phase pressurized control valve (22) and vapour phase compression pump (24), and this passage also is communicated with through the vapour phase import (21) that a vapour phase pressurize one-way valve (23) and described vapour phase pressure replenish the capacity case.
The operating method of above-mentioned ambient temperature motor, its feature may further comprise the steps:
1) start-up control valve (9), liquid phase pressurized control valve (12), vapour phase pressurized control valve (22), vapour phase import barrier valve (29), vapour phase slowly-releasing control valve (4) are closed;
2) in stored in liquid phase case (3) and connecting pipeline fill with the flowing medium that a kind of boiling point is lower than ambient temperature, as condensing agent CHCIF2 and make the storage box internal pressure reach this medium at ambient temperature saturation vapour pressure 3-5 doubly;
3) close liquid phase import barrier valve (2);
4) medium of the same race of injection one half volume in vapour phase pressure replenishes capacity case (20) and the additional capacity case (11) of liquid phase pressure, the space of second half volume is the saturated vapour of this kind medium;
5) will start capacity case (10) is evacuated;
6) inject the saturated vapour of medium of the same race in all airtight casings and the pipeline at other;
7) read each manometric numerical value, and according to pressure gauge numerical value the parameter of liquid phase compression pump (13) and vapour phase compression pump is set, calculation method of parameters is:
When pressure gauge 30 numerical value descend 30% the time, the liquid phase compression pump starts, and stops automatically after the pressure recovery;
When pressure gauge 28 numerical value descend 20% the time, the gas phase compression pump starts, and stops automatically after the pressure recovery;
8) regulate liquid phase pressurize one-way valve (14) and vapour phase pressurize one-way valve (23);
When pressure medium in the liquid phase volume case 3 reaches this medium at ambient temperature during 9 times of saturation vapour pressure force value, liquid phase pressurize one-way valve begins pressure release;
When vapor pressure value in the vapor phase channel 26 reach this medium at ambient temperature the saturation vapour pressure force value 95% the time, vapour phase pressurize one-way valve begins pressure release;
9) close liquid phase control of export valve (7) and liquid phase import barrier valve (2);
10) open liquid phase pressurized control valve (12) and vapour phase pressurized control valve (22);
11) timely and appropriate discovery is opened start-up control valve (9), vapour phase import barrier valve (29), liquid phase import barrier valve (2) successively, makes the liquid and vapor capacity of medium enter the speed of changing voice from boosting energy-saving heat exchanger (1), and enters startup capacity case (10) after the supercharging;
When 12) treating that the numerical value of liquid phase delivery gauge (8) is identical with the manometric numerical value of stored in liquid phase case, open liquid phase control of export valve (7), close start-up control valve (9);
13) open vapour phase slowly-releasing control valve (4);
14) closed clutch (18) makes power output;
15) load of adjustment power output wheel (17) makes the power engine smooth running.
About the described speed of changing voice from the in-built explanation of boosting energy-saving heat exchanger: this heat exchanger is formed by 3 sections: promptly both vapor compression section, vapour-liquid mixing section, spray the supercharging section, above-mentioned three sections form two chambers.What use in this heat exchanger is the medium that a kind of boiling point is lower than ambient temperature.Utilize material liquid phase compressibility less than the vapour phase compressibility, the vapour phase compressibility is less than the compressible physical features of vapour-liquid two-phase, in the rapid mixing process, form the fluidised form complexity, have a super compressible stream-liquid two-phase flow body, mixed rate of flow of fluid changes supersonic speed into by former velocity of sound rapidly, advance face and produce shock-wave effect, directly change self heat energy of liquid-vapor mixture into kinetic energy, make outlet pressure be several times as much as inlet pressure.This device is applied in the secondary propulsion system (SPS) of nuclear powered submarine the earliest, also is widely used in the heat exchange industry that heats at present.Actual measurement shows, in used in the heat supply field, the pressurized effect of this device was bright, but supercharging several times to 10 times.Because of its good pressurized effect, in heating heat exchange industry, the replaceable part or all of heating secondary cycle water pump of its function of increasing pressure, this device is based on two phase flow, the hot rerum natura of steam, the ternary stickiness, ultrasound velocity or next supersonic matrix principle, use continuity equation, energy equation, theorem of momentum, physical laws such as thermomechanics first and second laws, utilize steam and in mixed process, passed by the liquid phase of injection, mass transfer, the transfer function of energy and kinetic energy, generation is heated rapidly and is given birth to heat transfer by the liquid phase of injection in the mixed process incident, mass transfer, the transfer function of energy and momentum, produce the heavy again effect of heating rapidly and supercharging, in the heat exchange field, not only make water-exit temperature reach the requirement of heating and heat supply water, and operation can replace recycle pump substantially under design conditions.This device is applied to the present invention, can be by the pressurized effect in its gas-liquid transfer process, middle through liquid vapour two-phase mixed process generation shock-wave effect, make the thermal power transfer in the circulatory mediator become kinetic energy, and that medium heat energy obtains from environment in cyclic process is effectively additional, thus the final purpose that realizes the thermal power transfer in the environment is become kinetic energy.
The motion state of ambient temperature engine operation process medium of the present invention:
1) the medium liquid and vapor capacity enters the speed of changing voice from the boosting energy-saving heat exchanger by the vapour phase import and the liquid phase import of speed from boosting energy-saving heat exchanger (1) of changing voice respectively;
2) changing voice speed under the effect of boosting energy-saving device, the liquid and vapor capacity medium that enters boosts to original several times, exports with liquid phase state then;
3) liquid phase medium of above-mentioned output enters stored in liquid phase case (3);
4) partly entering stored in liquid phase case (3) medium transfers vapour phase to, because of the conversion of liquid vapour phase makes the temperature of medium descend;
5) temperature raise after low temperature vapour phase medium absorbed surrounding environment by endothermic plate, entered the speed of changing voice again from boosting energy-saving heat exchanger (1) through the vapour phase import;
6) import of low temperature liquid phase medium knot liquid phase enters the speed of changing voice from boosting energy-saving heat exchanger (1),
According to last preface circulation.
Ambient temperature motor of the present invention can be available kinetic energy with the temperature transition of surrounding material such as empty G﹠W etc., has novel structure, can effectively increase the utilizable energy source, the advantage that economic value and social value are high.
Description of drawings
Fig. 1 is a structural representation of the present invention.
The profile of product of the present invention is not subjected to the restriction of this figure, and only the profile change also belongs to protection domain of the present utility model.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the present invention is described further, embodiment: the ambient temperature motor, be provided with the speed of changing voice from the boosting energy-saving heat exchanger, and be provided with main device A, starting drive B, liquid phase supplementary device C and vapour phase supplementary device D;
Described main device A, be provided with the speed of changing voice from boosting energy-saving heat exchanger 1, the liquid entering hole of this heat exchanger is communicated with the liquid phase outlet of a stored in liquid phase case 3 by the liquid phase inlet passage 31 of a band liquid phase import barrier valve 2, be provided with a vapour phase slow release device 5 in this stored in liquid phase case, the vapor phase exit of this vapour phase slow release device is communicated with steamer chamber 19 steam inlets of steam turbine by a vapor phase channel that has vapour phase slowly-releasing valve 4, the indoor steamer of this steamer is in transmission connection through clutch 18 and power output wheel 17, the steam ouput of this steamer chamber is communicated with from the vapour phase import of boosting energy-saving heat exchanger with the described speed of changing voice by a vapor phase channel 26, on this vapor phase channel, be provided with endothermic plate 27, controlled electric heating apparatus 271, steam gauge 28 and vapour phase import barrier valve 29 are provided with pressure gauge 30 on described stored in liquid phase case; The speed of changing voice is with the liquid channel 6 of liquid phase control of export valve 7 to be communicated with the liquid phase import of described stored in liquid phase case from the liquid phase outlet of boosting energy-saving heat exchanger by one;
Described starting drive B is provided with startup capacity case 10, and this startup capacity case is provided with the liquid phase import, and this liquid phase import is communicated with from the liquid phase outlet passage 6 of boosting energy-saving heat exchanger with the described speed of changing voice by autocontrol valve 9 and liquid phase delivery gauge 8;
Described liquid phase supplementary device C is provided with liquid phase pressure and replenishes capacity case 11, and this capacity case is provided with the liquid phase outlet, and this liquid phase outlet is communicated with the liquid phase pressurization passageway 16 of described stored in liquid phase case by liquid phase pressurized control valve 12 and liquid phase compression pump 13; The outlet of this liquid phase also is communicated with the bottom of stored in liquid phase case by described liquid phase pressurized control valve 12 and liquid phase compression pump 13 and a liquid phase pressurize one-way valve 14;
Described vapour phase supplementary device D, be provided with vapour phase pressure and replenish capacity case 20, this capacity case is provided with vapor phase exit, this vapor phase exit is communicated with the steam ouput vapor phase channel of described steamer chamber by the passage 25 that has vapour phase pressurized control valve 22 and vapour phase compression pump 24, and this passage also is communicated with through the vapour phase import 21 that a vapour phase pressurize one-way valve 23 and described vapour phase pressure replenish the capacity case.
The above-mentioned ambient temperature motor of present embodiment is operated operation by the following method:
1) start-up control valve 9, liquid phase pressurized control valve 12, vapour phase pressurized control valve 22, vapour phase import barrier valve 29, vapour phase slowly-releasing control valve 4 are closed;
2) in stored in liquid phase case 3 and connecting pipeline fill with the flowing medium that a kind of boiling point is lower than ambient temperature, as condensing agent CHCIF2 and make the storage box internal pressure reach this medium at ambient temperature saturation vapour pressure 3-5 doubly;
3) close liquid phase import barrier valve 2;
4) medium of the same race of injection one half volume in vapour phase pressure replenishes capacity case 20 and the additional capacity case 11 of liquid phase pressure, the space of second half volume is the saturated vapour of this kind medium;
5) will start capacity case 10 is evacuated;
6) inject the saturated vapour of medium of the same race in all airtight casings and the pipeline at other;
7) read each manometric numerical value, and according to pressure gauge numerical value the parameter of liquid phase compression pump 13 and vapour phase compression pump is set, calculation method of parameters is:
When pressure gauge 30 numerical value descend 30% the time, the liquid phase compression pump starts, and stops automatically after the pressure recovery;
When pressure gauge 28 numerical value decline 20% is that the gas phase compression pump starts, and stops automatically after the pressure recovery;
8) regulate liquid phase pressurize one-way valve 14 and vapour phase pressurize one-way valve 23;
When pressure medium in the liquid phase volume case 3 reaches this medium at ambient temperature during 9 times of saturation vapour pressure force value, liquid phase pressurize one-way valve begins pressure release;
When vapor pressure value in the vapor phase channel 26 reach this medium at ambient temperature the saturation vapour pressure force value 95% the time, vapour phase pressurize one-way valve begins pressure release;
9) close liquid phase control of export valve 7 and liquid phase import barrier valve 2;
10) open liquid phase pressurized control valve 12 and vapour phase pressurized control valve 22
11) timely and appropriate discovery is opened start-up control valve 9, vapour phase import barrier valve 29, liquid phase import barrier valve 2 successively, makes the liquid and vapor capacity of medium enter the speed of changing voice from boosting energy-saving heat exchanger 1, and enters startup capacity case 10 after the supercharging;
When 12) treating that the numerical value of liquid phase delivery gauge 8 is identical with the manometric numerical value of stored in liquid phase case, open liquid phase control of export valve 7, close start-up control valve 9;
13) open vapour phase slowly-releasing control valve 4;
14) closed clutch 18 makes power output;
15) load of adjustment power output wheel 17 makes the power engine smooth running.
It below only is 1 embodiment of this patent; should be pointed out that for those skilled in the art, under the prerequisite that does not break away from the principle of the invention; can also make some improvements and modifications, these improvements and modifications also should be considered as the protection domain of this patent.

Claims (1)

1. an ambient temperature motor that uses following method operation is provided with the speed of changing voice from the boosting energy-saving heat exchanger, it is characterized in that: be provided with main device (A), starting drive (B), liquid phase supplementary device (C) and vapour phase supplementary device (D);
Described main device (A), be provided with the speed of changing voice from boosting energy-saving heat exchanger (1), the liquid entering hole of this heat exchanger is communicated with the liquid phase outlet of a stored in liquid phase case (3) by the liquid phase inlet passage (31) of a band liquid phase import barrier valve (2), be provided with a vapour phase slow release device (5) in this stored in liquid phase case, the vapor phase exit of this vapour phase slow release device is communicated with steamer chamber (19) steam inlet of steam turbine by a vapor phase channel that has vapour phase slowly-releasing valve (4), the indoor steamer of this steamer is in transmission connection through clutch (18) and power output wheel (17), the steam ouput of this steamer chamber is communicated with from the vapour phase import of boosting energy-saving heat exchanger with the described speed of changing voice by a vapor phase channel (26), on this vapor phase channel, be provided with endothermic plate (27), controlled electric heating apparatus (271), steam gauge (28) and vapour phase import barrier valve (29) are provided with pressure gauge (30) on described stored in liquid phase case; The speed of changing voice is with the liquid channel (6) of liquid phase control of export valve (7) to be communicated with the liquid phase import of described stored in liquid phase case from the liquid phase outlet of boosting energy-saving heat exchanger by one;
Described starting drive (B), be provided with startup capacity case (10), this startup capacity case is provided with the liquid phase import, and this liquid phase import is communicated with from the liquid phase outlet passage (6) of boosting energy-saving heat exchanger with the described speed of changing voice by autocontrol valve (9) and liquid phase delivery gauge (8);
Described liquid phase supplementary device (C), be provided with liquid phase pressure and replenish capacity case (11), this capacity case is provided with the liquid phase outlet, and this liquid phase outlet is communicated with the liquid phase pressurization passageway (16) of described stored in liquid phase case by liquid phase pressurized control valve (12) and liquid phase compression pump (13); The outlet of this liquid phase also is communicated with the bottom of stored in liquid phase case by described liquid phase pressurized control valve (12) and liquid phase compression pump (13) and a liquid phase pressurize one-way valve (14);
Described vapour phase supplementary device (D), be provided with vapour phase pressure and replenish capacity case (20), this capacity case is provided with vapor phase exit, this vapor phase exit is communicated with the steam ouput vapor phase channel of described steamer chamber by the passage (25) that has vapour phase pressurized control valve (22) and vapour phase compression pump (24), and this passage also is communicated with through the vapour phase import (21) that a vapour phase pressurize one-way valve (23) and described vapour phase pressure replenish the capacity case;
The operating method of above-mentioned ambient temperature motor, its feature may further comprise the steps:
1) start-up control valve (9), liquid phase pressurized control valve (12), vapour phase pressurized control valve (22), vapour phase import barrier valve (29), vapour phase slowly-releasing control valve (4) are closed;
2) in stored in liquid phase case (3) and connecting pipeline fill with the flowing medium that a kind of boiling point is lower than ambient temperature, as condensing agent CHCIF2 and make the storage box internal pressure reach this medium at ambient temperature saturation vapour pressure 3-5 doubly;
3) close liquid phase import barrier valve (2);
4) medium of the same race of injection one half volume in vapour phase pressure replenishes capacity case (20) and the additional capacity case (11) of liquid phase pressure, the space of second half volume is the saturated vapour of this kind medium;
5) will start capacity case (10) is evacuated;
6) inject the saturated vapour of medium of the same race in all airtight casings and the pipeline at other;
7) read each manometric numerical value, and according to pressure gauge numerical value the parameter of liquid phase compression pump (13) and vapour phase compression pump is set, calculation method of parameters is:
When pressure gauge 30 numerical value descend 30% the time, the liquid phase compression pump starts, and stops automatically after the pressure recovery;
When pressure gauge 28 numerical value descend 20% the time, the gas phase compression pump starts, and stops automatically after the pressure recovery;
8) regulate liquid phase pressurize one-way valve (14) and vapour phase pressurize one-way valve (23);
When pressure medium in the liquid phase volume case 3 reaches this medium at ambient temperature during 9 times of saturation vapour pressure force value, liquid phase pressurize one-way valve begins pressure release;
When vapor pressure value in the vapor phase channel 26 reach this medium at ambient temperature the saturation vapour pressure force value 95% the time, vapour phase pressurize one-way valve begins pressure release;
9) close liquid phase control of export valve (7) and liquid phase import barrier valve (2);
10) open liquid phase pressurized control valve (12) and vapour phase pressurized control valve (22);
11) timely and appropriate discovery is opened start-up control valve (9), vapour phase import barrier valve (29), liquid phase import barrier valve (2) successively, makes the liquid and vapor capacity of medium enter the speed of changing voice from boosting energy-saving heat exchanger (1), and enters startup capacity case (10) after the supercharging;
When 12) treating that the numerical value of liquid phase delivery gauge (8) is identical with the manometric numerical value of stored in liquid phase case, open liquid phase control of export valve (7), close start-up control valve (9);
13) open vapour phase slowly-releasing control valve (4);
14) closed clutch (18) makes power output;
15) load of adjustment power output wheel (17) makes the power engine smooth running.
CN 201110223217 2011-08-05 2011-08-05 Ambient temperature engine Expired - Fee Related CN102269141B (en)

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Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
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CN102269141B CN102269141B (en) 2013-08-21

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5219530A (en) * 1991-02-15 1993-06-15 Board Of Regents Of The University Of Washington Apparatus for initiating pyrolysis using a shock wave
WO2000060226A1 (en) * 1999-04-06 2000-10-12 Branko Stankovic Brayton or brayton-rankine combined cycle with hot-gas recirculation and inverse mixing ejector
RU2193096C1 (en) * 2001-08-02 2002-11-20 Дочернее открытое акционерное общество "Центральное конструкторское бюро нефтеаппаратуры" Открытого акционерного общества "Газпром" Method of operation of gas turbine plant
CN101196375A (en) * 2007-12-24 2008-06-11 常州市绿空能源设备有限公司 Impact wave heater
CN201184755Y (en) * 2008-02-03 2009-01-21 新疆东海热能科技开发有限公司 Acoustic-speed-varying supercharging heat pump type heat exchanger

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5219530A (en) * 1991-02-15 1993-06-15 Board Of Regents Of The University Of Washington Apparatus for initiating pyrolysis using a shock wave
WO2000060226A1 (en) * 1999-04-06 2000-10-12 Branko Stankovic Brayton or brayton-rankine combined cycle with hot-gas recirculation and inverse mixing ejector
RU2193096C1 (en) * 2001-08-02 2002-11-20 Дочернее открытое акционерное общество "Центральное конструкторское бюро нефтеаппаратуры" Открытого акционерного общества "Газпром" Method of operation of gas turbine plant
CN101196375A (en) * 2007-12-24 2008-06-11 常州市绿空能源设备有限公司 Impact wave heater
CN201184755Y (en) * 2008-02-03 2009-01-21 新疆东海热能科技开发有限公司 Acoustic-speed-varying supercharging heat pump type heat exchanger

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