CN102588021B - Power generating system - Google Patents
Power generating system Download PDFInfo
- Publication number
- CN102588021B CN102588021B CN201210054673.6A CN201210054673A CN102588021B CN 102588021 B CN102588021 B CN 102588021B CN 201210054673 A CN201210054673 A CN 201210054673A CN 102588021 B CN102588021 B CN 102588021B
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- China
- Prior art keywords
- ammoniacal liquor
- chamber
- ammonia
- high pressure
- liquor
- Prior art date
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 115
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 103
- 238000010438 heat treatment Methods 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 238000001816 cooling Methods 0.000 claims abstract description 8
- 238000001704 evaporation Methods 0.000 claims abstract description 7
- 229910021529 ammonia Inorganic materials 0.000 claims description 57
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 45
- 230000008016 vaporization Effects 0.000 claims description 30
- 238000009834 vaporization Methods 0.000 claims description 29
- 238000005406 washing Methods 0.000 claims description 26
- 239000000243 solution Substances 0.000 claims description 21
- 238000006243 chemical reaction Methods 0.000 claims description 19
- 229940057995 liquid paraffin Drugs 0.000 claims description 16
- 238000002347 injection Methods 0.000 claims description 12
- 239000007924 injection Substances 0.000 claims description 12
- 239000012188 paraffin wax Substances 0.000 claims description 12
- 239000003570 air Substances 0.000 claims description 10
- 238000010248 power generation Methods 0.000 claims description 10
- 239000012080 ambient air Substances 0.000 claims description 9
- 239000011259 mixed solution Substances 0.000 claims description 6
- 238000010304 firing Methods 0.000 claims description 5
- 230000008020 evaporation Effects 0.000 abstract description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 abstract 12
- 239000007789 gas Substances 0.000 description 10
- 239000003365 glass fiber Substances 0.000 description 9
- 239000007788 liquid Substances 0.000 description 7
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 238000005057 refrigeration Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000002207 thermal evaporation Methods 0.000 description 2
- 230000005619 thermoelectricity Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The invention relates to a power generating system high in energy efficiency, which comprises a heating system, an ammonia water separating device, a first high-pressure gas storage tank and a second high-pressure gas storage tank. An outlet of the first high-pressure gas storage tank is connected with a gas inlet of a gas motor, an outlet of the second high-pressure gas storage tank is connected with an inlet end of an expansion valve through a cooling pipe positioned in external air, an outlet end of the expansion valve is connected with an inlet end of a refrigerating pipe, and an outlet end of the refrigerating pipe is connected with a diluted ammonia water generating chamber used for dissolving ammonia gas into water. A strong ammonia water generating chamber is communicated with one side of the diluted ammonia water generating chamber and connected with a gas outlet of the gas motor, and the refrigerating pipe is arranged in ammonia water solution of the strong ammonia water generating chamber. The strong ammonia water generating chamber is connected with an ammonia water evaporation chamber in the ammonia water separating device through a pipeline with a pump, and a diluted ammonia water outlet end of the ammonia water evaporation chamber is connected with the diluted ammonia water generating chamber.
Description
The application is divisional application, and the application number of original application is: 201010115528.5, and the applying date is: in March, 2010
2, invention and created name was: a kind of power generation system.
Technical field
The system that to the present invention relates to thermal power transfer be mechanical energy, is specially a kind of power generation system.
Background technique
In prior art, steam turbine generator is typical thermoelectricity conversion equipment, is widely used in thermoelectricity plant.Its deficiency is: existing steam turbine generator is to adopt hot water and steam driving steam turbine to rotate generating, and the efficiency that the thermal power transfer of hot steam is electric energy is not generally higher than 30%, so its heat utilization rate is lower.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of simple in structure, power generation system that efficiency is higher.
In order to solve the problems of the technologies described above, the invention provides power generation system, it comprises: heating system a, for utilize heating system a heating ammonia spirit and by the ammonia steam evaporating through high-valency alcohol solution or liquid paraffin n wash to obtain the ammoniacal liquor segregating unit b of pure ammonia, for collecting the ammonia of ammoniacal liquor segregating unit b output and heating to form the first high pressure tank c and the second high pressure tank d of high pressure ammonia through heating system a; The outlet of the first high pressure tank c is connected with gas motor air intake; The outlet of the second high pressure tank d is connected with the entry end of expansion valve f through the cooling tube e that is placed in ambient air, the outlet end of expansion valve f is connected with the entry end of refrigerator pipes g, and the outlet end g1 of refrigerator pipes g generates chamber v with the light ammoniacal liquor for ammonia being dissolved in to water and is connected; The side that light ammoniacal liquor generates chamber v is communicated with concentrated ammonia liquor generation chamber j; Concentrated ammonia liquor generates chamber j and is connected with the gas outlet k of described gas motor, and described refrigerator pipes g is arranged in the ammonia spirit of concentrated ammonia liquor generation chamber j; Concentrated ammonia liquor generates chamber j and is connected with the ammoniacal liquor vaporization chamber b1 in ammoniacal liquor segregating unit b by the pipeline that is provided with pump m; The light ammoniacal liquor outlet end b8 of ammoniacal liquor vaporization chamber b1 generates chamber v with light ammoniacal liquor and is connected.
Further, in described ammoniacal liquor vaporization chamber b1, be provided with injection pipe, and be connected by the economizer bank p for preheating concentrated ammonia liquor that is placed in ambient air between this injection pipe and described pump m; Injection pipe is distributed in whole ammoniacal liquor vaporization chamber b1, and is distributed with spray-hole on the tube wall of injection pipe, to spray concentrated ammonia liquor, can greatly accelerate the evaporation of ammonia.
Further, described light ammoniacal liquor outlet end b8 and light ammoniacal liquor generate between the v of chamber and are connected by the precooling pipe q for pre-cold ammoniacal liquor that is placed in ambient air, and the entry end of precooling pipe q is provided with flow control valve r.
Further, described ammoniacal liquor segregating unit b comprises: the top cover b2 that is placed in the ammonia spirit liquid level top of described ammoniacal liquor vaporization chamber b1, top cover b2 top is provided with the first u of washing chamber and the second w of washing chamber that are isolated from each other, so that described the first high pressure tank c and the second high pressure tank d have different air pressure; And described high-valency alcohol solution or liquid paraffin n are located in the first u of washing chamber and the second w of washing chamber.
Further, in described the first u of washing chamber and the second w of washing chamber, be provided with the multiple bend pipe b4 that communicate with described ammoniacal liquor vaporization chamber b1, the elbow of each bend pipe b4 extends into (outlet that is the elbow end of each bend pipe b4 extends in described high-valency alcohol solution or liquid paraffin n) in described high-valency alcohol solution or liquid paraffin n, ammonia steam is fully mixed with described high-valency alcohol solution or liquid paraffin n, guarantee fully separating of hot ammonia and water vapour.The first high pressure tank c and the second high pressure tank d are located at the top of high-valency alcohol solution or liquid paraffin n, and be provided with the first glass fibre layer between the entrance of the first high pressure tank c and the first u of washing chamber, between the entrance of the second high pressure tank d and the second w of washing chamber, be provided with the second glass fibre layer s, the first glass fibre layer and the second glass fibre layer s are isolated from each other, so that described the first high pressure tank c and the second high pressure tank d have different air pressure.
Further, between the bottom of described the first u of washing chamber and the second w of washing chamber and described ammoniacal liquor vaporization chamber b1, be respectively equipped with a water return pipeline t, this water return pipeline t has the vertical bending section t1 higher than the high-valency alcohol solution in described the first u of washing chamber and the second w of washing chamber or liquid paraffin n liquid level.Because the proportion of water is greater than high-valency alcohol solution or liquid paraffin, therefore adopt the water return pipeline t of this shape, be beneficial to and send isolated moisture in high-valency alcohol solution or liquid paraffin n back to described ammoniacal liquor vaporization chamber b1.
Further, described heating system a comprises: for holding the reaction vessel a1 of mixed solution of paraffin and ethanol, reaction vessel a1 below is provided with for described mixed solution being heated to 125 DEG C and above to generate the firing chamber a2 of alcohol vapour, on reaction vessel a1, be connected with the heat exchange return pipe a3 for the heat energy of heat outputting steam, this heat exchange return pipe a3 extends in the ammonia spirit of described ammoniacal liquor vaporization chamber b1, and is set around on described the first high pressure tank c and the second high pressure tank d.
Further, the air pressure of described high pressure ammonia is 8-13kg/cm
2, described heating system a is suitable for making the ammonia spirit in described ammoniacal liquor vaporization chamber b1 to remain on 36-70 DEG C.
Technique scheme of the present invention has the following advantages compared to existing technology: when (1) power generation system work of the present invention, utilize the ammonia spirit in heating system heating ammoniacal liquor segregating unit, make ammonia spirit be subject to thermal evaporation, and (now the temperature of ammonia is at least 36 DEG C, and air pressure is at 8-13kg/cm after separation ammonia and water vapour, to obtain high pressure ammonia
2, even higher).It is exothermic reaction that ammonia is got back in ammoniacal liquor, and ammonia temperature is raise, and corresponding ammonia concn will reduce, and water temperature raises, and the quality of the water dissolved ammonia of unit mass reduces.Therefore, must generate chamber and concentrated ammonia liquor generation chamber cooling to light ammoniacal liquor, otherwise light ammoniacal liquor generates chamber and concentrated ammonia liquor generation chamber will keep higher temperature, is unfavorable for the dissolving of ammonia and generates concentrated ammonia liquor.(2) ammonia spirit is subject to thermal evaporation, after high-valency alcohol, ammonia is separated with water vapour, has realized lower temperature (37-70 DEG C) in the situation that and also can evaporate ammonia, and obtained the ammonia (8-13kg/cm of higher pressure
2).(3) in heating system, firing chamber by the paraffin solution in reaction vessel be heated to 125 DEG C and more than, when the liquid ethanol that heat exchange return pipe refluxes enters the paraffin solution in reaction vessel, to there is quick exothermic reaction, thereby the water fast vaporizing in paraffin solution is become to hot ethanol steam and sends into heat exchange return pipe, and in periphery cooling rear formation liquid ethanol, be back in reaction vessel and again carry out exothermic reaction with paraffin, so iterative cycles.When the work of this heating system, the efficiency of Heat of Formation alcohol vapour is higher, with respect to the method for direct heating alcohol solution Heat of Formation alcohol vapour, this heating system can be saved 80% heat energy, so that the present invention has advantages of is can be significantly energy-conservation and user cost is lower.
Brief description of the drawings
For content of the present invention is more likely to be clearly understood, below the specific embodiment by reference to the accompanying drawings of basis, the present invention is further detailed explanation, wherein
Fig. 1 is the structural representation of the heating system in the power generation system in embodiment;
Fig. 2 is the structural representation of the power generation system in embodiment.
Embodiment
See Fig. 1 to 2, the power generation system of the present embodiment, comprising: heating system a, for utilize heating system a heating ammonia spirit and by the ammonia steam evaporating through high-valency alcohol solution or liquid paraffin n washing (adopting high-valency alcohol or liquid paraffin solution heat of dissociation ammonia and water vapour) obtaining the ammoniacal liquor segregating unit b of pure ammonia, for collecting the ammonia of ammoniacal liquor segregating unit b output and heating to form the first high pressure tank c and the second high pressure tank d of high pressure ammonia through heating system a; The outlet of the first high pressure tank c is connected with the air intake of gas motor through septum valve h, then drives all kinds of mechanokinetic equipment or the instruments of needing by gas motor, for example: vehicle, boats and ships, generator or the equipment of industrial product etc.
The outlet of the second high pressure tank d is connected with the entry end of expansion valve f through the cooling tube e that is placed in ambient air, the outlet end of expansion valve f is connected with the entry end of refrigerator pipes g, and the outlet end g1 of refrigerator pipes g generates chamber v with the light ammoniacal liquor for ammonia being dissolved in to water and is connected; The side that light ammoniacal liquor generates chamber v is communicated with concentrated ammonia liquor generation chamber j; Concentrated ammonia liquor generates chamber j and is connected with the gas outlet k of described gas motor, and described refrigerator pipes g is arranged in the ammonia spirit of concentrated ammonia liquor generation chamber j; Concentrated ammonia liquor generates chamber j and is connected with the ammoniacal liquor vaporization chamber b1 in ammoniacal liquor segregating unit b by the pipeline that is provided with pump m; The light ammoniacal liquor outlet end b8 of ammoniacal liquor vaporization chamber b1 generates chamber v with light ammoniacal liquor and is connected.
Cooling tube e is for the high pressure ammonia of cooling the second high pressure tank d output, then send into expansion valve step-down and generate the cold ammonia of 3 DEG C of left and right and send into refrigerator pipes g refrigeration, offset the heat energy of emitting when ammonia is dissolved in the water to generate at light ammoniacal liquor in chamber v and concentrated ammonia liquor generation chamber j.
In ammoniacal liquor vaporization chamber (b1), be provided with injection pipe, and be connected by the economizer bank p for preheating concentrated ammonia liquor that is placed in ambient air between this injection pipe and described pump m; Injection pipe is distributed in whole ammoniacal liquor vaporization chamber (b1), and is distributed with spray-hole on the tube wall of injection pipe.
After concentrated ammonia liquor in economizer bank p economizer bank, concentrated ammonia liquor is sent into described ammoniacal liquor vaporization chamber b1, to reduce the heating load of described heating system a, realize energy-conservation object.
Described light ammoniacal liquor outlet end b8 and light ammoniacal liquor generate between the v of chamber and are connected by the precooling pipe q for pre-cold ammoniacal liquor that is placed in ambient air, to reduce the energy consumption of refrigeration.And the entry end of precooling pipe q is provided with flow control valve r, send into described light ammoniacal liquor from ammoniacal liquor vaporization chamber b1 to generate ammoniacal liquor flow the pilot pressure of chamber v poor for controlling, thereby the ammonia steam output of controlling ammoniacal liquor vaporization chamber b1, makes the air pressure of the first high pressure tank c and the second high pressure tank d remain on 8-13kg/cm
2.
Described ammoniacal liquor segregating unit b comprises: the top cover b2 that is placed in the ammonia spirit liquid level top of described ammoniacal liquor vaporization chamber b1, top cover b2 top is provided with the first u of washing chamber and the second w of washing chamber that are isolated from each other, and described high-valency alcohol solution or liquid paraffin n are located in the first u of washing chamber and the second w of washing chamber.
In described the first u of washing chamber and the second w of washing chamber, be provided with the multiple bend pipe b4 that communicate with described ammoniacal liquor vaporization chamber b1, the elbow of each bend pipe b4 extends in described high-valency alcohol solution or liquid paraffin n, the first high pressure tank c and the second high pressure tank d are located at the top of high-valency alcohol solution or liquid paraffin n, and be provided with the first glass fibre layer between the entrance of the first high pressure tank c and the first u of washing chamber, between the entrance of the second high pressure tank d and the second w of washing chamber, be provided with the second glass fibre layer s, the first glass fibre layer and the second glass fibre layer s are isolated from each other.
Between the bottom of described the first u of washing chamber and the second w of washing chamber and described ammoniacal liquor vaporization chamber b1, be respectively equipped with a water return pipeline t, this water return pipeline t has the vertical bending section t1 higher than the high-valency alcohol solution in described the first u of washing chamber and the second w of washing chamber or liquid paraffin n liquid level.
Described glass fibre layer, as suction zones, further to reduce the water vapour containing in ammonia, is guaranteed the refrigeration of high pressure ammonia when by expansion valve d.
Described heating system a comprises: for holding the reaction vessel a1 of mixed solution of paraffin and ethanol, reaction vessel a1 below is provided with for described mixed solution being heated to 125 DEG C and above to generate the firing chamber a2 of alcohol vapour, on reaction vessel a1, be connected with the heat exchange return pipe a3 for the heat energy of heat outputting steam, this heat exchange return pipe a3 extends in the ammonia spirit of described ammoniacal liquor vaporization chamber b1, and is set around on described the first high pressure tank c and the second high pressure tank d.
The air pressure of described high pressure ammonia is 8-13kg/cm2, and described heating system a is suitable for making the ammonia spirit in described ammoniacal liquor vaporization chamber b1 to remain on 36-70 DEG C.Firing chamber a2 uses carbon, rock gas, all kinds of incendivity resources of former wet goods.
When paraffin temperature is at 125 DEG C and when above, the area of contact of paraffin molecule and ethanol molecule is very large, and paraffin molecule produces heat energy while contact with water molecule, and this heat energy, rapidly by ethanol evaporation, forms hot ethanol steam.Hot ethanol steam through heat exchange return pipe a3 output heat energy and with described ammoniacal liquor vaporization chamber b1, the first high pressure tank c and the second high pressure tank d heat exchange after be cooled to liquid ethanol, be back in reaction vessel a1 and again carry out exothermic reaction with paraffin, so circulation; During this time, firing chamber a2 all the time the temperature of the paraffin solution in reaction vessel a1 is remained on 125 DEG C and more than.
The air pressure of described high pressure ammonia is 8-13kg/cm2, and described heating system a is suitable for making the ammonia spirit in described ammoniacal liquor vaporization chamber b1 to remain on 37-70 DEG C.
In described refrigerator pipes g, be filled with hydrogen or argon gas, can further improve the refrigeration of the ammonia after step-down; The top that described light ammoniacal liquor generates chamber v is also provided with the reflow pipe for reflux described hydrogen or argon gas being connected with the entrance of described refrigerator pipes g.
Obviously, above-described embodiment is only for example of the present invention is clearly described, and is not the restriction to embodiments of the present invention.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here without also giving exhaustive to all mode of executions.And these belong to apparent variation that spirit of the present invention extended out or variation still among protection scope of the present invention.
Claims (1)
1. a power generation system, is characterized in that comprising: heating system (a), for utilize heating system (a) heating ammonia spirit and by the ammonia steam evaporating through high-valency alcohol solution or liquid paraffin (n) washing with obtain the ammoniacal liquor segregating unit (b) of pure ammonia, for collect the ammonia of ammoniacal liquor segregating unit (b) output and through heating system (a) heating to form the first high pressure tank (c) and second high pressure tank (d) of high pressure ammonia;
The outlet of the first high pressure tank (c) is connected with gas motor air intake;
The outlet of the second high pressure tank (d) is connected with the entry end of expansion valve (f) through the cooling tube (e) that is placed in ambient air, the outlet end of expansion valve (f) is connected with the entry end of refrigerator pipes (g), and the outlet end (g1) of refrigerator pipes (g) generates chamber (v) with the light ammoniacal liquor for ammonia being dissolved in to water and is connected; The side that light ammoniacal liquor generates chamber (v) is communicated with concentrated ammonia liquor generation chamber (j);
Concentrated ammonia liquor generates chamber (j) and is connected with the gas outlet (k) of described gas motor, and described refrigerator pipes (g) is arranged in the ammonia spirit of concentrated ammonia liquor generation chamber (j);
Concentrated ammonia liquor generates chamber (j) and is connected with the ammoniacal liquor vaporization chamber (b1) in ammoniacal liquor segregating unit (b) by the pipeline that is provided with pump (m);
The light ammoniacal liquor outlet end (b8) of ammoniacal liquor vaporization chamber (b1) generates chamber (v) with light ammoniacal liquor and is connected;
In described ammoniacal liquor vaporization chamber (b1), be provided with injection pipe, and be connected by the economizer bank for preheating concentrated ammonia liquor (p) that is placed in ambient air between this injection pipe and described pump (m); Injection pipe is distributed in whole ammoniacal liquor vaporization chamber
(b1) in, and be distributed with spray-hole on the tube wall of injection pipe;
Described light ammoniacal liquor outlet end (b8) and light ammoniacal liquor generate between chamber (v) and are connected by the precooling pipe (q) for pre-cold ammoniacal liquor that is placed in ambient air, and the entry end of precooling pipe (q) is provided with flow control valve (r);
Described heating system (a) comprising: for holding the reaction vessel (a1) of mixed solution of paraffin and ethanol, reaction vessel (a1) below is provided with for described mixed solution being heated to 125 DEG C and above to generate the firing chamber (a2) of alcohol vapour, on reaction vessel (a1), be connected with the heat exchange return pipe (a3) for the heat energy of heat outputting steam, this heat exchange return pipe (a3) extends in the ammonia spirit of described ammoniacal liquor vaporization chamber (b1), and be set around on described the first high pressure tank (c) and the second high pressure tank (d).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210054673.6A CN102588021B (en) | 2010-03-02 | 2010-03-02 | Power generating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210054673.6A CN102588021B (en) | 2010-03-02 | 2010-03-02 | Power generating system |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010115528 Division CN101793175A (en) | 2010-03-02 | 2010-03-02 | Power generation system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102588021A CN102588021A (en) | 2012-07-18 |
| CN102588021B true CN102588021B (en) | 2014-07-23 |
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ID=46477177
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210054673.6A Expired - Fee Related CN102588021B (en) | 2010-03-02 | 2010-03-02 | Power generating system |
Country Status (1)
| Country | Link |
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| CN (1) | CN102588021B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103993979B (en) * | 2013-05-11 | 2017-01-18 | 摩尔动力(北京)技术股份有限公司 | phase-change engine |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JPH09296706A (en) * | 1996-05-02 | 1997-11-18 | Yoshihide Nakamura | High-efficient power generation system |
| CN1199133A (en) * | 1997-05-13 | 1998-11-18 | 株式会社五十铃硅酸盐研究所 | Gas engine providing with gas fuel modifying device |
| CN1948864A (en) * | 2005-10-13 | 2007-04-18 | 中国科学院工程热物理研究所 | Work-cold joint supplied cross still state straight and reverse coupling heating power circulation system and method |
| JP4280135B2 (en) * | 2003-09-10 | 2009-06-17 | ヤマト設計株式会社 | Compost fermentation heat power generation method and compost fermentation heat power generation apparatus |
| CN101476494A (en) * | 2009-01-14 | 2009-07-08 | 牛东 | Energy conversion system for exhaust heat of heat engine |
| CN101514642A (en) * | 2008-02-19 | 2009-08-26 | 谷俊杰 | Residual heat reclaiming method, residual heat reclaiming system and used working fluid of absorption liquid |
-
2010
- 2010-03-02 CN CN201210054673.6A patent/CN102588021B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09296706A (en) * | 1996-05-02 | 1997-11-18 | Yoshihide Nakamura | High-efficient power generation system |
| CN1199133A (en) * | 1997-05-13 | 1998-11-18 | 株式会社五十铃硅酸盐研究所 | Gas engine providing with gas fuel modifying device |
| JP4280135B2 (en) * | 2003-09-10 | 2009-06-17 | ヤマト設計株式会社 | Compost fermentation heat power generation method and compost fermentation heat power generation apparatus |
| CN1948864A (en) * | 2005-10-13 | 2007-04-18 | 中国科学院工程热物理研究所 | Work-cold joint supplied cross still state straight and reverse coupling heating power circulation system and method |
| CN101514642A (en) * | 2008-02-19 | 2009-08-26 | 谷俊杰 | Residual heat reclaiming method, residual heat reclaiming system and used working fluid of absorption liquid |
| CN101476494A (en) * | 2009-01-14 | 2009-07-08 | 牛东 | Energy conversion system for exhaust heat of heat engine |
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| CN102588021A (en) | 2012-07-18 |
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Owner name: ZHU HAIYAN Free format text: FORMER OWNER: DING XUEQIANG Effective date: 20140623 |
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