| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 21 | Reaction heat storage method for hydride tanks | US11194 | 1979-02-12 | US4566281A | 1986-01-28 | Gary D. Sandrock; Edwin Snape |
| A system for hydrogen storage including a hydridable material associated with an amount of inert material of high heat capacity sufficient in amount to prevent, during hydriding, the temperature of the combined hydridable material-inert material from rising beyond that temperature at which the hydride of the hydridable material exhibits a hydrogen pressure equal to the partial pressure of hydrogen fed to the system. The system is insulated to inhibit heat transfer into or out of the system. | ||||||
| 22 | Vapor - liquid heat and / or mass exchange apparatus | JP2013524219 | 2011-08-10 | JP2013535655A | 2013-09-12 | スリニバス ガリメラ，; ジャレッド カーペンター デラハンティー，; アナンダ クリシュナ ナガバラプ， |
| 本発明は、統合された熱伝達および／または物質移動システムに使用できる、蒸気-液体熱および／または物質交換装置に関する。 高い熱伝達および物質移動率、最適温度プロファイル、小型化、および性能増加を達成するために、微小規模特性を備える適切な大きさの流路、および脱着器の１つまたはそれ以上機能部における、作動流体溶液、蒸気流、および／またはカップリング流体間の向流構成が実施されている。 本発明のある例示的な実施形態によると、脱着器部は、ほぼ上方向に流れる加熱流体と、上昇する脱着蒸気流に対し逆流の重力でほぼ下方向に流れる濃縮溶液とを用いる。 該システムの効率をさらに増加させるため、多様な種類のカラム構成を用いることができる。 さらにまた、マイクロチャンネルの表面をより伝達熱に変更できる。 | ||||||
| 23 | Chemical heat pump, which acts in the hybrid material | JP2009513095 | 2007-05-29 | JP2009539057A | 2009-11-12 | オルソン、レイ; ボリン、ゲラン |
| A chemical heal pump includes a reactor part (1) that contains an active substance and an evaporator/condenser part (3) that contains that portion of volatile liquid that exists in a condensed state and can be absorbed by the active substance. A channel (4) interconnects the reactor part and the evaporator/condenser part, In at least the reactor part a matrix (13) is provided for the active substance so that the active substance both in its solid state and its liquid state or its solution phase is hold or carried by or bonded to the matrix. The matrix is advantageously an inert material such as aluminium oxide and has pores, which are permeable for the volatile liquid and in which the active substance is located. In particular, a material can be used that has a surface or surfaces, at which the active substance can be bonded in the liquid state thereof. For example, the matrix can be a material comprising separate particles such as a powder or a compressed fibre material. | ||||||
| 24 | JPH03502235A - | JP50348088 | 1988-04-06 | JPH03502235A | 1991-05-23 | |
| PCT No. PCT/DK88/00063 Sec. 371 Date Jan. 2, 1990 Sec. 102(e) Date Jan. 2, 1990 PCT Filed Apr. 6, 1988 PCT Pub. No. WO88/08109 PCT Pub. Date Oct. 20, 1988.A solar collector absorption cooling system with a primary cooling circuit the evaporator (1) of which is connected with absorber ducts (26) in an absorber formed as a solar collector (12), said absorber ducts (26) including a coolant absorbing compound for the suction of coolant at night hours, and a secondary self-circulating cooling circuit with evaporator tubes (29) located in heat transferring contact with the absorber ducts (26) of the primary circuit to provide an enhanced cooling thereof. The absorber of the primary circuit is carried out as at least one sheet welded absorber panel (24, 25) and is accommodated in a solar collector frame (12) beneath and in parallel to a glass layer (15) facing the incident sun and to a thermal insulating layer (36) on the opposite side of the absorber panel. The evaporator tubes (b 29) of the secondary circuit that are made from well heat-conducting material are positioned in the valleys between the ducts (26) of the absorber panel (24, 25) facing the insulating layer (36). | ||||||
| 25 | Method of accumulating reaction heat for hydride tank | JP1592080 | 1980-02-12 | JPS55132632A | 1980-10-15 | GEERII DEIRU SANDOROTSUKU; EDOUIN SUNEEPU |
| 26 | SORPTION MODULE | US15534481 | 2015-11-30 | US20170343262A1 | 2017-11-30 | Roland Burk; Lars Ludwig |
| A sorption module for a sorption temperature-control device may include a housing enclosing a working chamber. A sorption zone and a phase change zone may be arranged in the working chamber where a working medium is displaceable reversibly between the sorption zone and the phase change zone. A sorption structure may be arranged in the sorption zone, and a phase change structure may be arranged in the phase change zone. An outer wall of the housing may include a double-walled section that may provide a cavity between an outer wall part and an inner wall part of the double-walled section, and the phase change zone may be arranged on an inner side of the inner wall part. | ||||||
| 27 | Vapor-liquid heat and/or mass exchange device | US13814792 | 2011-08-10 | US09464823B2 | 2016-10-11 | Srinivas Garimella; Jared Carpenter Delahanty; Ananda Krishna Nagavarapu |
| The invention is directed toward a vapor-liquid heat and/or mass exchange device that can be used in an integrated heat and/or mass transfer system. To achieve high heat and mass transfer rates, optimal temperature profiles, size reduction and performance increases, appropriately sized flow passages with microscale features, and countercurrent flow configurations between working fluid solution, vapor stream, and/or the coupling fluid in one or more functional sections of the desorber are implemented. In one exemplary embodiment of the present invention, a desorber section utilizes a heating fluid flowing in a generally upward direction and a concentrated solution flowing in a generally downward direction with gravity countercurrent to the rising desorbed vapor stream. To further increase the efficiency of the system, various types of column configurations can be used. Additionally, the surfaces of the microchannels can be altered to better transfer heat. | ||||||
| 28 | Absorption plate for an air conditioner | US14234229 | 2012-07-23 | US09440513B2 | 2016-09-13 | Emmanuel Boudard; Marc Gohlke; Remi Goulet; Xavier Dumont; Manuel Martinez |
| An absorption plate for a vehicle is crossed by a stream of liquid absorbent fluid flowing between two exchange surfaces arranged relatively opposite one another. The exothermal absorption of a coolant fluid in vapor phase takes place through the exchange surfaces by increasing a concentration of the coolant fluid in the absorbent fluid. The relative arrangement of the two exchange surfaces forces at least one portion of the stream of absorbent fluid to pass at least once through one of the exchange surfaces and causes mixing of the stream of the absorbed fluid. | ||||||
| 29 | SOLAR COOLING SYSTEM | US15067765 | 2016-03-11 | US20160195313A1 | 2016-07-07 | Harold Finkleman |
| In many parts of the world the electricity supply is unreliable and/or electricity costs are high, which means that in many cases conventional air cooling systems that are compressor-based and electrically powered are unreliable due to electrical power outages and/or they are expensive to operate. Some aspects of the invention provide an air cooling system. The air cooling system may include a solar energy gathering component that drives a cooling system. The air cooling system may include an absorption cooling system or a thermoelectric cooling system. The cooling system may include a solar collector matched with an air venting system. The cooling unit may hang on the inside of a window or on another vertical surface and utilize the heat and/or radiation from the sun to activate a cooling mechanism that, in turn, provides cooling via the cooling system. | ||||||
| 30 | SOLAR COOLING SYSTEM INTEGRATED IN BUILDING ENVELOPE | US14020845 | 2013-09-08 | US20150068239A1 | 2015-03-12 | Shishir Gupta; Sumit Sharma; Rahul Singh |
| The present invention provides a solar cooling system which is so small in size so that it can be used as a building material. The design based on absorption and adsorption refrigeration cycle has been developed to fulfill this objective. The design has been developed such that the system is completely independent and does not require any other source of energy apart from solar heat. Also an effort is made to design the system so that the cooling capacity is automatically increased or decreased based on available solar heat energy. | ||||||
| 31 | Countercurrent flow absorber and desorber | US328890 | 1981-12-09 | US4477396A | 1984-10-16 | William H. Wilkinson |
| Countercurrent flow absorber and desorber devices are provided for use in absorption cycle refrigeration systems and thermal boosting systems. The devices have increased residence time and surface area resulting in improved heat and mass transfer characteristics. The apparatuses may be incorporated into open cycle thermal boosting systems in which steam serves both as the refrigerant vapor which is supplied to the absorber section and as the supply of heat to drive the desorber section of the system. | ||||||
| 32 | Method and apparatus for use of heat taken up at low temperature | US189117 | 1980-09-22 | US4368623A | 1983-01-18 | Karl F. Knoche; Heinrich Trumper; Dieter Stehmeier |
| A method and apparatus for the use of heat taken up at low temperature is disclosed wherein a flow of transfer medium is passed through a low temperature heat source to absorb heat. The flow then passes through multiple, sequential stages of a heat pump which successively increase in temperature whereby the flow picks up heat. The flow then releases heat to the heat receiver and subsequently passes through multiple sequential degassing stages of the heat pump. The flow releases evaporation heat and is cooled to a suitable temperature for use in the low temperature heat source. The heat pump preferably includes a two substance mixture provided within a two portion, hermetically sealed chamber. | ||||||
| 33 | Refrigerating apparatus | US42493330 | 1930-01-31 | US1881568A | 1932-10-11 | HENNEY CHARLES F |
| 34 | Refrigerating apparatus | US40846629 | 1929-11-20 | US1861979A | 1932-06-07 | HANS ROHL |
| 332,160. Schwarzwaldwerke Lanz Ges. Nov. 30, 1928, [Convention date]. Refrigerating, absorption machines for.-The generator-absorber a is heated by a burner d disposed in a jacketed tube c, the heat passing from the inner to the outer tube walls by radiation only. The inside and outside surfaces of the outer and inner tube walls respectively may be roughened. During absorption, cold water is passed through the tube jacket. | ||||||
| 35 | 태양열 이용 냉난방 시스템 및 그의 제어방법 | KR1020160182748 | 2016-12-29 | KR101708379B1 | 2017-02-20 | 남현민; 이동규; 이병두; 강대오 |
| 본발명은, 태양열집열모듈과보조가열모듈을포함하고, 태양열집열모듈에서집열량이최대화되도록태양열집열모듈을순환하는열매체의유량을제어함으로써, 태양열집열모듈의이용률을보다향상시키고, 보조가열모듈의이용률은저감시켜전체효율을향상시킬수 있다. | ||||||
| 36 | PLAQUE D'ABSORPTION POUR CLIMATISEUR | EP12744097.2 | 2012-07-23 | EP2736742B1 | 2015-09-09 | BOUDARD, Emmanuel; GOHLKE, Marc; GOULET, Remi; DUMONT, Xavier; MARTINEZ, Manuel |
| 37 | VAPOR-LIQUID HEAT AND/OR MASS EXCHANGE DEVICE | EP11817010.9 | 2011-08-10 | EP2603759A2 | 2013-06-19 | GARIMELLA, Srinivas; DELAHANTY, Jared, Carpenter; NAGAVARAPU, Ananda, Krishna |
| The invention is directed toward a vapor-liquid heat and/or mass exchange device that can be used in an integrated heat and/or mass transfer system. To achieve high heat and mass transfer rates, optimal temperature profiles, size reduction and performance increases, appropriately sized flow passages with microscale features, and countercurrent flow configurations between working fluid solution, vapor stream, and/or the coupling fluid in one or more functional sections of the desorber are implemented. In one exemplary embodiment of the present invention, a desorber section utilizes a heating fluid flowing in a generally upward direction and a concentrated solution flowing in a generally downward direction with gravity countercurrent to the rising desorbed vapor stream. To further increase the efficiency of the system, various types of column configurations can be used. Additionally, the surfaces of the microchannels can be altered to better transfer heat. | ||||||
| 38 | AIR-COOLED ABSORPTION TYPE REFRIGERATING PLANT | EP03797718.8 | 2003-09-19 | EP1550831A1 | 2005-07-06 | OHIRA, Sin OSAKA GAS CO., LTD.; TANIGUCHI, Yoshihito TOHO GAS CO., LTD.; OKUDA, Noriyuki Daikin Industries, Ltd.; YASUO, Kouichi Daikin Industries, Ltd.; YAKUSHIJI, Fumiaki Daikin Industries, Ltd.; KAWABATA, Katsuhiro Daikin Industries Ltd.; KAWAI, Mitsuji Daikin Industries Ltd.; UEDA, Hiroki Daikin Industries Ltd.; TANIMOTO, Keisuke Daikin Industries Ltd. |
In a two stage air-cooled absorption refrigerating apparatus, a machine room (2) including a high-temperature generator (G2), a low-temperature generator (G1) and a space-heating heat exchanger (B) is provided at the longitudinal center of an apparatus body (1). On both sides of the machine room (2) in the longitudinal direction of the apparatus body (1), air-cooled heat exchangers (3) are arranged, each of the air-cooled heat exchangers including: an air-cooled heat exchanger unit (X) made of air-cooled absorbers (A) which are arranged on two opposed sides of the air-cooled heat exchanger (3) orthogonal to a barrier wall against the machine room (2), an air-cooled condenser (C) which is arranged between the lower ends of the air-cooled absorbers (A) to provide air intake surfaces below the air-cooled absorbers (A) and fans (F) which are arranged between the upper portions of the air-cooled absorbers (A); and a vaporizer (E) which is arranged substantially in the middle of the air-cooled absorbers (A). Thus, the air-cooled heat exchangers (3) are located on both sides of the machine room (2). |
||||||
| 39 | A SOLAR COLLECTOR ABSORPTION COOLING SYSTEM | EP88903203.0 | 1988-04-06 | EP0353237A1 | 1990-02-07 | KORSGAARD, Peter |
| PCT No. PCT/DK88/00063 Sec. 371 Date Jan. 2, 1990 Sec. 102(e) Date Jan. 2, 1990 PCT Filed Apr. 6, 1988 PCT Pub. No. WO88/08109 PCT Pub. Date Oct. 20, 1988.A solar collector absorption cooling system with a primary cooling circuit the evaporator (1) of which is connected with absorber ducts (26) in an absorber formed as a solar collector (12), said absorber ducts (26) including a coolant absorbing compound for the suction of coolant at night hours, and a secondary self-circulating cooling circuit with evaporator tubes (29) located in heat transferring contact with the absorber ducts (26) of the primary circuit to provide an enhanced cooling thereof. The absorber of the primary circuit is carried out as at least one sheet welded absorber panel (24, 25) and is accommodated in a solar collector frame (12) beneath and in parallel to a glass layer (15) facing the incident sun and to a thermal insulating layer (36) on the opposite side of the absorber panel. The evaporator tubes (b 29) of the secondary circuit that are made from well heat-conducting material are positioned in the valleys between the ducts (26) of the absorber panel (24, 25) facing the insulating layer (36). | ||||||
| 40 | Verfahren und Vorrichtung zur Nutzung von bei niedriger Temperatur aufgenommener Wärme | EP80105607.8 | 1980-09-18 | EP0025986B1 | 1983-11-23 | Knoche, Karl-Friedrich Prof. Dr.-Ing.; Trümper, Heinrich Prof. Dipl-Ing.; Stehmeier, Dieter, Dipl.-Ing. |
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