| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 1 | 利用再循环热致冷的设备和方法 | CN200410011816.0 | 2004-09-22 | CN1605815A | 2005-04-13 | 罗伯特·J·V·古特费尔德 |
| 一种用于其中产生热量的系统的冷却设备，包括用于接收所述热量的至少一部分的腔室，所述腔室内含有致冷剂；用于接收已经在所述腔室中加热的致冷剂的冷凝器，所述致冷剂在所述冷凝器中被加压和冷却，和至少一根连接于所述冷凝器并通向待冷却区域的蛇管，所述至少一根蛇管具有连接于所述冷凝器的第一部分，在所述第一部分下游的第二部分，和在所述第二部分下游的第三部分，所述第二下游部分包含用于使所述致冷剂自由膨胀从而导致所述区域冷却的孔口，所述第三下游部分从所述待冷却区域返回到所述腔室。 | ||||||
| 2 | 具有模块式连接件的热化学系统 | CN201180061270.8 | 2011-10-20 | CN103261818A | 2013-08-21 | L·里戈; F·金德贝泰; L·迪特吕 |
| 本发明涉及一种热化学系统，所述热化学系统包括反应器（1），或储存能够吸收气体的反应物的储存罩壳，气体通过沿着反应器的纵向轴（xx'）布置的扩散器（17，17'）被引入反应器中，反应物（2）和气体使得：当反应物和气体都存在时，反应物和气体是一化学反应的对象，所述化学反应具有通过反应物（2）吸收气体的作用，相反地，反应物和气体是一逆化学反应的对象，所述逆化学反应用于当反应物已吸收气体时，在施加于反应物的加热的作用下，解吸由反应物（2）所吸收的气体。该热化学系统的特征在于，扩散器包括气体供给部件（15a）、使气体在反应物（2）中分布的分布部件（15c，19）、过滤部件（17b，17c）和加热部件，这些不同的部件形成一子组件，所述子组件通过一闭塞元件（16）固定在反应器（1）的罩壳（9）上。 | ||||||
| 3 | 利用再循环热致冷的设备和方法 | CN200410011816.0 | 2004-09-22 | CN100485288C | 2009-05-06 | 罗伯特·J·V·古特费尔德 |
| 一种用于其中产生热量的系统的冷却设备，包括用于接收所述热量的至少一部分的腔室，所述腔室内含有致冷剂；用于接收已经在所述腔室中加热的致冷剂的冷凝器，所述致冷剂在所述冷凝器中被加压和冷却，和至少一根连接于所述冷凝器并通向待冷却区域的蛇管，所述至少一根蛇管具有连接于所述冷凝器的第一部分，在所述第一部分下游的第二部分，和在所述第二部分下游的第三部分，所述第二下游部分包含用于使所述致冷剂自由膨胀从而导致所述区域冷却的孔口，所述第三下游部分从所述待冷却区域返回到所述腔室。 | ||||||
| 4 | 具有模块式连接件的热化学系统 | CN201180061270.8 | 2011-10-20 | CN103261818B | 2015-09-30 | L·里戈; F·金德贝泰; L·迪特吕 |
| 本发明涉及一种热化学系统，所述热化学系统包括反应器(1)，或储存能够吸收气体的反应物的储存罩壳，气体通过沿着反应器的纵向轴(xx’)布置的扩散器(17，17’)被引入反应器中，反应物(2)和气体使得：当反应物和气体都存在时，反应物和气体是一化学反应的对象，所述化学反应具有通过反应物(2)吸收气体的作用，相反地，反应物和气体是一逆化学反应的对象，所述逆化学反应用于当反应物已吸收气体时，在施加于反应物的加热的作用下，解吸由反应物(2)所吸收的气体。该热化学系统的特征在于，扩散器包括气体供给部件(15a)、使气体在反应物(2)中分布的分布部件(15c，19)、过滤部件(17b，17c)和加热部件，这些不同的部件形成一子组件，所述子组件通过一闭塞元件(16)固定在反应器(1)的储存罩壳(9)上。 | ||||||
| 5 | 吸收水加热冷却器 | CN98809318.9 | 1998-11-11 | CN1161576C | 2004-08-11 | 船场保志; 大内富久; 三宅聪; 冈村满幸; 伊藤纪洋 |
| 本发明提供了使用溴化锂作为一吸收剂和水作为一致冷剂的一吸收水加热器/冷却器及其一高温再生器。该高温再生器设有一燃烧腔，该燃烧腔由在一燃烧器(4B)的一吹出口侧的一内筒(2)限定，其中一燃烧气体从燃烧器的吹出口吹出。一溶液被容纳在一液体腔室内，该液体腔室在燃烧腔的上侧和下侧延伸并且由一外筒(1)限定。一致冷剂蒸汽流出通道(8)被形成在外筒的一上部，并且气体排出通道(13，14)被形成在相对于燃烧器的燃烧腔的一端部。在燃烧腔的上侧和下侧的液体腔室之间提供连通的多个溶液导管(3)延伸穿过燃烧腔。这多个溶液导管大致分为设置在燃烧器的火焰内的一组(3A)、和设置成远离燃烧器的火焰的一组(3B)。这两组彼此隔开10～100mm。这样可获得对NOx的降低(还原)和抑制CO的产生。 | ||||||
| 6 | 吸收式冷热水机的高温再生器 | CN98803488.3 | 1998-11-11 | CN1161575C | 2004-08-11 | 船场保志; 大内富久; 三宅聪; 伊藤纪洋 |
| 本发明涉及吸收式冷热水机用的高温再生器，该高温再生器将溴化锂稀溶液加热，使其浓缩，分离制冷剂即水蒸气。在喷出燃烧气体的燃烧器(4B)的喷出口侧，用内筒(2)划分出燃烧室(11B)。在燃烧室的上下即被外筒(1)划分出的液室内收容着溶液。在外筒的上部形成制冷剂蒸气流出路(8)，在燃烧室的燃烧器的相反端形成着气体排出路(13、14)。连通燃烧室的上下液室的多个溶液管(3)贯通燃烧室。多个溶液管是扁平管，只在其侧面有翅片(16)。翅片只设在上游侧。借助该翅片促进充满扁平管内的溶液与燃烧气体之间进行热交换，促进溶液的流动。 | ||||||
| 7 | 吸收水加热器/冷却器及其高温再生器 | CN98809318.9 | 1998-11-11 | CN1271414A | 2000-10-25 | 船场保志; 大内富久; 三宅聪; 冈村满幸; 伊藤纪洋 |
| 本发明提供了使用溴化锂作为一吸收剂和水作为一致冷剂的一吸收水加热器/冷却器及其一高温再生器。该高温再生器设有一燃烧腔,该煅烧腔由在一燃烧器(4B)的一吹出口侧的一内筒(2)限定,其中一燃烧气体从燃烧器的吹出口吹出。一溶液被容纳在一液体腔室内,该液体腔室在燃烧腔的上侧和下侧延伸并且由一外筒(1)限定。一致冷剂蒸汽流出通道(8)被形成在外筒的一上部,并且气体排出通道(13,14)被形成在相对于燃烧器的燃烧腔的一端部。在燃烧腔的上侧和下侧的液体腔室之间提供连通的多个溶液导管(3)延伸穿过燃烧腔。这多个溶液导管大致分为设置在燃烧器的火焰内的一组(3A)、和设置成远离燃烧器的火焰的一组(3B)。这两组彼此隔开10～100mm。这样可获得对NOx的降低(还原)和抑制CO的产生。 | ||||||
| 8 | 吸收式冷温水机的高温再生器 | CN98803488.3 | 1998-11-11 | CN1251163A | 2000-04-19 | 船场保志; 大内富久; 三宅聪; 伊藤纪洋 |
| 本发明涉及吸收式冷温水机用的高温再生器,该高温再生器将溴化锂稀溶液加热,使其浓缩,分离制冷剂即水蒸气。在喷出燃烧气体的燃烧器(4B)的喷出口侧,用内筒(2)划分出燃烧室(11B)。在燃烧室的上下即被外筒(1)划分出的液室内收容着溶液。在外筒的上部形成制冷剂蒸气流出路(8),在燃烧室的燃烧器的相反端形成着气体排出路(13、14)。连通燃烧室的上下液室的多个溶液管(3)贯通燃烧室。多个溶液管是扁平管。只在其侧面有翅片(16)。翅片只设在上游侧。借助该翅片促进充满扁平管内的溶液与燃烧气体之间进行热交换,促进溶液的流动。 | ||||||
| 9 | Cooler | JP2002040468 | 2002-02-18 | JP2003247770A | 2003-09-05 | TANAKA MIZUHO |
| PROBLEM TO BE SOLVED: To provide a cooler having durability and less malfunction, with high cooling efficiency. SOLUTION: The cooler has the following components inside a medium circulation path 2: a liquid receiving tank 1 for storing a liquid medium; a medium heater 3 for heating and vaporizing the liquid medium from the tank 1; a condenser 11 for condensing and liquefying the medium vapor generating from the heater 3; and an evaporative cooling device 13 for vaporizing the condensed and liquefied medium and drawing the surrounding heat. A plurality of carbon fibers 6A are bundled around the outer periphery of the medium heater 3, and an insulated linear heating element 6 covered with an insulation enclosure 6B are wound around the outer periphery. The linear heating element 6 composed in this way has high mechanical strength and no breakage with high heating efficiency. COPYRIGHT: (C)2003,JPO | ||||||
| 10 | High temperature of the absorption chiller-heater regenerator and absorption chiller | JP1046993 | 1993-01-26 | JP3195100B2 | 2001-08-06 | 富久 大内; 孝夫 成瀬; 滋郎 杉本; 泰男 浦木; 道彦 相沢; 章 西口 |
| 11 | Arrangement for preventing freezing of the working medium in an absorption refrigerating apparatus | EP88850422.2 | 1988-12-14 | EP0323820A3 | 1990-12-12 | Walfridson, Magnus Tell; Färndahl, Stig Herman |
The invention refers to an arrangement at a refrigerator cabinet (10) having an absorption refrigerating apparatus (16,18) operated by a heating cartridge (40) from at least one electric current source or by a gas burner (38). The arrangement shows a control apparatus (74) which automatically starts the gas burner (38) when the supply of current to the heating cartridge (40) ceases. The refrigerating apparatus (18) is with exception of its evaporator (16) enclosed in a heat insulated chamber (20) through which surrounding air circulates for cooling of the refrigerating apparatus (18). In order to prevent the refrigerant in the refrigerating apparatus from freezing to plugs at low temperature of the surrounding air, which plugs put the refrigerating apparatus out of function, means (86) are arranged to limit the air circulation through the chamber (20) and a temperature sensing means (80) is located in the chamber for breaking the current to the heating cartridge (40) at a certain low temperature in the chamber (20) so that the gas burner (38) is put into operation. |
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| 12 | Arrangement for preventing freezing of the working medium in an absorption refrigerating apparatus | EP88850422.2 | 1988-12-14 | EP0323820A2 | 1989-07-12 | Walfridson, Magnus Tell; Färndahl, Stig Herman |
The invention refers to an arrangement at a refrigerator cabinet (10) having an absorption refrigerating apparatus (16,18) operated by a heating cartridge (40) from at least one electric current source or by a gas burner (38). The arrangement shows a control apparatus (74) which automatically starts the gas burner (38) when the supply of current to the heating cartridge (40) ceases. The refrigerating apparatus (18) is with exception of its evaporator (16) enclosed in a heat insulated chamber (20) through which surrounding air circulates for cooling of the refrigerating apparatus (18). In order to prevent the refrigerant in the refrigerating apparatus from freezing to plugs at low temperature of the surrounding air, which plugs put the refrigerating apparatus out of function, means (86) are arranged to limit the air circulation through the chamber (20) and a temperature sensing means (80) is located in the chamber for breaking the current to the heating cartridge (40) at a certain low temperature in the chamber (20) so that the gas burner (38) is put into operation. |
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| 13 | SYSTÈME THERMOCHIMIQUE À CONNEXION MODULAIRE | EP11779748.0 | 2011-10-20 | EP2630420A1 | 2013-08-28 | RIGAUD, Laurent; KINDBEITER, Francis; DUTRUY, Laurent |
| The present invention relates to a thermochemical system comprising a reactor (1) or a chamber for storing a reactive material capable of absorbing a gas that is taken into the reactor by a diffuser (17, 17') placed along the longitudinal axis (xx') of the latter, wherein the reactive material (2) and the gas are such that, when placed in the presence of each other, same are subjected to a reaction causing the reactive material (2) to absorb the gas, and conversely, same are subjected to a reaction for desorbing the gas, absorbed by the reactive material (2), by means of heating applied to the latter when it has absorbed gas. Said thermochemical system is characterized in that the diffuser includes a gas supply means (15a), a means (15c, 19) for dispensing the gas into the reactive material (2), a filtration means (17b, 17c), and a heating means. Said various means form a sub-assembly that is attached onto the housing (9) of the reactor (1) by means of a sealing element (16). | ||||||
| 14 | Arrangement for preventing freezing of the working medium in an absorption refrigerating apparatus | EP88850422.2 | 1988-12-14 | EP0323820B1 | 1992-06-17 | Walfridson, Magnus Tell; Färndahl, Stig Herman |
| 15 | SYSTÈME THERMOCHIMIQUE À CONNEXION MODULAIRE | EP11779748.0 | 2011-10-20 | EP2630420B1 | 2014-12-17 | RIGAUD, Laurent; KINDBEITER, Francis; DUTRUY, Laurent |
| 16 | An absorption-cycle refrigerating unit | EP02022162.8 | 2002-10-02 | EP1302732A1 | 2003-04-16 | Bora, Luca |
An absorption-cycle refrigerating unit, comprising an electrically heated boiler (2), covered with a layer (10) of mineral wool that is covered by an external enclosure (11) made of expanded plastic material. |
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| 17 | Absorption water heater/chiller and high temperature regenerator therefor | US09814713 | 2001-03-23 | US06470702B2 | 2002-10-29 | Yasushi Funaba; Norihiro Itou; Tomihisa Oouchi; Satoshi Miyake; Michiyuki Uchimura |
| An absorption water heater/chiller using lithium bromide as an absorbent and water as a refrigerant, and a high temperature regenerator therefor. The high temperature regenerator is provided with a combustion chamber defined by an inner tube (2) on the side of a blowout port of a burner (4B), from which a combustion gas is blown out. A solution is received in a liquid chamber, which extends on upper and lower sides of the combustion chamber and is defined by an outer tube (1). A refrigerant steam outflow passage (8) is formed in an upper portion of the outer tube, and gas discharge passages (13, 14) are formed at an end portion of the combustion chamber opposed to the burner. A plurality of solution tubes (3) providing communication between the liquid chamber portions on the upper and lower sides of the combustion chamber extend through the combustion chamber. The plurality of solution tubes are roughly divided into a group (3A) provided in flame of the burner, and a group (3B) provided away from the flame of the burner. The two groups are spaced from each other by 10-100 mm. Thus reduction of Nox is achieved and generation of CO is suppressed. | ||||||
| 18 | High temperature regenerator for absorption water cooling and heating machine | US09381397 | 1999-09-20 | US06279343B1 | 2001-08-28 | Yasushi Funaba; Norihiro Itou; Tomihisa Ohuchi; Satoshi Miyake |
| A high temperature regenerator for an absorption water cooling and heating machine for extracting steam as coolant by heating and condensing a dilute solution of lithium bromide. An inner casing (2) defines therein a combustion chamber (11B) on the blow out port side of a burner for blowing out combustion gas. The solution is filled in liquid chambers defined in an outer casing (1) above and below the combustion chamber. A coolant vapor outlet passage (8) is defined in the upper part of the outer casing, and gas exhaust passages (13, 14) are defined in the combustion chamber on a side remote from the burner. A plurality of solution tubes 3 communicated with the liquid chambers above and below the combustion chamber are extended through he combustion chamber. The plurality of solution tubes are plane tubes having fins (16) at their side surfaces. The fins are provided only on the upstream side. With these fins, the heat-exchange between the solution filled in the plane tubes and the combustion gas can be promoted so as to promote the flow of the solution. | ||||||
| 19 | Internally fired generator | US478981 | 1995-06-07 | US5692393A | 1997-12-02 | Michael W. Klintworth; U. Tina Kim |
| An absorption refrigeration system generator is disclosed which has an internal fire tube or combustion chamber for heating a composite fluid refrigerant. The fire tube includes at least one radially projecting heat transfer member on its interior surface for interaction with hot combustion gases. The generator is connected to a leveling chamber for maintaining a minimum quantity of fluid refrigerant in the generator. The leveling chamber comprises a reservoir connected to facilitate substantial equilibrium of the fluid levels within the generator and reservoir. The reservoir holds a quantity of weakened refrigerant solution flowing from the generator. A conduit within the reservoir transfers the weakened solution within the reservoir to the absorber under normal operating conditions. In the event the refrigerant level within the generator drops below a predetermined level, fluid flow out of the reservoir ceases. Thus, the generator fluid refrigerant level is prevented from dropping substantially below the predetermined level. | ||||||
| 20 | High temperature regenerator of an absorption type hot and cold water generator and absorption type hot and cold water generator | US181022 | 1994-01-14 | US5435154A | 1995-07-25 | Akira Nishiguchi; Tomihisa Ohuchi; Shigeo Sugimoto; Michihiko Aizawa; Takao Naruse; Yasuo Uraki |
| A high temperature regenerator of an absorption type hot and cold water generator and an absorption type hot and cold water generator capable of preventing corrosion from occurring by preventing local overheating at the heat transfer surface of the high temperature regenerator and capable of being miniaturized. The high temperature regenerator includes an outer case, an inner case, a plurality of solution pipes, a burner, a solution flow-in pipe, and a gas/liquid separation plate. The inner case is inside the outer case, and a solution is kept between the cases, with the inner case being submerged within this solution. The burner is mounted on the side of the outer case in such a way that heat can be supplied through the inner case, with the inside of the inner case serving as a combustion chamber. A plurality of solution pipes, through which the upper and lower portions of the inner case are connected, are disposed downstream of the combustion chamber, and the inside of each of the solution pipes is filled with the solution. The horizontal cross section of each of the solution pipes is elliptical, and two or more of the solution pipes are disposed so that the straight line portions in the elliptical shape become parallel to each other. The sections between the solution pipes serve as a combustion gas passage. | ||||||
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