| 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 | 用于空调的吸收板 | CN201280045867.8 | 2012-07-23 | CN103813916B | 2016-08-17 | E·布达尔; M·戈尔克; R·古莱; X·迪蒙; M·马蒂内 |
| 一种吸收板，特别是一种用于车辆的吸收式空调的吸收板，所述吸收板被在彼此相对布置的两个交换表面（35）之间流动的液体吸收流体（10）流穿过，通过提高吸收流体（10）中制冷剂流体的浓度，穿过所述两个交换表面（35）实现对蒸汽相的制冷剂流体的放热吸收，其特征在于，所述两个交换表面（35）的相对布置迫使至少一部分吸收流体流至少一次地穿过其中一个交换表面（35），并且促进所述吸收流体（10）流混合。 | ||||||
| 2 | 空冷吸收式冷冻装置 | CN03822493.3 | 2003-09-19 | CN1294394C | 2007-01-10 | 大平晋; 谷口圭仁; 奥田则之; 安尾晃一; 药师寺史朗; 川端克宏; 河合满嗣; 植田裕树; 谷本启介 |
| 一种空冷两段式空冷吸收式冷冻装置，在装置本体(1)的长方向中央部分，设置了包括高温再生器(G2)、低温再生器(G1)及暖房用热交换器(B)的机械室(2)。在机械室(2)长方向的两侧，设置空气冷热交换部分(3、3)，各空气冷热交换部分(3、3)包括空气冷热交换单元(X)和蒸发器(E)，空气冷热交换单元(X)由空冷吸收器(A、A)、配置在空冷吸收器(A、A)下端之间的空冷凝缩器(C)及配置在空冷吸收器(A、A)上部之间的风扇(F)形成；蒸发器(E)配置在空冷吸收器(A、A)的近似中央部分的。其结果，空气冷热交换部分(3、3)位于机械室(2)的两侧。 | ||||||
| 3 | 蒸气-液体热量和/或质量交换装置 | CN201180038928.3 | 2011-08-10 | CN103391799A | 2013-11-13 | S·格瑞梅拉; J·C·德拉汉蒂; A·K·纳加瓦拉普 |
| 本发明涉及一种能够用在一体的热量和/或质量传递系统中的蒸气-液体的热量和/或质量交换装置。为了实现较高的热量和质量传递率，优化温度分布，减小尺寸并提高性能，在解吸器的一个或多个功能部段中使用适当尺寸的具有微观特征的流道以及工作流体溶液、蒸气流和/或耦合流体之间的逆流流动构造。在本发明的一个示例实施例中，解吸部段使用沿大体向上方向流动的加热流体和在重力作用下沿大体向下方向、相对于上升解吸蒸气流逆流流动的浓缩溶液。为了进一步提高系统的效率，能使用各种类型的塔构造。此外，微通道的表面能改变以实现更好地传递热量。 | ||||||
| 4 | 新型的低温废热吸收式制冷器 | CN201610328277.6 | 2016-05-18 | CN106196716A | 2016-12-07 | 于慎波; 洛塔尔P.M.沃尔夫; 夏鹏鹏; 李红; 李野 |
| 本发明公开一种新型的低温废热吸收式制冷器，包括：热泵、吸收式制冷器，其特点是：热泵将低温废热转化为可供吸收式制冷器工作时使用的高温热量，热泵和吸收式制冷器之间没有传统的热能转换系统，热泵通过热量传递部件直接将热量提供给吸收式制冷器，吸热式制冷器的发生器的加热部件直接被热泵的冷凝器所替代。本发明降低了可利用的废热温度的最低阈值，提高了废热的利用率，由于该系统中热泵和制冷器之间没有传统的热能转换系统，热能从热泵到吸收式制冷器传送过程中没有热量损失，整个系统的热能利用率得到显著提高，大大提升了系统的效率。 | ||||||
| 5 | 蒸气-液体热量和/或质量交换装置 | CN201180038928.3 | 2011-08-10 | CN103391799B | 2016-10-12 | S·格瑞梅拉; J·C·德拉汉蒂; A·K·纳加瓦拉普 |
| 本发明涉及一种能够用在一体的热量和/或质量传递系统中的蒸气‑液体的热量和/或质量交换装置。为了实现较高的热量和质量传递率，优化温度分布，减小尺寸并提高性能，在解吸器的一个或多个功能部段中使用适当尺寸的具有微观特征的流道以及工作流体溶液、蒸气流和/或耦合流体之间的逆流流动构造。在本发明的一个示例实施例中，解吸部段使用沿大体向上方向流动的加热流体和在重力作用下沿大体向下方向、相对于上升解吸蒸气流逆流流动的浓缩溶液。为了进一步提高系统的效率，能使用各种类型的塔构造。此外，微通道的表面能改变以实现更好地传递热量。 | ||||||
| 6 | 用于空调的吸收板 | CN201280045867.8 | 2012-07-23 | CN103813916A | 2014-05-21 | E·布达尔; M·戈尔克; R·古莱; X·迪蒙; M·马蒂内 |
| 一种吸收板，特别是一种用于车辆的吸收式空调的吸收板，所述吸收板被在彼此相对布置的两个交换表面（35）之间流动的液体吸收流体（10）流穿过，通过提高吸收流体（10）中制冷剂流体的浓度，穿过所述两个交换表面（35）实现对蒸汽相的制冷剂流体的放热吸收，其特征在于，所述两个交换表面（35）的相对布置迫使至少一部分吸收流体流至少一次地穿过其中一个交换表面（35），并且促进所述吸收流体（10）流混合。 | ||||||
| 7 | 空冷吸收式冷冻装置 | CN03822493.3 | 2003-09-19 | CN1685182A | 2005-10-19 | 大平晋; 谷口圭仁; 奥田则之; 安尾晃一; 药师寺史朗; 川端克宏; 河合满嗣; 植田裕树; 谷本启介 |
| 一种空冷两段式空冷吸收式冷冻装置，在装置本体(1)的长方向中央部分，设置了包括高温再生器(G2)、低温再生器(G1)及暖房用热交换器(B)的机械室(2)。在机械室(2)长方向的两侧，设置了各自包括由空冷吸收器(A、A)、配置在空冷吸收器(A、A)下端之间的空冷凝缩器(C)及配置在空冷吸收器(A、A)上部之间的风扇(F)形成的空气冷热交换单元(X)；配置在空冷吸收器(A、A)的近似中央部分的蒸发器(E)的空气冷热交换部分(3、3)。其结果，空气冷热交换部分(3、3)位于机械室(2)的两侧。 | ||||||
| 8 | REBOILER | US14002608 | 2011-11-29 | US20130333866A1 | 2013-12-19 | Yoshiyuki Kondo; Hiromitsu Nagayasu; Takashi Kamijo; Osamu Miyamoto |
| There is provided a large-sized reboiler that can achieve space saving and reduction in plant cost. Specifically, there is provided a large-sized reboiler comprising a vessel of which a liquid is supplied from a lower part and a vaporized gas is discharged from an upper part; and a heat transfer tube group arranged in such a manner that a void penetrating in the up-and-down direction is formed in the vessel, wherein a maximum length of a cross-sectional figure of a flow path for the liquid exceeds 2 m, and the void occupies 5 to 10% of an area of the cross-sectional figure of the flow path. | ||||||
| 9 | Hybrid spray absorber | US12655868 | 2010-01-08 | US20100175395A1 | 2010-07-15 | Donald Charles Erickson |
| A hybrid absorber is disclosed for a closed absorption cycle apparatus. The hybrid absorber is comprised of a non-adiabatic section plus an adiabatic spray section in that order, with absorbent solution and vapor supplied sequentially to them. The spray section preferably also includes a non-adiabatic spray cooler. Coolant is supplied to the non-adiabatic absorber and the cooler either in parallel or in series, countercurrently to the absorbent. | ||||||
| 10 | CHEMICAL HEAT PUMP WORKING WITH A HYBRID SUBSTANCE | US12302868 | 2007-05-29 | US20090249825A1 | 2009-10-08 | Ray Olsson; Goran Bolin |
| 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. | ||||||
| 11 | Solar collector absorption cooling system | US457709 | 1990-01-02 | US4993234A | 1991-02-19 | Peter Korsgaard |
| 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). | ||||||
| 12 | Refrigeration | US5302735 | 1935-12-05 | US2107320A | 1938-02-08 | ZELLHOEFER GLENN F |
| 13 | Refrigeration apparatus | US25835828 | 1928-03-01 | US1814358A | 1931-07-14 | KAY WRIGHT LEONARD |
| 14 | Reboiler with void within the heat transfer tube group | US14002608 | 2011-11-29 | US10151540B2 | 2018-12-11 | Yoshiyuki Kondo; Hiromitsu Nagayasu; Takashi Kamijo; Osamu Miyamoto |
| There is provided a large-sized reboiler that can achieve space saving and reduction in plant cost. Specifically, there is provided a large-sized reboiler comprising a vessel of which a liquid is supplied from a lower part and a vaporized gas is discharged from an upper part; and a heat transfer tube group arranged in such a manner that a void penetrating in the up-and-down direction is formed in the vessel, wherein a maximum length of a cross-sectional figure of a flow path for the liquid exceeds 2 m, and the void occupies 5 to 10% of an area of the cross-sectional figure of the flow path. | ||||||
| 15 | ABSORPTION PLATE FOR AN AIR CONDITIONER | US14234229 | 2012-07-23 | US20150336444A1 | 2015-11-26 | Emmanuel Boudard; Marc Gohlke; Remi Goulet; Xavier Dumont; Manuel Martinez |
| The invention relates to an absorption plate, in particular of an absorption air conditioner for a vehicle, crossed by a stream of liquid absorbent fluid (10) flowing between two exchange surfaces (35) arranged relatively opposite one another, the exofhermal absorption of a so-called coolant fluid in vapour phase taking place through said exchange surfaces (35) by increasing a concentration of the coolant fluid in the absorbent fluid (10), characterised in that the relative arrangement of the two exchange surfaces (35) forces at least one portion of the stream of absorbent fluid (10) to pass at least once through one of the exchange surfaces (35) and causes mixing of the stream of absorbent fluid (10). | ||||||
| 16 | Intermittent absorption refrigeration system equipped with a waste energy storage unit | US14133739 | 2013-12-19 | US09194617B2 | 2015-11-24 | Syed Ahmed Mohammad Said; Muhammad Umar Siddiqui |
| A solar powered intermittent absorption refrigeration system utilizes helical coil heat exchangers for generation, absorption, dephlegmation, condensation and heat recovery. The thermo-siphon effect is used to supply and reject heat from the system, to recover and utilize heat from a waste energy unit, to reject heat of absorption, and to pressurize and depressurize the system. The system produces ice blocks during the nighttime without any requirement of electrical energy for the operation of the system. | ||||||
| 17 | INTERMITTENT ABSORPTION REFRIGERATION SYSTEM EQUIPPED WITH A WASTE ENERGY STORAGE UNIT | US14133739 | 2013-12-19 | US20150176869A1 | 2015-06-25 | Syed Ahmed Mohammad SAID; Muhammad Umar SIDDIQUI |
| A solar powered intermittent absorption refrigeration system utilizes helical coil heat exchangers for generation, absorption, dephlegmation, condensation and heat recovery. The thermo-siphon effect is used to supply and reject heat from the system, to recover and utilize heat from a waste energy unit, to reject heat of absorption, and to pressurize and depressurize the system. The system produces ice blocks during the nighttime without any requirement of electrical energy for the operation of the system. | ||||||
| 18 | Hybrid spray absorber | US12655868 | 2010-01-08 | US08800318B2 | 2014-08-12 | Donald Charles Erickson |
| A hybrid absorber is disclosed for a closed absorption cycle apparatus. The hybrid absorber is comprised of a non-adiabatic section plus an adiabatic spray section in that order, with absorbent solution and vapor supplied sequentially to them. The spray section preferably also includes a non-adiabatic spray cooler. Coolant is supplied to the non-adiabatic absorber and the cooler either in parallel or in series, countercurrently to the absorbent. | ||||||
| 19 | Chemical heat pump working with a hybrid substance | US12302868 | 2007-05-29 | US08695374B2 | 2014-04-15 | Ray Olsson; Göran Bolin |
| A chemical heat 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 held or carried by or bonded to the matrix. The matrix is advantageously an inert material such as aluminum 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 fiber material. | ||||||
| 20 | VAPOR-LIQUID HEAT AND/OR MASS EXCHANGE DEVICE | US13814792 | 2011-08-10 | US20130133346A1 | 2013-05-30 | 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. | ||||||
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