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 CN96198767.7 1996-10-11 CN1154816C 2004-06-23 T·L·温宁顿; R·J·格林; R·罗顿; R·B·乌瑟顿
一种旋转(10),包括一个蒸气发生器(20),一个冷凝器(24/34),一个蒸发器(42)和一个吸收器(40),以上各部分相互连接,以形成其所用挥发性液体成分及吸收液的循环液体流动途径。为了使该泵能在接近结晶临界点工作,该泵包括一个结晶控制装置,该控制装置在检测到结晶开始后,使易于结晶部位的液体温度升高。例如,结晶部位上游的压升高,会导致热液体的直接或间接分流,以提高结晶部位的液体温度。本文还披露了控制吸收混合物流速的装置,控制其浓度的装置;阻尼一个戽斗泵的装置;保证流至发生器表面的装置;用于该泵减压及扩大其工作范围的装置;更新换热器的特征;对该热泵进行金属组合的特征,以及用于该热泵的氢气吸气器的特征。
2 旋转吸收式 CN200380110725.6 2003-11-21 CN100398941C 2008-07-02 沙比尔·戈里蒂萨特基·雷托拉扎; 乌奈·奥内德拉·埃加尼亚; 若泽·曼努埃尔·卡诺·罗德里格斯
发明涉及一种旋转吸收式,包括旋转组件(1),该旋转组件包括:蒸汽发生器(2)、冷凝器(3)、蒸发器(4)和吸收器(5),它们都彼此相连从而形成用于挥发性流体成分和其吸收液体的流体流动路径。该泵还包括向蒸汽发生器传热的装置,该装置包括布置在旋转装置中的热交换单元(6),热流体流经该单元。传热装置还包括用于将所述热流体从静态环境传输到热交换单元的转接装置。传热装置还包括:布置在静态环境中的用于热流体的第一入口管和第一出口管;和同轴布置在旋转单元的旋转轴上的第二入口管和第二出口管,它们将静态环境的第一入口管和第一出口管与热交换器连接,转接装置包括旋转密封件,其将静态环境与旋转单元的旋转轴连接。
3 旋转吸收式 CN200380110725.6 2003-11-21 CN1878992A 2006-12-13 沙比尔·戈里蒂萨特基·雷托拉扎; 乌奈·奥内德拉·埃加尼亚; 若泽·曼努埃尔·卡诺·罗德里格斯
发明涉及一种旋转吸收式。本发明的泵包括旋转组件(1),该旋转组件包括:蒸汽发生器(2)、冷凝器(3)、蒸发器(4)和吸收器(5),它们都彼此相连从而形成用于挥发性流体成分和其吸收液体的流体流动路径。所述热泵还包括向所述蒸汽发生器(2)传热的装置,该传热装置包括布置在所述旋转装置(1)中的热交换单元(6),热流体流经该热交换单元。所述传热装置还包括用于将所述热流体从静态环境传输到所述热交换单元(6)的转接装置。
4 CN96198767.7 1996-10-11 CN1203655A 1998-12-30 T·L·温宁顿; R·J·格林; R·罗顿; R·B·乌瑟顿
一种旋转(10),包括一个蒸气发生器(20),一个冷凝器(24/34),一个蒸发器(42)和一个吸收器(40),以上各部分相互连接,以形成其所用挥发性液体成分及吸收液的循环液体流动途径。为了使该泵能在接近结晶临界点工作,该泵包括一个结晶控制装置,该控制装置在检测到结晶开始后,使易于结晶部位的液体温度升高。例如,结晶部位上游的压升高,会导致热液体的直接或间接分流,以提高结晶部位的液体温度。本文还披露了控制吸收混合物流速的装置,控制其浓度的装置;阻尼一个戽斗泵的装置;保证流至发生器表面的装置;用于该泵减压及扩大其工作范围的装置;更新换热器的特征;对该热泵进行金属组合的特征,以及用于该热泵的氢气吸气器的特征。
5 CN89101992.8 1989-02-01 CN1037960A 1989-12-13 科林·拉姆肖; 泰伦斯·温宁顿
吸收循环式包括一个旋转组件,该旋转组件包括蒸汽发生器(GE、14)、冷凝器(CO、23),吸收器(AB、22)、蒸发器(EV)和溶液热交换器(X、16)。蒸汽发生器、冷凝器和吸收器各包括一个器壁(分别为14、23、22)通过该器壁挥发成分(最好是)和/或液态吸收剂在组件转动时产生的的作用下产生流动。
6 JPH0472144B2 - JP5365084 1984-03-22 JPH0472144B2 1992-11-17 UIRIAMU TERUFUOODO KUROSU; KORIN RAMUSHOO
An absorption heat pump is described comprising at least an evaporator, an absorber, a vapor generator and a condenser and in which at least one of the components is in the form of one or more rotatable plates across the thickness of which plate(s) a heat transfer takes place. Such a heat pump can be designed in compact form.
7 Adsorption type heat pump and absorber combining evaporation JP5365084 1984-03-22 JPS59180262A 1984-10-13 UIRIAMU TERUFUOODO KUROSU; KORIN RAMUSHIYOO
An absorption heat pump is described comprising at least an evaporator, an absorber, a vapor generator and a condenser and in which at least one of the components is in the form of one or more rotatable plates across the thickness of which plate(s) a heat transfer takes place. Such a heat pump can be designed in compact form.
8 吸収式ヒートポンプ装置 JP2015147593 2015-07-27 JP6432462B2 2018-12-05 坪内 修
9 Rotary and absorbent heat pump JP7878994 1994-04-18 JPH07294055A 1995-11-10 MIRUTON EFU PURABUDA
PURPOSE: To obtain compact and mechanically simple heat pump facilities with a chamber where an evaporator and a condenser are mounted rotatably as one group so that they can be arranged concentrically with an absorber outside in the direction of the radius of the absorber, by composing the process of an absorbent heat pump integrally with rotary structure. CONSTITUTION: A pump is composed of a generator, a condenser 3, an evaporator 4, an absorbent cooler 5, and an absorber 1, and is equipped with a means for relating them operatively so that they function as the component of an absorbent heat pump. Also, a mounting means is provided, where the mounting means mounts the component of the heat pump so that the component is rotated as a unit. Then, the absorber 1 is composed of a hollow frusto body that receives the extremely thin film form of absorbent solution with nearly fixed thickness for treatment, and is tapered outward in a downstream direction, the absorber 1, the absorbent cooler 5, and the generator are arranged coaxially, and at the same time the condenser 3 and the evaporator 4 are arranged so that they are concentrical with the absorber 1 outside in the peripheral direction of the absorber 1. COPYRIGHT: (C)1995,JPO
10 Absorption cycle heat machine JP3487491 1991-03-01 JPH05118704A 1993-05-14 TERENSU RESURII UININTON; ROBAATO RAATON; KORIN RAMUSHIYOO
PURPOSE: To obtain an improvement in an efficiency of a heat exchange crossing a thickness of a plate for forming a part of an absorption cycle heat machine. CONSTITUTION: In the absorption cycle heat machine comprising a rotary assembling having a steam generator, a condenser, an evaporator and an absorber, a layer 200 of a thermal structure for improving an efficiency of a heat exchange crossing a disc is provided by increasing a surface area on an inner surface of a wall 116 of the disc of at least the absorber.
11 Heat pumps US051604 1998-04-14 US6035650A 2000-03-14 Terence Leslie Winnington; Richard John Green; Robert Lorton; Robert Brownlee Uselton
A rotary heat pump 10 comprises a vapor generator 20, a condenser 24/34, an evaporator 42 and an absorber 40 interconnected to provide cyclic fluid flow paths for a volatile fluid component and an absorbent fluid therefor. To allow operation of the pump close to the crystallization boundary the pump includes crystallization control means which cause the temperature of the fluid in the region prone to crystallization to be raised when the onset of crystallization is detected. For example the pressure increase upstream of a crystallization site may cause warm fluid to be diverted directly or indirectly to increase the fluid temperature at the crystallization site. The Specification also describes features for controlling the absorbent mixture flow rate; for controlling the concentration thereof; for damping a scoop pump; for assuming flow onto the generator face; for pressure relief and extended operation of the pump; to novel heat exchangers; to metal compositions for the heat pump, and to hydrogen getters for use in heat pumps.
12 Rotary absorption heat pump of improved performance US29619 1993-03-11 US5303565A 1994-04-19 Milton F. Pravda
A rotary absorption heat pump assembly. The assembly comprises a generator (2), condenser (3), evaporator (4), absorbent cooler (5), and absorber (1), all operatively associated to function as components of an absorption-type heat pump of high efficiency and superior operating characteristics. The heat pump is characterized by the presence of a tapered cylindrical absorber (1) which receives and processes, in the form of a very thin peripheral film ("d"), a predetermined amount of absorbent solution. The absorber (1) is arranged in abutting end-to-end relationship to the generator (2), with which it communicates. The condenser (3) and evaporator (4) are arranged end-to-end outside of the absorber (1) and absorbent cooler (5), concentrically therewith and radially spaced therefrom.
13 Rotary inertial thermodynamic multi-stage mass-flow divider US353147 1989-05-12 US5041076A 1991-08-20 Frederick W. Kantor
A multi-stage rotary inertial device and method in which rotary inertial thermodynamic impedance is used in the separation of materials according to their diferences in mass. Thus, an input flow composed of substances having two different masses is separated into two output flows having preferred concentrations, respectively, according to their different masses. Rotary inertial thermodynamic pumping is used for operation of intermediate separator stages. This can be controlled from outside the rotating device by selectively supplying heat to the rotating device.
14 Heat pumps US689190 1985-01-07 US4656839A 1987-04-14 William T. Cross; Colin Ramshaw
A centrifugal absorption heat pump in which the heat released on condensation of the vapor of a first working fluid is used to generate a vapor from a solution of a second working fluid, and/or heat released on absorption of a third working fluid in an absorbent is used to evaporate a fourth working fluid.
15 Rotary thermodynamic apparatus and method US598366 1984-04-09 US4524587A 1985-06-25 Frederick W. Kantor
A rotary inertial thermodynamic absorptive system which can be used as a gas-driven heat pump, a heat-flow-driven gas pump, or, in combination, a heat splitter for moving low-grade heat energy from a lower temperature source to a higher temperature heat sink. In one embodiment, an absorptive type rotary inertial thermodynamic device employs overspill/underspill barriers in its absorption and desorption chambers to achieve counterflow heat exchange therebetween and to ensure effective control of thermodynamic impedance.
16 Rotary thermodynamic apparatus and method US770316 1977-02-18 US4136530A 1979-01-30 Frederick W. Kantor
Rotary thermodynamic compression and refrigeration apparatus and methods in which the mechanical impedance and/or thermodynamic impedance of the system are controlled in order to obtain stable operation. By controlling these impedances, the overall pressure drop of the fluid flow in the system is made to increase with increasing fluid flow rate, thus ensuring stable operation.
17 Centrifugal absorptive thermodynamic apparatus and method US3456454D 1967-01-10 US3456454A 1969-07-22 KANTOR FREDERICK W
18 Air-conditioning apparatus US8491749 1949-04-01 US2559217A 1951-07-03 KEHOE ARTHUR H
19 Rotary absorption heat pump US10580009 2003-11-21 US07818977B2 2010-10-26 Xabier Gorritxategi Retolaza; Unai Oñederra Egaña; José Manuel Cano Rodríguez
Rotary absorption heat pump that comprises a rotary unit (1) that comprises a vapour generator (2), a condenser (3), an evaporator (4) and an absorber (5) interconnected to constitute fluid flow trajectories for a volatile fluid component and a liquid absorbing it. The heat pump also comprises heat transmission means for transmitting heat to the vapour generator (2), said heat transmission means comprising a heat exchanger (6) disposed in the rotary unit (1) through which a hot fluid flows, said heat transmission means also comprising adaptor means in order to transfer said hot fluid from a static environment to said heat exchanger (6).
20 Rotary Absorption Heat Pump US10580009 2003-11-21 US20080314069A1 2008-12-25 Xabier Gorritxategi Retolaza; Unai Onederra Egana; Jose Manuel Cano Rodriguez
Rotary absorption heat pump that comprises a rotary unit (1) that comprises a vapour generator (2), a condenser (3), an evaporator (4) and an absorber (5) interconnected to constitute fluid flow trajectories for a volatile fluid component and a liquid absorbing it. The heat pump also comprises heat transmission means for transmitting heat to the vapour generator (2), said heat transmission means comprising a heat exchanger (6) disposed in the rotary unit (1) through which a hot fluid flows, said heat transmission means also comprising adaptor means in order to transfer said hot fluid from a static environment to said heat exchanger (6).
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