| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 141 | Heat Pump | US11912135 | 2006-04-21 | US20090126371A1 | 2009-05-21 | Richard Powell; Derek William Edwards; Andrew Wilson; Frederick Thomas Murphy; Paul David Bernard Bujac |
| A heat pump device in which a temperature difference is established between two heat exchangers by inducing cyclical expansion and compression pulses in a working fluid vapour or gas which passes through an adsorbent porous solid located between the heat exchangers. | ||||||
| 142 | ABSORPTION COOLING SYSTEM | US11770062 | 2007-06-28 | US20080016902A1 | 2008-01-24 | Yehuda Artsiely |
| The invention provides an absorption cooling system of the type including a liquid absorbent that remains in the liquid phase throughout the operation cycle, and a refrigerant having both a liquid phase and a vapor phase in the cycle, the basic system being powered by heat extracted from a hot fluid and powered auxiliary components, the system including the five basic components of a generator, an economizer, a condenser, an evaporator and an absorber, and further including a fluid circuit for the rich solution including a circulation pump, a fluid circuit for the lean solution, and for the refrigerant gas extracted from the liquid absorbent and replaced therein, partial circuits for hot fluid and for a cooling fluid, a jet mixer operating to mix saturated refrigerant gas with the lean solution to re-form the rich solution, the improvement comprising installing means for increasing the pressure of the saturated refrigerant gas flowing from the evaporator to the jet mixer. | ||||||
| 143 | Exhaust heat utilizing refrigeration system | US10488533 | 2002-09-03 | US07155927B2 | 2007-01-02 | Norio Sawada; Kazuo Matsumoto |
| There is provided an exhaust-heat using refrigerating system which can add the function of refrigerant heater, condenser or super-cooler by using exhaust heat. The system comprises a heat pump apparatus 1 equipped with a compressor 12, a first heat exchanger 14, a pressure-reducing device 15 and a second heat exchanger 21, and an absorption type refrigerating machine 5 equipped with a regenerator 51 using exhaust heat as a heat source, a condenser 53, an evaporator 54 and an absorber 55. A third heat exchanger 17 is connected to the first heat exchanger 14 in parallel, and the heat source of the third heat exchanger 17 is achieved from the evaporator 54 of the absorption type refrigerating machine. | ||||||
| 144 | System and method for selective heating and cooling | US11120946 | 2005-05-04 | US20050193758A1 | 2005-09-08 | David Wells |
| A combined heating/cooling system and method is provided wherein an absorption tank (20) houses a refrigerant and absorbant mixture composition. A boiler (50) heats the pressurized mixture composition and vaporizes the refrigerant. Heated absorbant is passed back through a heat exchanger (40) to be delivered back into absorption tank (20) and the vaporized refrigerant is directed to a closed-loop thermal exchange system for selectively heating and cooling ambient air. The mixture may be a composition of NMP as the absorbant and HFC-245fa as the refrigerant. When such a composition is employed, pressure may be reduced such that less expensive construction materials, such as aluminum, may be incorporated into the boiler fluid circuit, such as in the heat exchanger (40). | ||||||
| 145 | Refrigerating method and refrigerating system utilizing gas hydrate | US10504510 | 2003-02-19 | US20050103027A1 | 2005-05-19 | Toshio Ichijo; Kikuo Nakamura |
| A refrigerating method and a refrigerating system utilizing a large decomposition heat absorbed at the time of decomposition of the gas hydrate and building up, by a pump, the pressure of liquid components generated due to the decomposition of gas hydrate and compressing only gas components by a compressor, the refrigerating method comprising the steps of generating the gas hydrate (H) by a hydrate generating reactor (11), decomposing the gas hydrate (H) into the liquid components (L) and the gas components (G) after depressurization to absorb heat, separating the decomposed liquid components (L) and gas components (G) from each other, building up the pressure of the liquid components (L) by the pump (16) and transferring to the hydrate generating reactor (11), and pressurizing and compressing only the gas components (G) by the compressor (17) and transferring to the hydrate generating reactor (11). | ||||||
| 146 | Exhaust heat utilizing refrigeration system | US10488533 | 2002-09-03 | US20050011209A1 | 2005-01-20 | Norio Sawada; Kazuo Matsumoto |
| There is provided an exhaust-heat using refrigerating system which can add the function of refrigerant heater, condenser or super-cooler by using exhaust heat. The system comprises a heat pump apparatus 1 equipped with a compressor 12, a first heat exchanger 14, a pressure-reducing device 15 and a second heat exchanger 21, and an absorption type refrigerating machine 5 equipped with a regenerator 51 using exhaust heat as a heat source, a condenser 53, an evaporator 54 and an absorber 55. A third heat exchanger 17 is connected to the first heat exchanger 14 in parallel, and the heat source of the third heat exchanger 17 is achieved from the evaporator 54 of the absorption type refrigerating machine. | ||||||
| 147 | Adsorbent for heat utilization system, adsorbent for regenerator system, regenerator system comprising the adsorbent, ferroaluminophosphate and method for production thereof | US10638357 | 2003-08-12 | US20040093876A1 | 2004-05-20 | Kouji Inagaki; Atsushi Kosaka; Satoshi Inoue; Yasukazu Aikawa; Takahiko Takewaki; Masanori Yamazaki; Hiromu Watanabe; Hiroyuki Kakiuchi; Miki Iwade |
| An adsorbent for regenerator systems, to a heat utilization system and a regenerator system that comprise the adsorbent, and to a ferroaluminophosphate and a method for production thereof. More precisely, the invention relates to an adsorbent favorable for regenerator systems, which efficiently utilizes the heat source obtainable from cars and the like to thereby realize efficient regenerator systems, to a regenerator system that comprises the adsorbent, to a ferroaluminophosphate to be the adsorbent favorable for regenerator systems, and to a method for production thereof. | ||||||
| 148 | Heat pump-driven external combustion engine | US10316033 | 2002-12-11 | US06715313B1 | 2004-04-06 | Atsusi Takafu |
| There are many heat sources on the earth, and those heat sources radiate heat continuously. Though some of such heat sources are utilized with heat exchange technologies now, they can't deliver power to us effectively. In addition, though external combustion engines can utilize the heat generated from fuel combustion, they let out much carbon dioxide at the same time. This invention has solved above problem. In this invention, the driving energy for the external combustion engine (2) comes from the heat ventilation part/absorption part of the heat pump (1); wherein said heat pump (1) is a metal oxide heat pump (11), and said external combustion engine is a Sterling Engine (21) or a thermo-metal engine (22). | ||||||
| 149 | METHOD OF HEAT TRANSFORMATION FOR GENERATING HEATING MEDIA WITH OPERATIONALLY NECESSARY TEMPERATURE FROM PARTLY COLD AND PARTLY HOT HEAT LOSS OF LIQUID-COOLED INTERNAL COMBUSTION PISTON ENGINES AND DEVICE FOR EXECUTING THE METHOD | US09601503 | 2000-08-02 | US06484501B1 | 2002-11-26 | Hans Otto Mieth; Peter Thomsen; Marcus Gunther |
| The invention relates to a process of heat transformation to convert the low-temperature waste heat from cooling circuits of block-type thermal power station (BTPS) reciprocating-piston combustion engines into steam or other heating media of a temperature required for operation by adopting the principle of the high-temperature heat pump according to which the low-temperature heat produced by recooling the engine cooling circuits to their required inflow temperature required by construction is transferred to a liquid working medium, is absorbed by the working media vapors by partial evaporation, and is brought, by compressing and condensing the working medium vapors, to the temperature of the in-plant heating media and is transferred to them. It is an object of the invention to provide a heat transformation process and devices for realizing the process according to the principle of the high-temperature heat pump using mechanical vapor compression by means of which the waste heat not only of the hot exhaust gas, but also the one of a proproportion as large as possible of the low-temperature waste heat from the cooling circuits for the cylinders, the lubricating oil, and the charging air/fuel mix may be used up to a lower temperature limit to be fixed for each project by conversion into the in-plant common heating medium in a technically reliable manner and at an economical relationship between the investment and operating expenditures to the output from the recuperated energy in reciprocating-piston engine BTPS for the heat supply to commercial and industrial enterprises. This is attained by the fact that inventive connections and devices prevent a drop below the ambient pressure in the critical low-temperature range and in all of the operating conditions of the heat transformer and the energy required for vapour compression is reduced to a minimum and, using steam expansion or hot-air prime movers, is gained completely or in part from the exhaust gas content of the BTPS engine (FIG. 1). | ||||||
| 150 | Heat pumps using organometallic liquid absorbents | US09622625 | 2000-08-16 | US06389841B1 | 2002-05-21 | Karl Thomas Feldman, Jr.; Craig M. Jensen |
| A family of organometallic liquid absorbents that can have their thermophysical properties tailored for specific applications. Processes to manufacture these liquid absorbents and methods to optimize their thermodynamic properties are included. These organometallic liquid absorbents are used in compressor driven and heat driven heat pumps (50) and cryocoolers (99). With optimum thermodynamic properties, these heat pumps systems are highly efficient. These liquid absorbents are not damaging to the environment, are non-toxic and non-corrosive and are applicable to environmentally clean and highly efficient heat pumps, refrigerators, air conditioners, process heating and cooling systems, electronics cooling systems, cryocoolers and gas separation processes. | ||||||
| 151 | Additive for improving performance and cooling capacity of vapor compression systems | US110851 | 1998-07-07 | US5987902A | 1999-11-23 | Robert P. Scaringe; Lawrence R. Grzyll |
| A performance enhancing additive is introduced into a vapor compression system used in cooling and the like. The additive is selected from a class of compounds, e.g. tetraglyme, and added in a predetermined concentration measured relative to the mass of the system's lubricant. The additive can be soluble or non-soluble in the lubricant used in the system's single-phase compressor. It can be added anywhere in the system to provide lower thermodynamic load on the system compressor. | ||||||
| 152 | Compression absorption heat pump | US973395 | 1997-12-11 | US5934101A | 1999-08-10 | Tsuneo Takaki; Mitsuaki Kanetsuki; Akira Ochikubo; Hajime Endou; Yoshinori Nagashima |
| The condensed water, as condensed by applying the VRC to a regeneration process, and the strong solution, as fed out of a regenerator, are employed as a heat source to preheat a weak solution so that the preheating amount of the weak solution is increased to improve the performance coefficient of a heat pump. At a heating time, moreover, the solution concentration is raised by utilizing the cooling heat of the absorbent liquid for the hating operations and by reserving a portion of the regenerated refrigerant liquid, thereby to provide a heat pump for the cooling/heating operations | ||||||
| 153 | Generator-absorber-heat exchange heat transfer apparatus and method and use thereof in a heat pump | US7675993 | 1993-06-15 | US5367884B1 | 1996-12-31 | PHILLIPS BENJAMIN A; ZAWACKI THOMAS S; MARSALA JOSEPH |
| Numerous embodiments and related methods for generator-absorber heat exchange (GAX) are disclosed, particularly for absorption heat pump systems. Such embodiments and related methods use the working solution of the absorption system for the heat transfer medium. | ||||||
| 154 | Chemical/mechanical system and method using two-phase/two-component compression heat pump | US347095 | 1994-11-23 | US5582020A | 1996-12-10 | Robert P. Scaringe; Fulin Gui; Lawrence R. Grzyll; Steve M. Benner |
| A heat pump system and method utilizes heat of mixing, in addition to the latent heat of solution, to increase cooling ability and thermal performance. The system includes a unique two-phase compressor for compressing a two-component mixture of liquid absorbent-refrigerant solution and superheated vapor to a high pressure. A generator extracts heat from the volume to be cooled by desorption and evaporation of the refrigerant from the high concentration solution in fluid connection with the inlet of the compressor. An absorber releases heat to surroundings by absorbing and condensing refrigerant vapor back into the liquid solution. A throttle valve controls the flow and reduces the pressure of the working fluid is in fluid connection with the absorber and the generator. | ||||||
| 155 | Generator-absorber-heat exchange heat transfer apparatus and method and use thereof in a heat pump | US076759 | 1993-06-15 | US5367884A | 1994-11-29 | Benjamin A. Phillips; Thomas S. Zawacki; Joseph Marsala |
| Numerous embodiments and related methods for generator-absorber heat exchange (GAX) are disclosed, particularly for absorption heat pump systems. Such embodiments and related methods use the working solution of the absorption system for the heat transfer medium. | ||||||
| 156 | Regenerative type air conditioning equipment | US834781 | 1992-02-13 | US5285645A | 1994-02-15 | Akira Yamada; Yasuo Koseki; Risuke Onoda; Fumiaki Yatsuboshi; Hirokuni Mizuno |
| A regenerative type air conditioning equipment in which the available concentration range of a heat accumulating liquid is widened, and the quantity of the heat accumulating liquid to be stored is decreased, so that the size of the equipment is reduced, with the conditioning equipment comprises a concentration difference regeneration device which, at least, cools a medium fed to an air conditioner, using a condensate liquid and a concentrated liquid produced by vaporizing the heat accumulating liquid, and a heat pump device which cools a coolant due to adiabatic expansion. The concentration difference regeneration device includes a container with a chamber for storing the condensate liquid, a spray nozzle which sprays the condensate liquid into the condensate liquid chamber, and an evaporator which vaporizes the sprayed condensate liquid under a low pressure. The heat pump device includes a heat exchanger which performs the heat exchange between the coolant and the medium to pass through the air conditioner, and an air cooling mode medium line in which the medium having passed through the air conditioner is circulated in the order of the evaporator, heat exchanger and air conditioner. | ||||||
| 157 | Dual cycle water chiller | US775424 | 1991-10-15 | US5212961A | 1993-05-25 | William J. Graf |
| A dual cycle water chiller or refrigerating system including both a compression-type (mechanical) refrigerator unit and an absorption-type refrigerator unit; further, having a condenser so configured and arranged as to power the absorption cycle substantially entirely from the heat rejected from the compression cycle. The compression and absorption units share a common hermetic housing. Moreover, the system in accordance with the invention involves a dual circuit evaporator whose elements contain the fluid to be cooled for both the compression and absorption units, these elements being so arranged that the fluid to be cooled is acted upon first by the absorption unit, and then by the compression unit, thus optimizing the operational characteristics of each cycle. | ||||||
| 158 | Combined absorption cooling/heating | US739690 | 1991-08-02 | US5127234A | 1992-07-07 | Richard R. Woods, Jr. |
| An improved process and apparatus for absorption cooling in which an absorbent-refrigerant solution from an absorber is heated in a generator producing absorbent-refrigerant vapor, the absorbent-refrigerant vapor is separated and condensed producing pure liquid refrigerant and an absorbent-enriched solution, the absorbent-enriched solution is returned to the absorber, the pure liquid refrigerant is evaporated producing pure refrigerant vapor, and the pure refrigerant vapor is absorbed into the absorbent-enriched solution. A dilute absorbent-refrigerant solution and a concentrated absorbent-refrigerant solution are generated simultaneously in a solution concentration means disposed between the absorber and generator. The dilute absorbent-refrigerant solution is heated to produce a first pure refrigerant vapor and the absorbent-enriched solution. The first pure refrigerant vapor is condensed in the generator in thermal contact with the absorbent-enriched solution producing pure liquid refrigerant. The pure liquid refrigerant is evaporated producing a second pure refrigerant vapor which is subsequently absorbed into the concentrated absorbent-refrigerant solution. | ||||||
| 159 | Thermodynamic cyclic process | US622365 | 1990-12-05 | US5121606A | 1992-06-16 | Jurgen Schukey |
| A thermodynamic cyclic process with a gaseous working medium, which is alternately compressed and expanded, in which process a working medium is employed, which experiences a volume expansion due to chemical processes at the higher temperature after the compression and a corresponding volume contraction at the lower temperature after the expansion, is to be improved so that a higher efficiency is achieved. This is achieved in that the volume contraction is endothermic. In this case, the cyclic process can increase the efficiency both in heat engines and also in heat pumps. | ||||||
| 160 | Combustion-powered refrigeration with decreased fuel consumption | US090127 | 1987-08-27 | US4745768A | 1988-05-24 | Hans P. Schorr; Daniel J. Dessanti |
| In refrigeration systems wherein the refrigerant compressor is driven by a prime mover powered by combustion of a fluid fuel, a notable saving in fuel consumption is achieved by utilizing waste heat in the hot exhaust gases from the prime mover in an absorption refrigeration unit that chills a coolant stream circulated to the condenser for the compressed refrigerant. Existing combustion-powered refrigeration systems can be improved by adding a lithium halide absorption unit to utilize heat in the exhaust gases to produce refrigeration that is used to condense the compressed refrigerant. A combustion turbine coupled to a centrifugal compressor is a preferred combination of prime mover and refrigerant compressor for economically producing tonnage refrigeration. | ||||||
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