| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 61 | 찰과부식 대응 요동베인형 펌프 엑츄에이터 | KR1020110033138 | 2011-04-11 | KR1020110116090A | 2011-10-25 | 신승호; 홍기용; 와타베토미지 |
| 요동베인형 펌프 엑츄에이터를 시판품에서 실현할 수 없는 25MPa 고압력에서 사용가능토록 하기 위해, 독자적인 씰 기구를 채용하고, 고효율 파력발전장치인 진자형 파력발전장치의 요동 베인펌프에 응용하여, 대동력 요동펌프로서 장기 실증시험을 했던 바, 강성이 높은 방향과 낮은 방향이 서로 역 방향인 수압부품(受壓部品)의 고강도 결합면에서 찰과부식에 의한 응착마모현상이 발생했다. 고효율 진자형 파력발전시스템의 조기 실용화를 위해 이상마모현상 해소라는 과제를 조속히 해결할 필요성이 있다.
중심축에 대해 방사방향의 강성이 낮은 실린더와 강성이 높은 사이드 커버와의 결합면에서, 고압력 작동유가 실린더 단면을 타원형에 가깝게 왜곡시킬 때 사이드 커버측도 마찬가지로 원통형상을 설치함으로서 같은 왜곡이 생기도록, 사이드 커버에는 실린더 측으로 돌출한 원통 형상부를 설치하였다. 또한 실린더에 고정되어 있는 고정 베인의 사이드 커버와의 접촉면에는 항상 저압측 작동실이 연통하는 관로를 설치했다. |
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| 62 | 유기 금속액 흡수제를 사용하는 열펌프 | KR1020007009209 | 1998-11-13 | KR1020010041159A | 2001-05-15 | 펠드만,케이.,토마스,쥬니어; 젠센,크레익,엠. |
| 본발명은특정용도를위해맞춰진열물리학적특성을가질수 있는유기금속액흡수제의군에관한것이다. 또한, 본발명에는이러한액체흡수제를제조하는공정및 이의열역학적특성을최적화시키기위한방법이포함된다. 이들유기금속액흡수제는압축기구동및 열구동열펌프(50) 및극저온냉각기(99)에사용된다. 최적의열역학적특성을갖는경우, 이들열펌프시스템은매우효율적이다. 이러한액체흡수제는환경에유해하지않으며, 비독성이고, 비부식성이어서환경을오염시키지않고매우효율적인열펌프, 냉장고, 공기조화기, 공정열및 냉각시스템, 전기냉각시스템, 극저온냉각기및 기체분리공정에적용될수 있다. | ||||||
| 63 | 압축기용 제습기, 1단 압축-흡수식 히트펌프 시스템 및 2단 압축-흡수식 히트펌프 시스템 | KR1020120000050 | 2012-01-02 | KR101265683B1 | 2013-05-22 | 박성룡; 김지영; 김민성; 백영진; 나호상; 박준택; 윤형기; 이영수; 장기창 |
| PURPOSE: A dehumidifier for a compressor, a single-stage compression-absorption type heat pump system, and a two-stage compression-absorption type heat pump system are provided to reduce damage to the compressor. CONSTITUTION: A dehumidifier for a compressor comprises first and second dehumidification members(11,12), a first flow passage control valve(30), and a second flow passage control valve(20). The first and second dehumidification members absorb the moisture. The first flow passage control valve includes: a first inlet where gaseous refrigerant of low temperature flows; a second inlet where gaseous refrigerant of high temperature and high pressure flows; a first through-hole communicated with the first dehumidification member; and a second through-hole communicated with the second dehumidification member. The second flow passage control valve includes: a first outlet communicated with an inlet of the compressor; a second outlet communicated with an external device; a third through-hole communicated with the first dehumidification member; and a fourth through-hole communicated with the second dehumidification member. [Reference numerals] (AA) Absorber; (BB) Compressor inlet; (CC) Desorber; (DD) Compressor outlet | ||||||
| 64 | 찰과부식 대응 요동베인형 펌프 엑츄에이터 | KR1020110033138 | 2011-04-11 | KR101155582B1 | 2012-06-19 | 신승호; 홍기용; 와타베토미지 |
| 요동베인형 펌프 엑츄에이터를 시판품에서 실현할 수 없는 25MPa 고압력에서 사용가능토록 하기 위해, 독자적인 씰 기구를 채용하고, 고효율 파력발전장치인 진자형 파력발전장치의 요동 베인펌프에 응용하여, 대동력 요동펌프로서 장기 실증시험을 했던 바, 강성이 높은 방향과 낮은 방향이 서로 역 방향인 수압부품(受壓部品)의 고강도 결합면에서 찰과부식에 의한 응착마모현상이 발생했다. 고효율 진자형 파력발전시스템의 조기 실용화를 위해 이상마모현상 해소라는 과제를 조속히 해결할 필요성이 있다.
중심축에 대해 방사방향의 강성이 낮은 실린더와 강성이 높은 사이드 커버와의 결합면에서, 고압력 작동유가 실린더 단면을 타원형에 가깝게 왜곡시킬 때 사이드 커버측도 마찬가지로 원통형상을 설치함으로서 같은 왜곡이 생기도록, 사이드 커버에는 실린더 측으로 돌출한 원통 형상부를 설치하였다. 또한 실린더에 고정되어 있는 고정 베인의 사이드 커버와의 접촉면에는 항상 저압측 작동실이 연통하는 관로를 설치했다. |
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| 65 | SWING VANE-TYPE PUMP ACTUATOR WHICH PREVENTS FRETTING CORROSION | EP11769108.9 | 2011-04-14 | EP2562421B1 | 2017-03-29 | WATABE, Tomiji; SHIN, Seung-Ho; HONG, Key-Yong |
| 66 | Absorptionskältemaschine mit wässrigem Kältemittel | EP10153267.9 | 2010-02-11 | EP2218982A2 | 2010-08-18 | Steinbrück, Matthias |
Die Erfindung betrifft ein Verfahren zur Erzeugung von Kälte mittels einer Absorptionskältemaschine mit Es soll nun eine Absorptionskältemaschine geschaffen werden, die mit einem wässrigen Kältemittel zuverlässig Temperaturen weit unter dem Gefrierpunkt von Wasser bei Umgebungsdruck schaffen kann. Dies wird dadurch erreicht, dass der aus dem Lösungsmittel ausgetriebene Wasserdampf einem Resorber (27) zugeführt wird, wobei in dem Resorber (27) eine Lösung aus Wasser und Frostschutzmittel aufgenommen ist, in der der Wasserdampf absorbiert wird, und wobei die Lösung aus Wasser und Frostschutzmittel in den Verdampfer (1) geleitet wird, um das Wasser aus der Lösung zu verdampfen.
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| 67 | RESORPTIONS-WÄRMEWANDLERANLAGE | EP85900099.4 | 1984-12-05 | EP0164382B1 | 1988-05-18 | MUCIC, Vinko |
| Heat pumps, refrigerating units, thermal transformers and the like, actuated by means of a dual working material, particularly a mixture of ammonia and water, according to the resorption principle, operate with two solution cycles (I, II) wherein the working medium in liquid phase is brought from a lower pressure level to a higher pressure level and is expanded to a new lower pressure level, a connection (38, 40) existing respectively for the lower pressure and the upper pressure between the solution cycles (I, II), wherein the working medium in a vapour phase is exchanged. To compensate all the differences of concentration and quantity of the working medium in the two solution cycles (I, II) which occur during operation, there is provided in parallel to one of the two connections (38, 40) for the working medium in the vapour state a compensation connection (44) for the flowing liquid substance having a different concentration. The quantitative flow (Y) of the liquid working medium flowing in the compensation connection (44) is regulated by means of a central computer (48) as a function of the concentrations of the working medium flowing in the connections (38, 40) between the solution cycles (I, II), as well as of the amount (2) of the working medium in the vapour state circulating in one of the connections and of the concentration of the liquid working medium circulating in the compensation line (44). | ||||||
| 68 | Machine a induction thermique | EP84115702.7 | 1984-12-18 | EP0147770B1 | 1988-01-07 | Sterlini, Jacques |
| 69 | Absorption-resorption heat pump | EP85201904.1 | 1985-11-18 | EP0183316B1 | 1987-05-27 | Bassols Rheinfelder, Juan |
| An absorption-resorption heat pump comprising a first circuit including a desorber and an absorber interconnected by conduits having a heat exchanger provided therein, so that a first circulatory flow of a first system of liquid substances can be maintained by suitable means from the desorber to the absorber via one of the conduits and from the absorber to the desorber via another one of the conduits, and a second circuit including a resorber or condenser and an evaporator likewise interconnected by conduits having a heat exchanger provided therein, so that a second circulatory flow of a second system of essentially similar liquid substances can be maintained by suitable means from the evaporator to the resorber or condenser via one of the conduits and from the resorber or condenser to the evaporator via another one of the conduits. The desorber of the first circuit is connected through a conduit for a volatile component of the first system of substances to the resorber or condenser of the second circuit and the evaporator of the second circuit is connected through a conduit for a volatile component of the second system of substances to the absorber of the first circuit. A branch circuit extends from a point in the second circuit to the desorber section of the first circuit. | ||||||
| 70 | Absorption-resorption heat pump | EP85201904.1 | 1985-11-18 | EP0183316A1 | 1986-06-04 | Bassols Rheinfelder, Juan |
An absorption-resorption heat pump comprising a first circuit including a desorber (2) and an absorber (1) interconnected by conduits (3,4) having a heat exchanger (5) provided therein, so that a first circulatory flow of a first system of liquid substances can be maintained by suitable means from the desorber (2) to the absorber (1) via one (4) of the conduits and from the absorber (1) to the desorber (2) via another one (3) of the conduits, and a second circuit including a resorber or condenser (8) and an evaporator (12) likewise interconnected by conduits (9, 13) having a heat exchanger (15) provided therein, so that a second circulatory flow of a second system of essentially similar liquid substances can be maintained by suitable means from the evaporator (12) to the resorber or condenser (8) via one (13) of the conduits and from the resorber or condenser (8) to the evaporator (12) via another one (9) of the conduits. The desorber (2) of the first circuit is connected through a conduit (7) for a volatile component of the first system of substances to the resorber or condenser (8) of the second circuit and the evaporator (12) of the second circuit is connected through a conduit (11) for a volatile component of the second system of substances to the absorber (1) of the first circuit. A branch circuit (19) extends from a point in the second circuit to the desorber section (2) of the first circuit. A storage vessel (18) is provided at a point downstream of the heat exchanger (15) in that section of the second circuit where liquid passes from the evaporator (12) to the resorber (8), which storage vessel (18) includes an overflow mechanism, and the branch conduit (19) is connected to this overflow mechanism. |
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| 71 | Procédé de production de froid et/ou de chaleur mettant en oeuvre un cycle à absorption utilisant le dioxyde de carbone comme fluide de travail | EP82401237.1 | 1982-07-01 | EP0070756A2 | 1983-01-26 | Rojey, Alexandre; Cheron, Jacques |
Procédé de production de froid et/ou de chaleur mettant en œuvre un cycle à absorption utilisant le dioxyde de carbone comme fluide de travail. Le cycle comprend 4 étapes : une désorption en (D2) et une absorption à pression relativement élevée en (EC2), suivies d'une désorption en (EV2) et d'une absorption à pression relativement basse en (A2). Le procédé rend possible l'utilisation, comme fluide de travail, du dioxyde de carbone, composé particulièrement bon marché et sûr d'emploi. |
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| 72 | Variable effect thermal machine | EP81305131 | 1981-10-29 | EP0052452A3 | 1982-12-01 | Kauffman, Kenneth W. |
High, intermediate and low pressure stages are provided in a thermal machine including sealed chambers permitting maintenance of respective pressures but permitting flow of vapor from one vessel to a second within a stage and providing for the flow of an absorbent solution among the vessels in different stages. The intermediate stage includes resorption and regeneration vessels which are thermally coupled, respectively, to a generation vessel and an absorption vessel in the high and low pressure stages, so that a variable friction of the absorber heat may be transferred to the regenerator and of the resorber heat to the generator. The machine can adjust to a wide range of available heat source and heat rejection temperatures while maintaining high efficiency. Several versions of the machine, some including an evaporator and a condensor and others including a power converter, and using fluids selected for each purpose, may be applied to heat pumping, chilling, temperature amplification, power production and desalination. |
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| 73 | COMPACT RESORPTION MACHINE | PCT/EP2009005900 | 2009-08-13 | WO2010017991A3 | 2010-04-15 | WEIMER THOMAS |
| The invention relates to a system for heating or cooling, having a resorption circuit that has at least one absorber (3) and at least one desorber (1), wherein the at least one absorber or the at least one desorber is configured at least as one compact heat exchange device, or at least as one membrane contactor, wherein the heat exchange device is selected from a group consisting of plate heat exchangers and spiral heat exchangers. The invention further relates to a respective method for heating or cooling. | ||||||
| 74 | SWING VANE-TYPE PUMP ACTUATOR WHICH PREVENTS FRETTING CORROSION | PCT/KR2011002686 | 2011-04-14 | WO2011129642A2 | 2011-10-20 | WATABE TOMIJI; SHIN SEUNG-HO; HONG KEY-YONG |
| A test for operation over an extended period was performed on a high-power swing pump in which an independent seal device was employed, and a swing vane pump of a high-efficiency, pendulum-type wave power generating system was applied to use a swing vane-type pump actuator at a high pressure of 25MPa, as opposed to conventional, commercially available actuators. Test results showed that abrasive wear occurs by fretting corrosion at high-strength joint surfaces of hydraulic components in which a high-strength direction and a low-strength direction oppose each other. A need exists to quickly overcome abnormal wear and put a high efficiency wave power generating system into practical use. When a cylinder, the strength of which is low in the radiation direction with respect to a center shaft, and a side cover, the strength of which is high in the radiation direction, are coupled together to form joint surfaces therebetween, a cylindrical portion, which protrudes toward the cylinder, is arranged at the cylinder cover, such that the same distortion occurs to the side cover as that of the cross-section of the cylinder, which is distorted to a nearly elliptical shape by high-pressure working fluids. In addition, a pipeline, with which a low-pressure side working chamber is always in communication, is installed on the surface of a static vane fixed at the cylinder, wherein said surface of the static vane contacts the side cover. | ||||||
| 75 | COABSORBENT CYCLES HEAT PUMPING AND MECHANICAL WORK PRODUCING PROCEDURE AND APPLYING INSTALLATION | PCT/RO2007000018 | 2007-09-24 | WO2008094057A3 | 2008-10-02 | STAICOVICI MIHAIL DAN |
| Procedure of producing combined heating, cooling and electrical power with high global efficiency, using coabsorbent truncated heat pumping cycles of much higher thermal efficiency than those known so far in coupling with a known thermodynamic Rankine power cycle, thermally connected with two fluids of low temperature potential, e.g. (5-75) °C, but with sensible different temperatures, AT = (10 - 50) °C, identified as heat pumping coabsorbent truncated cycles sink and heat sources, the hottest one at least or both coming of the thermal coupling with the power cycle, the first fluid of higher temperature, e.g. 40 °C during the cold season and (50-80) °C during the warm season, being a fraction of that which extracted the heat from the power cycle exothermic condensing or low cogeneration processes and the second one, of lower temperature, e.g. (5-35) °C, being a fraction of that which was cooled by the power cycle sink source. | ||||||
| 76 | KOMPAKTE RESORPTIONSMASCHINE | EP09777879.9 | 2009-08-13 | EP2321590B1 | 2018-03-28 | WEIMER, Thomas |
| 77 | Absorptionskältemaschine mit wässrigem Kältemittel | EP10153267.9 | 2010-02-11 | EP2218982A3 | 2011-08-03 | Steinbrück, Matthias |
Die Erfindung betrifft ein Verfahren zur Erzeugung von Kälte mittels einer Absorptionskältemaschine mit Es soll nun eine Absorptionskältemaschine geschaffen werden, die mit einem wässrigen Kältemittel zuverlässig Temperaturen weit unter dem Gefrierpunkt von Wasser bei Umgebungsdruck schaffen kann. Dies wird dadurch erreicht, dass der aus dem Lösungsmittel ausgetriebene Wasserdampf einem Resorber (27) zugeführt wird, wobei in dem Resorber (27) eine Lösung aus Wasser und Frostschutzmittel aufgenommen ist, in der der Wasserdampf absorbiert wird, und wobei die Lösung aus Wasser und Frostschutzmittel in den Verdampfer (1) geleitet wird, um das Wasser aus der Lösung zu verdampfen.
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| 78 | THERMISCHE PROZESSE DES AUSDAMPFENS, KONDENSIERENS UND ABSORBIERENS UND IHRE KOMBINATIONEN | EP91903722.6 | 1991-02-04 | EP0531293B1 | 1996-02-14 | Vinz, Peter, Dr.-Ing. |
| Process involving no heat loss using evaporation, condensation and absorption for thermal separation of absorptive and non-absorptive liquid mixtures, and processes for complete conversion of heat into entropy-free useful work, and a process for heat insultion can be derived from the Gibbs-Helmholtz law. The invention concerns the se energy processes and various forms of execution thereof. | ||||||
| 79 | Procédé à cycle de resorption pour les pompes à chaleur | EP83400795.7 | 1983-04-21 | EP0093051B1 | 1989-09-20 | Rodié-Talbère, Henri |
| 80 | Thermal induction machine | EP84115702 | 1984-12-18 | EP0147770A3 | 1985-08-14 | Sterlini, Jacques |
