子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 81 | Method for operating adsorption refrigerating system | JP2007303690 | 2007-10-26 | JP2008215799A | 2008-09-18 | MIKHEEV VALDIMIR |
| <P>PROBLEM TO BE SOLVED: To provide a method for operating an adsorption refrigerating system and a system suitable for performing the method. <P>SOLUTION: A method for operating an adsorption refrigerating system is provided. The system comprises a primary adsorption pump so arranged as to communicate with a primary chamber for containing a coolant, a secondary adsorption pump, and a high fluid impedance conduit in which the secondary adsorption pump and the primary chamber are disposed in the communicating state. The method comprises a step of saturating the primary and secondary adsorption pumps with the coolant whilst each pump is at its operational temperature. The pumps are then heated above their operational temperatures to desorb the coolant such that the coolant pressure in the primary chamber and the secondary adsorption pump substantially equalizes through the conduit whilst the primary chamber is cooled. The secondary adsorption pump is then cooled causing coolant gas to be adsorbed and therefore a reduction in temperature and pressure of the coolant in the primary chamber is effected. <P>COPYRIGHT: (C)2008,JPO&INPIT | ||||||
| 82 | Generating method of cooling for building air conditioning due to the thermal chemical methods | JP2007546109 | 2005-12-13 | JP2008524544A | 2008-07-10 | クデール ジャンピエール; スティトゥー ドリス; スピネ ベルナール |
| 本発明は、最高温度が７０℃である間接的熱源と、温度が１５℃であるヒートシンクとを使用してビルを空調するための装置及び方法に関する。
本装置は３〜４つの熱化学的ダイポールを含み、各ダイポールは蒸発器−凝縮器ユニットと、リアクターとを含み、蒸発器−凝縮器ユニットと、リアクターとは、ガスＧをこれらの蒸発器−凝縮器ユニット及びリアクター間で循環させるための手段と、ガスの流れを妨害するための手段とによって連結される。 各リアクターは、ガスＧと、液体または固体との間の可逆性プロセスの座（seat）であり、蒸発器−凝縮器ユニットが、ガスＧの気液相変化の座（seat）であり、各リアクターは、各リアクター間での熱交換のための手段と、熱交換を制御するための手段とを備え、各ダイポールでの熱化学的プロセスは同一又は相違し得、装置は、最高温度が７０℃である可変温度Ｔｃの熱源と、温度Ｔｏが１５℃であるヒートシンクとを使用する。 |
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| 83 | Refrigeration equipment and how to use the reversible sorption system | JP2004523847 | 2003-07-11 | JP2006500542A | 2006-01-05 | スティトゥ，ドゥリス; スピンナー，ベルナルド; ベルトラン，オリビエ |
| 【課題】本発明の目的は、比較的低い作動温度Ｔ
Ｕで且つ大幅に短縮されたサイクル温度と、より高性能で単位体積当たり極めて高い冷凍力を有する装置を提供することにある。
【解決手段】本発明は、可逆収着系によるＴ Ｕでの冷凍に関する。 同設備は、ガスＧと収着体Ｓ間の可逆収着がそこで生ずる反応装置（１）と、ガスＧに関わる可逆収着がそこで生ずる装置（２）と、装置（２）を反応装置（１）と連絡させる手段と、それらを分離する手段を具備し、クラウジウス・クラペイロンのプロットにおいて（２）における可逆現象の平衡曲線が（１）における可逆収着の平衡曲線のそれより低い温度範囲内にあることを特徴とする。 装置（２）は、ガスＧの他に、冷凍作動温度Ｔ Ｕを下回る凝固温度Ｔ Ｓを有する液体／固体の相変化物質Ｍを含む。 種々の製品を凍結するためにもしくは冷水または氷を製造するために有用である。 |
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| 84 | Refrigerator with a sorption refrigeration device operating intermittently | JP13426993 | 1993-06-04 | JP3254041B2 | 2002-02-04 | エッベ オスカー エッベソン ベント |
| A refrigerator is provided with a refrigerating unit in the form of an apparatus showing at least one couple of containers, where each couple comprises a first and a second container (18 and 20, respectively) communicating with each other through a pipe (22) and each container containing a substance which, when being heated gives off a gaseous working medium and when being cooled absorbs the gaseous working medium. The first container (18) is arranged to be heated from the storage compartment (16) of the refrigerator, which compartment thereby is cooled. The second container (20) is provided with a heating means (34). Each container is provided with an arrangement for, when need arises, conducting heat away from the respective container, which arrangement comprises a cooling circuit (26,28,30,32 and 36,38,30,32, respectively), in which, when need arises, a pump (26, 36) brings a cooling liquid to cool the respective container. The liquid is cooled in a radiator (32) arranged on the refrigerator. The cooling circuit is only partly filled with the cooling liquid, so that the liquid sinks back to a level (40) below the container, when the cooling liquid circulation is shut off. |
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| 85 | Method and apparatus for the purification of 貯冷 and water | JP50902391 | 1991-04-29 | JP3043408B2 | 2000-05-22 | チエング，チエン―エン |
| 86 | Thermochemical 蓄排 heat method and apparatus | JP12785686 | 1986-06-02 | JPH0833262B2 | 1996-03-29 | DEIDEIE PEIRU; NATARI MAZE; SHIRUAN MOORAN; BERUNAARU SUPINEERU |
| 87 | Three-phase type heat pump | JP13345084 | 1984-06-29 | JPS6026261A | 1985-02-09 | DEIDEIE PEIRU; JIYORUJIYU KUROZA; BERUNAARU SUPINNERU |
| 88 | ADSORBER AND ADSORBER-TYPE HEAT PUMP | EP11857366.6 | 2011-01-24 | EP2669603B1 | 2018-08-01 | ASO, Noriyasu; MANABE, Toshio |
| An adsorber includes: two or more adsorbents with different coolant vapor-pressure conditions and different coolant temperature conditions corresponding to a lower limit value for a coolant adsorption amount and an upper limit value for the coolant adsorption amount; a container that contains at least one of the adsorbents and in which a coolant is sealable; and a channel pipe that extends through the container, is thermally in contact with the two or more adsorbents, and functions as a channel. | ||||||
| 89 | SELF-DRIVEN THERMAL COMPRESSION HEAT PUMP REFRIGERATION METHOD | EP15812225 | 2015-05-22 | EP3147589A4 | 2018-02-28 | LI HONG; ZHOU YONGKUI |
| The present invention relates to a self-driving heat compression-type heat pump refrigerating method. According to the method, high-temperature steam is prepared, with condensed heat generated by a heat compression-type heat pump refrigerating circulation system, as a driving heat source for heat compression-type heat pump refrigerating circulation system to drive the heat compression-type heat pump refrigerating circulation system. By consuming only a very small amount of electricity, the present invention can prepare the driving steam by using condensing heat generated by refrigerating media steam. The heat generated during the circulation of a system itself is used as a driving heat source, realizing refrigerating and heating. The present invention is highly efficient and energy-saving. | ||||||
| 90 | HYBRID HEAT PIPE | EP16171915.8 | 2016-05-30 | EP3252398A1 | 2017-12-06 | BOLIN, Göran |
There is disclosed a heat transferring device comprising a number of spaces and conduits together with heat transferring elements and a heat exchanger as well as a heat source. The invention is highly suitable for all applications where heat is to be transferred from a small volume to a large area. It is also suitable where the same large area needs to be cooled. It is possible to achieve even temperature distribution on a large surface when the heat source a small. The energy consumption is reduced compared to more traditional technologies. The number of moving parts is minimized which gives lower costs for use, manufacture, maintenance etc. The invention is very versatile and can be utilized in many different applications where it is desired to transfer heat from one point to a large area. It can also be used for cooling purposes.
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| 91 | BEHÄLTER MIT WÄRMETAUSCHER FÜR KOMPAKTE SORPTIONSKÄLTEANLAGEN UND -WÄRMEPUMPEN SOWIE SORPTIONSKÄLTEANLAGE UND -WÄRMEPUMPE MIT EINEM SOLCHEN BEHÄLTER | EP04739498.6 | 2004-06-01 | EP1636528B1 | 2017-10-11 | SCHWEIGLER, Christian; KREN, Christoph; HARM, Mario |
| 92 | ADSORBER AND ADSORBER-TYPE HEAT PUMP | EP11857366 | 2011-01-24 | EP2669603A4 | 2016-08-24 | ASO NORIYASU; MANABE TOSHIO |
| An adsorber includes: two or more adsorbents with different coolant vapor-pressure conditions and different coolant temperature conditions corresponding to a lower limit value for a coolant adsorption amount and an upper limit value for the coolant adsorption amount; a container that contains at least one of the adsorbents and in which a coolant is sealable; and a channel pipe that extends through the container, is thermally in contact with the two or more adsorbents, and functions as a channel. | ||||||
| 93 | VERFAHREN ZUM BETREIBEN EINER ZYKLISCH ARBEITENDEN THERMISCHEN ADSORBTIONSWÄRME- ODER -KÄLTEANLAGE UND VORRICHTUNG | EP12722353.5 | 2012-05-16 | EP2710311B1 | 2016-08-10 | SOMMER, Sebastian; DASSLER, Ingo |
| 94 | VAPOR-LIQUID HEAT AND/OR MASS EXCHANGE DEVICE | EP11817010 | 2011-08-10 | EP2603759A4 | 2015-01-14 | GARIMELLA SRINIVAS; DELAHANTY JARED CARPENTER; NAGAVARAPU ANANDA KRISHNA |
| 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. | ||||||
| 95 | VERFAHREN ZUM BETREIBEN EINER ZYKLISCH ARBEITENDEN THERMISCHEN ADSORBTIONSWÄRME- ODER -KÄLTEANLAGE UND VORRICHTUNG | EP12722353.5 | 2012-05-16 | EP2710311A2 | 2014-03-26 | SOMMER, Sebastian; DASSLER, Ingo |
| The invention relates to a method and a device for operating a cyclical thermal adsorption heating or refrigeration system having a desorption phase and an adsorption phase, comprising at least one adsorber/desorber unit, a refrigerant cyclically adsorbed during the adsorption phase and desorbed during the desorption phase, and an evaporator/condenser unit that acts as an evaporator or as a condenser depending on the process phase. The method and the device intended for carrying out the method are characterized by a cyclic heat recovery that occurs at the same time in a heat recovery circuit having a temporary store and a heat transfer medium, comprising the following steps. At the end of the desorption phase, the heat transfer medium having a low temperature is brought from the temporary store into thermal contact with the evaporator/condenser unit, and at the same time the hot heat transfer medium is transferred from the evaporator/condenser unit into the temporary store in a first temporary storage phase. At the end of the adsorption phase, the heat transfer medium having the higher temperature is brought from the temporary store into thermal contact with the evaporator/condenser unit. At the same time, the cold heat transfer medium is transferred from the evaporator/condenser unit into the temporary store in a second temporary storage phase. | ||||||
| 96 | WÄRMEPUMPE NACH DEM ADSORPTIONSPRINZIP | EP10775811.2 | 2010-11-08 | EP2496895A2 | 2012-09-12 | BURK, Roland |
| The invention relates to a heat pump according to the adsorption principle, comprising a plurality of hollow elements each having an adsorbent, wherein a working medium is enclosed in each of the hollow elements is displaceable between the adsorbent and a phase change area, wherein a heat-transporting fluid in a variable fluid circuit (101) can flow through the hollow elements by means of a valve arrangement (108). The hollow elements are brought into thermal contact with the fluid in the area of the adsorbent, wherein the flow through the hollow elements changes cyclically with the fluid, wherein at least two of the hollow elements are flown through parallel from the fluid at least in one, in particular each position of the valve arrangement, and at least two of the hollow elements are flown through serially one after the other. | ||||||
| 97 | CHEMICAL HEAT PUMP WORKING WITH A HYBRID SUBSTANCE | EP07748186.9 | 2007-05-29 | EP2021704A1 | 2009-02-11 | OLSSON, Ray; BOLIN, Göran |
| 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. | ||||||
| 98 | Wärmepumpe | EP08009044.2 | 2008-05-16 | EP2015006A2 | 2009-01-14 | Burk, Roland |
Die Erfindung betrifft eine Wärmepumpe mit Hohlkörpern (1), die jeweils mindestens eine erste Zone (4) und mindestens eine zweite Zone (5) umfassen, zwischen denen ein Arbeitsmittel reversibel verlagerbar ist, wobei ein Gleichgewicht des Zusammenwirkens des Arbeitsmittels mit jeder der Zonen (4,5) von thermodynamischen Zustandsgrößen abhängt. Um den Wirkungsgrad einer Wärmepumpe zu verbessern, weisen die Hohlkörper (1) jeweils eine erste Wirkfläche (6) mit der ersten Zone (4) auf, die einer zweiten Wirkfläche (7) mit der zweiten Zone (5) gegenüberliegt.
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| 99 | PRODUCTION DE FROID A TRES BASSE TEMPERATURE DANS UN DISPOSITIF THERMOCHIMIQUE. | EP05815190.3 | 2005-11-03 | EP1809956A1 | 2007-07-25 | STITOU, Driss; MAZET, Nathalie; LE PIERRES, Nolwenn Rozenn |
| The invention relates to a thermochemical device and method for producing very low-temperature refrigeration. The inventive device produces refrigeration whose temperature Tf<-20 °C from a heat source available at a Th temperature of 60-80 °C and a heat sink at an ambient temperature To of 10-25 °C. Said device comprises two in-phase operating coupled dipoles. One dipole is regenerateable from a heat source at a temperature Th and a heat sink at To temperature and can produce refrigeration at the Tf temperature with the heat sink at a temperature less than the ambient temperature To. The other dipole is regeneratable from the heat source at the temperature Th and the heat sink at the temperature To. | ||||||
| 100 | PRODUCTION DE FROID A TRES BASSE TEMPERATURE DANS UN DISPOSITIF THERMOCHIMIQUE. | EP05814788.5 | 2005-11-04 | EP1809955A1 | 2007-07-25 | MAZET, Nathalie; STITOU, Driss |
| The invention relates to a thermochemical device and method for producing very low-temperature refrigeration. The inventive device produces refrigeration whose temperature Tf<-20 °C from a heat source available at a Th temperature of 60-80 °C and a heat sink at an ambient temperature To of 10-25 °C. Said device comprises two coupled dipoles operating in an opposite-phase mode. Thermochemical phenomena in one dipole are such that said dipole can produce refrigeration at the Tf by means of a heat sink at the ambient temperature To. The thermochemical phenomena in the other dipole are selected such that said dipole is regeneratable from a heat source Th and the heat sink at the temperature To. | ||||||
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