| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 221 | Equipment for storing blood | US386116 | 1989-07-28 | US4928502A | 1990-05-29 | Susumu Kumada; Mikio Mori; Ryoji Nagatani; Tadami Ano |
| The equipment of the present invention has a plurality of storing cases in which the blood is stored and which is refrigerated by respectively provided Stirling refrigerator, in a keeping-cool room kept at a low temperature. According to the present invention, it is possible to obtain a very low temperature condition less than the recrystallization temperature of the ice in each of the storing cases, refrigerating each storing case wherein the blood is stored by each Stirling refrigerator with high performance coefficient in a very low temperature. A very low temperature condition is realized at a low cost and a high recovery is obtained, which results in that a great deal of blood is stored stably. Furthermore, taking blood in and out is carried out automatically and without the necessity of the operator's entering the keeping-cool room, by providing means for putting the blood in each storing case and taking it out from each storing case and performing the remote control of this means. | ||||||
| 222 | Two-statge sorption type cryogenic refrigerator including heat regeneration system | US304149 | 1989-01-31 | US4875346A | 1989-10-24 | Jack A. Jones; Liang-Chi Wen; Steven Bard |
| A lower stage chemisorption refrigeration system physically and functionally coupled to an upper stage physical adsorption refrigeration system. Waste heat generated by the lower stage cycle is regenerated to fuel the upper stage cycle thereby greatly improving the energy efficiency of a two-stage sorption refrigerator. The two stages are joined by disposing a first pressurization chamber providing a high pressure flow of a first refrigerant for the lower stage refrigeration cycle within a second pressurization chamber providing a high pressure flow of a second refrigerant for the upper stage refrigeration cycle. The first pressurization chamber is separated from the second pressurization chamber by a gas-gap thermal switch which at times is filled with a thermoconductive fluid to allow conduction of heat from the first pressurization chamber to the second pressurization chamber. | ||||||
| 223 | Heat exchange method using natural flow of heat exchange medium | US56419 | 1979-07-10 | US4295342A | 1981-10-20 | James Parro |
| Heat exchange is effected in a simple and economical manner by allowing natural flow, i.e., without mechanical compressors, pumps, etc., of a heat exchange fluid such as a conventional refrigerant liquid between two heat exchangers which are exposed to air at different temperatures. The two heat exchangers, which may conveniently take the form of fin-tube heat exchangers, for example, are arranged with one end at a higher elevation than the other, the upper ends of the two exchangers being connected in direct communication and the lower ends being likewise connected. As the refrigerant liquid absorbs heat and evaporates in the heat exchanger exposed to the warmer air the vapor travels through the upper connecting line to the other heat exchanger, where it rejects heat and is condensed, the liquid flows through the lower connecting line back to the first heat exchanger, and so on, with heat exchange between the two air streams or masses occurring during the natural, continuous flow of the refrigerant in gaseous and liquid form. | ||||||
| 224 | Method and apparatus for conserving energy in an air conditioning system | US94656 | 1979-11-15 | US4277952A | 1981-07-14 | George Martinez, Jr. |
| A method and apparatus for conserving energy in the operation of a conventional air conditioning system in a large building employing a water cooled condenser, an evaporator, a chilled water circuit, and a refrigerant compressor or heat source in an absorption-type air conditioner wherein the compressor or heat source is not energized, the cooling tower is operated, and the water tubes in the evaporator and the water tubes in the condenser are connected to a heat exchanger to effect heat exchange therebetween. | ||||||
| 225 | Cooling process for subambient and above ambient temperatures | US583345 | 1975-06-02 | US4015439A | 1977-04-05 | Sidney Simon Stern |
| The present invention relates to the provision for cooling in systems where above ambient cooling temperatures are indicated, for at least certain system services, while water as a coolant therein is contraindicated. | ||||||
| 226 | Air conditioner | US46529774 | 1974-04-29 | US3913345A | 1975-10-21 | GOETTL WILLIAM H |
| A combination air conditioner comprising a refrigeration type air conditioner and an evaporatively cooled type air conditioner wherein the evaporatively cooled air conditioner is spaced from the condenser of the refrigeration type air conditioner so as not to substantially interfere with air flow through said condenser normal to the operation of said refrigeration type air conditioner. The evaporative cooler so spaced from the condenser being adapted to deliver evaporatively cooled air to the condenser to augment thermal dynamic operation thereof. Additionally, the evaporative cooler is provided with means adapted to operate the fan thereof only without evaporative cooling, to augment operation of the condenser by increasing airflow thereover. Control means for the evaporative cooler comprising a plurality of temperature responsive devices adapted to cause the fan of the evaporative cooler to force air towards said condenser at a plurality of different elevated temperatures and a further temperature responsive switch is also adapted to operate the pump of the evaporative cooler to deliver water to the evaporative cooler pads thereof for maximum augmentation of the condenser operation by the evaporative cooler.
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| 227 | Refrigeration apparatus and method of operating for powered and nonpowered cooling modes | US3744273D | 1972-03-27 | US3744273A | 1973-07-10 | WARE C |
| This specification discloses the method and apparatus for operating a refrigeration system in both powered and nonpowered (free cooling) modes of operation including the method and apparatus for rapidly converting from one mode to the other.
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| 228 | Hydrate decomposition refrigeration process | US19335962 | 1962-05-07 | US3243966A | 1966-04-05 | GLEW DAVID N |
| 229 | Thermo- | US3118285D | US3118285A | 1964-01-21 | ||
| 230 | Refrigeration apparatus | US8491561 | 1961-01-25 | US3073126A | 1963-01-15 | STAEBLER LLOYD A |
| 231 | Refrigeration system | US5122060 | 1960-08-22 | US3052100A | 1962-09-04 | HOMKES BARTELL J |
| 232 | Refrigeration apparatus | US8485061 | 1961-01-25 | US3037358A | 1962-06-05 | SCOFIELD DONALD W |
| 233 | Refrigerating apparatus | US55889156 | 1956-01-13 | US2892321A | 1959-06-30 | KRITZER RICHARD W |
| 234 | Automatic low temperature ice system | US67410733 | 1933-06-02 | US2009372A | 1935-07-23 | MOORE MARION R |
| 235 | 制冷式散热架结构 | CN201020109513.3 | 2010-01-29 | CN201590031U | 2010-09-22 | 许建财; 郑志鸿; 林贞祥; 林国仁 |
| 一种制冷式散热架结构，包括一散热板、一温度传导体、一离心式风扇、一散热体以及一制冷组件；散热板内表面上配置有温度超导组件，温度传导体设于温度超导组件上，另于散热板上侧设有一排热孔；而离心式风扇介于温度传导体与排热孔之间，散热体又介于风扇与排热孔之间，且制冷组件的热端面与散热体相贴、冷端面则设于温度超导组件上；可通过温度超导组件将制冷组件产生的低温快速传导至散热板上，以提供均匀的低温表面来获得散热效果。 | ||||||
| 236 | 一种高效太阳能动力热管热水装置 | CN200520065745.2 | 2005-10-14 | CN2854412Y | 2007-01-03 | 李凡 |
| 本实用新型是一种高效太阳能动力热管热水装置。包括有压缩机(1)、冷凝器(2)、节流装置(5)、蒸发集热器(6)，压缩机(1)及节流装置(5)两端分别并联有第一电磁阀(3)及第二电磁阀(4)，压缩机(1)及第一电磁阀(3)的工质出口通过管路与冷凝器(2)的工质入口相通，压缩机(1)及第一电磁阀(3)的工质入口通过管路与蒸发集热器(6)的工质出口相通，冷凝器(2)的工质出口通过管路与第二电磁阀(4)及节流装置(5)的入口相通，第二电磁阀(4)及节流装置(5)的出口通过管路与蒸发集热器(6)的工质入口相通。本实用新型在阳光充沛时，以太阳能热管工况工作；在阳光不足、阴雨天及夜间时，以热泵工况工作，集中了太阳能热水器和热泵热水器优点，实际能效比高达5－20倍以上。 | ||||||
| 237 | 直接膨張およびポンピング冷媒節約冷却を持つ冷却システム | JP2017563934 | 2016-06-10 | JP2018521288A | 2018-08-02 | リン,ジーヨン; マダーラ,スティーブン; ドルシック,ベネディクト・ジェイ; シラート,スティーブン; シュッテ,ダニエル・ジェイ |
| 冷却システムは、ポンピング冷媒節約および直接膨張冷却の両方を有する。ポンピング冷媒節約が冷却要求を満たすのに十分な冷却を提供することができるほど外気温度が低い場合は、ポンピング冷媒節約冷却のみが、冷却を提供するために使用される。ポンピング冷媒節約が冷却要求を満たすのに必要とされる冷却の全てではないが一部を提供することができるほど外気温度が低い場合は、ポンピング冷媒節約は、100パーセントの能力で作動され、直接膨張冷却は、必要とされる任意の補助冷却を提供する能力で作動される。ポンピング冷媒節約がいかなる冷却も提供できないほど外気温度が高いならば、その場合、直接膨張冷却のみが、冷却を提供するために使用される。 | ||||||
| 238 | 熱媒体流路切替装置およびこれを備えた空気調和装置 | JP2016534324 | 2015-06-09 | JP6188946B2 | 2017-08-30 | 高松 亮平; 小川 瑞樹; 斉藤 浩二; 今泉 賢; 本村 祐治 |
| 239 | 冷凍装置の昇華デフロストシステム及び昇華デフロスト方法 | JP2015532991 | 2014-11-25 | JPWO2015093235A1 | 2017-03-16 | 吉川 朝郁; 朝郁 吉川; 神村 岳; 岳 神村; 貴弘 古舘; 深野 修司; 修司 深野 |
| 冷凍庫の内部に設けられ、ケーシング及び該ケーシングの内部に設けられた熱交換管を有する冷却器と、CO2冷媒を冷却液化する冷凍機と、熱交換管に接続され、冷凍機で冷却液化されたCO2冷媒を熱交換管に循環させる冷媒回路とを有する冷凍装置の昇華デフロストシステムである。冷凍庫の庫内空気を除湿するための除湿装置と、熱交換管の入口路及び出口路に接続された循環路形成路によって形成されるCO2循環路と、熱交換管の入口路及び出口路に設けられ、デフロスト時に閉じて前記CO2循環路を閉回路とする開閉弁と、CO2循環路に設けられたCO2冷媒の循環手段と、温ブラインとCO2循環路を循環するCO2冷媒とを熱交換させる第1熱交換部と、デフロスト時に閉回路を循環するCO2冷媒の凝縮温度が冷凍庫の庫内空気中の水蒸気の氷点以下の凝縮温度となるように、CO2冷媒の圧力を調整する圧力調整部とを備え、ドレン受け部を設けずにデフロストを可能にする。【選択図】図1 | ||||||
| 240 | 冷凍装置のデフロストシステム及び冷却ユニット | JP2015532990 | 2014-11-25 | JPWO2015093233A1 | 2017-03-16 | 吉川 朝郁; 朝郁 吉川; 佐野 誠; 誠 佐野; 巌 寺島; 大樹 茅嶋 |
| 冷凍庫の内部に設けられ、ケーシングの内部に導設された熱交換管及びドレン受け部を有する冷却器と、CO2冷媒を冷却液化する冷凍機と、前記冷凍機で冷却液化したCO2冷媒を前記熱交換管に循環させるための冷媒回路と、前記熱交換管の入口路及び出口路から分岐し、前記熱交換管と共にCO2循環路を形成するデフロスト回路と、デフロスト時に閉じて前記CO2循環路を閉回路とする開閉弁と、デフロスト時に前記閉回路を循環するCO2冷媒を圧力調整するための圧力調整部と、前記冷却器より下方に設けられ、前記デフロスト回路及び第1加熱媒体であるブラインが循環する第1ブライン回路が導設され、前記ブラインで前記デフロスト回路を循環するCO2冷媒を加熱するための第1熱交換部とを備え、デフロスト時に前記閉回路でCO2冷媒をサーモサイフォン作用により自然循環させる。【選択図】図1 | ||||||
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