| 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 | 一种热量内部循环利用常规压缩热泵/两级吸收复合制冷系统 | CN201410652818.1 | 2014-11-17 | CN104457019A | 2015-03-25 | 何一坚; 李荣; 吴杰; 蒋云云; 陈光明; 王祎 |
| 本发明公开了一种热量内部循环利用常规压缩热泵/两级吸收复合制冷系统，由第一发生器、第一冷凝器、第一储液器、第一节流阀、第一冷凝过冷器、第一吸收器、第一溶液泵、第三储液器、第一溶液换热器、第三节流阀、第二发生器、第三内部换热器、第二储液器、第二节流阀、第一蒸发单元、第二吸收器、第二溶液泵、第二溶液换热器、第四节流装置、第五储液器和第一压缩机、第一内部换热器、过冷器、第一回热器、第五节流装置、第二内部换热器按一定的规律连接。本发明由太阳能、废热等低品位热和机械功两种形式的能量驱动，高效利用了常规压缩热泵子系统排出的极低品位的冷凝热，大幅度提高了电能和低品位热能的利用率，实现了系统能量的高效利用。 | ||||||
| 62 | 蒸气吸收制冷 | CN201180047645.5 | 2011-09-29 | CN103282731A | 2013-09-04 | P·D·寇尔斯 |
| 以如下方式执行蒸气吸收制冷：在冷凝级(98)中使蒸气形式的制冷剂冷凝以获得冷凝的制冷剂，并使其进入膨胀/蒸发级(16)，在该膨胀/蒸发级中，所述制冷剂与高温介质(29)进行热传递以使得至少一些制冷剂被蒸发。蒸发制冷剂从蒸发级进入吸收级(30)，在该吸收级中，一部分制冷剂在第一压力下被吸收到吸收剂中，从而得到部分富制冷剂吸收剂。在压缩吸收级(58)中，该吸收剂在比第一压力高的第二压力下与蒸发制冷剂接触，从而得到从压缩吸收级进入其中该级蒸气形式的制冷剂被回收的制冷剂再生级(62)的富制冷剂吸收剂以及得到贫制冷剂吸收剂。回收的制冷剂再循环进入冷凝级，贫制冷剂吸收剂再循环进入吸收级，在吸收级中所述贫制冷剂吸收剂构成吸收剂。 | ||||||
| 63 | 一种冷热平衡机组 | CN201310025625.9 | 2013-01-21 | CN103075842A | 2013-05-01 | 巢民强 |
| 本发明属于新能源与节能环保领域，提供了一种冷热平衡机组，是一种涉及将系统中的冷量和热量分离并平衡循环，在无与外界（外系统）换热的状态下，同步输出循环平衡的冷量和热量，运行中无能量浪费的冷热平衡机组。其包括用压缩机、热源侧换热器、热力膨胀阀、冷源侧换热器、汽液分离器用管道串联连接。在制热时，冷源侧的冷量可能通过翅片散热器或水路循环散热等换热装置在空气或水中或冷媒中传递到用冷的终端得到有效利用；在制冷时，热源侧的热量可能通过翅片散热器或水路循环散热等换热装置在空气或水中或冷媒中传递到用热的终端得到有效利用。本发明可以成倍提高机组冷热量使用效率，实现零排放和能源循环利用，极大地节省投资成本，可广泛应用于各行各业，具有深远广泛社会价值和经济价值。 | ||||||
| 64 | 用于汽车的改进的吸附式空调装置 | CN200980138017.0 | 2009-09-22 | CN102165275A | 2011-08-24 | E·布达尔; V·布鲁佐 |
| 本发明涉及这样一种类型的装置，它包括：脱附器(100)，吸附器(400)，冷凝器(200)和蒸发器。脱附器(100)和吸附器(400)中充满了由制冷流体和吸附流体形成的至少两种互溶体的混合体，该混合体在吸附器(400)中结合到一起，吸附流体对制冷流体的吸附就发生在该吸附器中。一个增大压力差的部件设置在脱附器(100)和冷凝器(200)之间，以便少许增加冷凝器(200)处的压力和/或少许减小脱附器(100)处的压力，并以此改善空调装置的性能。本发明涉及吸附式空调装置，汽车的空调装置，以及汽车。 | ||||||
| 65 | 废热利用制冷系统 | CN02817043.1 | 2002-09-03 | CN1549913A | 2004-11-24 | 沢田范雄; 松本和夫 |
| 提供一种废热利用制冷系统，该废热利用制冷系统通过使用废热能增加制冷剂预热器、冷凝器或过冷却器的功能。所述系统包括：热泵装置(1)，所述热泵装置配备有压缩机(12)、第一热交换器(14)、减压装置(15)和第二热交换器(21)；以及吸收型制冷机(5)，所述吸收型制冷机配备有使用废热作为热源的回热器(51)、冷凝器(53)、蒸发器(54)和吸收器(55)。第三热交换器(17)并联地连接至第一热交换器(14)，第三热交换器(17)的热源从吸收型制冷机的蒸发器(54)获得。 | ||||||
| 66 | 热泵装置和利用干燥剂起辅助作用的空调系统 | CN200410030190.8 | 1997-01-16 | CN1536280A | 2004-10-13 | 前田健作 |
| 本发明公布了一种将利用干燥剂起辅助作用的空调器和一个热泵装置结合起来的高效的空调系统。该热泵装置具有一个用于从吸收流体中分离致冷剂蒸气的解吸器；一个用于压缩致冷剂蒸气的压缩机；一个用于吸收致冷剂蒸气至吸收流体中的吸收器；一条用于使吸收流体在吸收器和解吸器之间循环的吸收流体通道；一条用于利用压缩机将在该解吸器中产生的致冷剂蒸气输送至该吸收器中的致冷剂压缩通道；和一个用于抽出在吸收器和/或解吸器中产生的吸收热量和解吸作用所需热量的热介质通道装置。 | ||||||
| 67 | 带蒸汽压缩的并联三效吸收式制冷装置 | CN01142614.4 | 2001-12-11 | CN1139767C | 2004-02-25 | 陆震; 袁从杰; 范林; 曹卫华 |
| 一种带蒸汽压缩的并联三效吸收式制冷装置，在制冷剂回路中的中压发生器和低压发生器之间接入蒸汽压缩装置，将中压发生器发生的水蒸汽经压缩后再送入低压发生器。本发明使高压发生器的发生温度得以降低，缓解了高温溴化锂水溶液对金属材料的腐蚀，经压缩进入低压发生器的水蒸汽具有较高的温度和压力，有利于改善低压发生器的发生条件。本发明的蒸汽压缩装置也可置于高压发生器和中压发生器之间，并适用于现有各种连接方式的并联型三效吸收式制冷装置。本发明并不增加系统结构的复杂程度，却具有显著优越性，能解决三效溴化锂吸收式制冷机组高温腐蚀问题，提高能源利用率，具有良好的市场发展前景。 | ||||||
| 68 | 能量转换装置 | CN95117351.0 | 1995-09-19 | CN1066815C | 2001-06-06 | 池上康之; 上原春男 |
| 本发明涉及能量转换装置的改进，所述能量转换装置使用一种混合介制，将热能从低温热源传送到高温热源，以便提高能量转换效率，改善蒸发器和冷凝器的性能，并且降低该装置的生产成本。此外，本发明在部分负载时也能改善性能。所述能量转换装置包括蒸发器，压缩机、冷凝器、气-液分离器、膨胀装置、减压阀以及热交换环路，还可以包括一个回收器，所述压缩机被连结到所述膨胀装置(例如一台涡轮机)上。 | ||||||
| 69 | 使用有机金属液体吸收剂的热泵 | CN98813978.2 | 1998-11-13 | CN1291221A | 2001-04-11 | K·T·小费尔德曼; C·M·詹森 |
| 本发明公开了一类适于特定用途的具有热物理性能的有机金属液体吸收剂。也包括这类液体吸收剂的制造方法和优化其热物理性能的方法。这些有机金属液体吸收剂用于压缩机驱动或热驱动的热泵(50)和低温冷冻机(99)。由于这些热泵具有最佳的热力学性质,它们具有高的效率。这些液体吸收剂不会危害环境,没有毒性和腐蚀性,可用于环境清洁和高效的热泵、冰箱、空调机、工程加热和冷却系统、电子冷却系统、低温冷冻机和气体分离过程。 | ||||||
| 70 | 发生器－吸收器－换热传热装置和方法及其在热泵中的应用 | CN97194280.3 | 1997-04-29 | CN1217053A | 1999-05-19 | 本杰明·A·菲利普斯; 托马斯·S·扎瓦斯基 |
| 发生器－吸收器换热装置(GAX)(300,400)包括:发生器(12)和吸收器(14),吸收器(14)的内部压力低于发生器(12)内部压力,并在两端各自高低温区,形成相应温度范围,温度范围构成相应重叠传热区;流体流动通路,循环致冷剂富、中和弱浓度的液体,到达和通过发生器(12)和吸收器(14)高温,传热和低温区;以及换热回路(352,356,362,435,440,442,444),在液体具有富液浓度的地区(D),接受发生器(12)的液体,并在上述传热区之间,循环上述富液,从而,从吸收器(14)向发生器(12)传热。 | ||||||
| 71 | 热泵装置和利用干燥剂起辅助作用的空调系统 | CN97100425.0 | 1997-01-16 | CN1162094A | 1997-10-15 | 前田健作 |
| 本发明公布了一种将利用干燥剂起辅助作用的空调器和一个热泵装置结合起来的高效的空调系统。该热泵装置具有一个用于从吸收流体中分离致冷剂蒸气的解吸器；一个用于压缩致冷剂蒸气的压缩机；一个用于吸收致冷剂蒸气至吸收流体中的吸收器；一条用于使吸收流体在吸收器和解吸器之间循环的吸收流体通道；一条用于利用压缩机将在该解吸器中产生的致冷剂蒸气输送至该吸收器中的致冷剂压缩通道；和一个用于抽出在吸收器和/或解吸器中产生的吸收热量和解吸作用所需热量的热介质通道装置。 | ||||||
| 72 | 发生器-吸收器-热交换的热传输装置、方法及其在热泵中的应用 | CN95190811.1 | 1995-08-24 | CN1135255A | 1996-11-06 | 本杰明·A·菲利普斯; 托马斯·S·扎瓦奇 |
| 公开了用于发生器-吸收器热交换(GAX)的许多实施的和有关的方法，特别是用于吸收热泵系统的实施例和方法。这些实施例和有关方法采用吸收系统的工作溶液作热传输介质。 | ||||||
| 73 | 能量转换装置 | CN95117351.0 | 1995-09-19 | CN1128842A | 1996-08-14 | 池上康之; 上原春男 |
| 本发明涉及能量转换装置的改进，所述能量转换装置使用一种混合介制，将热能从低温热源传送到高温热源，以便提高能量转换效率，改善蒸发器和冷凝器的性能，并且降低该装置的生产成本。此外，本发明在部分负载时也能改善性能。所述能量转换装置包括蒸发器，压缩机、冷凝器、气—液分离器、膨胀装置、减压阀以及热交换环路，还可以包括一个回收器，所述压缩机被连结到所述膨胀装置(例如一台涡轮机)上。 | ||||||
| 74 | 변온증발 혼합냉매의 액상 냉매 농도측정장치 및 방법과 이를 구비한 흡수식, 1단 압축-흡수식, 그리고 2단 압축-흡수식 히트펌프 | KR1020120000051 | 2012-01-02 | KR101333040B1 | 2013-11-26 | 박성룡; 정시영; 김민성 |
| 본 발명에 따른 변온증발 혼합냉매의 액상냉매 농도 측정장치 및 방법은, 변온증발 혼합냉매 중 포화상태의 액상의 혼합냉매가 설정건도로 일시 저장되도록 컨테이너가 구비되고, 상기 액상의 혼합냉매의 온도와 압력을 측정하여, 미리 저장된 변온증발 혼합냉매의 포화상태의 포화 증기압, 온도, 건도 및 농도 사이의 관계에 대한 데이터 베이스를 통해 농도를 계산할 수 있다. 따라서, 농도 측정을 위한 구성이 컨테이너, 온도센서와 압력센서만으로 매우 간단하여, 비용이 적게 드는 이점이 있다. 또한, 포화상태의 액상의 혼합냉매가 흐르는 유로 상에 컨테이너를 설치하여 측정하기 때문에, 추출하는 경우에 발생하는 증발이나 새는 현상이 없으므로 농도 측정 오차가 최소화될 수 있다. 또한, 기존 설비에도 유동의 방해없이 장착이 용이하다. 또한, 액상의 혼합냉매가 상기 컨테이너로 유입된 후 내부를 채우고 다시 토출되기 때문에, 액상의 혼합냉매의 농도를 실시간으로 측정하고 표시할 수 있다.
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| 75 | 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 | ||||||
| 76 | 정류기, 1단 압축-흡수식 히트펌프 시스템 및 2단 압축-흡수식 히트펌프 시스템 | KR1020110110238 | 2011-10-27 | KR1020130045973A | 2013-05-07 | 박성룡; 김지영; 김민성; 백영진; 나호상; 박준택; 윤형기; 이영수; 장기창 |
| PURPOSE: A rectifier, a one-stage compression-absorption type heat pump system, and a two-stage compression-absorption type heat pump system are provided to control the number of unit modules of a second rectification module, thereby manufacturing a gaseous refrigerant with high purity and refrigerant-absorbent mixed solution at a low concentration by using the refrigerant-gas mixture at a high concentration. CONSTITUTION: A rectifier comprises a first rectification module(10) and a second rectification module(20). The first rectification module includes a first heating member(11), a first cooling member(12), and a first heat transmitting member(130). The first heating member heats a refrigerant-absorbent mixture, thereby evaporating refrigerant from the mixture. The first cooling member cools and condenses the absorbent included in the evaporated refrigerant, thereby removing the absorbent from the evaporated refrigerant. The first heat transmitting member heat exchanges the condensed absorbent and the evaporated refrigerant and evaporates the refrigerant included in the condensed absorbent, thereby making the evaporated refrigerant flow to the first cooling member. [Reference numerals] (AA) Compressor; (BB) High-purity gaseous refrigerant; (CC,FF,KK) Hot water; (DD,GG) Cooling water; (EE,HH) Absorbent; (II) High-density refrigerant-absorbent mixture; (JJ) Expansion device; (LL) Absorber; (MM) Weak solution of refrigerant-absorbent mixture | ||||||
| 77 | 열병합 발전부의 폐열을 이용한 냉방 시스템 | KR1020080049852 | 2008-05-28 | KR100911777B1 | 2009-08-13 | 박종수 |
| A cooling system using the waste heat of a cogeneration unit is provided to cool the indoor using the waste heat in the summer season by exchanging the waste heat with an absorption freezing unit. A cooling system using the waste heat of a cogeneration power generation unit comprises a cogeneration unit, a heat pump system(20), an absorption freezing unit(30), and a cooling heat exchanger(40). The cogeneration unit comprises a boiler(11). The heat pump system has an evaporator(23). The evaporator exchanges the heat of the refrigerant and waste heat after collecting the waste heat generated in a boiler of the cogeneration unit. The absorption freezing unit exchanges the heat with the refrigerant flowing in the heat pump system and performs air-cooling of the indoor. A flow path passes the refrigerant of the absorption freezing unit and a heat pump. | ||||||
| 78 | 열병합 발전 시스템 | KR1020040104362 | 2004-12-10 | KR1020060065875A | 2006-06-14 | 유윤호; 최영섭; 조은준; 이재원; 황윤제 |
| A cogeneration system is disclosed in which waste heat generated from a drive source such as an engine is used in at least one of a compression type air conditioner and an absorption type air conditioner, thereby being capable of achieving an enhancement in cooling/heat capacity. The cogeneration system includes a generator (2), a drive source, a compression type air conditioner (10), an absorption type air conditioner (20), and a waste heat recoverer adapted to recover the waste heat of the drive source, and to supply the recovered waste heat to at least one of the compression type air conditioner (10) and the absorption type air conditioner (20). The absorption type air conditioner (20) can use waste heat during a cooling operation thereof, so that it is possible to enhance the efficiency of using waste heat. | ||||||
| 79 | 열역학적 순환공정용 장치 | KR1019880700151 | 1987-06-11 | KR1019950006403B1 | 1995-06-14 | 지타마쉬넨바우-운트퍼슝게엠베하 |
| 내용 없음. | ||||||
| 80 | 흡착식 축열장치 및 이를 포함하는 시스템 | KR1019900009413 | 1990-06-21 | KR1019930008821B1 | 1993-09-15 | 요네자와야스오; 오니시도시야; 오꾸무라신이찌; 사까이아끼요시; 나까노히로끼; 마쓰시다마사오; 모리가와아쓰시; 요시하라모도시 |
| An adsorption thermal storage apparatus formed of an evacuated vessel comprising therein a refrigerant, and an adsorbent heating or cooling section and a refrigerant condensing or evaporating section located in communication with each other, the former section including an adsorbent and finned heat transfer tubes, the latter section including heat transfer tubes placed in dishes. An adsorption thermal storage system comprising the aforesaid apparatus; a heat source (e.g. a condenser of a compression refrigerator) for adsorbent heating; a cold source (e.g. an evaporator) for refrigerant condensation; an exothermic heat source (e.g. cooling tower); an endothermic heat source (e.g. air cooling coil); and a utilization equipment (e.g. air conditioner), the foregoing elements being connected so that during thermal storage period, the adsorbent heating or cooling section and the refrigerant condensing or evaporating section communicate with the heat source and the cold source, respectively, whereas during utilization period, the adsorbent section communicates with the exothermic heat source or heat utilization equipment and the refrigerant section communicates with cold utilization equipment or the endothermic heat source. By the desorption, the refrigerant is condensed and thermal energy is stored whereas cold is generated by latent heat of evaporation of the refrigerant liquid and heat, by adsorption heat of the refrigerant vapor, whereby heat and cold may be utilized singly or simultaneously. | ||||||
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