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    • 4. 发明授权
    • Refrigeration system, compressing and heat-releasing apparatus and heat-releasing device
    • 制冷系统,压缩和放热装置和散热装置
    • US07690217B2
    • 2010-04-06
    • US10531705
    • 2003-10-24
    • Koichiro TakeEtsuo ShinmuraYuichi Furukawa
    • Koichiro TakeEtsuo ShinmuraYuichi Furukawa
    • F25B1/00
    • F28D1/05366F25B1/10F25B9/008F25B39/04F25B40/00F25B2309/061F25B2400/072F25B2500/01F25B2500/18F28D1/0443F28D2021/0073F28F2009/0287
    • A refrigeration system including a two-stage type compressor having independent low-pressure and high-pressure compressing portions, a heat-releasing device having independent primary and secondary heat-releasing paths, an expansion valve and a cooler. The refrigerant primarily compressed by the low-pressure compressing portion is primarily released in heat by the primary heat-releasing path. The primarily heat-released refrigerant is secondarily compressed by the high-pressure compressing portion. The secondarily compressed refrigerant is secondarily released in heat by the secondary heat-releasing path to thereby obtain a low-temperature and high-pressure refrigerant. The low-temperature and high-pressure refrigerant is decompressed and expanded by an expansion valve and passes through the cooler to absorb the heat in a room air, and then returns to the low-pressure compressing portion of the compressor. In this system, the refrigerant temperature during the heat-releasing procedure can be kept low.
    • 一种包括具有独立的低压和高压压缩部分的两级式压缩机的制冷系统,具有独立的一次和二次散热路径的散热装置,膨胀阀和冷却器。 主要由低压压缩部压缩的制冷剂主要通过一次散热路径被放热。 主要由热释放的制冷剂被高压压缩部二次压缩。 二次压缩的制冷剂通过二次放热路径被二次释放,从而获得低温高压的制冷剂。 低温高压制冷剂通过膨胀阀进行减压膨胀,通过冷却器吸收室内空气中的热量,然后返回到压缩机的低压压缩部。 在该系统中,可以将散热过程中的制冷剂温度保持为低。
    • 7. 发明申请
    • HEAT EXCHANGER
    • 热交换器
    • US20070251682A1
    • 2007-11-01
    • US11736724
    • 2007-04-18
    • Hironaka Sasaki
    • Hironaka Sasaki
    • F28D1/02
    • F28D1/05391F25B39/00F28D1/0391F28D2021/0073F28F1/022F28F9/0221F28F9/0224F28F9/0246F28F9/0278
    • A gas cooler includes paired header tanks, and a plurality of parallel flat tubes disposed between the header tanks. Each header tank is configured such that an outside plate, an inside plate, and an intermediate plate are brazed together in layers. When the height of each flat tube is represented by T (mm), the distance between each of the opposite longitudinal end surfaces of each flat tube and an outer surface of the corresponding intermediate plate is represented by L (mm), and the width of each communication hole of the intermediate plate is represented by W (mm), relations L≧0.7 T and 1.1 T≦W≦2.5 T are satisfied. This gas cooler can minimize an increase in pressure loss when supercritical refrigerant flows from the flat tubes into first refrigerant flow sections of the outside plate and flows from the first refrigerant flow sections into the flat tubes.
    • 气体冷却器包括成对的集水箱和设置在集水箱之间的多个平行的扁平管。 每个集水箱构造成使得外板,内板和中间板被层压在一起。 当每个扁平管的高度用T(mm)表示时,每个扁平管的每个相对纵向端面与相应中间板的外表面之间的距离用L(mm)表示,宽度 中间板的每个连通孔由W(mm)表示,满足关系L> = 0.7T和1.1T <= W <= 2.5T。 当超临界制冷剂从扁平管流入外板的第一制冷剂流动部分并且从第一制冷剂流动部分流入扁平管时,该气体冷却器可以最小化压力损失的增加。
    • 10. 发明申请
    • HEAT EXCHANGER
    • 热交换器
    • US20040256090A1
    • 2004-12-23
    • US10874112
    • 2004-06-22
    • Yoshiki KatohMasaaki KawakuboKen MutoEtsuo Hasegawa
    • F28F007/00
    • F28D1/05366F25B2309/061F28D7/0008F28D2021/0073F28D2021/0085F28F1/045
    • A heat exchanger is used in a vapor-compression type refrigerator where a pressure of a refrigerant at a high-pressure portion reaches and exceeds a critical pressure. A low-pressure refrigerant flows through the heat exchanger. The heat exchanger comprises a flat tube; refrigerant channels included in the tube; and inner pillars disposed between the refrigerant channels. A tensile strength of material of the tube is defined as S nullN/mm2null; of one of the refrigerant channels, a dimension approximately parallel with a major-axis direction of the tube, as Wp nullmmnull; and, of one of the pillars, a thickness approximately parallel with the major-axis direction of the tube, as Ti nullmmnull. Here, null447nullWp/null10{circumflex over (null)}(1.54nulllog10S)nullnull533/null10{circumflex over (null)}(1.98nulllog10S)nullnullnullTinullnull447nullWp/null10{circumflex over (null)}(1.54nulllog10S)nullnull533/null10{circumflex over (null)}(1.98nulllog10S)nullnullnull2.3.
    • 在高压部分的制冷剂的压力达到并超过临界压力的蒸气压缩式冰箱中使用热交换器。 低压制冷剂流过热交换器。 热交换器包括扁平管; 包括在管中的制冷剂通道; 以及设置在制冷剂通道之间的内柱。 管的材料的拉伸强度定义为S [N / mm 2]; 一个制冷剂通道,大致与管的长轴方向平行的尺寸为Wp [mm]; 并且其中一个支柱的厚度与管的长轴方向大致平行,为Ti [mm]。 这里,[447xWp / {10 {circumflex over()}(1.54xlog10S)} - 533 / {10 {circumflex over()}(1.98xlog10S)}] <= Ti <= [447xWp / {10 {circumflex over() }(1.54xlog10S)} - 533 / {10 {circumflex over()}(1.98xlog10S)}] x2.3。