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    • 3. 发明授权
    • Point cooling
    • 点冷却
    • US06412288B1
    • 2002-07-02
    • US09762359
    • 2001-04-13
    • Mikael Orsén
    • Mikael Orsén
    • F17C902
    • B29C45/7337A61F7/00B29C35/16B29C2035/165C21D1/613F25D3/10F25D29/001
    • The present invention relates to a method and a device for point cooling. The cooling device comprises a cooling channel provided with a defined small end surface (9, 39) and an outlet valve (11) separated therefrom, a container (13) with liquid carbon dioxide and an access conduit (15a-c, 43) connected to said container (13) provided with a nozzle (17, 45) localized to said cooling channel, whereby liquid carbon dioxide is brought to flow from the container out through said nozzle. The invention further comprises to choose the overpressure of the container, adjust the outlet valve (11) and design the nozzle in such a way that the pressure in the cooling channel (7, 35) is kept above the so-called triple point of carbon dioxide and that the distance between the nozzle (17, 45) and the defined small end surface (9, 39) is adapted so as to substantially gasify the carbon dioxide at said end surface. The device is particularly intended for point cooling of a injection moulded or cast detail (31) with a sharp edge (33) or a varying material thickness, whereby the cooling channel (35) is provided in a moulding tool (37) intended for the detail.
    • 本发明涉及点冷却的方法和装置。 冷却装置包括设置有限定的小端面(9,39)和与其分离的出口阀(11)的冷却通道,具有液态二氧化碳的容器(13)和连接到其上的通路导管(15a-c,43) 设置有设置有位于所述冷却通道的喷嘴(17,45)的所述容器(13),由此液体二氧化碳从所述容器通过所述喷嘴流出。 本发明还包括选择容器的超压,调节出口阀(11)并设计喷嘴,使得冷却通道(7,35)中的压力保持在所谓的碳三重点上方 并且喷嘴(17,45)和限定的小端面(9,39)之间的距离适于使得在所述端面处基本上气化二氧化碳。 该装置特别用于具有尖锐边缘(33)或变化的材料厚度的注射成型或铸造细节(31)的点冷却,由此冷却通道(35)设置在用于 详情。
    • 4. 发明授权
    • Method of evaporating a low temperature liquid medium
    • 蒸发低温液体介质的方法
    • US06263678B1
    • 2001-07-24
    • US09591910
    • 2000-06-09
    • Friedemann Suttrop
    • Friedemann Suttrop
    • F17C902
    • B64G1/50F02C7/224F17C9/02F17C13/10F17C2203/012F17C2221/012F17C2223/0153F17C2223/033F17C2225/0123F17C2227/0393F17C2260/032F17C2270/0189F28D7/026F28D7/106F28D2021/0033F28D2021/0047Y02E60/321Y02P90/45
    • In a method and evaporator device for evaporating a low temperature liquid medium, such as hydrogen for example, the hydrogen is first evaporated and at least partially superheated in a forward-flowing first channel, and is then directed to flow back in the opposite direction in a second return-flowing channel. The second channel is especially interposed between the first channel and a passage through which flows a heat-providing medium such as a hot exhaust gas. Thus, the superheated hydrogen flowing in the second channel serves as an intermediate layer for heat transfer from the heat-providing medium through the hydrogen in the second channel to the low temperature, initially liquid hydrogen in the first channel. The heat exchange surfaces in contact with the heat-providing medium are not directly adjacent the extremely cold surfaces in contact with the in-flowing low temperature liquid hydrogen, and the superheated hydrogen acts as a buffer between the hot side and the cold side of the evaporator. As a result, the evaporator has a very low structural weight, and condensation and icing problems can be avoided even when using a hot medium and a cold medium having extremely different temperatures.
    • 在用于蒸发例如氢气的低温液体介质的方法和蒸发器装置中,首先在向前流动的第一通道中蒸发氢并且至少部分地过热,然后将氢引导回向相反方向 第二回流通道。 第二通道特别介于第一通道和流过诸如热废气之类的供热介质的通道之间。 因此,在第二通道中流动的过热氢气用作从第二通道中的从供热介质通过氢气到第一通道中的低温初始液态氢的热传递的中间层。 与供热介质接触的热交换表面不直接邻近与流动中的低温液态氢接触的极冷的表面,并且过热的氢气充当热侧和冷端之间的缓冲区 蒸发器。 结果,蒸发器具有非常低的结构重量,并且即使当使用具有极高温度的热介质和冷介质时也可以避免冷凝和结冰问题。