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    • 1. 发明授权
    • Vaporization chambers and associated methods
    • 气化室及相关方法
    • US09574713B2
    • 2017-02-21
    • US12938761
    • 2010-11-03
    • Terry D. TurnerBruce M. WildingMichael G. McKellarLee P. Shunn
    • Terry D. TurnerBruce M. WildingMichael G. McKellarLee P. Shunn
    • F28D15/00F17D1/18
    • F17D1/18F28C3/08F28D15/00F28D2021/0064F28F13/08F28F13/12Y10T137/0391
    • A vaporization chamber may include at least one conduit and a shell. The at least one conduit may have an inlet at a first end, an outlet at a second end and a flow path therebetween. The shell may surround a portion of each conduit and define a chamber surrounding the portion of each conduit. Additionally, a plurality of discrete apertures may be positioned at longitudinal intervals in a wall of each conduit, each discrete aperture of the plurality of discrete apertures sized and configured to direct a jet of fluid into each conduit from the chamber. A liquid may be vaporized by directing a first fluid comprising a liquid into the inlet at the first end of each conduit, directing jets of a second fluid into each conduit from the chamber through discrete apertures in a wall of each conduit and transferring heat from the second fluid to the first fluid.
    • 蒸发室可以包括至少一个管道和壳体。 所述至少一个管道可以在第一端处具有入口,在第二端处具有出口以及其间的流动路径。 壳体可以围绕每个管道的一部分并且限定围绕每个导管部分的腔室。 另外,多个离散的孔可以以每个导管的壁的纵向间隔定位,多个离散孔中的每个离散的孔的尺寸和构造可以将流体射流引导到从腔室到每个管道中。 可以通过将包含液体的第一流体引导到每个管道的第一端处的入口中来将液体蒸发,将第二流体的射流通过每个管道的壁中的离散孔引导到来自腔室的每个导管中,并将热量从 第二流体到第一流体。
    • 4. 发明申请
    • VAPORIZATION CHAMBERS AND ASSOCIATED METHODS
    • 蒸发器和相关方法
    • US20120103428A1
    • 2012-05-03
    • US12938761
    • 2010-11-03
    • Terry D. TurnerBruce M. WildingMichael G. McKellarLee P. Shunn
    • Terry D. TurnerBruce M. WildingMichael G. McKellarLee P. Shunn
    • F17D1/18
    • F17D1/18F28C3/08F28D15/00F28D2021/0064F28F13/08F28F13/12Y10T137/0391
    • A vaporization chamber may include at least one conduit and a shell. The at least one conduit may have an inlet at a first end, an outlet at a second end and a flow path therebetween. The shell may surround a portion of each conduit and define a chamber surrounding the portion of each conduit. Additionally, a plurality of discrete apertures may be positioned at longitudinal intervals in a wall of each conduit, each discrete aperture of the plurality of discrete apertures sized and configured to direct a jet of fluid into each conduit from the chamber. A liquid may be vaporized by directing a first fluid comprising a liquid into the inlet at the first end of each conduit, directing jets of a second fluid into each conduit from the chamber through discrete apertures in a wall of each conduit and transferring heat from the second fluid to the first fluid.
    • 蒸发室可以包括至少一个管道和壳体。 所述至少一个管道可以在第一端处具有入口,在第二端处具有出口以及其间的流动路径。 壳体可以围绕每个管道的一部分并且限定围绕每个导管部分的腔室。 另外,多个离散的孔可以以每个导管的壁的纵向间隔定位,多个离散孔中的每个离散的孔的尺寸和构造可以将流体射流引导到从腔室到每个管道中。 可以通过将包含液体的第一流体引导到每个管道的第一端处的入口中来将液体蒸发,将第二流体的射流通过每个管道的壁中的离散孔引导到来自腔室的每个导管中,并将热量从 第二流体到第一流体。
    • 5. 发明申请
    • METHODS OF CONVEYING FLUIDS AND METHODS OF SUBLIMATING SOLID PARTICLES
    • 输送流体的方法和下游固体颗粒的方法
    • US20120042957A1
    • 2012-02-23
    • US13284737
    • 2011-10-28
    • Terry D. TurnerBruce M. Wilding
    • Terry D. TurnerBruce M. Wilding
    • F15D1/00
    • F28C3/10B01D7/02Y10T137/0318
    • A heat exchanger and associated methods for sublimating solid particles therein, for conveying fluids therethrough, or both. The heat exchanger includes a chamber, and a porous member having a porous wall having pores in communication with the chamber and an interior of the porous member. A first fluid is conveyed into the porous member while a second fluid is conveyed into the porous member through the porous wall. The second fluid may form a positive flow boundary layer along the porous wall to reduce or eliminate substantial contact between the first fluid and the interior of the porous wall. The combined first and second fluids are conveyed out of the porous member. Additionally, the first fluid and the second fluid may each be conveyed into the porous member at different temperatures and may exit the porous member at substantially the same temperature.
    • 一种用于升华固体颗粒的热交换器和相关方法,用于输送流体通过其中或两者。 该热交换器包括一个腔室和一个具有多孔壁的多孔构件,多孔壁具有与腔室连通的孔和多孔构件的内部。 第一流体被输送到多孔构件中,而第二流体通过多孔壁输送到多孔构件中。 第二流体可以沿着多孔壁形成正的流动边界层,以减少或消除第一流体和多孔壁的内部之间的实质接触。 组合的第一和第二流体被输送出多孔构件。 此外,第一流体和第二流体可以各自在不同温度下被输送到多孔构件中并且可在基本相同的温度下离开多孔构件。
    • 8. 发明申请
    • METHODS, APPARATUSES AND SYSTEMS FOR PROCESSING FLUID STREAMS HAVING MULTIPLE CONSTITUENTS
    • 用于处理具有多个组成部分的流体流的方法,装置和系统
    • US20090145167A1
    • 2009-06-11
    • US11951484
    • 2007-12-06
    • Terry D. TurnerBruce M. WildingDennis N. BinghamMichael G. McKellarKerry M. Klingler
    • Terry D. TurnerBruce M. WildingDennis N. BinghamMichael G. McKellarKerry M. Klingler
    • F25J3/00F25J1/00
    • F25J3/0625F25J3/0635F25J3/064F25J3/0645F25J3/0655F25J3/0665
    • Methods, apparatuses and systems for processing fluid streams having multiple constituents are provided including embodiments utilizing ascending temperature separation processes as well as combined ascending and descending temperature separation processes. For example, in one embodiment, a mixed gas stream may be processed by flowing the stream through multiple heat exchangers, expanding the stream, and then separating the stream into a liquid portion and a vapor portion. The vapor portion, having an increased or decreased concentration of an identified constituent may then pass through the heat exchangers again in reverse order and collected. The liquid portion may then be subjected to further, sequential separation acts which each take place at increasing temperatures. In another embodiment, numerous, sequential separation acts take place in, for example, at decreasing temperatures and, subsequently, at increasing temperatures. Such a mixed fluid stream, for example, may include constituents such as hydrogen, carbon monoxide and methane.
    • 提供了用于处理具有多个成分的流体流的方法,装置和系统,包括利用上升温度分离过程以及组合的上升和下降温度分离过程的实施例。 例如,在一个实施例中,混合气流可以通过流过多个热交换器,使流膨胀,然后将流分离成液体部分和蒸汽部分来加工。 具有增加或减少的识别组分浓度的蒸气部分然后可以以相反的顺序再次通过热交换器并收集。 然后可以对液体部分进行进一步的连续分离作用,每个分离作用在升高的温度下发生。 在另一个实施方案中,许多顺序的分离作用发生在例如降低的温度下,随后在升高的温度下进行。 例如,这样的混合流体流可以包括诸如氢气,一氧化碳和甲烷的组分。