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    • 7. 发明授权
    • Steam conditioning system
    • 蒸汽调节系统
    • US09593598B2
    • 2017-03-14
    • US14710852
    • 2015-05-13
    • Holtec International
    • Akhilesh Vidyutkumar BapatIndresh RampallVytautas Vincas Maciunas
    • F22G5/12F01K17/04F01K9/00F01K3/18F28B9/02F28B1/02
    • F01K17/04F01K3/18F01K9/003F22G5/12F28B1/02F28B9/02F28F2250/06F28F2265/00
    • A steam conditioning system for discharging bypass steam into a condenser of a steam powered generating plant and other uses. The system includes a steam conditioning device comprising an inner evaporative core and an outer shell. The core may be formed of a tubular piping section disposed at least partially inside the outer shell forming an annular space therebetween. An inlet end of the core receives steam from a piping header fluidly connected to an upstream desuperheating pressure reducing station which injects liquid coolant into the steam stream. Steam discharges through the core outlet end into the outer shell, reverses direction, and flows into the condenser. In one embodiment, the steam conditioning device may be disposed inside the dome of the condenser except for the inlet end. The device intends to increase flow residence time to evaporate entrained carryover coolant droplets in the incoming steam before release to the condenser.
    • 一种用于将旁路蒸汽排放到蒸汽发电设备的冷凝器中的蒸汽调节系统和其它用途。 该系统包括蒸汽调节装置,其包括内部蒸发核心和外部壳体。 芯部可以由至少部分地设置在外壳内部的管状管道部分形成,在其间形成环形空间。 芯的入口端部从流体连接到上游减温减压站的管道集管接收蒸汽,其将液体冷却剂注入到蒸汽流中。 蒸汽通过芯出口端排放到外壳中,反向,并流入冷凝器。 在一个实施例中,除了入口端之外,蒸汽调节装置可以设置在冷凝器的圆顶内部。 该装置旨在增加流动停留时间,以在释放到冷凝器之前蒸发进入的蒸汽中夹带的携带冷却剂液滴。
    • 8. 发明授权
    • Series-parallel condensing system
    • 串并联冷凝系统
    • US07926555B2
    • 2011-04-19
    • US11821816
    • 2007-06-26
    • Frank David SanderlinHerman Peter Fay
    • Frank David SanderlinHerman Peter Fay
    • F28B9/02F28F27/02
    • F28B1/02F28B1/06F28B7/00F28B9/06F28B11/00
    • A series-parallel condensing system comprised of an air-cooled condenser, a surface condenser, a circulating water system and a cooling tower, body of water, or other equivalent heat sink. The cooling tower, being an evaporative device, consumes water. In the simplest embodiment of the invention steam is condensed in a two-stage series process with steam first fed to an air-cooled condenser where the majority of the steam is condensed and then to a surface condenser, which in conjunction with the circulating water system and cooling tower condenses the remaining steam. This embodiment achieves the greatest degree of water conservation. The function of the surface condenser is to replace the dephlegmator of the air-cooled condenser, which results in a significant reduction in the size and cost of the air-cooled condenser and also yields improved plant performance and operational simplicity. In a second embodiment, where additional makeup water is available, a steam bypass system is added converting the system from a series condensing process into a series-parallel process. In this arrangement steam exiting the turbine flows through both the air-cooled condenser and also through the bypass system with final condensation taking place in the surface condenser.
    • 一种串并联冷凝系统,包括空气冷却冷凝器,表面冷凝器,循环水系统和冷却塔,水体或其他等效散热器。 作为蒸发装置的冷却塔消耗水。 在本发明的最简单的实施方案中,蒸汽在两级串联方法中冷凝,蒸汽首先进料到空气冷却的冷凝器中,其中大部分蒸汽被冷凝,然后到达表面冷凝器,其结合循环水系统 并且冷却塔冷凝剩余的蒸汽。 该实施例达到最大程度的节水。 表面冷凝器的功能是取代空冷冷凝器的分凝器,这导致空冷冷凝器的尺寸和成本的显着降低,并且还产生改进的设备性能和操作简单性。 在第二实施例中,在可用附加补充水的情况下,添加蒸汽旁路系统,将系统从串联冷凝过程转换为串并联过程。 在这种布置中,离开涡轮的蒸汽流过空气冷却的冷凝器,并且还通过旁路系统,在表面冷凝器中发生最终的冷凝。
    • 10. 发明授权
    • Moisture separator reheater with thermodynamically enhanced means for
substantially eliminating condensate subcooling
    • US4206802A
    • 1980-06-10
    • US890674
    • 1978-03-27
    • William G. ReedJack S. MazerRussell L. Shade, Jr.
    • William G. ReedJack S. MazerRussell L. Shade, Jr.
    • B01D53/26F04F5/46F22B37/26F28B9/02F22G1/00F28D7/06F28F9/22
    • B01D53/26F04F5/461F22B37/266
    • A Moisture Separator Reheater (MSR) has a plurality of tube bundles which receive high-pressure saturated (tubeside) steam therein. Steam to be reheated (shellside steam) is passed in heat-exchange relationship with the tubes of the first and second reheater tube bundles after first being dried by the panels of a moisture separator. It emerges from the shell of the reheater dried and heated. In the reheater tube bundles saturated steam at temperatures and pressures substantially higher than the shellside steam transfers heat to the shellside steam by condensation within the tubes. The steam in the second stage tube bundle is at a temperature and pressure that is substantially higher than that of the steam in the first stage tube bundle and is heating shellside steam at a higher temperature than the shellside inlet steam to the first stage tube bundle. A greater quantity of tubeside steam than is theoretically necessary is passed through the tube bundles. This excess steam causes scavenging of the tube bundle to substantially eliminate condensate subcooling and related instabilities. Scavenging steam is provided to the first stage tube bundle with essentially no thermodynamic loss by passing the exhausted scavenging steam from the second stage tube bundle through a high differential pressure (.DELTA.P) thermocompressor where it is isentropically expanded. It then entrains a higher rate of exhausted scavenging steam from the first stage tube bundle. The mixed discharge from the thermocompressor is then fed to the inlet of the first stage tube bundle, resulting in a high rate of scavenging steam therein. Minimal thermodynamic loss is achieved since the first stage scavenging steam is reused to continually scavenge the first stage tube bundle, rather than being exhausted to a lower energy point in the system, as is conventionally done, as for example to a feedwater heater.