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    • 53. 发明授权
    • Multistage pressure condenser and steam turbine plant having the same
    • 多级压力冷凝器和蒸汽轮机厂有相同的
    • US09488416B2
    • 2016-11-08
    • US13684916
    • 2012-11-26
    • Mitsubishi Heavy Industries, Ltd.
    • Issaku FujitaJiro KasaharaSeiho Utsumi
    • F28B1/00F28B1/02F28B7/00F01K9/00F28B9/08
    • F28B1/00F01K9/003F28B1/02F28B7/00F28B9/08
    • A multistage pressure condenser includes, a high pressure chamber and a low pressure chamber, a pressure partition wall which partitions an inner portion of the low pressure chamber to an upper portion and a lower portion, a cooling pipe group which condenses low pressure side steam to low pressure side condensate, a reheat chamber positioned in the lower portion of the low pressure chamber and in which the low pressure side condensate which flows down through the porous plate is stored, high pressure side steam introduction portion for introducing high pressure side steam in the high pressure chamber to the reheat chamber, liquid-film forming portion which guides the low pressure side condensate which flows down through the porous plate to the reheat chamber while dispersing the low pressure side condensate on a surface, and air feeder for promoting the flow of the high pressure side steam.
    • 多级压力冷凝器包括高压室和低压室,将低压室的内部分隔成上部和下部的压力分隔壁,将低压侧蒸汽冷凝至 低压侧冷凝物,位于低压室下部的再热室,其中存储有向下流过多孔板的低压侧冷凝物,高压侧蒸汽引入部,用于将高压侧蒸汽导入 向再热室施加高压室,将低压侧冷凝物向下流过多孔板的低压侧冷凝物引导至再热室,将低压侧冷凝物分散在表面上的液膜形成部, 高压侧蒸汽。
    • 54. 发明授权
    • Condenser
    • 冷凝器
    • US08833744B2
    • 2014-09-16
    • US13719346
    • 2012-12-19
    • Akira NemotoNaoki SugitaniYoshio Mochida
    • Akira NemotoNaoki SugitaniYoshio Mochida
    • B01F3/04F28B1/02F28B7/00F28F1/00F28B9/08
    • F28F1/00F28B1/02F28B7/00F28B9/08Y10S165/192Y10S261/10
    • A condenser includes a high pressure side condenser, a high pressure side cooling tube bank, a high pressure side hot well, a low pressure side condenser, a low pressure side cooling tube bank, a pressure shroud provided inside the low pressure side condenser, a low pressure side hot well, high pressure steam introducing portion, low pressure side condensate introducing portion, a flash box which communicates with at least one of the high pressure side hot well and the low pressure side hot well, flashes a heater drain from a feed water heater, and urges at least one of the high pressure side hot well and the low pressure side hot well to recover the flashed heater drain, and a flash steam path which introduces flash steam generated inside the flash box into at least one of the high pressure side hot well and the low pressure side hot well.
    • 冷凝器包括高压侧冷凝器,高压侧冷却管堤,高压侧热井,低压侧冷凝器,低压侧冷却管堤,设置在低压侧冷凝器内的压力罩, 低压侧热井,高压蒸汽引入部分,低压侧冷凝物引入部分,与高压侧热井和低压侧热井中的至少一个连通的闪光箱,从进料中闪烁加热器排水 并且促使高压侧热井和低压侧热井中的至少一个回收闪蒸的加热器排水口,并且将闪蒸箱内产生的闪蒸蒸汽引入至少一个高温的闪蒸蒸汽路径 压力侧热井和低压侧热井。
    • 55. 发明申请
    • MULTISTAGE PRESSURE CONDENSER AND STEAM TURBINE PLANT HAVING THE SAME
    • 多级压力冷凝器和蒸汽涡轮机厂
    • US20130167536A1
    • 2013-07-04
    • US13684916
    • 2012-11-26
    • Mitsubishi Heavy Industries, Ltd.
    • Issaku FUJITAJiro KASAHARASeiho UTSUMI
    • F28B1/00F01K9/00
    • F28B1/00F01K9/003F28B1/02F28B7/00F28B9/08
    • A multistage pressure condenser includes, a high pressure chamber and a low pressure chamber, a pressure partition wall which partitions an inner portion of the low pressure chamber to an upper portion and a lower portion, a cooling pipe group which condenses low pressure side steam to low pressure side condensate, a reheat chamber positioned in the lower portion of the low pressure chamber and in which the low pressure side condensate which flows down through the porous plate is stored, high pressure side steam introduction portion for introducing high pressure side steam in the high pressure chamber to the reheat chamber, liquid-film forming portion which guides the low pressure side condensate which flows down through the porous plate to the reheat chamber while dispersing the low pressure side condensate on a surface, and air feeder for promoting the flow of the high pressure side steam.
    • 多级压力冷凝器包括高压室和低压室,将低压室的内部分隔成上部和下部的压力分隔壁,将低压侧蒸汽冷凝至 低压侧冷凝物,位于低压室下部的再热室,其中存储有向下流过多孔板的低压侧冷凝物,高压侧蒸汽引入部,用于将高压侧蒸汽导入 向再热室施加高压室,将低压侧冷凝物向下流过多孔板的低压侧冷凝物引导至再热室,将低压侧冷凝物分散在表面上的液膜形成部, 高压侧蒸汽。
    • 57. 发明申请
    • Combined cycle power plant with auxiliary air-cooled condenser
    • 具有辅助风冷冷凝器的联合循环发电厂
    • US20060123767A1
    • 2006-06-15
    • US11012953
    • 2004-12-14
    • Michael Briesch
    • Michael Briesch
    • F02C6/18
    • F01K23/10F01K9/00F28B1/06F28B7/00Y02E20/16
    • A combined cycle power plant (20) including a main air-cooled condenser (22) condensing steam at a first pressure and an auxiliary air-cooled condenser (24) condensing steam at a second pressure higher than the first pressure. Designing an air-cooled combined cycle power plant for startup on a hot day can significantly increase the size and cost of the required air-cooled condenser. Adding an auxiliary air-cooled condenser having appropriate thermal characteristics relative to a main air cooled compressor to the steam bypass circuit of an air-cooled combined cycle power plant enables the plant to meet plant startup requirements during periods of peak thermal load in a more cost effective manner than would be achievable with the main air cooled condenser alone.
    • 一种联合循环发电厂(20),其包括在第一压力下冷凝蒸汽的主空气冷凝器(22)和在高于第一压力的第二压力下冷凝蒸汽的辅助空气冷却冷凝器(24)。 设计一个风冷的联合循环发电厂在炎热的一天启动可以显着增加所需的空冷冷凝器的尺寸和成本。 将相对于主空气冷却压缩机具有适当热特性的辅助风冷式冷凝器加入到空气冷却联合循环发电厂的蒸汽旁路回路中,使得该工厂能够在更高成本的峰值热负荷期间满足工厂启动要求 有效的方式比单独使用主要的空气冷却冷凝器可以实现。
    • 58. 发明授权
    • Apparatus for removing pollutants from stack effluents
    • US3766971A
    • 1973-10-23
    • US3766971D
    • 1971-05-13
    • BAUM E
    • BAUM E
    • B01D51/10F28B1/00F28B7/00F28B11/00F28B3/00
    • F28B1/00B01D51/10F28B7/00F28B11/00
    • A series of controlled gradient condensers for removing gaseous hydrocarbon pollutants from the stack effluent of an industrial treating plant, such as a veneer dryer. The gaseous effluent stream is conducted from the industrial treating plant to a precooler to bring the effluent temperature to the condensation point of the highest boiling pollutant. Thereafter the effluent stream is passed through a successive series of controlled gradient condenser, each operating in a temperature range lower than that of the immediately preceding condenser. The first several condensers are air cooled and designed to remove the higher boiling pollutants. Each air cooled condenser is wrapped with one or more heater coils, the turns of which are not uniformly wound about the condenser tubes but are more widely spaced toward the outlet or cold end of the condenser. Electric power to each heater coil is controlled by a respective power controller responsive to temperature sensors located inside the condenser for measuring a temperature gradient along the path of flow of the effluent. If any measured temperature gradient exceeds a predetermined maximum allowable limit, the power controller adjusts the electric power through the appropriate heater coil to restore the temperature gradient, and thus the cooling rate, to a value below the maximum limit. As long as the predetermined maximum temperature gradient or cooling rate for each gaseous pollutant is not exceeded the formation of aerosol is avoided and substantially all of the pollutant condenses in collectable liquid form on the walls of the condenser, thereby cleansing the effluent. Each condenser has a reservoir which collects the condensed pollutants by gravity feed, while the uncondensed remaining effluent passes to the next succeeding condenser. The last in the series of condensers is water cooled for condensing those pollutants having the lowest boiling points. The temperature gradient in the water cooled condenser is controlled by temperature sensors, similar to those in the air cooled condensers, which modulate the flow of coolant by controlling the power to the coolant pump. The different temperature ranges at which the respective condensers operate are preferably fixed so that the minimum temperature at the outlet of a respective condenser is greater than the highest melting point of any pollutant condensed within that condenser, so as to prevent solidification of the pollutants and fouling of the condensers. Immersion heaters in the condenser reservoirs further aid in preventing solidification. If solidification of one or more pollutants collected in a particular condenser cannot be avoided, scraper paddles are provided to scrape the solid material off the condenser walls for disposal through a solids removal port. The reservoir of the last in the series of condensers, from which the remaining effluent is vented to the atmosphere, includes a reservoir auxiliary cooling system for the purpose of further reducing effluent temperature if necessary to remove any remaining contaminants.