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    • 5. 发明申请
    • METHOD AND APPARATUS FOR SAFETY OPERATION OF EXTRACTION STEAM TURBINE UTILIZED FOR POWER GENERATION PLANT
    • 用于发电厂的提取蒸汽轮机的安全运行方法和装置
    • US20140373541A1
    • 2014-12-25
    • US14478648
    • 2014-09-05
    • FUJI ELECTRIC CO., LTD.
    • Yoshifumi KATO
    • F01D17/08F01K13/02F01K7/18F01D17/10
    • F01D17/08F01D17/10F01D17/145F01D21/14F01K7/04F01K7/18F01K13/02F05D2220/31F05D2270/301
    • A safety operation method includes detecting a steam pressure inside a high-pressure casing of the high-pressure part and a steam pressure inside a low-pressure casing of the low-pressure part; obtaining a low-pressure casing limit pressure as a reference corresponding to a pressure of the high-pressure casing in each detection, on a basis of a pressure correlation line expressing a prescribed special relation between preset high-pressure casing pressure and low-pressure casing pressure of the extraction steam turbine; comparing the low-pressure casing limit pressure with the detected pressure of the low-pressure casing; and forcibly throttling an opening of the main steam control valve to reduce the flow rate of steam flowing into the high-pressure part, in a state in which the extraction control valves continue controlling an operation of the extraction steam pressure, when the detected pressure of the low-pressure casing is judged to be higher than the low-pressure casing limit pressure.
    • 一种安全操作方法,包括检测高压部分的高压壳体内的蒸汽压力和低压部件的低压壳体内的蒸汽压力; 基于表示规定的预设高压套管压力和低压套管的特殊关系的压力相关线,在每次检测中获得低压套管极限压力作为对应于高压套管的压力的基准 抽汽汽轮机的压力; 将低压套管极限压力与低压套管的检测压力进行比较; 并且当检测到的压力达到检测压力时,在抽出控制阀继续控制提取蒸汽压力的操作的状态下,强制地节流主蒸汽控制阀的开口,以减少流入高压部分的蒸汽的流量 低压套管被判断为比低压套管极限压力高。
    • 6. 发明授权
    • Apparatus and method of geothermal energy conversion
    • 地热能转换装置与方法
    • US4138851A
    • 1979-02-13
    • US820984
    • 1977-08-01
    • Alfred N. RogersLeon Awerbuch
    • Alfred N. RogersLeon Awerbuch
    • F01K7/18F01K17/04F03G7/04F03G7/00
    • F01K7/18F01K17/04F03G7/04Y02E10/10Y10S203/17Y10S203/21
    • A system using a number of flash chambers for converting the heat energy of geothermal brine to useful work. The system uses steam from flashed brine to vaporize a portion of distilled water or distillate in one or more heat exchangers to produce steam to drive a turbine which, in turn, operates a generator or the like to produce useful work. Before the distillate reaches the heat exchanger, it is preheated as it flows through a series of flash chambers in countercurrent relationship to the flow of geothermal brine therethrough. The brine flashes in each flash chamber and the flashed vapor mixes with the distillate flowing through the flash chamber to pre-heat the distillate. The heat energy of the unvaporized part of the distillate in the heat exchanger can form additional steam which is also supplied to the turbine. The heat content of the unflashed part of the distillate can be used in several ways to heat a working fluid in a closed loop containing a second turbine. The unflashed distillate can either be directed through a second heat exchanger which also receives a second working fluid so as to heat the latter, or the unflashed distillate can be flashed and the flashed vapor is placed in heat exchange relationship to the working fluid. Condensate formed in the latter case can be used as fresh product water. Inorganic salts from the brine can also be derived from the system.
    • 一种使用多个闪蒸室将系统的地热盐水热能转化为有用功的系统。 该系统使用来自闪蒸盐水的蒸汽蒸发一个或多个热交换器中的蒸馏水或馏出物的一部分,以产生蒸汽来驱动涡轮,其又运行发电机等以产生有用的工作。 在馏出物到达热交换器之前,当其与通过其中的地热盐水的流动呈逆流关系时,它被预热。 卤水在每个闪光室中闪烁,闪蒸的蒸气与流过闪蒸室的馏出物混合,以预热蒸馏物。 热交换器中馏出物的未蒸发部分的热能可以形成额外的蒸汽,其也被供应到涡轮机。 馏出物的未燃烧部分的热含量可以以多种方式用于加热含有第二涡轮机的闭合回路中的工作流体。 未燃烧的馏出物可以被引导通过第二热交换器,其也接收第二工作流体以加热后者,或者未闪蒸的馏出物可以被闪蒸并且闪蒸的蒸汽与工作流体成热交换关系。 在后一种情况下形成的冷凝水可用作新鲜水产品。 盐水中的无机盐也可以从系统中得到。
    • 10. 发明授权
    • Method and plant for co-generation of heat and power
    • US10233789B2
    • 2019-03-19
    • US15034097
    • 2014-10-31
    • SASOL TECHNOLOGY PROPRIETARY LIMITED
    • Franco GaspariniRian WesselsCorné Welgemoed
    • F01K23/10F02C6/18F22B1/18F22G5/12F01K7/18F01K13/02F01K17/02F01K23/06
    • A method of operating a combined heat and power plant (10) (CHP plant) includes generating hot flue gas and cooling the hot flue gas in a sequence of cooling steps to recover heat and to generate steam in a heat recovery steam generator (16) (HRSG). The HRSG (16) includes an LP steam evaporator (36) designed to generate steam at least over a pressure range of from 2 bar(g) to 18 bar(g) so that either LP steam or MP steam can selectively be generated by the LP steam generator (36), thereby to cool the hot flue gas, and an MP steam superheater (24) upstream of the LP steam evaporator (36) to superheat MP steam in heat exchange with the hot flue gas thereby to cool the hot flue gas. The method further includes, when no or insufficient MP steam is being imported to the MP steam superheater (24) to ensure safe operation of the MP steam superheater, and/or when a demand exists for exporting MP steam which cannot be satisfied by imported MP steam superheated in the MP steam superheater (24), and/or when a demand exists for MP steam in the CHP plant which cannot be satisfied by imported MP steam, operating the LP steam evaporator (36) at an operating pressure in the range of between 8 bar(g) and 18 bar(g) to generate MP steam to wet the MP steam superheater (24) and/or to satisfy at least to some extent said demand for MP steam, and thereafter, when sufficient MP steam is being imported to the MP steam superheater (24) from external of the CHP plant (10) to ensure safe operation of the MP steam superheater (24), and/or when any demand for exported MP steam is satisfied by imported MP steam which is superheated in the MP steam superheater (24) and then exported, and/or when there is no more demand for exporting of MP steam, and/or when the demand for MP steam in the CHP plant (10) is being satisfied at least to some extent by imported MP steam, reducing the operating pressure of the LP steam evaporator (36) to a pressure in the range of between 2 bar(g) and 8 bar(g) thereby to generate LP steam.