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By means of nuclear power or fossil fuels heated gas turbine plant

机译:通过核电或化石燃料加热燃气轮机厂

摘要

1,263,124. Gas turbine plant - closed cycle type. SIEMENS A. G. April 24, 1969 [April 24, 1968], No.21111/69. Heading F1G. [Also in Division G6] The invention relates to a gas turbine plant of the closed circuit type comprising a first compressor and a second compressor, part only of the working fluid passing through the second compressor, which part is taken from the working fluid path downstream of the low-pressure side of a recuperative heat exchanger, the part being delivered after compression to re-join the remaining part of the working fluid at the high-pressure side of the heat exchanger at a point which is at a higher temperature than that at which the remaining part enters the heat exchanger. In Fig. 1 the working fluid, CO 2 , is heated in a heat exchanger 10 by heat exchange with a fluid heated in a nuclear reactor not shown, the CO 2 discharging at 300 ata and 500‹C. and passing through valves 30, 31 to a compressor-drive turbine 13 and a power turbine 14, the fluids discharging from the turbines at 57 ata and 320‹ C. being re-united and passing to the low-pressure side of a recuperative heat exchanger 19. The fluid then passes at 56 ata and 85‹ C. through a cooler 22 and thence through a compressor 16 driven by the turbine 14. The fluid then divides, the major portion (70%) passing through cooler 21, compressor 18 which is also driven by turbine 14, thence through the highpressure side 20 of the heat exchanger 19, the fluid finally discharging at 305 ata and 273‹ C. back to the working fluid heater 10. The remaining portion (30%) of the working fluid from the compressor 16 passes direct to the compressor 17 which is driven by the turbine 13, discharging therefrom at 308 ata and 190‹ C. and passing through non-return valve 32 to an intermediate point a of the high-pressure coil 20 of the heat exchanger 19. An auxiliary cooler 23 controlled by a valve 37 is provided; a by-pass valve 36 is also provided. In Fig. 2 the low-pressure working fluid discharging from the heat exchanger 19 is divided, part (70%) passing through cooler 21 to compressor 18 from which it passes to the high-pressure side 20 of the heat exchanger from which it discharges at 305 ata and 327‹ C. back to the working fluid heater 10. The remaining part (30%) of the working fluid passes through valve 35 to the compressor 17 and then passes through N R V 32 to re-unite with the 70% at intermediate point a of the high-pressure coil 20. In Fig. 3 the working fluid is heated, at relatively low-pressure directly in the nuclear reactor 11, the heated fluid passing to the lowpressure side of the heat exchanger 19 where it heats the high-pressure working fluid in coil 20, the working fluid discharging at 300 ata and 436‹ C. and dividing to pass to the two turbines 14 and 13, the fluid streams from the turbines re-uniting and passing at 120 ata and 334‹ C. to the nuclear reactor 11. The low-pressure fluid passes through the heat exchanger 19 and then divides, part (75%) passing through cooler 21 and thence at 110 ata and 40‹ C. to the compressor 16 from which it discharges at 305 ata and 73‹ C. to high-pressure coil 20 of the heat exchanger 19. The second part (25%) of the working fluid passes to the compressor 17 from which it discharges at 303 ata and 177‹ C. to an intermediate point a of the high-pressure coil 20, the re-united stream then passing to the turbines 13, 14. In Fig. 5 the working fluid is heated in a heat exchanger 121 by combustion gases from a furnace 12, the fluid at 300 ata and 500‹ C. dividing and passing to two turbines 13, 14, the exhaust streams from the turbines re-uniting at 93 ata and 364‹ C. and passing to the low-pressure side of the heat exchanger 19. The flow then divides, part (70%) passing through cooler 21 and thence through compressor 16 to the high-pressure coil 20 of the heat exchanger 19. The remaining part (30%) passes through the compressor 17 and discharges at 308 ata and 197‹ C. to re-unite with the 70% part at intermediate point a of the high-pressure coil 20. The re-united stream then passes through heater 121 and discharges therefrom at 300 ata and 500‹ C. to the turbines 13, 14. Part of the low-pressure fluid from the heat exchanger 19 is tapped off at point b and passed through air pre-heater 123, the working fluid being returned at point b of the cooler 21.
机译:1,263,124。燃气轮机厂-封闭循环型。 SIEMENS A. G. 1969年4月24日[1968年4月24日],编号21111/69。标题F1G。 [也在G6部分中]本发明涉及一种闭合回路类型的燃气轮机设备,其包括第一压缩机和第二压缩机,仅一部分工作流体通过第二压缩机,该部分从下游的工作流体路径获取。换热器的低压侧的一部分,在压缩后被输送以在温度高于该温度的点处重新结合热交换器高压侧的工作流体的其余部分。其余部分进入热交换器。在图1中,工作流体CO 2在热交换器10中通过与在未示出的核反应堆中加热的流体进行热交换而被加热,CO 2在300ata和500℃下排出。并通过阀30、31到达压缩机驱动涡轮13和动力涡轮14,从涡轮排出的流体在57 ata和320°C时重新结合,并流到回热的低压侧换热器19。然后,流体在56 ata和85°C下通过冷却器22,然后通过涡轮14驱动的压缩机16。然后流体分流,主要部分(70%)通过冷却器21和压缩机18。它也由涡轮机14驱动,然后通过热交换器19的高压侧20,流体最终在305 ata和273℃下排放回工作流体加热器10。工作的其余部分(30%)来自压缩机16的流体直接进入由涡轮机13驱动的压缩机17,该涡轮机在308 ata和190°C下从涡轮机13排出,并通过止回阀32到达高压线圈20的中间点a。热交换器19。由阀门控制的辅助冷却器23。提供了ve 37;还设置有旁通阀36。在图2中,从热交换器19排出的低压工作流体被分成一部分(70%),该部分通过冷却器21到达压缩机18,压缩机18从压缩机18流到热交换器的高压侧20,从压缩机18排出。在305 ata和327℃下返回工作流体加热器10。其余部分(30%)的工作流体通过阀35到达压缩机17,然后通过NRV 32再次与70%高压线圈20的中间点a。在图3中,工作流体在相对低压下直接在核反应堆11中被加热,加热后的流体流向热交换器19的低压侧,在此处加热该流体。盘管20中的高压工作流体,工作流体在300 ata和436 ‹C时排放,并分流到两个涡轮机14和13,来自涡轮的流体流在120 ata和334 ‹处重新结合并通过C.到达核反应堆11。低压流体通过hea t交换器19,然后将一部分(75%)通过冷却器21,然后在110 ata和40°C下分流到压缩机16,压缩机在305 ata和73°C下从压缩机16排到压缩机的高压盘管20。热交换器19。第二部分(25%)的工作流体进入压缩机17,在303 ata和177°C下从压缩机17排放到高压盘管20的中间点a然后进入涡轮机13、14。在图5中,工作流体在热交换器121中被来自炉子12的燃烧气体加热,该流体在300 ata和500°C下分流并进入两个涡轮机13、14。然后,来自涡轮的废气流在93 ata和364 ‹C时重新结合,并流至热交换器19的低压侧。然后,气流分开,一部分(70%)通过冷却器21,然后通过压缩机其余部分(30%)通过图16所示的部分通向热交换器19的高压盘管20。其余部分(30%)通过压缩机17并在308ata排出。 197℃和197℃重新结合,使高压盘管20的中间点a处70%的部分重新结合。然后,重新结合的物流通过加热器121,并以300ata和500℃从加热器121排放到涡轮机中。参照图13,图14,来自热交换器19的一部分低压流体在b点被抽出并通过空气预热器123,工作流体在冷却器21的b点被返回。

著录项

  • 公开/公告号DE1751226B2

    专利类型

  • 公开/公告日1973-02-15

    原文格式PDF

  • 申请/专利权人

    申请/专利号DE19681751226

  • 发明设计人

    申请日1968-04-24

  • 分类号F02C1/04;

  • 国家 DE

  • 入库时间 2022-08-23 07:11:27

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