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Improvements in or relating to the regulation of reheat steam temperatures in boilers

机译:改进或有关调节锅炉再热蒸汽温度

摘要

1,049,280. Regulating steam temperatures. SULZER BROS Ltd. Oct. 29, 1965 [Oct. 29, 1964], No. 45931/65. Heading F4A. The temperature of reheated steam entering a low pressure turbine 19 is controlled by varying the heat exchange between the reheat steam and live steam on its way to a high pressure turbine 12, in a coaxial tube heat exchanger 11 situated in the flue of the boiler. Water from pump 1 is fed through the economizer 3 and evaporator 5 of once-through force flow, force flow or natural circulation boiler 2. The high pressure steam produced is separated from any water in trap 7, and then passed through superheater surface 9 to tube 10, from whence the flow splits into two parts, part flowing through inner tube 20 of coaxial tube heat exchanger 11 to give up heat to reheat steam passing in co-current flow through outer tube 21, and then flowing to tube 14, via superheater surface 13, while the remainder flows directly to tube 14 .through by-pass line 22. From tube 14 the recombined high pressure flow passes through superheater surface 15 to high pressure turbine; 12. The partly expanded steam from high pressure turbine 12 flows for reheating through outer tube 21 of the heat exchanger 11 and through reheat superheater surface 17 on its way to low pressure turbine 19. The temperature of the reheat steam at the inlet to turbine 19 is maintained constant by varying the high pressure steam flow through the by-pass 22 by valve means 23, and by injecting cooling water into the pipe 10, under the action of controller 25 actuated by temperature detector 24. The high pressure steam temperature at the inlet to turbine 12 is maintained constant by injecting water into pipe 14 under the action of controller 31, actuated by temperature detector 30. In modifications the by-passed superheater surface 13 may be situated before the coaxial tube heat exchanger 11, and the water injection into tube 10 may occur after the branching off of by-pass line 22 (Fig. 2, not shown).
机译:1,049,280。调节蒸汽温度。 SULZER BROS Ltd.,1965年10月29日[Oct. 1964年第29期],第45931/65号。标题F4A。在位于锅炉烟道中的同轴管式换热器11中,通过改变再热蒸汽与新鲜蒸汽之间的热交换来控制进入低压涡轮19的再热蒸汽的温度,该热交换在进入高压涡轮12的途中。来自泵1的水通过一次性力流,力流或自然循环锅炉2的节能器3和蒸发器5进料。产生的高压蒸汽与疏水阀7中的所有水分离,然后通过过热器表面9输送至管道10从那里分成两部分,一部分流过同轴管式热交换器11的内管20以散发热量,以重新加热并流通过外管21的蒸汽,然后流经管道14过热器表面13,而其余部分则通过旁路管线22直接流到管子14。重新组合的高压流从过热器表面15穿过过热器表面15到达高压涡轮机。 12.来自高压涡轮机12的部分膨胀的蒸汽流经热交换器11的外管21并通过再加热过热器表面17以在通往低压涡轮机19的途中进行再加热。在涡轮机19的入口处的再加热蒸汽的温度。在由温度检测器24致动的控制器25的作用下,通过阀装置23改变通过旁路22的高压蒸汽流量,并向管道10中注入冷却水,使蒸汽保持恒定。通过在温度检测器30的控制下,在控制器31的作用下将水注入管道14,可将涡轮机12的入口保持恒定。在改进方案中,旁路过热器表面13可以位于同轴管式热交换器11之前,并且注水进入旁通管22(图2,未显示)后,可能会进入管10。

著录项

  • 公开/公告号GB1049280A

    专利类型

  • 公开/公告日1966-11-23

    原文格式PDF

  • 申请/专利权人 SULZER BROTHERS LIMITED;

    申请/专利号GB19650045931

  • 发明设计人

    申请日1965-10-29

  • 分类号F22G5/20;

  • 国家 GB

  • 入库时间 2022-08-23 13:57:08

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