首页> 外国专利> Operation of a circulating fluidised bed boiler system - recovering heat at different loads by maintaining large enough flow of solid material in heat exchanger chamber

Operation of a circulating fluidised bed boiler system - recovering heat at different loads by maintaining large enough flow of solid material in heat exchanger chamber

机译:循环流化床锅炉系统的运行-通过在热交换器室内保持足够大的固体物料流量来回收不同负荷的热量

摘要

Improved method of operating a circulating fluidised bed (CFB) system including a heat exchanger chamber formed in the lower part of the return duct, having one wall section in common with the combustion chamber, comprises (a) establishing a fast fluidised bed of solid particles in the combustion chamber so that a particle suspension of flue gases and solid particles entrained therein is caused to flow upwardly in the combustion chamber and be discharged through the discharge opening; (b) sepg. solid particles from the particle suspension; (c) directing sepd. solid particles into a return duct having a heat exchange chamber in its lower portion; (d) establishing a bed of solid particles in the heat exchanger chamber; (e) reintroducing solid particles from the heat exchanger chamber into the combustion chamber through the solid particle inlet in the common wall section; and (f) introducing additional solid particles directly from the combustion chamber into the lower part of the return duct; such that (g) during high load conditions a large solid particle flow is entrained with the flue gases and recycled through the separator, return duct and heat exchanger chamber into the combustion chamber, providing the desired heat transfer capacity; whilst (h) during low load conditions solid particles are caused to flow directly from the combustion chamber into the heat exchanger chamber through a passage in the common wall between them, the direct solid flow enhancing the heat transfer capacity so that it achieves the desired level. Also claimed is a CFB reactor system.
机译:一种改进的操作循环流化床(CFB)系统的方法,该系统包括在回流管下部形成的热交换器室,该室具有与燃烧室共用的一个壁段,​​该方法包括(a)建立固体颗粒的快速流化床在燃烧室内,使烟道气和夹带在其中的固体颗粒的颗粒悬浮液在燃烧室内向上流动,并通过排出口排出。 (b)隔。来自颗粒悬浮液的固体颗粒; (c)指导sepd。固体颗粒进入返回管,该返回管的下部具有热交换室。 (d)在热交换器室中建立固体颗粒床; (e)通过公共壁部分中的固体颗粒入口将固体颗粒从热交换器室重新引入燃烧室; (f)将额外的固体颗粒直接从燃烧室引入回流管的下部; (g)在高负荷条件下,大量固体颗粒流被烟道气夹带,并通过分离器,回流管和热交换器室循环到燃烧室,从而提供所需的传热能力; (h)在低负荷条件下,固体颗粒通过燃烧室中共同壁上的通道直接从燃烧室流入热交换器室,直接固体流增强了传热能力,从而达到了所需的水平。还要求保护的是CFB反应器系统。

著录项

  • 公开/公告号FI109935B

    专利类型

  • 公开/公告日2002-10-31

    原文格式PDF

  • 申请/专利权人 FOSTER WHEELER ENERGIA OY;

    申请/专利号FI19950002155

  • 发明设计人 HYPPAENENTIMO;

    申请日1995-05-05

  • 分类号F23C10/10;

  • 国家 FI

  • 入库时间 2022-08-22 00:45:27

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