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METHOD FOR OPERATION OF A STEAM TURBINE INSTALLATION, AND ALSO A DEVICE FOR PRODUCING STEAM FROM LOCAL COAL

机译:汽轮机安装的操作方法,以及一种从地方煤矿生产蒸汽的装置

摘要

1. The method of operation of a steam turbine installation with at least one brown coal heated steam boiler, in which brown coal is dried, preferably indirectly dried in a fluidized bed dryer, which is at least partially heated by steam from the steam-water mixture circulation loop of the steam boiler, the gas from the steam boiler is subjected to absorption cleaning to separate the CO, and the energy necessary for absorption cleaning is taken at least partially from the drying process. 2. The method according to claim 1, characterized in that the residual heat of at least a portion of the secondary steam formed during the drying of brown coal is used to regenerate the saturated CO solvent. A method according to one of claims 1 or 2, characterized in that at least one condensing heat exchanger is used to regenerate a saturated CO solvent, into which at least part of the secondary steam stream from the drying process is supplied. The method according to claim 3, characterized in that the secondary steam supplied to the condensing heat exchanger is compressed to a pressure of 3 to 5 bar, preferably to a pressure of 4 bar (absolute). The method according to claim 4, characterized in that the compression of the secondary steam is carried out using low pressure steam from the steam-water mixture circulation loop of the steam production process. The method according to one of claims 1, 2, 4 or 5, characterized in that a part of the energy necessary for the regeneration of the solvent is selected in the form of low pressure steam from the circulation circuit of the steam-water mixture in a steam turbine. The method according to claim 3, characterized in that part of the energy necessary for the regeneration of the solvent is taken in the form of low-pressure steam from the
机译:1.一种具有至少一个褐煤加热的蒸汽锅炉的汽轮机设备的操作方法,其中褐煤被干燥,优选在流化床干燥器中间接干燥,该流化床干燥器至少部分地被来自蒸汽水中的蒸汽加热蒸汽锅炉的混合循环回路,将蒸汽锅炉的气体进行吸收净化以分离出CO,吸收净化所需的能量至少部分来自干燥过程。 2.根据权利要求1所述的方法,其特征在于,在褐煤干燥期间形成的二次蒸汽的至少一部分的剩余热量用于再生饱和CO溶剂。 3.根据权利要求1或2中的一项所述的方法,其特征在于,至少一个冷凝热交换器用于再生饱和的CO溶剂,来自干燥过程的至少一部分二次蒸汽流被供应到所述饱和的CO溶剂中。 4.根据权利要求3所述的方法,其特征在于,供应到所述冷凝热交换器的二次蒸汽被压缩至3至5巴的压力,优选地被压缩至4巴的压力(绝对)。 5.根据权利要求4所述的方法,其特征在于,使用来自所述蒸汽生产过程的蒸汽-水混合物循环回路的低压蒸汽来压缩所述次级蒸汽。 6.根据权利要求1、2、4或5中的一项所述的方法,其特征在于,从所述蒸汽-水混合物的循环回路中以低压蒸汽的形式选择用于溶剂再生的能量的一部分。蒸汽轮机。 4.根据权利要求3所述的方法,其特征在于,所述溶剂的再生所必需的能量的一部分以来自所述塔的低压蒸汽的形式获得。

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