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Process and plant for drying lignite in a fluidised-bed dryer

机译:在流化床干燥机中干燥褐煤的方法和设备

摘要

In the case of known processes for drying moist bulk materials in a fluidised bed, the drier is fed from outside not only the fluidising medium but also a high-energy heating medium, whereas the vapours discharged remain unutilised. By the process according to the invention, the feeding of heating medium from outside is to be avoided, the energy balance improved and the emission of vapours reduced. For this purpose, a partial stream (15) of the vapours (10), subjected to dust separation in an electrostatic precipitator (11), is compressed into saturated steam for use as a heating medium (18) in a compressor (14), with the supply of electric energy and the injection (17) of vapour condensate (29). A second partial stream (13) serves as fluidising medium for the preheated bulk material (5) passed through the drier (6). The preheating takes place in a heat exchanger (2), which has a partial stream (3) of the vapour condensate (21) flowing through it. After phase separation in an expansion vessel (4), the vapour phase (23) of the condensate is fed to the partial stream (16). The process is suitable in particular for the drying of pit-moist lignite or of moist sewage sludge. IMAGE
机译:在用于在流化床中干燥湿的散装物料的已知方法的情况下,不仅从流化介质而且从高能加热介质向外部供给干燥机,而排出的蒸气仍然未被利用。通过根据本发明的方法,避免了从外部进给加热介质,改善了能量平衡并且减少了蒸气的排放。为此,在静电除尘器(11)中经过灰尘分离的部分蒸汽(10)(15)被压缩成饱和蒸汽,用作压缩机(14)中的加热介质(18),并提供电能和蒸汽冷凝液(29)的注入(17)。第二部分流(13)用作流经干燥器(6)的预热的散装物料(5)的流化介质。该预热在热交换器(2)中进行,该热交换器(2)具有蒸汽冷凝物(21)的一部分流(3)流过该热交换器。在膨胀容器(4)中进行相分离之后,将冷凝物的气相(23)进料至分流(16)。该方法特别适合于干燥褐煤或潮湿的污水污泥。 <图像>

著录项

  • 公开/公告号EP0273406B1

    专利类型

  • 公开/公告日1993-03-31

    原文格式PDF

  • 申请/专利权人 RHEINBRAUN AKTIENGESELLSCHAFT;

    申请/专利号EP19870119180

  • 发明设计人 KLUTZ HANS-JOACHIM DIPL.-ING.;

    申请日1987-12-24

  • 分类号F26B3/08;F26B23/00;

  • 国家 EP

  • 入库时间 2022-08-22 05:06:40

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