首页> 外国专利> AN APPARATUS FOR DEASHING COAL BY DRY BENEFICATION USING A CIRCULATING FLUIDIZED BED LOOP

AN APPARATUS FOR DEASHING COAL BY DRY BENEFICATION USING A CIRCULATING FLUIDIZED BED LOOP

机译:用循环流化床干法脱硫对煤进行脱色的装置

摘要

Thus the main object of the present invention is to provide a method of deashing of coal fines (- 1mm) using circulating fluidized bed. Gas-solid fluidization plays a central role in many chemical processes, metallurgical and energy conversion processes. Passing a gas through a bed of solids forms a gas-solid fluidized bed. When this happens, the bed of solids takes on certain fluid-like characteristics. From a chemical processing point of view, the fluidized bed is an excellent way of contacting gaseous reactants with catalyst particles in a heterogeneous gas phase reaction. For the purpose of the present invention, the mixing and segregation pattern in circulating fluidized beds consisting of fine particles and coarse particles having different density, size distributions and terminal settling velocity were investigated using a 0.1016 m ID and 5.62 m height riser of circulating fluidized bed system. Attention is focused on understanding the interaction and mechanism between the particles and the conditions in which complete mixing or segregation is possible in circulating fluidized beds. Effort is made to find out the extent of ash from coal in the circulating fluidized bed at a typical gas velocity and solids circulation rate. Coal comprises lighter organic carbonaceous materials and heavier inorganic inert material leaving behind on ignition what is called commonly as ash. On fluidization heavier inert materials comprising heavier minerals segregates and less lighter material moves up at the top resulting in the benefication process. In the present invention the circulating fluidized bed system uses a blower for blowing air into two air lines, a fast bed column and a slow bed column for keeping the bed respectively in a fluidized condition and a minimum fluidized condition. A cyclone separator is provided at the end of the slow bed column for feeding the solids carried over form the fast bed to be separated by the cyclone separator and collected at its exit end. The heavier separated particles fall back to the slow bed column and transferred to the fast bed column via a solid transfer line for recycling. The present invention thus provides an apparatus for deashing coal by dry benefication, using a circulating fluidized bed loop comprises a fast bed column and a slow bed column, each having a bed of solids and provided with a distributor for blowing in air from a rotary air blower; a cyclone separator provided at the distal end of said slow bed column for receiving and for getting the solid separated from solid fines; and a solid transfer line provided for circulating solids from said slow bed column to said fast bed column for recycling the separated solids.
机译:因此,本发明的主要目的是提供一种使用循环流化床脱灰煤屑(-1mm)的方法。气固流化在许多化学过程,冶金和能量转换过程中起着核心作用。使气体通过固体床形成气固流化床。发生这种情况时,固体床具有某些类似流体的特性。从化学加工的观点来看,流化床是在非均相气相反应中使气态反应物与催化剂颗粒接触的极佳方法。为了本发明的目的,使用0.1016m ID和5.62m高的上升流化床研究了由具有不同密度,尺寸分布和最终沉降速度的细颗粒和粗颗粒组成的循环流化床中的混合和分离模式。系统。注意力集中在理解颗粒与循环流化床中可能完全混合或分离的条件之间的相互作用和机理。努力找出在典型的气体速度和固体循环速率下循环流化床中煤中灰分的程度。煤包含较轻的有机碳质材料和较重的无机惰性材料,这些物质通常在燃烧时会留下灰烬。在流化过程中,包含较重矿物的较重惰性材料会分离,而较轻质的材料会在顶部向上移动,从而导致选矿过程。在本发明中,循环流化床系统使用鼓风机将空气吹入两条空气管线,快速床塔和慢速床塔分别将床保持在流化状态和最小流化状态。在慢床塔的端部设有旋风分离器,用于输送从快速床带走的固体,该固体被旋风分离器分离并在其出口端收集。较重的分离出的颗粒落回到慢床塔中,并通过固体传输线转移到快速床塔中进行回收。因此,本发明提供了一种使用干法选矿脱灰煤的设备,该设备使用了循环流化床回路,该循环流化床回路包括快速床塔和慢速床塔,每个均具有固体床,并设有用于从旋转空气吹入空气的分配器。鼓风机设置在所述慢床塔的远端的旋风分离器,用于接收固体和从固体细粉中分离出固体。固体输送管线用于将固体从所述慢床塔循环到所述快速床塔以回收分离的固体。

著录项

  • 公开/公告号IN2006KO00101A

    专利类型

  • 公开/公告日2009-06-19

    原文格式PDF

  • 申请/专利权人

    申请/专利号IN101/KOL/2006

  • 申请日2006-02-01

  • 分类号C10L1/32;B01J8/00;

  • 国家 IN

  • 入库时间 2022-08-21 19:27:26

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号