首页> 外国专利> APPARATUS FOR SALT SEPARATION UNDER SUPERCRITICAL WATER CONDITIONS

APPARATUS FOR SALT SEPARATION UNDER SUPERCRITICAL WATER CONDITIONS

机译:在超临界水条件下分离盐的装置

摘要

Apparatus for salt separation (2) under supercritical water conditions, comprising a heat exchanger (4) and a fluidized bed reactor (6). The fluidized bed reactor comprising a supercritical water pressure containing wall (8) defining therein a fluidized bed chamber (10) connected to an inlet system (16) at one end thereof and an outlet system (18) configured to separate solids from supercritical fluid at another end thereof. The fluidized bed chamber receives a fluidized bed (12) therein and is configured to receive through the inlet system (16) a liquefied aqueous substance (14) for treatment in the fluidized bed chamber. The inlet system (16) comprises an inlet chamber (20) and a fluidization plate (22) positioned between the inlet chamber (20) and the fluidized bed chamber (10). The fluidized bed chamber extends between the inlet system (16) and outlet system (18) and comprises an entry section (10a) adjacent the inlet system (16), an outlet section (10c) adjacent the outlet system (18), and a mid-section (10b) extending between the entry section and the outlet section. The heat exchanger (4) extends along the fluidized bed chamber (10) and is configured to generate a decreasing temperature gradient in the fluidized bed chamber from the outlet section (10c) to the entry section (10a), the temperature gradient in the outlet section and mid-section being supercritical for aqueous substances and being subcritical for aqueous substances in the entry section (10a) adjacent the fluidization plate (22).
机译:用于在超临界水条件下分离盐的装置( 2 ),包括热交换器( 4 )和流化床反应器( 6 )。该流化床反应器包括超临界水压壁( 8 ),该壁在其中限定了与入口系统( 16 )连接的流化床室( 10 )。 >)在其一端,出口系统( 18 )在其另一端用于将固体与超临界流体分离。流化床腔室在其中接收流化床( 12 ),并配置为通过进口系统( 16 )接收液化的含水物质( 14 >)在流化床室中进行处理。进气系统( 16 )包括进气室( 20 )和位于进气室()之间的流化板( 22 ) 20 )和流化床室( 10 )。流化床室在入口系统( 16 )和出口系统( 18 )之间延伸,并包括入口部分( 10 a) )靠近入口系统( 16 ),出口部分( 10 c )靠近出口系统( 18 ),以及在入口部分和出口部分之间延伸的中间部分( 10 b )。热交换器( 4 )沿流化床室( 10 )延伸,并配置为在流化床室中从出口部分( 10 c )到入口部分( 10 a ),出口部分和中间部分的温度梯度为在流化板( 22 )附近的入口段( 10 a )中,对于含水物质而言是超临界的,对于含水物质而言是亚临界的。

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