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1. 发明申请

WO2017082847A1 PLASMA GASIFICATION REACTOR AND METHOD 审中-公开
标题翻译：等离子体气化反应器和方法
公开(公告)号：WO2017082847A1
公开(公告)日：2017-05-18
申请号：PCT/TR2016/050434
申请日：2016-11-11
申请人： KOYUN, Ahmet , YAYALIK, Ibrahim
发明人： KOYUN, Ahmet , YAYALIK, Ibrahim
IPC分类号： C10J3/08 , C10J3/72 , C10J3/57
CPC分类号： C10J3/08 , C10J3/57 , C10J3/723 , C10J2300/1238
摘要： The invention is related to a reactor (1) comprising at least one temperature unit (20) which provides high temperature, at least one waste inlet (11) from which the fuel and/or wastes are fed to the reactor (1), at least one reactant inlet (13 and/or 14 and/or 17), at least one melt outlet (15) which provides exiting of the melts formed by inorganic substances coming from the fuel and/or wastes via heat, at least one high temperature region (12) where endothermic reactions occur and a gas outlet (16) which provides that the fuel and/or wastes entering to the reactor (1) are directed to the high temperature region (12) such that the gasification does not start before they enter to this region (12) and therefore, where the gases leaving the reactor (1) as a result of the reaction exit from the reactor (1) by passing through the high temperature region (12) and which has a different openness from the waste inlet (11); having a high temperature region (12) positioned between the waste inlet (11) and gas outlet (16), and body (10) which has a form providing that the wastes pass through the high temperature region (12) such that the gasification does not start before the fuel and/or wastes entering to the reactor (1) enter to the high temperature region (12) and therefore, that the gases having at least 1200°C temperature exit from the reactor (1) and to the working method (100) of this reactor (1).
摘要翻译：本发明涉及包括至少一个提供高温的温度单元（20）的反应器（1），至少一个废物入口（11），供给燃料和/或废物的废物入口（11）（1）至少一个反应物入口（13和/或14和/或17），至少一个熔体出口（15），其提供由来自燃料和/或废物的无机物质形成的熔体通过热量使至少一个发生吸热反应的高温区域（12）和提供进入反应器（1）的燃料和/或废物导向高温区域（12）的气体出口（16）在进入该区域（12）之前气化没有开始，因此由于反应而离开反应器（1）的气体通过高温区域（12）从反应器（1）排出，并且具有与废物入口（11）不同的开放性; 具有位于废物入口（11）和气体出口（16）之间的高温区域（12）和具有提供废物通过高温区域（12）的形式的主体（10），使得气化确实在进入反应器（1）的燃料和/或废物进入高温区域（12）并且因此从反应器（1）出来并具有至少1200℃温度的气体和工作方法（100）（1）。

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