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Gasification processes and apparatus for the production of synthesis gas by partial oxidation of ash-containing fuels under elevated pressure and quench cooling the crude gas

机译:通过在高压下将含灰分的燃料部分氧化并骤冷来生产合成气的气化方法和设备

摘要

A method for the production of raw gas with fine dust is below 20 μm by gasification pulverised fuel containing ashes, such as bituminous coal, lignite and petroleum cokes in the free flow with a free oxygen-containing oxidizing agent by partial oxidation at pressures between the ambient pressure and 80 bar, as well as temperatures between 1.200 to 1.900 degrees, comprising the steps of pneumatic dosing for dust gasification reaction in a reactor with a cooled reactor space contour, quench cooling, crude gas washing and partial condensation, wherein:– a fuel dust with a water content of less than 10 ma% and a grain size of 200 μm is supplied to a pneumatic metering system, wherein the pulverised fuel by means of a bunker (1.1) in at least a pressure lock (1.2), and with a pressure between the ambient pressure and 80 bar with a condensate free gas is a metering vessel (1.3) is supplied, in the lower part of an inert gas (1.8.) is introduced, so that a fluidized bed with a density of from 350 to 420 kg / m3 extending through supply pipes (1.4) to the burner (2.2) of the reactor (2),– the via a conduit (1.4) the reactor (2) pulverised fuel supplied together with a free oxygen-containing oxidizing agent in the reaction chamber (2.3), with a coolant screen (2.4), is subjected to a partial oxidation, the ash of the fuel and melted together with the hot gasification gas via the drainage device (2.5) in the quenching chamber (3.1) of the quench cooler (3) is converted,– the quenching at temperatures between 180 and 260°C,– the quenched, gas pipe call for the purification of entrained fine dust having a crude gas is subjected to washing (4),– the crude gas for the removal of fine dust is 20 μm and salt in a condensation stage is about 5 to 10°C. is cooled indirectly.
机译:一种通过气化含灰分的灰烬燃料(如烟煤,褐煤和石油焦),与游离含氧氧化剂通过自由氧化,在20毫米至20微米之间的压力下自由流动的方法,生产粉尘小于20μm的原料气的方法。环境压力和80 bar,以及1.200至1.900度之间的温度,包括以下步骤:在具有冷却的反应器空间轮廓的反应器中进行气动加料以进行粉尘气化反应,骤冷,粗洗和部分冷凝,其中:将水分含量小于10 ma%且粒度小于200μm的燃料粉尘输送到气动计量系统中,其中,至少在一个压力锁(1.2)中通过仓(1.1)来粉化燃料,在环境压力和80 bar之间的压力下,在无冷凝水的情况下,向计量容器(1.3)输送惰性气体(1.8。)的下部,从而使流化床的密度为F rom 350至420 kg / m 3 穿过供应管(1.4)到达反应堆(2)的燃烧器(2.2),–通过导管(1.4)反应堆(2)粉碎的燃料在反应室(2.3)中与游离的含氧氧化剂一起供应,并带有冷却剂滤网(2.4)进行部分氧化,燃料的灰分和热的气化气体通过排水装置融化(2.5)在淬火冷却器(3)的淬火室(3.1)中进行了转换–在180至260°C的温度下进行淬火–淬火的煤气管要求净化夹带的粗粉尘进行洗涤(4),–用于去除细粉尘的粗气体小于20μm,冷凝阶段的盐大约为5至10°C。间接冷却。

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