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GASIFICATION REACTOR AND METHOD FOR ENTRAINED-FLOW GASIFICATION.

机译:气化反应器和气流床气化方法。

摘要

The invention relates to a method and a device for obtaining synthesis gas by the gasification of liquid or finely comminuted, solid fuels at a pressure of 0.3 to 8 Mpa at a temperature in the range of 1200 to 2000°C with oxygen-containing, gaseous gasification agents in a cooled reactor (3), wherein liquid slag is deposited on the walls thereof. The reactor is located in a first pressure container. The obtained synthesis gas is generated in a first reaction chamber (2), arranged at the top of the reactor. In the upper region thereof, the substances to be used are fed. Liquid slag is deposited on the side walls thereof and can run off freely without the surface of the slag solidifying. At the bottom side thereof, an opening (6) with a dripping edge (7) is located, from where the obtained synthesis gas can be withdrawn toward the bottom and the liquid slag running down can drain. A second chamber (8) connects to the opening at the bottom, the synthesis gas being kept dry and being cooled in said second chamber (8). A water film that is produced by suitable devices and that falls freely delimits the second chamber. A third chamber (15) connects to the second chamber at the bottom and in it cooling takes place by adding water to the synthesis gas. A water bath (21) connects to the bottom of the third chamber, the drained and already solidified or still liquid slag particles dropping into said water bath. At the bottom or on the side of the third chamber (15), but above the water bath (21), the generated and cooled synthesis gas is withdrawn from the pressure container (4).
机译:本发明涉及一种通过在0.3至8MPa的压力下,在1200至2000℃的温度范围内用含氧的气态气化液体或细粉碎的固体燃料来获得合成气的方法和装置。冷却反应器(3)中的气化剂,其中液体炉渣沉积在其壁上。反应器位于第一压力容器中。所获得的合成气在布置在反应器顶部的第一反应室(2)中产生。在其上部区域中进料要使用的物质。液态炉渣沉积在其侧壁上,并且可以自由流走,而炉渣的表面不会凝固。在其底侧处设置有具有滴落边缘(7)的开口(6),从那里可以将所获得的合成气朝底部抽出,并且可以将流下的液体炉渣排出。第二腔室(8)连接至底部的开口,合成气保持干燥并在所述第二腔室(8)中冷却。由合适的装置产生并自由落下的水膜界定了第二腔室。第三腔室(15)在底部连接到第二腔室,并且在第三腔室中通过向合成气中添加水来进行冷却。水浴(21)连接到第三腔室的底部,排干并已经凝固或仍为液态的炉渣颗粒滴入所述水浴中。在第三腔室(15)的底部或侧面,但是在水浴(21)的上方,所产生并冷却的合成气从压力容器(4)中抽出。

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