该系统由移动床热解反应器、移动床气化反应器和流化床燃烧反应器组成。
The system is composed of three reactors, a gas-solid countercurrent moving bed gasifier, a moving bed pyrolysis reactor and a riser-type combustor.
通过在移动床气化炉的造气实验表明，该气化型焦完全符合工业化造气用煤要求，可替代焦炭作为生产半水煤气的原料。
It has been proved that the formed coke is qualified to be used as industrial gasification coal that produces gas with the formed coke in the moving bed gasify furnace.
分析了流化床、气流床和移动床煤气化工艺优缺点和煤气化工艺的发展趋势。
The advantages and disadvantages of fluidized bed, entrained flow bed and moving bed coal gasification technology and their current trends were analyzed.
本论文构建了基于固体热载体加热模式的逆流外循环移动床催化气化反应体系。
The novel catalytic gasification process with solid heat carrier is called External Circulating Countercurrent Moving Bed gasification system.
本论文构建了基于固体热载体加热模式的逆流外循环移动床催化气化反应体系。
The novel catalytic gasification process with solid heat carrier is called External Circulating Countercurrent Moving Bed gasification system.
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