首页> 外国专利> METHOD FOR CONVERTING BIOMASS INTO SYNTHESIS GAS USING A PRESSURIZED MULTI-STAGE PROGRESSIVELY EXPANDING FLUIDIZED BED GASIFIER FOLLOWED BY AN OXYBLOWN AUTOTHERMAL REFORMER TO REDUCE METHANE AND TARS

METHOD FOR CONVERTING BIOMASS INTO SYNTHESIS GAS USING A PRESSURIZED MULTI-STAGE PROGRESSIVELY EXPANDING FLUIDIZED BED GASIFIER FOLLOWED BY AN OXYBLOWN AUTOTHERMAL REFORMER TO REDUCE METHANE AND TARS

机译:用加压多级逐步膨胀流化床气化炉,然后用氧吹自热重整器减少甲烷和塔斯气,将生物质转化为合成气的方法

摘要

The invention provides systems and methods for converting biomass into syngas using a pressurized multi-stage progressively expanding fluidized bed gasifier to eliminate or reduce the formation of methane, volatiles such as BTX, and tars. The gasifier may include a reactive stage that may receive a biomass feed through a feed line and oxygen through an oxygen feed line. The gasifier may also include a fluidized bed section that may be configured to receive the reaction products from the first stage, mix them and perform fluidized bed activity. A gasifier may also have a disengagement section that may be configured to separate fluidized media and particulate matter from syngas product. A gasification system may also include oxyblown catalytic autothermal reactor and a cryogenic air separation unit.
机译:本发明提供使用加压的多级逐步膨胀流化床气化器以消除或减少甲烷,挥发物如BTX和焦油的形成的将生物质转化为合成气的系统和方法。气化器可以包括反应阶段,该反应阶段可以通过进料管线接收生物质进料并且通过氧气进料管线接收氧气。气化器还可以包括流化床部分,其可以被配置为接收来自第一阶段的反应产物,将它们混合并进行流化床活性。气化器还可以具有分离段,该分离段可以构造成将流化介质和颗粒物质与合成气产物分离。气化系统还可包括氧吹催化自热反应器和低温空气分离单元。

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