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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Investigation of a dual cold-flow fluidized bed for calcium looping gasification process
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Investigation of a dual cold-flow fluidized bed for calcium looping gasification process

机译:用于钙循环气化过程的双冷流流化床的研究

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摘要

In this paper, a compact fluidized bed gasifier is proposed for the calcium looping gasification process to produce hydrogen-rich gas with CO2 capture. The design of compact fluidized bed gasifier is according to the adsorption properties of lime under different partial pressure of CO2 and temperature. The compact fluidized bed gasifier consists of two sections: an upper riser and a lower bubbling fluidized bed. The fluid dynamics feasibility of the proposed dual fluidized bed with compact fluidized bed gasifier was evaluated in a cold flow model. The cold flow model can operate in a stable state under designed conditions. Most of the bed materials (>90%) stay in the lower bubbling fluidized bed. The effect of the total solid inventory and the fluidizations in both the lower bubbling fluidized bed and the regenerator on the solid recirculation flux is marginal because of the high resistance in the loop-seal of the lower bubbling fluidized bed to the regenerator. The solid recirculation flux can be controlled effectively by loop-seals, but the fluidization number in the supply section of the loop-seal must be kept lower than 1. No gas leakage was detected in the cold flow model under the designed conditions. (C) 2019 Elsevier B.V. All rights reserved.
机译:在本文中,提出了一种紧凑的流化床气化器,用于钙循环气化过程,用CO2捕获生产富含氢气的气体。紧凑型流化床气化器的设计是根据二氧化碳和温度不同部分压力的石灰的吸附性能。紧凑型流化床气化器由两个部分组成:上部提升管和下鼓泡流化床。在冷流模型中评价了具有紧凑型流化床气化器的所提出的双流化床的流体动力学可行性。冷流模型可以在设计的条件下在稳定状态下操作。大多数床材料(> 90%)停留在较低鼓泡流化床。由于下鼓泡流化床的环密封件到再生器的较高阻力,总固体清洗剂和较低鼓泡流化床和再生器中的流化物中的效果是边缘的。可以通过环密封件有效地控制固体再循环通量,但是环形密封的供应部分中的流化数必须保持低于1。在设计的条件下,在冷流量模型中没有检测到气体泄漏。 (c)2019年Elsevier B.V.保留所有权利。

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