Mixing characteristics of triplet loop biological fluidized bed reactors was investigated.
研究了三重环流生物流化床反应器混合特性。
Hydrodynamics and mass transfer of triplet loop biological fluidized bed reactors were studied in terms of gas holdup, liquid circulation velocity and volumetric mass transfer coefficient.
从气相含率、液体循环速度和体积氧传质系数方面研究自行设计新型结构的三重环流生物流化床的流体力学与传质特性。
The fixed bed reactor, fluidized bed reactor and slurry reactors were compared on their structure, production capacity, materials, products and operating conditions.
并对固定床、流化床和浆态床反应器的结构、生产能力、原料及产物组成和操作条件等进行了比较。
The characteristics of fixed bed reactor, fluidized bed reactor, membrane reactor and other reactors which were developed recently were summarized.
另外还对固定床、流化床、膜反应器以及一些新开发的反应器的特点进行了讨论。
In the paper, the process characteristic and flow of several major MTG processes including fixed bed, fluidized bed and multi-tube reactors are reviewed, and these processes are compared.
介绍了固定床工艺、流化床工艺、多管式反应器以及一步法甲醇制汽油（MTG）的工艺特点及其流程，并对几种工艺进行了比较。
The reactors are fixed bed or fluidized bed.
反应器为固定床或流化床。
The reactors are fixed bed or fluidized bed.
反应器为固定床或流化床。
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