下吸式固定床气化炉由于具有结构简单，易于操作，产出气焦油含量低等优点已经得到了广泛的应用。
Suction under the fixed bed gasifier with simple structure, easy to operate, the output gas low tar content advantages has been widely used.
结果实现了苯胺催化加氢制环己胺列管式固定床反应器的优化设计与操作。
ResultsThe optimal design and operation of the fixed tube array reactor for catalytic hydrogenation of aniline was realized.
将吸附带以某一虚拟速度运动，通过物料衡算可以建立固定床吸附操作模型方程。
Supposing adsorption belt moves at a suppositional rate, the adsorption model equation in fixed bed can be set up through material calculation.
对固定床气化炉来说，煤的热稳定性是影响正常气化操作的重要因素。
For a fixed bed gasifier speaking, thermal stability of coal gasification is affect the normal operation of important factor.
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 fixed bed reactor, fluidized bed reactor and slurry reactors were compared on their structure, production capacity, materials, products and operating conditions.
建立了充填国产s101钒催化剂的、单段流向变换周期操作固定床反应器的非均相动态模型。
The heterogeneous transient model of a fixed - bed reactor packed with vanadium catalyst, S101, for catalytic oxidation of SO2 and operating in a flow direction switched periodically was developed.
建立了充填国产s101钒催化剂的、单段流向变换周期操作固定床反应器的非均相动态模型。
The heterogeneous transient model of a fixed - bed reactor packed with vanadium catalyst, S101, for catalytic oxidation of SO2 and operating in a flow direction switched periodically was developed.
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