工业提升管反应器 commercial riser reactors
In order to make the best use of the energy and FCC catalyst of FCCU, the catalytic cracking of mixed C4 only and the recycle of it to produce propylene and iso-butene had been conducted using riser reactor.
由于混合C4反应需要较高的反应温度以及较大的剂油比,为了充分利用催化裂化装置的热量以及催化剂,在实验室提升管反应器上进行了混合C4单独反应和回炼增产丙烯和异丁烯的实验。
参考来源 - 醚化后混合C·2,447,543篇论文数据，部分数据来源于NoteExpress
粒径分布对于提升管反应器非常重要，应引起足够的重视。
Thus the particle size distribution in a riser reactor should be taken into full consideration.
并且使提升管反应器的流型更加接近活塞流，进一步减少返混。
The flux in the riser reactor is close to plug flow, which greatly demotes the back mixing.
催化裂化提升管反应器数学模型基本上都是基于平推流反应器的假设建立起来的。
Mathematical models for Fluid Catalytic Cracking (FCC) riser reactors were built generally on the basis of assumption of "plug flow" pattern within risers.
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