流化床反应器裂解原油制烯烃的基础研究

T. Kunugi, D. Kunii, H. Tominaga, T. Sakai, Shunsuke Mabuchi, Kosuke Takeshige
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引用次数: 2

摘要

利用含碳流化床反应器对原油热解制烯烃进行了基础研究。测试了7种原油。对科威特、米纳斯原油、科威特馏分油和残留物进行了特别详细的检查。热解条件为:温度750 ~ 850℃;停留时间,0.2 ~ 1sec;水蒸气对碳氢化合物的重量稀释比为0.5 ~ 2。根据改良后的表征因子(K=3√TB’/d)绘制产物产量图。产物产率随热解程度的变化用强度函数表示(IF=T•θ0.06)。这些专著提供了在给定反应温度(T,°F)和停留时间(θ,秒)和蒸汽稀释下,估计已知50%精馏点(TB′,°R)和比重(d, @ 60°F)的任何原油的热解结果的方法。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Basic Study on Pyrolysis of Crude Oils for Olefin Production by Use of Fluidized Bed Reactor
The basic study on pyrolysis of crude oils for olefin production was made by use of a fluidized bed reactor containing carbon particles. Seven crude oils were tested. Kuwait, Minas crudes, and Kuwait distillates and residues were examined particularly in detail. Pyrolysis conditions were: temperaturer 750∼850°C; residence time, 0.2∼1sec; and the steam to hydrocarbon dilution ratio by weight 0.5∼2. The yields of products were plotted against the modified characterization factor (K=3√TB'/d) of the respective feed. Changes in the product yields with pyrolysis severity were represented in terms of the intensity function (IF=T•θ0.06). These monographs provide the means for estimating the pyrolysis results of any crude oil with known 50% distillation point (TB', °R) and specific gravity (d, @ 60°F) at given reaction temperature (T, °F) and residence time (θ, sec) with steam dilution.
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