Improved Butadiene Technology for Naphtha Crackign

机译：改进的丁二烯技术用于石脑油裂解

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Most butadiene is obtained as a coproduct from ethylene production during the steam cracking of naphtha. A typical crude C_4 stream derived from a medium-boiling-range naphtha (C_5-C_8) feedstock in a high-severity steam cracker operation has the following composition ranges: butadiene (35 to 50 wt-

机译：在石脑油的蒸汽裂化过程中，大多数丁二烯是作为乙烯生产的副产品获得的。在高强度蒸汽裂化塔操作中，由中沸程石脑油（C_5-C_8）原料衍生的典型C_4粗物流具有以下组成范围：丁二烯（35至50 wt-

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来源
《8th ethylene producers' conference》|1996年|p.631-637|共7页
会议地点 San Diego CA(US);San Diego CA(US)
作者
H.Abrevaya; B.V.Vora; R.A.Lentz;
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正文语种 eng
中图分类化学工业;
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2. Improved butadiene purification technology [J] . Hydrocarbon Engineering Group Hydrocarbon Processing . 2001,第2期

机译：改进的丁二烯纯化技术
3. Improved butadiene purification technology [J] . Kane L., Romanow S. Hydrocarbon Processing . 2001,第2期

机译：改进的丁二烯纯化技术
4. Maximizing naphtha productivity in oil refinery with improved crude mixing using linear programming method [C] . Poghosyan Vahan, Abula Baiherula International Conference on Industrial Engineering and Systems Management . 2013

机译：通过使用线性规划方法改进原油混合，最大限度地提高炼油厂的石脑油生产率
5. Separation of Light Naphtha for the Octane Upgrading of Gasoline: Adsorption and Membrane Technologies and New Adsorbents. [D] . Barcia, Patrick da Silva. 2010

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Improved Butadiene Technology for Naphtha Crackign

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