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Production method of single ring aromatic hydrocarbon and production plant of single ring aromatic hydrocarbon

机译:单环芳烃的生产方法及单环芳烃的生产装置

摘要

As for this invention, 10 capacity % distillation temperature above the 140 and 90 capacity % making with the raw materials oil and the aromatic production catalyst contact where distillation temperature is below the 380, being production method of the single ring aromatic hydrocarbon which produces the reaction product which includes the single ring aromatic hydrocarbon, the aforementioned raw materials oil, the disassembly improvement reactor which accommodates the aforementioned aromatic production catalyst (10) process and the aforementioned disassembly improvement reactor which are introduced (10) process and the aforementioned raw materials oil which make the aforementioned raw materials oil contact with the aforementioned aromatic production catalyst in inside the aforementioned disassembly improvement reactor (10)Before introducing inside, heating the aforementioned raw materials oil beforehand, gas-liquid partition stage and the aforementioned vapor fraction and the aforementioned liquid fraction which for the vapor fraction and the liquid fraction gas-liquid are separated the respective aforementioned disassembly improvement reactor (10) the introduction process which is introduced into the position where the inside differs mutually and, it has heating process and the aforementioned gas-liquid mixtures style which form gas-liquid mixtures style.
机译:对于本发明,作为产生反应的单环芳香烃的制造方法,在140℃以上为10容量%的蒸馏温度,在380℃以下为90℃以下时以原料油与芳香族生成催化剂接触而成为90容量%。包括单环芳烃,上述原料油,容纳上述芳香族生成催化剂(10)工序的分解改进反应器和引入的(10)工序的上述分解改进反应器的产品,以及上述原料油。在上述分解改进反应器(10)的内部使上述原料油与上述芳族生产催化剂接触,在引入内部之前,预先加热上述原料油,气液分配阶段以及上述蒸气馏分和前述物质蒸气馏分和液体馏分气液分离后的液体馏分分别在上述的分解促进反应器(10)中引入到内部相互不同的位置的引入工序,具有加热工序和上述气体-液体混合物样式,形成气-液混合物样式。

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