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APPARATUS AND METHOD FOR PRODUCING ENVIRONMENTALLY-FRIENDLY SOLVENT OIL USING FISCHER-TROPSCH SYNTHETIC OIL

机译:用费-托合成油生产环境友好型溶剂油的装置和方法

摘要

Provided is an apparatus and method for producing an environmentally-friendly solvent oil using a Fischer-Tropsch synthetic oil. The device comprises a hydrorefining reactor (A), a hydrogenation reactor (B), a hot high-pressure separator (C), an alkaline tower (D), a rectification tower (E), and a condenser (F). The method comprises feeding a mixture of the Fischer-Tropsch synthetic oil and hydrogen into the hydrorefining reactor (A), then feeding a mixture of the resultant product and hydrogen into the hydrogenation reactor (B), and the final product entering the hot high-pressure separator (C) to be separated into a gas-phase fraction and a liquid-phase fraction. The gas-phase fraction flows through the alkaline tower (D), and enters the condenser (F) for separation. A mixture of the separated gas portion and fresh hydrogen flows back to the hydrorefining reactor (A) and the hydrogenation reactor (B). The liquid-phase fraction obtained from the hot high-pressure separator (C) enters the rectification tower (E), and is fractionated to produce a naphtha fraction, an environmentally-friendly solvent oil and an unconverted oil.
机译:提供一种使用费-托合成油生产环保溶剂油的设备和方法。该装置包括加氢精制反应器(A),氢化反应器(B),热高压分离器(C),碱塔(D),精馏塔(E)和冷凝器(F)。该方法包括将费托合成油和氢气的混合物进料到加氢精制反应器(A)中,然后将生成的产物和氢气的混合物进料到加氢反应器(B)中,最终产物进入高温减压分离器(C)分离成气相部分和液相部分。气相馏分流过碱性塔(D),然后进入冷凝器(F)进行分离。分离的气体部分和新鲜氢气的混合物流回到加氢精制反应器(A)和氢化反应器(B)。从热的高压分离器(C)获得的液相馏分进入精馏塔(E),并进行分馏以产生石脑油馏分,环境友好的溶剂油和未转化的油。

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