首页> 外国专利> Process for the Production of High Quality Middle Distillates from Mild Hydrocrackers and Vacuum Gas Oil Hydrotreaters in Combination with External Feeds in the Middle Distillate Boiling Range

Process for the Production of High Quality Middle Distillates from Mild Hydrocrackers and Vacuum Gas Oil Hydrotreaters in Combination with External Feeds in the Middle Distillate Boiling Range

机译:中温沸腾范围内由轻度加氢裂化器和减压瓦斯油加氢处理机与外部进料结合生产高质量中间馏分的方法

摘要

PURPOSE: Provided are a mild hydrocracking apparatus using external material in the boiling range of middle distillates and a method for producing high quality middle distillates from a vacuum light oil hydrotreating apparatus. CONSTITUTION: The method includes the steps of: (a) passing a hydrocarbonaceous feedstock to a first hydroprocessing zone having one or more beds containing hydroprocessing catalyst; (b) passing the effluent of step (a) directly to a hot high pressure separator; (c) passing the vapor stream from step (b) after cooling and partial condensation to a hot hydrogen stripper containing at least one bed of hydrotreating catalyst; (d) passing the overhead vapor stream from the hot hydrogen stripper of step (c), after cooling and contacting with water, to a first cold high pressure separator; (e) passing the liquid stream from the hot hydrogen stripper of step (c) to a bed of hydroprocessing catalyst in the second reactor stage; (f) passing the overhead from the cold high pressure separator of step (d) to an amine absorber; (g) passing the separator bottoms of step (b) to a second reaction stage; (h) passing the vapor stream of step (g) after cooling to a second cold high-pressure separator; (i) passing the liquid effluent of step (g) after cooling to the cold high-pressure separator of step (h) to separate hydrogen and light hydrocarbonaceous gases from the liquid effluent; (j) passing the vapor stream from steps (h) and (i) after further cooling and separation of condensate, to the make-up hydrogen compressor; (k) passing the compressed hydrogen from the make-up hydrogen compressor to the primary reactor loop; and (l) passing the liquid effluent from steps (h) and (i) to the fractionation system.
机译:目的:提供一种在中间馏分沸腾范围内使用外部材料的温和加氢裂化装置,以及一种从轻质轻油加氢处理装置生产高质量中间馏分的方法。组成:该方法包括以下步骤:(a)使含烃原料进入具有一个或多个含加氢处理催化剂床的第一加氢处理区; (b)将步骤(a)的流出物直接送入高温高压分离器; (c)将步骤(b)的蒸气流冷却并部分冷凝后,送入装有至少一个加氢处理催化剂床的热氢汽提器中; (d)在冷却并与水接触之后,将来自步骤(c)的热氢汽提塔的塔顶蒸气流送至第一冷高压分离器; (e)使液体流从步骤(c)的热氢汽提器进入第二反应器阶段的加氢处理催化剂床中; (f)将塔顶馏出物从步骤(d)的冷高压分离器输送至胺吸收剂; (g)使步骤(b)的分离器底部进入第二反应阶段; (h)冷却后,使步骤(g)的蒸气流通过第二冷高压分离器; (i)冷却后,使步骤(g)的液体流出物进入步骤(h)的冷高压分离器,以从液体流出物中分离出氢气和轻质烃类气体; (j)在进一步冷却和分离冷凝物之后,将来自步骤(h)和(i)的蒸气流送至补充氢气压缩机; (k)将压缩氢气从补充氢气压缩机传递到初级反应器回路; (l)使来自步骤(h)和(i)的液体流出物进入分馏系统。

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