首页> 外国专利> PROCESS OF MAXIMIZING PRODUCTION OF CHEMICAL RAW MATERIALS BY GASEOUS PHASE CATALYTIC CRACKING CRUDE OIL WITH MULTI-STAGES IN MILLISECONDS IN COMBINATION WITH HYDROGENATION

PROCESS OF MAXIMIZING PRODUCTION OF CHEMICAL RAW MATERIALS BY GASEOUS PHASE CATALYTIC CRACKING CRUDE OIL WITH MULTI-STAGES IN MILLISECONDS IN COMBINATION WITH HYDROGENATION

机译:气态多相气相多相气相催化裂化原油最大限度地提高化学原料的生产过程

摘要

The invention provides a process of maximizing production of chemical raw materials by gaseous phase catalytic cracking crude oil with multi-stages in milliseconds in combination with hydrogenation, comprising: a high-efficiency atomizing nozzle sprays the preheated crude oil into an upper portion of the downflow modification reaction tube, the produced oil mist is mixed with a high temperature heat carrier flowing downward from a first return controller for pyrolysis in milliseconds and then the pyrolysis products are subject to a gas-solid separation; the coked heat carrier obtained by the separation enters into a modification regeneration reactor to conduct a regeneration reaction, the obtained high temperature heat carrier returns to a top of the downflow reaction tube to participate in circulation, the regeneration gas is subject to heat exchange and then output; the high temperature oil and gas produced by the pyrolysis reaction directly flow into the millisecond cracking reactor and conduct a cracking reaction with the regenerated cracking catalyst and subject to a gas-solid separation; then the cracking catalyst to be regenerated enters the crack regeneration reactor and performs a regeneration reaction and then are subject to a gas-solid separation, the obtained high temperature crack catalyst passes through a second return controller and flows into the millisecond cracking reactor to participate the circulation reaction, the obtained flue gas is subject to heat exchange and then output; the cracked oil and gas produced by the cracking reaction enter into a fractionation tower for separation, thereby obtain the cracked gas, gasoline fraction, diesel fraction, recycle oil and oil slurry; furthermore, the diesel fraction, recycle oil and oil slurry are subject to saturation or open-ring in a hydrogenation reactor, return and mix with crude oil such that the mixture is used as a raw material.
机译:本发明提供了一种通过在几毫秒内将气相多级气相催化裂化原油并与氢化结合来最大化化学原料生产的方法,该方法包括:高效的雾化喷嘴将预热的原油喷入下流的上部在改性反应管中,将产生的油雾与从第一回流控制器向下流动的高温载热体混合,在毫秒内进行热解,然后对热解产物进行气固分离;分离得到的焦化热载体进入改性再生反应器进行再生反应,所获得的高温热载体返回到下流反应管顶部参与循环,使再生气体进行热交换后,输出;热解反应产生的高温油气直接流入毫秒级裂化反应器,与再生裂化催化剂进行裂化反应,进行气固分离。然后将要再生的裂化催化剂进入裂化再生反应器并进行再生反应,然后进行气固分离,所获得的高温裂化催化剂通过第二回流控制器进入毫秒级裂化反应器以参与反应。循环反应,将得到的烟气进行热交换后输出。裂解反应产生的裂解油气进入分馏塔进行分离,得到裂解气,汽油馏分,柴油馏分,循环油和油浆。此外,柴油馏分,循环油和油浆在氢化反应器中经受饱和或开环,返回并与原油混合,使得该混合物用作原料。

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