首页> 外国专利> PREPARATION OF LIGHT HYDROCARBONACEOUS LIQUID IN DELAYED COKER

PREPARATION OF LIGHT HYDROCARBONACEOUS LIQUID IN DELAYED COKER

机译:延迟焦化器中轻质烃类液体的制备

摘要

PURPOSE: To provide a process to produce a light hydrocarbonaceous liquid in a high yield with a low yield of coke. ;CONSTITUTION: The process for producing a light hydrocarbonaceous liquid in a delayed coker containing a coke drum comprising (A) heating a hydrocarbonaceous feed for a coke drum thereby obtaining an intermediate product and (B) introducing the intermediate product into the coke drum, converting it into a final product containing light liquid and coke and separating the light liquid from the coke, wherein the step (A) is carried out in combination either with a step (A)(i) or (A)(ii); the step (A)(i) comprising maintaining the feed without externally supplied water or hydrogen in an enclosed space during the step (A), and subjecting the feed at a pressure not less than about 35.2 kg/cm2 gauge and then reducing the pressure below about 35.2 kg/cm2 gauge prior to the step (B); and the step (A)(ii) comprising contacting the intermediate product from the step (A) with a stripping material (preheated at about 482°C or higher and in a gaseous state at the preheated temperature and the atmospheric pressure) prior to or during the step (B) to solve a part thereof in the stripping material.;COPYRIGHT: (C)1993,JPO
机译:目的:提供一种以高收率和低收率焦炭生产轻质烃类液体的方法。 ;组成:在包含焦炭塔的延迟焦化器中生产轻质烃类液体的方法,该方法包括(A)加热焦炭塔的烃类进料从而获得中间产物,以及(B)将中间产物引入焦炭塔中,进行转化将其制成包含轻质液体和焦炭并将轻质液体与焦炭分离的最终产物,其中步骤(A)与步骤(A)(i)或(A)(ii)结合进行;步骤(A)(i)包括在步骤(A)期间将饲料保持在没有外部供应的水或氢的密闭空间中,并使饲料经受不小于约35.2kg / cm 2的压力。 Sup>表,然后在步骤(B)之前将压力降低到35.2 kg / cm 2 表以下。所述步骤(A)(ii)包括在步骤A之前或之后,使步骤(A)的中间产物与汽提材料(在约482℃或更高温度下预热并且呈气态,在预热温度和大气压下)接触。在步骤(B)中将其一部分溶解在剥离材料中。;版权所有:(C)1993,日本特许厅

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