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机构地区:[1]华东理工大学大型工业反应器工程教育部工程研究中心化学工程联合国家重点实验室,上海200237 [2]中国石化洛阳分公司
出 处:《石油炼制与化工》2011年第12期11-15,共5页Petroleum Processing and Petrochemicals
摘 要:采用提升管催化裂化装置,考察脱沥青油(DAO)以及抽提条件分别为剂油质量比2∶1、抽提温度80℃;剂油质量比2∶1、抽提温度85℃两种工况下对DAO进行糠醛抽提所得到的抽余油A与B等三种催化裂化原料的裂化性能。实验结果表明:DAO经过糠醛抽提后所得抽余油的催化裂化转化率较高,轻质油收率较高,重油和焦炭产率较低,其催化裂化性能和裂化产品的性质均优于DAO。In this paper, pilot plant riser reactor was used to evaluate the catalytic cracking performances of desaphalted oil (DAO) and its raffinate oils (denoted as feed A and feed B),which were obtained by extracting DAO with furfural under the conditions of furfural/DAO mass ratio of 2,extraction temperature of 80℃ and 85℃ ,respectively. Experimental results indicated that compared with DAO, both feed A and feed B exhibited improved catalytic cracking performances: higher heavy oil conversion and light oil yield,lower yields of coke and slurry oil, besides, the properties of cracking products from feed A and feed B are also better in some ways.
分 类 号:TE624.41[石油与天然气工程—油气加工工程]
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