摘要
蒽油加氢装置使用ⅥB族及Ⅷ族的Mo、W、Ni活性组分作为催化剂,通过精制-裂化一段串联法对蒽油进行加氢改质,可得到馏程在155-335℃的燃料油组分和53-152℃的石脑油组分,液相收率为98%-102%。产品作为重整原料及低凝柴油调和组分,比蒽油具有更好的经济效益。
Anthracene oil hydrogenation devices use active components Mo, W, Ni of VIB and VIII family as the catalyst,through a series of method of refined-cracking to take hydro-upgrading on anthracene oil,and we can get the fuel oil component with distillation range between 155-53-152 ℃ and naphtha components of 53-152 ℃ and the oil recovering rate is between 98% - 102%. The products, as the reformed feedstock and low freezing diesel reconciled components, has better economic benefit than anthracene oil.
作者
庞皓
赵长锁
王锦程
刘勇
Pang Hao;Zhao Changsuo;Wang Jincheng;Liu Yong(Baoshun technology co., LTD. Henan, 455000)
出处
《当代化工研究》
2016年第7期78-79,共2页
Modern Chemical Research
关键词
蒽油
加氢
工艺
anthracene oil
hydrogenation
technology