摘要
介绍了C_6^+增产BTX的工艺流程,该流程可在催化剂的作用下将C_9^+中的重芳烃和非芳经脱烷基、歧化、非芳裂解等反应,转化为BTX(苯、甲苯、二甲苯)和乙烷、丙烷、少量甲烷和丁烷,无需溶剂抽提,经简单精馏即可分离得到苯、甲苯、混合二甲苯,具有产品附加值高、能耗低、清洁环保等特点。将该工艺技术与传统的芳烃抽提技术进行经济性比较发现,新技术可产生可观的经济效益和社会效益。
This paper studies a new technology which converts C_9^+ heavy aromatics and non-aromatics into BTX( benzene,toluene and xylene),ethane,propane and a small amount of methane and butane via dealkylation, transalkylation and non-aromatics cracking reactions in the presence of catalysts, and benzene,toluene and mixed xylene can be separated via simple distillation without solvents. It has the characteristics of high value-added products, low energy consumption and eco-friendliness. The economic comparison of this advanced technology with the traditional aromatics extraction technology shows that this new technology can produce considerable economic and social benefits and is worth popularization.
出处
《乙烯工业》
CAS
2018年第3期1-5,共5页
Ethylene Industry
关键词
裂解汽油加氢
C6^+增产BTX
芳烃抽提
经济性比较
pyrolysis gasoline hydrogenation
producing more BTX from C_6^+ fractions
aromatics extraction
economic comparison