Recent advancements in ethylene and propylene production using the UOP/Hydro MTO process

被引:435
作者
Chen, JQ
Bozzano, A
Glover, B
Fuglerud, T
Kvisle, S
机构
[1] UOP LLC, Des Plaines, IL 60017 USA
[2] Hydro ASA, N-3901 Porsgrunn, Norway
关键词
UOP/Hydro MTO process; gas-to-olifins; ethylene/propylene product;
D O I
10.1016/j.cattod.2005.07.178
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The UOP/Hydro MTO process utilizes a SAPO-34-containing catalyst that provides up to 80% yield of ethylene and propylene at near-complete methanol conversion. This paper discusses new advancements related to the technology which can increase the carbon selectivity from methanol to ethylene-plus-propylene to about 85-90% and can extend the range of propylene-to-ethylene production ratios to more than 2.0. The MTO technology has the potential to play an important role in the European olefin industry as part of a segregated gas-to-olefins (GTO) chain, utilizing dedicated imported methanol or DME as a low-cost feedstock. Furthermore, the ethylene/propylene product flexibility can contribute to meet the increasing propylene demand. The technology is also attractive due to low specific CO2 emissions. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:103 / 107
页数:5
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