Loading…

Benzene reduction in gasoline range streams by adsorption processes using a PVDC–PVC carbon molecular sieve

[Display omitted] •A PVDC carbon molecular sieve presented high selectivity for benzene adsorption.•The process can be used for benzene content reduction in gasoline feeds.•A one step direct procedure removed benzene along linear and branched paraffins.•A two step procedure removed linear paraffins...

Full description

Saved in:
Bibliographic Details
Published in:Fuel (Guildford) 2014-11, Vol.135, p.459-467
Main Authors: Laredo, Georgina C., Castillo, Jesus, Cano, Jose L.
Format: Article
Language:English
Subjects:
Citations: Items that this one cites
Items that cite this one
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
Description
Summary:[Display omitted] •A PVDC carbon molecular sieve presented high selectivity for benzene adsorption.•The process can be used for benzene content reduction in gasoline feeds.•A one step direct procedure removed benzene along linear and branched paraffins.•A two step procedure removed linear paraffins before benzene adsorption.•Benzene and paraffins enriched fractions can be improved in separated processes. A PVDC–PVC derived carbon molecular sieve (CMS-IMP12) was used for adsorbing the benzene contained in a sample of reforming gasoline from a Mexican Refinery. First an olefin free benzene enriched fraction (H-BHC) was obtained by distillation-hydrogenation. The adsorption process may be carried out in one and two-steps. In the one-step procedure, benzene was adsorbed along other hydrocarbons in a 28mL/100gads yield. The benzene enriched fraction (BEF) contained linear and branched paraffins and cycloparaffins (56%) and benzene (43%). In the two-step procedure, linear paraffins (PEF) were selectively separated from the H-BHC by 5A molecular sieve (7mL/100gads). Then, the paraffins free fraction (PFF, 30mL/100gads) was submitted to a further separation using the CMS material. The resulted adsorbed product (BEF, 42mL/100gads) was formed mainly by iso- and cycloparaffins (50%) and benzene (48%). The octane number of the one-step was lower than the two-steps benzene free fraction (BFF) (67 and 76, respectively) due to the presence of paraffins in the first one. In any case, the benzene may be recuperated from the BEF by distillation and the octane number of the recovered PEF and BFF may be improved by any commercial isomerization process.
ISSN:0016-2361
1873-7153
DOI:10.1016/j.fuel.2014.07.014