Simulation of gasoline vapor recovery by pressure swing adsorption

被引:38
|
作者
Liu, YJ
Ritter, JA [1 ]
Kaul, BK
机构
[1] Univ S Carolina, Swearingen Engn Ctr, Dept Chem Engn, Columbia, SC 29208 USA
[2] ExxonMobil Res & Engn Co, Florham Pk, NJ 07932 USA
关键词
pressure swing adsorption; gasoline vapor recovery; multicomponent adsorption; computer simulation; mathematical modeling;
D O I
10.1016/S1383-5866(00)00066-6
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A multicomponent pressure swing adsorption (PSA)-gasoline vapor recovery (GVR) process simulator was used to carry out full-scale simulations of the recovery of butane, benzene and/or heptane vapors from nitrogen using BAX activated carbon. This mixture of vapors simulates the recovery of gasoline vapors from tank filling operations. PSA-GVR processes utilizing both feed and carrier gas pressurization were investigated, with different feed mixtures varying from two to four components, including nitrogen. A long tail in the butane vapor concentration wave was always present when feed pressurization was used, and it led to butane vapor breakthrough, whereas the process having the same conditions but pressurized with carrier gas produced pure light product (nitrogen). Thus, carrier gas pressurization in lieu of feed pressurization should be used in PSA-GVR processes. The presence of the heavier vapor components in the feed resulted in a creeping wave phenomenon, which pushed the butane concentration wave toward the light product end of the column. They also produced higher temperatures in the column, which effectively lowered the adsorbent capacity. These effects have significant implications with regard to environmental regulations and must be accounted for in the design of PSA-GVR processes. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:111 / 127
页数:17
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