Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
5477130 | Energy | 2017 | 15 Pages |
Abstract
In a refining complex, an absorption-stabilization process used in the production of end-use petro-products (i.e. stable gasoline and liquefied petroleum gas) is energy-intensive and costly. A new absorption-stabilization process with a two-stage condensation section is introduced in this work to further improve energy-use performance. In the new process, a condenser, a condensed oil tank, and a side-reboiler are integrated into the original process and then a heat integration scheme is performed. Compared with the existing process, the proposed process can reduce the cold utility and hot utility by 17.98% and 25.65%, respectively, as well as decrease the total annual operating costs of the heat exchanger network by 17.48%. Additionally, the process retrofit reduces the annual operating costs of cooling water and steam by about $346,617Â at the expense of capital costs around $487,006, and the corresponding payback period is approximately 17 months.
Related Topics
Physical Sciences and Engineering
Energy
Energy (General)
Authors
X.G. Liu, C. He, C.C. He, J.J. Chen, B.J. Zhang, Q.L. Chen,