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Reusing energy lowers fuel needs of distillation towers

Journal Article · · Chem. Eng. (N.Y.); (United States)
OSTI ID:7018779
In this article, the author outlines a procedure for heat-integrating parallel distillation trains typical in a large plant. In a complex producing several grades of petroleum fuels, aromatics and olefins, the distillation towers reject a lot of heat in the 150 to 350/degree/F range through the condensers, pump-around exchangers and intermediate condensers to the cooling water or air. Yet, it is not uncommon in the same plant to have distillation towers requiring reboilers in the 150 to 300/degree/F range. Here, the heat is supplied by steam or direct-fired fuel. By reusing the heat rejected by some towers in the intermediate reboilers and reboilers of other towers, one can significantly reduce consumption of utilities. Detailed design recommendations on what to do to achieve this goal are presented. It is demonstrated that a systematic approach at maximizing heat integration in distillation systems can offer large utility savings. In existing plants, the major elements for these savings can be implemented by increasing the capital investment for distillation-tower exchangers, drums, piping and pumps.
Research Organization:
Exxon Chem Co, Florham Park, NJ, USA
OSTI ID:
7018779
Journal Information:
Chem. Eng. (N.Y.); (United States), Journal Name: Chem. Eng. (N.Y.); (United States) Vol. 89:12; ISSN CHEEA
Country of Publication:
United States
Language:
English