The plant seeking longer runtime contacted the original beer column equipment supplier. The supplier was updated with the operating issues and with the expectations for the replacement. Subsequently, a thorough fouling-hydraulic analysis of original and troubled high-performance trays was performed. Several scenarios were considered to explain the bottleneck impacting this 17-ft (5.2 m) diameter column. The complete analysis and column modifications were presented. These were accepted and swiftly and safely implemented. Conventional trays replaced existing high-performance trays. The new internals had features that assure uniform hydraulics to maximize mass transfer performance, and the most critical one, process uptime.
Since the debottlenecking activities in early 2Q2017, the bioethanol plant is operating at 168 MGPY and longer runtimes, and with expansion plans to produce 185 MGPY of ethanol.
This paper confirms that importance of a robust design of mass transfer equipment for critical applications, fouling in specific; and that in some applications, a well-designed conventional tray can “out-perform” a poorly-designed high-performance one.
See more of this Group/Topical: Topical 8: Kister Distillation Symposium
