(378l) Optimizing Fractionation Condenser System CAPEX and OPEX—Case Studies & Performance

Whether designing a new fractionation train or debottlenecking an existing one, there are opportunities in condenser systems that are often overlooked. This presentation will focus on two key concepts.

1). Fractionation systems often experience operational issues or bottlenecks caused by the condenser system, either by design or through creep capacity over time. Two case studies from refining and midstream industries will be shared where design of new condensers for fractionation systems considered overhead line pressure drop causing superheat entering the condenser. This superheat can impact sizing and/or performance of the condenser as well as the entire distillation system. Potential root causes for missing these design details in today’s industry will be discussed. One case study will demonstrate simultaneous reduction of both CAPEX and OPEX costs. These same considerations can be used to evaluate and debottleneck existing systems.

2) A case study will be presented from the design of a now operating facility for a feed/condenser heat integration scheme. Common arrangements of such an exchanger from both refining and midstream experiences will be covered. The best overall layout of an actual depropanizer system with key detailed design considerations to ensure operation success will be shared, which realized both CAPEX and OPEX savings for the project. Retrofitting existing system with this heat integration scheme may debottleneck condenser limited fractionation systems for higher capacity at relatively lower costs than traditional methods.