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- Team H Final Report ...ng, Vince Kenny, Matthew Leung, Matthew Nathal, John Plaxco, Spencer Saldaña, Micah Zuckerman, Erik Zuehlke32 KB (4,673 words) - 19:03, 13 March 2015
- Team G2 Final Report This report is part of an ongoing project to design a process to produce ethylene and NGLs from shale gas. The inlet raw shale ga42 KB (6,617 words) - 21:08, 13 March 2015
- Team D: Final Report ...ght has exposed a discrepancy in water supply contingency and demonstrated a need for non-natural freshwater sources.38 KB (5,751 words) - 18:02, 10 March 2016
- Team G: Newport Desalination Plant This reports outlines the design and evaluation of a multi-stage flash distillation plant located in Newport, Oregon. As the hu42 KB (5,773 words) - 13:16, 11 March 2016
- Team G1 Final Report The purpose of this project was to design a natural gas processing plant integrated with an ethylene production plant.44 KB (4,967 words) - 18:46, 13 March 2015
- ...ds into products. Reactor design is a vital step in the overall design of a process. It is important to ensure that the equipment specified will be ca In a batch reactor, the reagents are added together and allowed to react for a given amount of time. The compositions change with time, but there is no f90 KB (13,688 words) - 00:56, 22 February 2016