Natural Gas Processing From Midstream to Downstream 2018
DOI: 10.1002/9781119269618.ch17
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An Energy Integrated Approach to Design a Supercritical Fischer‐Tropsch Synthesis Products Separation and Solvent Recovery System

Abstract: The data analyzed in section 5.2 were conducted in part by Dr. Buping Bao and were published in 2010. All other work conducted for the thesis was completed by the student independently.

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“…The FTS-SCS reactor was simulated with the reaction equations reported by Abusrafa et al [37] Also, a value of α = 0.95 was considered for the Anderson-Schulz-Flory (ASF) products distribution. [38] T A B L E 1 Hazard identification and risk assessment (HIRA) hazard ranking with fire and explosion damage index (FEDI) values.…”
Section: Application To the Gtl Processmentioning
confidence: 99%
“…The FTS-SCS reactor was simulated with the reaction equations reported by Abusrafa et al [37] Also, a value of α = 0.95 was considered for the Anderson-Schulz-Flory (ASF) products distribution. [38] T A B L E 1 Hazard identification and risk assessment (HIRA) hazard ranking with fire and explosion damage index (FEDI) values.…”
Section: Application To the Gtl Processmentioning
confidence: 99%