| contributor author | امیررضا زمانی میقانی | en |
| contributor author | مهدی پناهی | en |
| contributor author | محمدعلی فنائی شیخ الاسلامی | en |
| contributor author | Amirreza Zamani Meighani | fa |
| contributor author | Mehdi Panahi | fa |
| contributor author | Mohammad Ali Fanaei Shykholeslami | fa |
| date accessioned | 2020-06-06T14:28:15Z | |
| date available | 2020-06-06T14:28:15Z | |
| date copyright | 5/6/2018 | |
| date issued | 2018 | |
| identifier uri | https://libsearch.um.ac.ir:443/fum/handle/fum/3398021?show=full | |
| description abstract | Optimization of a staged natural gas to hydrocarbon liquids (GTL) process while natural gas feed is also a degree of freedom is considered. The target is to design a self-optimizing control structure which works near optimum in a wide range of operation without the need to update the controlled variables (CVs) setpoints or change the control loops. Maximum possible throughput and the bottleneck of the process are found. The self-optimizing CVs are proposed for the optimal operation of this process. | en |
| language | English | |
| title | Self-Optimizing Control Structure Design for a Staged Fischer-Tropsch GTL Process – Steady State Analysis | en |
| type | Conference Paper | |
| contenttype | External Fulltext | |
| subject keywords | Staging | en |
| subject keywords | Maximum Throughput | en |
| subject keywords | Throughput Manipulator (TPM) | en |
| subject keywords | Process Bottleneck | en |
| identifier link | https://profdoc.um.ac.ir/paper-abstract-1068579.html | |
| identifier articleid | 1068579 | |
