Conceptual Design of Pyrolytic Oil Upgrading Process Enhanced by Membrane-Integrated Hydrogen Production System
Hydrotreatment is an efficient method for pyrolytic oil upgrading; however, the trade-off between the operational cost on hydrogen consumption and process profit remains the major challenge for the process designs. In this study, an integrated process of steam methane reforming and pyrolytic oil hyd...
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doaj-ca1db51005384d3385f68bd1cd36da5a2020-11-25T00:20:23ZengMDPI AGProcesses2227-97172019-05-017528410.3390/pr7050284pr7050284Conceptual Design of Pyrolytic Oil Upgrading Process Enhanced by Membrane-Integrated Hydrogen Production SystemBo Chen0Tao Yang1Wu Xiao2Aazad khan Nizamani3R & D Center of Hydroprocesing technology, SINOPEC Dalian Research Institute of Petroleum and Petrochemicals, Dalian 116045, ChinaR & D Center of Hydroprocesing technology, SINOPEC Dalian Research Institute of Petroleum and Petrochemicals, Dalian 116045, ChinaChemical Engineering Department, Dalian University of Technology, Dalian 116045, ChinaChemical Engineering Department, Dalian University of Technology, Dalian 116045, ChinaHydrotreatment is an efficient method for pyrolytic oil upgrading; however, the trade-off between the operational cost on hydrogen consumption and process profit remains the major challenge for the process designs. In this study, an integrated process of steam methane reforming and pyrolytic oil hydrotreating with gas separation system was proposed conceptually. The integrated process utilized steam methane reformer to produce raw syngas without further water–gas-shifting; with the aid of a membrane unit, the hydrogen concentration in the syngas was adjusted, which substituted the water–gas-shift reactor and improved the performance of hydrotreater on both conversion and hydrogen consumption. A simulation framework for unit operations was developed for process designs through which the dissipated flow in the packed-bed reactor, along with membrane gas separation unit were modeled and calculated in the commercial process simulator. The evaluation results showed that, the proposed process could achieve 63.7% conversion with 2.0 wt% hydrogen consumption; the evaluations of economics showed that the proposed process could achieve 70% higher net profit compared to the conventional plant, indicating the potentials of the integrated pyrolytic oil upgrading process.https://www.mdpi.com/2227-9717/7/5/284hydrogen productionpyrolytic oil hydro-processingprocess modelingsyngas |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Bo Chen Tao Yang Wu Xiao Aazad khan Nizamani |
spellingShingle |
Bo Chen Tao Yang Wu Xiao Aazad khan Nizamani Conceptual Design of Pyrolytic Oil Upgrading Process Enhanced by Membrane-Integrated Hydrogen Production System Processes hydrogen production pyrolytic oil hydro-processing process modeling syngas |
author_facet |
Bo Chen Tao Yang Wu Xiao Aazad khan Nizamani |
author_sort |
Bo Chen |
title |
Conceptual Design of Pyrolytic Oil Upgrading Process Enhanced by Membrane-Integrated Hydrogen Production System |
title_short |
Conceptual Design of Pyrolytic Oil Upgrading Process Enhanced by Membrane-Integrated Hydrogen Production System |
title_full |
Conceptual Design of Pyrolytic Oil Upgrading Process Enhanced by Membrane-Integrated Hydrogen Production System |
title_fullStr |
Conceptual Design of Pyrolytic Oil Upgrading Process Enhanced by Membrane-Integrated Hydrogen Production System |
title_full_unstemmed |
Conceptual Design of Pyrolytic Oil Upgrading Process Enhanced by Membrane-Integrated Hydrogen Production System |
title_sort |
conceptual design of pyrolytic oil upgrading process enhanced by membrane-integrated hydrogen production system |
publisher |
MDPI AG |
series |
Processes |
issn |
2227-9717 |
publishDate |
2019-05-01 |
description |
Hydrotreatment is an efficient method for pyrolytic oil upgrading; however, the trade-off between the operational cost on hydrogen consumption and process profit remains the major challenge for the process designs. In this study, an integrated process of steam methane reforming and pyrolytic oil hydrotreating with gas separation system was proposed conceptually. The integrated process utilized steam methane reformer to produce raw syngas without further water–gas-shifting; with the aid of a membrane unit, the hydrogen concentration in the syngas was adjusted, which substituted the water–gas-shift reactor and improved the performance of hydrotreater on both conversion and hydrogen consumption. A simulation framework for unit operations was developed for process designs through which the dissipated flow in the packed-bed reactor, along with membrane gas separation unit were modeled and calculated in the commercial process simulator. The evaluation results showed that, the proposed process could achieve 63.7% conversion with 2.0 wt% hydrogen consumption; the evaluations of economics showed that the proposed process could achieve 70% higher net profit compared to the conventional plant, indicating the potentials of the integrated pyrolytic oil upgrading process. |
topic |
hydrogen production pyrolytic oil hydro-processing process modeling syngas |
url |
https://www.mdpi.com/2227-9717/7/5/284 |
work_keys_str_mv |
AT bochen conceptualdesignofpyrolyticoilupgradingprocessenhancedbymembraneintegratedhydrogenproductionsystem AT taoyang conceptualdesignofpyrolyticoilupgradingprocessenhancedbymembraneintegratedhydrogenproductionsystem AT wuxiao conceptualdesignofpyrolyticoilupgradingprocessenhancedbymembraneintegratedhydrogenproductionsystem AT aazadkhannizamani conceptualdesignofpyrolyticoilupgradingprocessenhancedbymembraneintegratedhydrogenproductionsystem |
_version_ |
1725368084379729920 |