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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Main Authors: Bo Chen, Tao Yang, Wu Xiao, Aazad khan Nizamani
Format: Article
Language:English
Published: MDPI AG 2019-05-01
Series:Processes
Subjects:
Online Access:https://www.mdpi.com/2227-9717/7/5/284
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spelling 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
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