Change search
CiteExportLink to record
Permanent link

Direct link
Cite
Citation style
  • apa
  • harvard1
  • ieee
  • modern-language-association-8th-edition
  • vancouver
  • Other style
More styles
Language
  • de-DE
  • en-GB
  • en-US
  • fi-FI
  • nn-NO
  • nn-NB
  • sv-SE
  • Other locale
More languages
Output format
  • html
  • text
  • asciidoc
  • rtf
Integration of solid oxide electrolyser, entrained gasification, and Fischer-Tropsch process for synthetic diesel production: Thermodynamic analysis
KTH, School of Industrial Engineering and Management (ITM), Energy Technology. Polytech Univ Turin POLITO, Dept Energy, Corso Duca Abruzzi 24, I-10129 Turin, Italy.
KTH, School of Industrial Engineering and Management (ITM), Energy Technology.ORCID iD: 0000-0002-3661-7016
KTH, School of Industrial Engineering and Management (ITM), Energy Technology.
KTH, School of Industrial Engineering and Management (ITM), Energy Technology. Polytechnic University of Turin (POLITO), Corso Duca degli Abruzzi 24, Turin, Italy.
2018 (English)In: International journal of hydrogen energy, ISSN 0360-3199, E-ISSN 1879-3487, Vol. 43, no 10, p. 4785-4803Article in journal (Refereed) Published
Abstract [en]

A novel integrated renewable-based energy system for production of synthetic diesel is proposed and simulated in this study. This system merges solid oxide electrolyser (SOE), entrained gasification (EG) and Fischer-Tropsch (FT) technologies. Two case scenarios are considered here. In the first case, the electrolyser unite produce syngas through co-electrolysis of steam and carbon dioxide, while in the second case only steam is electrolyzed. The effects of SOEC and EG operating pressure and temperatures on the system performance in each case are investigated and compared. It is shown that the operating condition of electrolyser subsystem has a more considerable effect on the performance of the integrated system as compared to the gasification subsystem. Also waste heat recovery results in about 43 and 2 percentage point increase in energy and exergy efficiency, respectively. It is also shown that internal recovering of oxygen has the best effect on the system performance.

Place, publisher, year, edition, pages
Elsevier, 2018. Vol. 43, no 10, p. 4785-4803
Keyword [en]
Solid oxide electrolyser, Entrained gasification, Fischer-Tropsch, Synthetic fuel production, Energy analysis, Exergy analysis
National Category
Energy Engineering
Identifiers
URN: urn:nbn:se:kth:diva-226796DOI: 10.1016/j.ijhydene.2018.01.138ISI: 000429399400001Scopus ID: 2-s2.0-85041958332OAI: oai:DiVA.org:kth-226796DiVA, id: diva2:1202326
Note

QC 20180427

Available from: 2018-04-27 Created: 2018-04-27 Last updated: 2018-04-27Bibliographically approved

Open Access in DiVA

No full text in DiVA

Other links

Publisher's full textScopus

Authority records BETA

Martin, Andrew R.

Search in DiVA

By author/editor
Samavati, MahrokhMartin, Andrew R.Nemanova, VeraSantarelli, Massimo
By organisation
Energy Technology
In the same journal
International journal of hydrogen energy
Energy Engineering

Search outside of DiVA

GoogleGoogle Scholar

doi
urn-nbn

Altmetric score

doi
urn-nbn
Total: 12 hits
CiteExportLink to record
Permanent link

Direct link
Cite
Citation style
  • apa
  • harvard1
  • ieee
  • modern-language-association-8th-edition
  • vancouver
  • Other style
More styles
Language
  • de-DE
  • en-GB
  • en-US
  • fi-FI
  • nn-NO
  • nn-NB
  • sv-SE
  • Other locale
More languages
Output format
  • html
  • text
  • asciidoc
  • rtf