Experimental Study and Thermodynamic Analysis of Hydrogen Production through a Two-Step Chemical Regenerative Coal Gasification
Hydrogen, as a strategy clean fuel, is receiving more and more attention recently in China, in addition to the policy emphasis on H<sub>2</sub>. In this work, we conceive of a hydrogen production process based on a chemical regenerative coal gasification. Instead of using a lumped coal g...
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doaj-5ecf52b2d3414cc4b0f56287b7f696482020-11-25T00:13:43ZengMDPI AGApplied Sciences2076-34172019-07-01915303510.3390/app9153035app9153035Experimental Study and Thermodynamic Analysis of Hydrogen Production through a Two-Step Chemical Regenerative Coal GasificationWei Li0Song He1Sheng Li2Ningbo Institute of Technology, Zhejiang University, Ningbo 315000, ChinaInstitute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, ChinaInstitute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, ChinaHydrogen, as a strategy clean fuel, is receiving more and more attention recently in China, in addition to the policy emphasis on H<sub>2</sub>. In this work, we conceive of a hydrogen production process based on a chemical regenerative coal gasification. Instead of using a lumped coal gasification as is traditional in the H<sub>2</sub> production process, herein we used a two-step gasification process that included coking and char-steam gasification. The sensible heat of syngas accounted for 15−20% of the total energy of coal and was recovered and converted into chemical energy of syngas through thermochemical reactions. Moreover, the air separation unit was eliminated due to the adoption of steam as oxidant. As a result, the efficiency of coal to H<sub>2</sub> was enhanced from 58.9% in traditional plant to 71.6% in the novel process. Further, the energy consumption decreased from 183.8 MJ/kg in the traditional plant to 151.2 MJ/kg in the novel process. The components of syngas, H<sub>2</sub>, and efficiency of gasification are herein investigated through experiments in fixed bed reactors. Thermodynamic performance is presented for both traditional and novel coal to hydrogen plants.https://www.mdpi.com/2076-3417/9/15/3035hydrogen productiongasificationthermodynamic analysisfixed bed reactor |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Wei Li Song He Sheng Li |
spellingShingle |
Wei Li Song He Sheng Li Experimental Study and Thermodynamic Analysis of Hydrogen Production through a Two-Step Chemical Regenerative Coal Gasification Applied Sciences hydrogen production gasification thermodynamic analysis fixed bed reactor |
author_facet |
Wei Li Song He Sheng Li |
author_sort |
Wei Li |
title |
Experimental Study and Thermodynamic Analysis of Hydrogen Production through a Two-Step Chemical Regenerative Coal Gasification |
title_short |
Experimental Study and Thermodynamic Analysis of Hydrogen Production through a Two-Step Chemical Regenerative Coal Gasification |
title_full |
Experimental Study and Thermodynamic Analysis of Hydrogen Production through a Two-Step Chemical Regenerative Coal Gasification |
title_fullStr |
Experimental Study and Thermodynamic Analysis of Hydrogen Production through a Two-Step Chemical Regenerative Coal Gasification |
title_full_unstemmed |
Experimental Study and Thermodynamic Analysis of Hydrogen Production through a Two-Step Chemical Regenerative Coal Gasification |
title_sort |
experimental study and thermodynamic analysis of hydrogen production through a two-step chemical regenerative coal gasification |
publisher |
MDPI AG |
series |
Applied Sciences |
issn |
2076-3417 |
publishDate |
2019-07-01 |
description |
Hydrogen, as a strategy clean fuel, is receiving more and more attention recently in China, in addition to the policy emphasis on H<sub>2</sub>. In this work, we conceive of a hydrogen production process based on a chemical regenerative coal gasification. Instead of using a lumped coal gasification as is traditional in the H<sub>2</sub> production process, herein we used a two-step gasification process that included coking and char-steam gasification. The sensible heat of syngas accounted for 15−20% of the total energy of coal and was recovered and converted into chemical energy of syngas through thermochemical reactions. Moreover, the air separation unit was eliminated due to the adoption of steam as oxidant. As a result, the efficiency of coal to H<sub>2</sub> was enhanced from 58.9% in traditional plant to 71.6% in the novel process. Further, the energy consumption decreased from 183.8 MJ/kg in the traditional plant to 151.2 MJ/kg in the novel process. The components of syngas, H<sub>2</sub>, and efficiency of gasification are herein investigated through experiments in fixed bed reactors. Thermodynamic performance is presented for both traditional and novel coal to hydrogen plants. |
topic |
hydrogen production gasification thermodynamic analysis fixed bed reactor |
url |
https://www.mdpi.com/2076-3417/9/15/3035 |
work_keys_str_mv |
AT weili experimentalstudyandthermodynamicanalysisofhydrogenproductionthroughatwostepchemicalregenerativecoalgasification AT songhe experimentalstudyandthermodynamicanalysisofhydrogenproductionthroughatwostepchemicalregenerativecoalgasification AT shengli experimentalstudyandthermodynamicanalysisofhydrogenproductionthroughatwostepchemicalregenerativecoalgasification |
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