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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Main Authors: Wei Li, Song He, Sheng Li
Format: Article
Language:English
Published: MDPI AG 2019-07-01
Series:Applied Sciences
Subjects:
Online Access:https://www.mdpi.com/2076-3417/9/15/3035
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spelling 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&#8722;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&#8722;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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