Optimisation of the Autothermal NH<sub>3</sub> Production Process for Power-to-Ammonia

The power-to-ammonia process requires flexible operation due to intermittent renewable energy supply. In this work, we analyse three-bed autothermal reactor systems for design and off-design performance for power-to-ammonia application. The five reactor systems differ in terms of inter-stage cooling...

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Main Authors: Izzat Iqbal Cheema, Ulrike Krewer
Format: Article
Language:English
Published: MDPI AG 2019-12-01
Series:Processes
Subjects:
Online Access:https://www.mdpi.com/2227-9717/8/1/38
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spelling doaj-b4197b225dcf4b44893c9a8a51ae2b962020-11-25T00:29:31ZengMDPI AGProcesses2227-97172019-12-01813810.3390/pr8010038pr8010038Optimisation of the Autothermal NH<sub>3</sub> Production Process for Power-to-AmmoniaIzzat Iqbal Cheema0Ulrike Krewer1Institute of Energy and Process Systems Engineering, Technische Universität Braunschweig, 38106 Braunschweig, GermanyInstitute of Energy and Process Systems Engineering, Technische Universität Braunschweig, 38106 Braunschweig, GermanyThe power-to-ammonia process requires flexible operation due to intermittent renewable energy supply. In this work, we analyse three-bed autothermal reactor systems for design and off-design performance for power-to-ammonia application. The five reactor systems differ in terms of inter-stage cooling methods, i.e., direct cooling by quenching (2Q), combination of indirect and direct cooling (HQ and QH) and indirect cooling (2H) with variations. At optimum nominal operation conditions, the inter-stage indirect cooling (2H) reactor systems result in the highest NH<sub>3</sub> production. For off-design performance analysis, NH<sub>3</sub> production is minimised or maximised by varying one of the following process variables at a time: inert gas, feed flow rate or H<sub>2</sub>-to-N<sub>2</sub> ratio. For each variation, the effect on H<sub>2</sub> intake, recycle stream load and recycle-to-feed ratio is also analysed. Among the three process variables, the H<sub>2</sub>-to-N<sub>2</sub> ratio provided ca. 70% lower NH<sub>3</sub> production and 70% lower H<sub>2</sub> intake than at nominal operation for all five reactor systems. Operation of autothermal reactor systems at significantly lower H<sub>2</sub> intake makes them reliable for power-to-ammonia application; as during energy outage period, shutdown can be delayed.https://www.mdpi.com/2227-9717/8/1/38haber–bosch synthesisautothermal reactor systemsflexibility analysis
collection DOAJ
language English
format Article
sources DOAJ
author Izzat Iqbal Cheema
Ulrike Krewer
spellingShingle Izzat Iqbal Cheema
Ulrike Krewer
Optimisation of the Autothermal NH<sub>3</sub> Production Process for Power-to-Ammonia
Processes
haber–bosch synthesis
autothermal reactor systems
flexibility analysis
author_facet Izzat Iqbal Cheema
Ulrike Krewer
author_sort Izzat Iqbal Cheema
title Optimisation of the Autothermal NH<sub>3</sub> Production Process for Power-to-Ammonia
title_short Optimisation of the Autothermal NH<sub>3</sub> Production Process for Power-to-Ammonia
title_full Optimisation of the Autothermal NH<sub>3</sub> Production Process for Power-to-Ammonia
title_fullStr Optimisation of the Autothermal NH<sub>3</sub> Production Process for Power-to-Ammonia
title_full_unstemmed Optimisation of the Autothermal NH<sub>3</sub> Production Process for Power-to-Ammonia
title_sort optimisation of the autothermal nh<sub>3</sub> production process for power-to-ammonia
publisher MDPI AG
series Processes
issn 2227-9717
publishDate 2019-12-01
description The power-to-ammonia process requires flexible operation due to intermittent renewable energy supply. In this work, we analyse three-bed autothermal reactor systems for design and off-design performance for power-to-ammonia application. The five reactor systems differ in terms of inter-stage cooling methods, i.e., direct cooling by quenching (2Q), combination of indirect and direct cooling (HQ and QH) and indirect cooling (2H) with variations. At optimum nominal operation conditions, the inter-stage indirect cooling (2H) reactor systems result in the highest NH<sub>3</sub> production. For off-design performance analysis, NH<sub>3</sub> production is minimised or maximised by varying one of the following process variables at a time: inert gas, feed flow rate or H<sub>2</sub>-to-N<sub>2</sub> ratio. For each variation, the effect on H<sub>2</sub> intake, recycle stream load and recycle-to-feed ratio is also analysed. Among the three process variables, the H<sub>2</sub>-to-N<sub>2</sub> ratio provided ca. 70% lower NH<sub>3</sub> production and 70% lower H<sub>2</sub> intake than at nominal operation for all five reactor systems. Operation of autothermal reactor systems at significantly lower H<sub>2</sub> intake makes them reliable for power-to-ammonia application; as during energy outage period, shutdown can be delayed.
topic haber–bosch synthesis
autothermal reactor systems
flexibility analysis
url https://www.mdpi.com/2227-9717/8/1/38
work_keys_str_mv AT izzatiqbalcheema optimisationoftheautothermalnhsub3subproductionprocessforpowertoammonia
AT ulrikekrewer optimisationoftheautothermalnhsub3subproductionprocessforpowertoammonia
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