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@ARTICLE{Li:878078,
author = {Li, Jiarong and Lin, Jin and Heuser, Philipp and Heinrichs,
Heidi and Xiao, Jinyu and Liu, Feng and Robinius, Martin and
Song, Yonghua and Stolten, Detlef},
title = {{O}ptimal {C}onfiguration of {W}ind-to-{A}mmonia with the
{E}lectric {N}etwork and {H}ydrogen {S}upply {C}hain: {A}
{C}ase {S}tudy of {I}nner {M}ongolia},
reportid = {FZJ-2020-02620},
year = {2020},
note = {$https://www.researchgate.net/publication/342520278_Optimal_Configuration_of_Wind-to-Ammonia_with_the_Electric_Network_and_Hydrogen_Supply_Chain_A_Case_Study_of_Inner_Mongolia$},
abstract = {Description:Converting wind energy into ammonia (WtA) has
been recognized as a promising pathway to enhance the usage
of wind generation. This paper proposes a generic optimal
configuration model of WtA at the network level to minimize
the ammonia production cost by optimizing capacities and
locations of WtA facilities including wind turbines,
electrolyzers, hydrogen tanks and optimizing supply modes
among regions. Specifically, the temporal fluctuation
characteristics of wind resources, the operation flexibility
of the ammonia synthesis reactor and the transport distances
are considered. Three typical supply modes, i.e., the Local
WtA, the EN (electric network)-based WtA and the HSC
(hydrogen supply chain)-based WtA, combined with two energy
transport modes including EN and HT (Hydrogen truck
trailers) are included with the consideration of the maximal
energy transport capacity of EN and transport distance per
day of HT (500km). Real data of Inner Mongolia (a typical
province in China with rich wind resources and existing
ammonia industries) is employed to verify the effectiveness
and significance of proposed model. The effect of above
significant factors on optimal planning capacity of WtA
facilities and optimal energy transport modes is analyzed,
which provides guidelines for WtA configuration. The
economic analysis shows that the average LCOA (levelized
cost of ammonia) for WtA is approximately 0.57 euro/kg in
Inner Mongolia and comparable to that for CtA
(coal-to-ammonia, 0.41 euro/kg) with a reduction of $30\%$
in capacity cost of the facilities.},
cin = {IEK-3},
cid = {I:(DE-Juel1)IEK-3-20101013},
pnm = {134 - Electrolysis and Hydrogen (POF3-134)},
pid = {G:(DE-HGF)POF3-134},
typ = {PUB:(DE-HGF)25},
url = {https://juser.fz-juelich.de/record/878078},
}