Mixed-Integer Linear Programming (MILP) Approach for the Synthesis of Efficient Power-to-Syngas Processes
Within the context of energy transition scenarios toward renewable resources, superstructure optimization is implemented for the synthesis of sustainable and efficient Power-to-Syngas processes. A large number of reactors (reverse water-gas-shift, steam reforming, dry reforming, tri-reforming, metha...
Main Authors: | , , |
---|---|
Format: | Article |
Language: | English |
Published: |
Frontiers Media S.A.
2020-09-01
|
Series: | Frontiers in Energy Research |
Subjects: | |
Online Access: | https://www.frontiersin.org/article/10.3389/fenrg.2020.00161/full |
id |
doaj-0dbfd5a061d449d2842137a63ef15c25 |
---|---|
record_format |
Article |
spelling |
doaj-0dbfd5a061d449d2842137a63ef15c252020-11-25T01:23:06ZengFrontiers Media S.A.Frontiers in Energy Research2296-598X2020-09-01810.3389/fenrg.2020.00161549457Mixed-Integer Linear Programming (MILP) Approach for the Synthesis of Efficient Power-to-Syngas ProcessesAndrea Maggi0Marcus Wenzel1Kai Sundmacher2Kai Sundmacher3Department for Process Systems Engineering, Max-Planck-Institute for Dynamics of Complex Technical Systems, Magdeburg, GermanyDepartment for Process Systems Engineering, Max-Planck-Institute for Dynamics of Complex Technical Systems, Magdeburg, GermanyDepartment for Process Systems Engineering, Max-Planck-Institute for Dynamics of Complex Technical Systems, Magdeburg, GermanyDepartment for Process Systems Engineering, Otto-von-Guericke University, Magdeburg, GermanyWithin the context of energy transition scenarios toward renewable resources, superstructure optimization is implemented for the synthesis of sustainable and efficient Power-to-Syngas processes. A large number of reactors (reverse water-gas-shift, steam reforming, dry reforming, tri-reforming, methane partial oxidation reactor, and water electrolyzer) and separators (PSA, TSA, cryogenics, membranes, and gas-liquid scrubbing) are included within a single MILP framework, accounting for typical operating conditions of each process-unit, under the specified simplifying assumptions. Power is minimized in the context of sustainable feedstocks: water and biogas or carbon dioxide from direct air-capture. The objective function adds the thermal to the electrical contribution to the total power, the latter being weighted by a pseudo-price of null (i.e., sustainable, in-house electricity production), or unitary value (i.e., electricity purchased, possibly generated from non-sustainable sources). Simultaneous operations of multiple reactor technologies are allowed to identify possible synergies. With biogas and null value of the pseudo-price, the results identify plant configurations mainly run via electricity, which constitutes up to 97% of the total power for co-operating partial oxidation of methane and water electrolysis. Alternatively, lower total demands are attained at the expenses of thermal duty when electricity is penalized: the endothermic reactors are operated. With carbon dioxide, the total power demand dramatically increases due to the large consumptions of direct-air capture and water electrolysis. The resulting topologies always favor membrane separation, adsorption, and cryogenics over absorption technologies.https://www.frontiersin.org/article/10.3389/fenrg.2020.00161/fullsustainabilitysyngassuperstructurebiogasCO2 utilizationPower-to-X |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Andrea Maggi Marcus Wenzel Kai Sundmacher Kai Sundmacher |
spellingShingle |
Andrea Maggi Marcus Wenzel Kai Sundmacher Kai Sundmacher Mixed-Integer Linear Programming (MILP) Approach for the Synthesis of Efficient Power-to-Syngas Processes Frontiers in Energy Research sustainability syngas superstructure biogas CO2 utilization Power-to-X |
author_facet |
Andrea Maggi Marcus Wenzel Kai Sundmacher Kai Sundmacher |
author_sort |
Andrea Maggi |
title |
Mixed-Integer Linear Programming (MILP) Approach for the Synthesis of Efficient Power-to-Syngas Processes |
title_short |
Mixed-Integer Linear Programming (MILP) Approach for the Synthesis of Efficient Power-to-Syngas Processes |
title_full |
Mixed-Integer Linear Programming (MILP) Approach for the Synthesis of Efficient Power-to-Syngas Processes |
title_fullStr |
Mixed-Integer Linear Programming (MILP) Approach for the Synthesis of Efficient Power-to-Syngas Processes |
title_full_unstemmed |
Mixed-Integer Linear Programming (MILP) Approach for the Synthesis of Efficient Power-to-Syngas Processes |
title_sort |
mixed-integer linear programming (milp) approach for the synthesis of efficient power-to-syngas processes |
publisher |
Frontiers Media S.A. |
series |
Frontiers in Energy Research |
issn |
2296-598X |
publishDate |
2020-09-01 |
description |
Within the context of energy transition scenarios toward renewable resources, superstructure optimization is implemented for the synthesis of sustainable and efficient Power-to-Syngas processes. A large number of reactors (reverse water-gas-shift, steam reforming, dry reforming, tri-reforming, methane partial oxidation reactor, and water electrolyzer) and separators (PSA, TSA, cryogenics, membranes, and gas-liquid scrubbing) are included within a single MILP framework, accounting for typical operating conditions of each process-unit, under the specified simplifying assumptions. Power is minimized in the context of sustainable feedstocks: water and biogas or carbon dioxide from direct air-capture. The objective function adds the thermal to the electrical contribution to the total power, the latter being weighted by a pseudo-price of null (i.e., sustainable, in-house electricity production), or unitary value (i.e., electricity purchased, possibly generated from non-sustainable sources). Simultaneous operations of multiple reactor technologies are allowed to identify possible synergies. With biogas and null value of the pseudo-price, the results identify plant configurations mainly run via electricity, which constitutes up to 97% of the total power for co-operating partial oxidation of methane and water electrolysis. Alternatively, lower total demands are attained at the expenses of thermal duty when electricity is penalized: the endothermic reactors are operated. With carbon dioxide, the total power demand dramatically increases due to the large consumptions of direct-air capture and water electrolysis. The resulting topologies always favor membrane separation, adsorption, and cryogenics over absorption technologies. |
topic |
sustainability syngas superstructure biogas CO2 utilization Power-to-X |
url |
https://www.frontiersin.org/article/10.3389/fenrg.2020.00161/full |
work_keys_str_mv |
AT andreamaggi mixedintegerlinearprogrammingmilpapproachforthesynthesisofefficientpowertosyngasprocesses AT marcuswenzel mixedintegerlinearprogrammingmilpapproachforthesynthesisofefficientpowertosyngasprocesses AT kaisundmacher mixedintegerlinearprogrammingmilpapproachforthesynthesisofefficientpowertosyngasprocesses AT kaisundmacher mixedintegerlinearprogrammingmilpapproachforthesynthesisofefficientpowertosyngasprocesses |
_version_ |
1725123459728539648 |