Process Intensification Strategies for Power-to-X Technologies

被引:18
作者
Cholewa, Thomas [1 ,2 ]
Semmel, Malte [1 ]
Mantei, Franz [1 ]
Guettel, Robert [2 ]
Salem, Ouda [1 ]
机构
[1] Fraunhofer Inst Solar Energy Syst ISE, Heidenhofstr 2, D-79110 Freiburg, Germany
[2] Ulm Univ, Inst Chem Engn, Albert Einstein Allee 11, D-89081 Ulm, Germany
关键词
process intensification; Power-to-X; process integration; dimethyl ether; oxymethylene ether; ammonia; reactive distillation; adsorptive separation; OXYMETHYLENE-DIMETHYL ETHER; LIQUID-LIQUID EQUILIBRIUM; SITU WATER REMOVAL; AMMONIA-SYNTHESIS; FUEL; METHANOL; STORAGE; DEHYDROGENATION; EFFICIENCY; OXIDATION;
D O I
10.3390/chemengineering6010013
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Sector coupling remains a crucial measure to achieve climate change mitigation targets. Hydrogen and Power-to-X (PtX) products are recognized as major levers to allow the boosting of renewable energy capacities and the consequent use of green electrons in different sectors. In this work, the challenges presented by the PtX processes are addressed and different process intensification (PI) strategies and their potential to overcome these challenges are reviewed for ammonia (NH3), dimethyl ether (DME) and oxymethylene dimethyl ethers (OME) as three exemplary, major PtX products. PI approaches in this context offer on the one hand the maximum utilization of valuable renewable feedstock and on the other hand simpler production processes. For the three discussed processes a compelling strategy for efficient and ultimately maintenance-free chemical synthesis is presented by integrating unit operations to overcome thermodynamic limitations, and in best cases eliminate the recycle loops. The proposed intensification processes offer a significant reduction of energy consumption and provide an interesting perspective for the future development of PtX technologies.
引用
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页数:18
相关论文
共 97 条
[1]   Ammonia-fed fuel cells: a comprehensive review [J].
Afif, Ahmed ;
Radenahmad, Nikdalila ;
Cheok, Quentin ;
Shams, Shahriar ;
Kim, Jung H. ;
Azad, Abul K. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2016, 60 :822-835
[2]   MULTIFUNCTIONAL REACTORS FOR HETEROGENEOUS CATALYSIS [J].
AGAR, DW ;
RUPPEL, W .
CHEMIE INGENIEUR TECHNIK, 1988, 60 (10) :731-741
[3]   ACTIVATION OF NITROGEN BY ALKALI-METAL PROMOTED TRANSITION-METAL .1. AMMONIA SYNTHESIS OVER RUTHENIUM PROMOTED BY ALKALI-METAL [J].
AIKA, K ;
OZAKI, A ;
HORI, H .
JOURNAL OF CATALYSIS, 1972, 27 (03) :424-&
[4]  
Allan R. P., 2021, IPCC, 2021: Summary for Policymakers
[5]  
An W., 2008, J CHEM ENG, V82, p948 955, DOI [10.1002/cjce.5450820510, DOI 10.1002/CJCE.5450820510]
[6]  
[Anonymous], 2003, ANGEW CHE, DOI [10.1002/ange.200301553, DOI 10.1002/ANGE.200301553]
[7]  
Ayvali T, 2021, JOHNSON MATTHEY TECH, V65, P275, DOI 10.1595/205651321X16043240667033
[8]   Dimethyl ether: A review of technologies and production challenges [J].
Azizi, Zoha ;
Rezaeimanesh, Mohsen ;
Tohidian, Tahere ;
Rahimpour, Mohammad Reza .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2014, 82 :150-172
[9]   Hydrolyzed polyoxymethylenedimethylethers as liquid fuels for direct oxidation fuel cells [J].
Baranton, Steve ;
Uchida, Hiroyuki ;
Tryk, Donald A. ;
Dubois, Jean Luc ;
Watanabe, Masahiro .
ELECTROCHIMICA ACTA, 2013, 108 :350-355
[10]   Optimal design of intensified processes for DME synthesis [J].
Bildea, Costin Sorin ;
Gyorgy, Romuald ;
Brunchi, Cristian C. ;
Kiss, Anton A. .
COMPUTERS & CHEMICAL ENGINEERING, 2017, 105 :142-151