Membrane Reactor Supported by MXene (Ti3C2T X ) for Hydrogen Production by Ammonia Decomposition

被引:11
|
作者
Wu, Chengliang [1 ]
Jin, Yun [1 ]
Fan, Yiyi [1 ]
Wong, Ngie Hing [2 ]
Sunarso, Jaka [2 ]
Meng, Xiuxia [1 ]
Yang, Naitao [1 ]
机构
[1] Shandong Univ Technol, Sch Chem & Chem Engn, Zibo 255049, Peoples R China
[2] Swinburne Univ Technol, Fac Engn Comp & Sci, Res Ctr Sustainable Technol, Kuching 93350, Sarawak, Malaysia
基金
中国国家自然科学基金;
关键词
FUEL-CELL; CATALYST; STORAGE; HYBRID;
D O I
10.1021/acs.energyfuels.3c01348
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Hydrogen (H-2) production by ammonia (NH3)decomposition offers a solution to the energy problem. In this work,an MXene (titanium carbide, Ti3C2T (X) ) membrane was successfully synthesized by depositingit onto the anodic aluminum oxide (AAO) substrate using vacuum-assistedfiltration. Then, a membrane reactor supported by MXene was developedfor H-2 production by NH3 decomposition. TheMXene membrane reactor could achieve an H-2 permeance of2.85 x 10(-7) mol m(-2) s(-1) Pa-1 and an H-2/N-2 selectivity of 20 at 773.15 K. Next, a Ni-La/& gamma;-Al2O3 catalyst prepared by impregnation and sinteringwas added to catalyze the NH3 decomposition process. Theexperimental results showed that the reactor could achieve a 99% NH3 conversion at 773.15 K, i.e., 9% higher than that of thepacked catalytic reactor (without membrane). A mathematical modelof the membrane reactor was developed to explain the experimentalresults. The calculated activation energies (E (ad)) of the MXene membrane for H-2 and N-2 permeances were 64.95 and 69.53 kJ mol(-1), respectively.The activation energy (E (ar)) of NH3 decomposition was 147.8 kJ mol(-1). Boththe experimental and modeling results showed that the membrane reactorcould enhance NH3 conversion and promote the productionof high-purity H-2.
引用
收藏
页码:9760 / 9769
页数:10
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