TY - JOUR
T1 - Integration of ammonia synthesis gas production and N2O decomposition into a membrane reactor
AU - Zhang, Xiaochen
AU - Li, Chaoqun
AU - He, Zhenyu
AU - Han, Te
N1 - Publisher Copyright:
© 2020 American Chemical Society.
PY - 2021/2/24
Y1 - 2021/2/24
N2 - H2/N2 synthesis gas is of great importance for the ammonia industry, and its production process is both complex and energy consuming. Nitrous oxide (N2O) is a potent greenhouse gas (GHG) that also depletes the stratospheric ozone. Here, we propose a novel concept of a membrane reactor in which ammonia synthesis gas production, N2O decomposition, and water splitting are combined. In this process, oxygen produced from N2O decomposition and water splitting is removed by a dense oxygen permeable membrane, which then reacts with oxygen-consuming gas. This promising membrane reactor process has been successfully demonstrated by experiment. By optimizing the N2O and H2O flow rate, a complete N2O decomposition is achieved, and a synthesis gas with a molar ratio of H2/N2 = 3:1 is produced at the same time. At 850 °C, a H2 production rate of 14.85 mL/min and a N2 production rate of 5.07 mL/min are derived from the membrane reactor with 100% N2O conversion and 29.60% H2O conversion. The reactor also exhibits excellent stability over a 300 h long-term test. This study will give some constructive guides to the subsequent work on process intensification through the membrane reactor and may lead to the development of green chemical production.
AB - H2/N2 synthesis gas is of great importance for the ammonia industry, and its production process is both complex and energy consuming. Nitrous oxide (N2O) is a potent greenhouse gas (GHG) that also depletes the stratospheric ozone. Here, we propose a novel concept of a membrane reactor in which ammonia synthesis gas production, N2O decomposition, and water splitting are combined. In this process, oxygen produced from N2O decomposition and water splitting is removed by a dense oxygen permeable membrane, which then reacts with oxygen-consuming gas. This promising membrane reactor process has been successfully demonstrated by experiment. By optimizing the N2O and H2O flow rate, a complete N2O decomposition is achieved, and a synthesis gas with a molar ratio of H2/N2 = 3:1 is produced at the same time. At 850 °C, a H2 production rate of 14.85 mL/min and a N2 production rate of 5.07 mL/min are derived from the membrane reactor with 100% N2O conversion and 29.60% H2O conversion. The reactor also exhibits excellent stability over a 300 h long-term test. This study will give some constructive guides to the subsequent work on process intensification through the membrane reactor and may lead to the development of green chemical production.
UR - http://www.scopus.com/inward/record.url?scp=85096392149&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.0c04015
DO - 10.1021/acs.iecr.0c04015
M3 - Article
AN - SCOPUS:85096392149
SN - 0888-5885
VL - 60
SP - 3066
EP - 3072
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 7
ER -