An efficient green route for hexamethylene-1,6-diisocyanate synthesis by thermal decomposition of hexamethylene-1,6-dicarbamate over Co3O4/ZSM-5 catalyst: An indirect utilization of CO2
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An efficient green route for hexamethylene-1,6-diisocyanate synthesis by thermal decomposition of hexamethylene-1,6-dicarbamate over Co3O4/ZSM-5 catalyst: An indirect utilization of CO2
An efficient green route for hexamethylene-1,6-diisocyanate synthesis by thermal decomposition of hexamethylene-1,6-dicarbamate over Co3O4/ZSM-5 catalyst: An indirect utilization of CO2
中国化学工程学报(英文版)2017年25卷第12期 页码:1760-1770
Affiliations:
University of Chinese Academy of Sciences,Beijing,China,100049
Muhammad Ammar, Yan Cao, Peng He, 等. An efficient green route for hexamethylene-1,6-diisocyanate synthesis by thermal decomposition of hexamethylene-1,6-dicarbamate over Co3O4/ZSM-5 catalyst: An indirect utilization of CO2[J]. 中国化学工程学报(英文版), 2017,25(12):1760-1770. DOI: 10.1016/j.cjche.2017.03.032.
O
Muhammad Ammar, Yan Cao, Peng He, 等. An efficient green route for hexamethylene-1,6-diisocyanate synthesis by thermal decomposition of hexamethylene-1,6-dicarbamate over Co3O4/ZSM-5 catalyst: An indirect utilization of CO2[J]. 中国化学工程学报(英文版), 2017,25(12):1760-1770. DOI: 10.1016/j.cjche.2017.03.032.DOI:
An efficient green route for hexamethylene-1,6-diisocyanate synthesis by thermal decomposition of hexamethylene-1,6-dicarbamate over Co3O4/ZSM-5 catalyst: An indirect utilization of CO2
as rawmaterial for chemical synthesis has the potential for substantial economic and green benefits. Thermal decomposition of hexamethylene-1
6-dicarbamate (HDC) is a promising approach for indirect utilization of CO
2
to produce hexamethylene-1
6-diisocyanate (HDI). In this work
a green route was developed for the synthesis of HDI by thermal decomposition of HDC over Co
3
O
4
/ZSM-5 catalyst
using chlorobenzene as lowboiling point solvent. Different metal oxide supported catalysts were prepared by incipientwetness impregnation (IWI)
PEG-additive (PEG) and deposition precipitation with ammonia evaporation (DP) methods. Their catalytic performances for the thermal decomposition of HDC were tested. The catalyst screening results showed that Co
3
O
4
/ZSM-5
25
catalysts prepared by different methods showed different performances in the order of Co
3
O
4
/ZSM-5
25(PEG)
N Co
3
O
4
/ZSM-5
25(IWI)
N Co
3
O
4
/ZSM-5
25(DP)
. The physicochemical pr
operties of Co
3
O
4
/ZSM- 5
25
catalyst were characterized by XRD
FTIR
N
2
adsorption-desorption measurements
NH
3
-TPD and XPS. The superior catalytic performance of Co
3
O
4
/ZSM-5
25(PEG)
catalyst was attributed to its relative surface content of Co
3+
surface lattice oxygen content and total acidity. Under the optimized reaction conditions: 6.5% HDC concentration in chlorobenzene
1 wt% Co
3
O
4
/ZSM-5
25(PEG)
catalyst
250 ℃ temperature
2.5 h time
800 ml·min-1 nitrogen flow rate and 1.0 MPa pressure
the HDC conversion and HDI yield could reach 100% and 92.8% respectively. The Co
3
O
4
/ZSM-5
25(PEG)
catalyst could be facilely separated from the reaction mixture
and reused without degradation in catalytic performance. Furthermore
a possible reaction mechanism was proposed based on the physicochemical properties of the Co
3
O
4
/ZSM-5
25
catalysts.
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相关作者
liguo Wang
Huiquan Li
Peng He
Ammar Muhammad
Yafang Chi
Yan Cao
Zhibing Zhang
Bowen Jiang
相关机构
3 University of Chinese Academy of Sciences
2 National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of Sciences
School of Chemistry and Chemical Engineering, Nanjing University
State Key Laboratory of Chemical Engineering, School of Chemical Engineering and Technology, Tianjin University
The Co-Innovation Center of Chemistry and Chemical Engineering of Tianjin