2Hydrothermal CO2 conversion using zinc as reductant: Batch reaction, modeling and parametric analysisof the process

被引:19
作者
Roman-Gonzalez, Daniel [1 ,4 ]
Moro, Alberto [1 ]
Burgoa, Fernando [1 ]
Perez, Eduardo [2 ]
Nieto-Marquez, Antonio [3 ]
Martin, Angel [1 ,4 ]
Dolores Bermejo, M. [1 ,4 ]
机构
[1] Univ Valladolid, Dept Chem Engn & Environm Technol, High Pressure Proc Grp, Valladolid, Spain
[2] Univ Valladolid, TERMOCAL Res Grp, Thermodynam & Calibrat, Escuela Ingn Ind, Paseo Cauce 59, E-47011 Valladolid, Spain
[3] UPM, ETSIDI, Dept Mech Chem & Ind Design Engn, Madrid, Spain
[4] Univ Valladolid, Inst BioEcon BioEcoUVa, Valladolid, Spain
关键词
CO2; reduction; Hydrothermal; Zinc; Modeling; Formic acid; Batch; CARBON-DIOXIDE; HYDROTHERMAL CONDITIONS; FORMIC-ACID; METHANOL; FUELS; WATER;
D O I
10.1016/j.supflu.2018.07.003
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Hydrothermal CO2 reduction using Zn as reductant was investigated. This process has the advantage of avoiding the use of hydrogen with all its safety and environmental concerns, and allows an easy integration with CO2 capture as NaHCO3. In this work, this reaction was studied in batch reactors at temperatures from 275 to 325 degrees C. Conversions up to 60% were obtained with 100% selectivity towards formic acid, at reaction times between 10 and 180 min. A mathematical model correlated with data from literature was developed and is able to correctly predict both experimental and literature data with an averaged error of 3.5%. Main variables of the process were analyzed: temperature, Zn/HCO3- ratio, heating rate, Zn particle size, pressure, etc. The optimum reaction conditions found were 300 degrees C with a rapid heating, and particle sizes of 10 mu m. Zn excess dramatically improves the yield, but a lower excess can be compensated at high pressures.
引用
收藏
页码:320 / 328
页数:9
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