Department of Chemical Engineering and Biochemical Engineering, College of Chemistry and Chemical Engineering, Xiamen University, Xiamen 361005, Fujian, China.
Bioresour Technol. 2012 Apr;110:676-81. doi: 10.1016/j.biortech.2012.01.124. Epub 2012 Jan 31.
Biomass char, by-product of Dunaliella salina pyrolysis at a final pyrolysis temperature of 500°C, was used as feedstock material in this study. The reactions of biomass char with CO(2) were performed in a fixed-bed reactor to evaluate the effect of temperature and steam on the CO(2) conversion, CO yield and gas composition. The CO(2) conversion and CO yield without steam and catalyst reached about 61.84% and 0.99mol/(mol CO(2)) at 800°C, respectively. Steam and high temperature led to high CO(2) conversion. A new approach for improving H(2) was carried out by using biomass char and Au/Al(2)O(3) catalyst, which combined steam gasification of biomass char and water gas shift reaction, and the H(2) concentration was 1.8 times higher than without catalyst. The process not only mitigated CO(2) emission and made use of residual biomass char, but also created renewable source.
在最终热解温度为 500°C 的条件下,利用杜氏盐藻热解的副产物生物质焦作为原料进行研究。在固定床反应器中进行生物质焦与 CO(2)的反应,以评估温度和蒸汽对 CO(2)转化率、CO 产率和气体成分的影响。在没有蒸汽和催化剂的情况下,反应温度为 800°C 时,CO(2)转化率和 CO 产率分别约为 61.84%和 0.99mol/(mol CO(2))。蒸汽和高温导致 CO(2)转化率提高。通过使用生物质焦和 Au/Al(2)O(3)催化剂,采用生物质焦的水蒸气气化和水煤气变换反应的新方法,提高了 H(2)浓度,比没有催化剂时提高了 1.8 倍。该工艺不仅减少了 CO(2)的排放,利用了剩余的生物质焦,还创造了可再生能源。