Loker Hydrocarbon Research Institute and Department of Chemistry, University of Southern California , University Park, Los Angeles, California 90089-1661, United States.
J Am Chem Soc. 2018 Feb 7;140(5):1580-1583. doi: 10.1021/jacs.7b12183. Epub 2018 Jan 24.
Herein we report an efficient and recyclable system for tandem CO capture and hydrogenation to methanol. After capture in an aqueous amine solution, CO is hydrogenated in high yield to CHOH (>90%) in a biphasic 2-MTHF/water system, which also allows for easy separation and recycling of the amine and catalyst for multiple reaction cycles. Between cycles, the produced methanol can be conveniently removed in vacuo. Employing this strategy, catalyst Ru-MACHO-BH and polyamine PEHA were recycled three times with 87% of the methanol producibility of the first cycle retained, along with 95% of catalyst activity after four cycles. CO from dilute sources such as air can also be converted to CHOH using this route. We postulate that the CO capture and hydrogenation to methanol system presented here could be an important step toward the implementation of the carbon neutral methanol economy concept.
在这里,我们报告了一种用于串联 CO 捕获和加氢制甲醇的高效、可回收系统。在水性胺溶液中捕获 CO 后,在两相 2-MTHF/水体系中以高收率(>90%)将 CO 加氢转化为 CHOH,这也允许胺和催化剂的轻松分离和循环使用,进行多个反应循环。在循环之间,可以在真空中方便地去除生成的甲醇。采用这种策略,Ru-MACHO-BH 催化剂和多胺 PEHA 可以循环使用三次,保留了第一个循环中 87%的甲醇产率,并且在四个循环后保留了 95%的催化剂活性。空气中等稀释源的 CO 也可以通过这种途径转化为 CHOH。我们推测,这里提出的 CO 捕获和加氢制甲醇系统可能是实现碳中和甲醇经济概念的重要一步。