ChemSusChem. 2014 Mar;7(3):785-94. doi: 10.1002/cssc.201301181.
Carbon dioxide hydrogenation to form hydrocarbons was conducted on two iron-based catalysts, prepared according to procedures described in the literature, and on a new iron spinel catalyst. The CO2 conversion measured in a packed-bed reactor was limited to about 60% because of excessive amounts of water produced in this process. Switching to a system of three packed-bed reactors in series with interim removal of water and condensed hydrocarbons increased CO2 conversion to as much as 89%. The pure spinel catalyst displayed a significantly higher activity and selectivity than those of the other iron catalysts. This process produces a product called green feed, which is similar in composition to the product of a high-temperature, iron-based Fischer–Tropsch process from syngas. The green feed can be readily converted into renewable fuels by well-established technologies.
二氧化碳加氢转化为烃类在两种铁基催化剂上进行,这两种催化剂是按照文献中描述的程序制备的,同时还在一种新型铁尖晶石催化剂上进行了实验。在填充床反应器中测量的 CO2 转化率由于该过程中产生了大量的水而被限制在约 60%。切换到三个填充床反应器串联的系统,中间去除水和冷凝烃类,可以将 CO2 转化率提高到 89%。纯尖晶石催化剂的活性和选择性明显高于其他铁基催化剂。该工艺生产的产品称为绿色原料,其组成与高温铁基费托合成工艺从合成气生产的产品相似。绿色原料可以通过成熟的技术很容易地转化为可再生燃料。