Abstract
Hydrogenation of CO2 to formic acid (HCO2H) and methanol (MeOH) provides access to valuable products in a low-carbon economy. The development of effective processes for the production of pure HCO2H is still in progress. Hydrogenation of CO2 to MeOH is thermodynamically much more favorable (DG= 9.5 kJ/mole). However, homogeneous catalysts were kinetically not capable of reducing CO2 to MeOH until recently. In the MeOH process, the first organometallic catalyst being capable of the CO2 reduction to MeOH is immobilized in a stationary ionic liquid (IL) phase. The MeOH formed is continuously stripped from the IL phase by excess reaction gases.
| Original language | English |
|---|---|
| Pages (from-to) | 1428 |
| Journal | Chemie Ingenieur Technik |
| Volume | 86 |
| Issue number | 9 |
| Early online date | 28 Aug 2014 |
| DOIs | |
| Publication status | Published - Sep 2014 |
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Continuous-flow hydrogenation of CO2 using molecular catalysts. / Wesselbaum, S.; Vom Stein, T.; Hintermair, U.; Klankermayer, J.; Leitner, W.
In: Chemie Ingenieur Technik, Vol. 86, No. 9, 09.2014, p. 1428.Research output: Contribution to journal › Article
}
TY - JOUR
T1 - Continuous-flow hydrogenation of CO2 using molecular catalysts
AU - Wesselbaum, S.
AU - Vom Stein, T.
AU - Hintermair, U.
AU - Klankermayer, J.
AU - Leitner, W.
PY - 2014/9
Y1 - 2014/9
N2 - Hydrogenation of CO2 to formic acid (HCO2H) and methanol (MeOH) provides access to valuable products in a low-carbon economy. The development of effective processes for the production of pure HCO2H is still in progress. Hydrogenation of CO2 to MeOH is thermodynamically much more favorable (DG= 9.5 kJ/mole). However, homogeneous catalysts were kinetically not capable of reducing CO2 to MeOH until recently. In the MeOH process, the first organometallic catalyst being capable of the CO2 reduction to MeOH is immobilized in a stationary ionic liquid (IL) phase. The MeOH formed is continuously stripped from the IL phase by excess reaction gases.
AB - Hydrogenation of CO2 to formic acid (HCO2H) and methanol (MeOH) provides access to valuable products in a low-carbon economy. The development of effective processes for the production of pure HCO2H is still in progress. Hydrogenation of CO2 to MeOH is thermodynamically much more favorable (DG= 9.5 kJ/mole). However, homogeneous catalysts were kinetically not capable of reducing CO2 to MeOH until recently. In the MeOH process, the first organometallic catalyst being capable of the CO2 reduction to MeOH is immobilized in a stationary ionic liquid (IL) phase. The MeOH formed is continuously stripped from the IL phase by excess reaction gases.
UR - http://www.scopus.com/inward/record.url?scp=84911872427&partnerID=8YFLogxK
UR - http://dx.doi.org/10.1002/cite.201450069
U2 - 10.1002/cite.201450069
DO - 10.1002/cite.201450069
M3 - Article
AN - SCOPUS:84911872427
VL - 86
SP - 1428
JO - Chemie Ingenieur Technik
JF - Chemie Ingenieur Technik
SN - 0009-286X
IS - 9
ER -