Abstract
Hydrocarbons and methanol are considered the preferred products of catalytic reduction of CO derived from clean natural gas. Atom-economical synthesis of methanol catalyzed by soluble transition metal complexes as single-site catalyst precursors was studied under mild reaction conditions. Methanol could be effectively synthesized at low temperatures (≤ 150°C) using the complexed Ni/alkali metal alkoxide/methanol/glyme catalyst system with high turnover numbers. The low operating temperature fell in the range where high conversion (> 90%) per pass of synthesis gas to methanol is thermodynamically allowed under a low operating pressure (< 5 MPa). The Ni system provided an excellent opportunity to establish a time-resolved structure/activity/product selectivity relationship under mild conditions. The base-activated Ni system achieved high per pass CO conversion and high methanol selectivity that together impart atom-economy to the methanol synthesis reaction. The atom-economy combined with observed high turnover numbers might result in a process that produces methanol cheaply enough to be considered as a feedstock.
| Original language | English |
|---|---|
| Pages (from-to) | 209-214 |
| Number of pages | 6 |
| Journal | Topics in Catalysis |
| Volume | 32 |
| Issue number | 3-4 |
| DOIs | |
| State | Published - Mar 2005 |
Keywords
- Atom-economical catalysis
- Carbon monoxide reduction
- Hydrogenation
- Methanol synthesis
- Single-site catalyst
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