Table 1. Summary of a Selection of TMNP Catalysts Applied to CO Hydrogenation to Higher Alcohols.

catalyst	catalyst type	reaction conditions	% CO conversion (selectivity for higher alcohols)	ref
Rh–Mo–K/MWCNT	alkali-promoted BMNP	T = 593 K; p = 8.3 MPa; GHSVa = 3.6 m3 (STP)/(h kg cat) over 24 h; H2/CO molar ratio = 1	40.1 (24.6)	(124)
4.5 wt % Co–Rh–Mo–K/MWCNT	alkali-promoted TMNP		45.2 (31.4)
6.0 wt % Co–Rh–Mo–K/MWCNT			48.9 (27.8)
4.5 wt % Co–Rh–Mo–K/AC			31.2 (18.8)
6.0 wt % Co–Rh–Mo–K/AC			35.3 (15.9)
4.5 wt % Co–Rh–Mo–K/AC-Darco (microporous)	alkali-promoted TMNP	T = 603 K; p = 8.3 MPa; GHSVa = 3.6 m3 (STP)/(h kg cat) over 48 h; H2/CO molar ratio = 2	35.6 (11.7)	(125)
4.5 wt % Co–Rh–Mo–K/AC-RX3 Extra (microporous)			39.6 (12.1)
4.5 wt % Co–Rh–Mo–K/AC-Fluid Coke (mesoporous)			41.8 (12.7)
4.5 wt % Co–Rh–Mo–K/AC-CGP Super (mesoporous)			44.5 (13.1)
4.5 wt % Co–Rh–Mo–K/MWCNTs			52.4 (16.8)

^aGas hourly space velocity.