Table 2.
Conventional catalytic conversions of crude glycerol to chemicals
| Product | Pathway | Product productivity | Reference |
|---|---|---|---|
| (2,2-dimethyl-1,3-dioxolan-4-yl) methyl acetate | Oxygenate synthesized compound | NAa | [78] |
| Acrolein | Fuidized bed, tungsten doped zirconia catalyst | 21% | [79] |
| Monoglyceride | Two-step process, purification of the monoglyceride produced from glycerolysis of palm stearin | ~99% purity | [86] |
| Glycerolysis of soybean oil | ~42% | [87] | |
| Gaseous products | Steam reforming process; platinum alumina as catalyst | NAa | [80] |
| Thermal decomposition of crude glycerol by pyrolysis | NAa | [82] | |
| Steam gasification with in situ CO2 removal | 88 vol.% H2 purity | [83] | |
| Hydrothermal reforming of crude glycerol | ~90 vol.% H2 purity | [84] | |
| Co-gasification of crude glycerol and hardwood chips | NAa | [85] |
a represents data are not available