Progress in (catalytic) pyrolysis of industrial lignin from 2015 to 2021a.
| Raw material | Lignin type | Reactor type | Reaction temperature (°C) | Yield (wt%) | Main products after degradation | Ref. |
|---|---|---|---|---|---|---|
| Corncob residue | OL | Fixed bed reactor | 350 | 16.2 (Monomer) | H, MV | 53 |
| Cork | AL | Fixed bed reactor | 650 | 54 (Bio-oil) | Aromatics | 54 |
| Douglas fir, radial pine | AL | Vertical pyrolysis furnace | 600 | 5.02 (Monomer) | P, C | 55 |
| Corn cob | HL | 20.48 (Monomer) | ||||
| — | AL | Microwave reactor | — | 3.36 (±0.40) | P | 56 |
| 0.51 | C | |||||
| 1.84 | Methoxyphenol | |||||
| 0.50 (±0.04) | BTEXS | |||||
| — | AL | Pyrolysis gas chromatography/mass spectrometry | 800 | 51.39 (Monomer) | P, C, dimethylphenol | 57 |
| 20.83 (Monomer) | ||||||
| 18.01 (Monomer) | ||||||
| Corn straw | AL | Fixed bed reactor | 450 | 29 (Bio-oil) | H, MV | 58 |
| Radial pine | AL | Fluidized bed reactor | 475 | 4.3 (Monomer) | G, eugenol | 59 |
| 525 | 6.8 (Monomer) | Alkylphenol, C | ||||
| 575 | 12.0 (Monomer) | Aromatics | ||||
| Maple | AHL | Pyrolysis gas chromatography/mass spectrometry | 550 | 17.87 | D | 60 |
| 650 | 14.47 | |||||
| 550 | 13.05 | Isoeugenol | ||||
| 650 | 14.14 | |||||
| Straw | 800 | 8.87 | T | |||
| 900 | 8.55 | |||||
| Rice husk | 800 | 7.73 | T | |||
| 900 | 9.47 | |||||
| — | KL | Fixed bed reactor | 500 | ∼32 (Bio-oil) | Alkylphenol, aromatics, BTEX | 61 |
| 600 | Selectivity 14.56 | BTEX | ||||
| Selectivity 13.35 | Other aromatics, etc. | |||||
| Birch and poplar mixed | — | Fixed bed reactor | 500 | 15.29 (Monomer) | Phenolic aromatic hydrocarbon | 62 |
| Eucalyptus | 12.57 (Monomer) | |||||
| Black liquor | AL | Fixed bed reactor | 600 | 20.34 (Bio-oil) | Monomer aromatics, polycyclic aromatic hydrocarbons, phenols | 63 |
| Corn cob | AHL | Fixed bed reactor | 550 | 28.30 | B, T, xylene | 64 |
HL: hydrolyzed lignin.