Table 3.
Pre-treatment methods for lignocellulosic biomass conversion to bio-based products advantage and disadvantages as adapted from Cheah et al. [66].
| Treatment method | Cost | Toxic byproducts | Range of biomass applicable | Advantage/disadvantages |
|---|---|---|---|---|
| Acid pre-treatment | √ | x | √ | Inhibitors limited by dilute acid use |
| Freezing | √ | √ | x | Freezing/thawing cycles |
| Milling | √ | √ | √ | Used for bioethanol and biogas production |
| Liquid hot water | √ | √ | x | High water and energy inputs |
| Organic solvent (Organosolv) | x | x | √ | Low boiling point of the solvent. Solvent recycling is required |
| Oxidation | x | √ | √ | High cost of ozone generation. Ozone handling is required |
| Steam explosion | x | x | √ | High cost of steam generation |
| Extruction | √ | √ | √ | Hydrolysis efficiency is improved |
| Wet oxidation | x | √ | x | Less water use as no washing is required |
| CO2 explosion | x | √ | √ | High cost for pressure maintenance |
| Microwave irradiation | x | √ | √ | More effective than conventional heating |
| Ultrasound | x | √ | √ | Low temperature and time required |
| Ammonium fiber expansion | x | √ | √ | Less effective for biomass with high lignin contents |
| Ionic liquid | x | √ | √ | Stability and reuse. Instability may cause contamination |
| Biological pre-treatment | √ | √ | √ | Increases delignification. Able to reduce polymerisation |
| Hydrothermal liquefaction | x | √ | √ | Lignocellulosic materials are depolymerised into bio-oil, biogas, biochar and water-soluble compounds |