Table 5.
Summary of kinetic models along with substrates used, parameters used and key highlights.
| Sr. No | Model name | Substrate used | Pre-treatment method | Operating parameters used to fit kinetic data | Order of reaction | Key points | References |
|---|---|---|---|---|---|---|---|
| 1 | Psuedo-first order rate kinetics | Banana skin, cowpea shells, maize stalks, rice husk | Acid hydrolysis (Sulphuric acid) | Temperature, acid concentration | First | Increase in temperature and acid concentration improves sugar yields | [115] |
| 2 | Semi-mechanistic kinetic model | Sugarcane straw | Hydrothermal | Temperature, concentration profiles of monomers formed | First | Reaction rate increased with increase in temperature | [116] |
| 3 | Model for delignification | Sorghum, Wheat straw, Bamboo | Alkali peroxide | Alkali loading, pre-treatment temperature and enzyme loading | First | Extent of delignification increases with increase in alkaline loading. Increase in temperature and enzyme concentration increases the conversion. | [117] |
| 4 | MM model for cellulase | Miscanthus and oat hulls, oil palm petiole | Chemical (combined method using Nitric acid and Sodium hydroxide) | Substrate loading | First | Rate of enzyme hydrolysis increases with increase in substrate concentration | [118,119] |
| 5 | Chrastil's model | Apple Pomace | Combined (Alkaline + acid + enzymatic) | Mixing speed, substrate concentration | – | Better sugar yields are obtained at lower mixing speeds, maximum constant substrate concentration | [120] |
| 6 | HCH-1 three parameter model | AFEX treated wheat straw | AFEX | Enzyme loading, Substrate concentration |
First | Sugar yield increases with increased substrate concentration | [121] |
| 7 | Langmuir adsorption model | Corn stover, defatted and bleached cotton linter | Dilute alkali and acid, cellulosic solvent | Substrate concentration, enzyme loading | – | Sugar yields were better at lower substrate loadings and a wide range of enzyme concentrations | [122,123] |
| 8 | Intermediate and end product inhibition | Corn stover | Dilute acid | Substrate concentration, temperature, product concentration | First | Model predicts well the hydrolysis performance | [124] |
| 9 | Valjamae and Kopelman model | Passion fruit peel | Solvent extraction | Glucose concentration, enzyme ratio | – | Glucose concentration increases with increase in enzyme volume ratio | [114] |
| 10 | Deactivation and reactivation reaction rate mechanism | Corn cob | Alkaline peroxide oxidation | Substrate concentration, hydrolysis time | Second | Product concentration reaches maximum at optimum substrate loading and hydrolysis time | [125] |