Achieving maximum sugar yield.

Saccharification — the process of converting cellulose and hemicellulose into fermentable sugars — is a considerable cost in the biomass to bioproduct pipeline.

We take the following factors into consideration:

  • Biomass composition
  • Type of pretreatment
  • Dosage and efficiency of the hydrolytic catalyst or enzymes

We integrate pretreatment and saccharification to establish the optimum process parameters and selection of methodologies.

Saccharification Process Options

Cocktail Optimization of Enzymes

As the severity factor of the pretreatment process decreases, the sugar yield after enzymatic hydrolysis also decreases. Hence different types of enzymes and higher dosages are required to achieve maximum sugar yield from cellulose and hemicellulose fractions of the pretreated biomass. We offer a cocktail of enzymes such as cellulases, hemicellulases, and other accessory enzymes for complete hydrolysis.

High Solids Enzymatic Hydrolysis

Maintaining high solids concentrations throughout the biomass conversion process is important for final product titer with reduced intensity of the separation process. High substrate concentration allows for the production of a concentrated sugar solution, which, in turn, is beneficial in separation processes after fermentation. The extent to which solids loading can be increased in hydrolysis varies with the type of feedstock, pretreatment process, and enzyme/catalyst. 

Solid/Liquid Separation

After saccharification, lignin-rich solid is separated from the sugar-rich aqueous phase using centrifugation and/or filtration. The solid residue could be used for lignin valorization or other applications. 

Mass/Energy Balance

A mass balance, also called a material balance, is a meticulous accounting of material entering and leaving a system. Mass balance is essential to establish a process as it is required to calculate the actual conversion of feedstock, monitor process flow, identify bottle-necks in processes, and model large scale processes in desired reactors. Similarly, an energy balance can be established across a process by assuming that net energy loss from a reactor is zero.