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Anaerobic digestion is a biochemical conversion process, which produces fuel for energy through an enclosure called a digester.
Developments in the enzymes themselves must be accompanied by optimization of the biochemical conversion process to allow for the lowest possible product costs to be achieved.
In practice, the performance of a biochemical conversion process, i.e. the bioreactor performance, is essentially determined by the benefit/cost ratio.
The biochemical conversion process requires higher pretreatment and enzyme costs, has low fermentability of the mixed sugar stream (C 5), and generates inhibitory soluble compounds (Munasinghe and Khanal 2010).
In addition, non-carbohydrate materials in biomass cannot be converted into ethanol in the biochemical conversion process (Henstra et al. 2007) and require special care for downstream waste management.
A simple and cost-effective biochemical conversion process consisting of hydrothermal treatment, enzymatic hydrolysis and fermentation of pretreated whole slurry (PWS) was developed for producing l-lactic acid (L-LA) from oil palm trunk (OPT).
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Biochemical conversion: Biochemical conversion processes make use of the enzymes of bacteria and other microorganisms to breakdown biomass.
Biomass fuel is found to be a suitable energy source that can be converted to higher energy content fuels through direct combustion, thermochemical conversion, or biochemical conversion processes [5].
Nonetheless, the real hallmark of microalgae is the fact that these microscopic organisms can provide the biomass feedstock for the flexible production of several different types of renewable and sustainable biofuels such as biodiesel, bioethanol, biogas, biohydrogen among others via thermochemical and biochemical conversion processes.
As the growing season progresses, yield is increased but the feedstock's amenability to biochemical conversion processes may be decreased.
In typical biochemical conversion processes for lignocellulosic ethanol [ 1], the process model consists of three main unit operations: pretreatment, enzymatic hydrolysis, and fermentation.
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