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To determine the effect of cell mass (biocatalyst) concentration, reactions were carried out with increasing cell mass concentrations (100 to 400 kg/m3).
To determine the effect of substrate concentration, reactions were carried out with the increasing concentrations of quinic acid (2 to 20 mM).
The mitochondrial adenosine triphosphatase subunit 6 (ATP6) was amplified using the primer combinations ATP6-3/ATP6-4 ATP6-3/ATP6-4 ATP6-3/ATP6-4 Taq Porymerase sATP6-3/ATP6-4 sATP6-3/ATP6-4 sATP6-3/ATP6-4ed andve and the cycling profiles described by Kretzer and Bruns [ 26].
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The acid rock reaction experiments were performed by varying acid concentration, reaction temperature and flow velocity.
The operational factors were initial phenol concentration, reaction time, and Cu/TiO2 dosage.
The biodiesel production process parameters are the alcohol:oil molar ratio, catalyst concentration, reaction temperature and reaction time.
The results showed that the rate of acid reaction can be accelerated by increasing acid concentration, reaction temperature and velocity.
Three factors KMnO4 concentration, reaction temperature, and reaction duration were tested in a two-level full-factorial design-of-experiment.
The effects of catalyst concentration, reaction time and reaction temperature were investigated in detail.
Three main factors, which include catalyst (NaOH) concentration, reaction temperature and time, were varied according to a central composite design.
Additionally, effect of enzyme type, enzyme concentration, reaction time and temperature were evaluated subsequently in following experiments.
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