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Continuous and smooth films were deposited by using a glass reactor with quartz-coating inside and quartz reactor, which could avoid both Ca (< 1 at.%) and other impurities.
Furthermore, a scale-out (scale-up) was performed with a non-resonant microwave continuous-flow system, achieving a maximum throughput of 11 mmol h−1 by using a glass reactor with an inner diameter of 3 mm at a flow rate of 1 mL min−1.
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Try using a glass cage.
The photocatalytic degradation of CV, MB, and p-NP experiments were conducted in a glass reactor using synthesized TiO2 samples as a photocatalyst under UV irradiation for different reaction times.
For the thermolysis process, a glass reactor was used for the thermolysis experiments at atmospheric pressure.
To perform dye degradation, a glass reactor (diameter = 4 cm, height = 6 cm) was used, and the reactor was placed on the magnetic churn dasher.
In the process of degradation of methyl orange, a glass reactor (diameter = 4 cm, height = 6 cm) was used and the reactor was placed on the magnetic churn dasher.
The catalytic reaction was carried out in a glass reactor (glass thickness 80 mm).
Experiments were conducted inside a glass reactor (11 × 11 × 25 cm) with a reflective wall.
The transesterification reaction of sesame oil was carried out in a glass reactor (1-L capacity).
The aminopropyl silica was then placed in a glass reactor and heated to 100 °C.
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