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The samples were then transferred to 100% methanol in a freezer at −20 °C for storage.
The syngas is then converted into methanol in a high-pressure process using a catalyst made of copper, zinc and aluminum.
Separately, 3.3 mg CuBr and 8.0 mg Bpy was dissolved in 10 mL methanol in a 50-mL Schlenck flask and degassed with N2.
In this work, the production of dimethyl ether from the dehydration reaction of methanol in a reactive distillation is studied.
It is further noteworthy that the presence of methanol in a high-temperature water medium completely suppresses the (5) production.
In the transesterification of soybean oil with methanol in a batch reactor, the same differences in activity are encountered.
The third case study handles an advanced subject in process intensification, the production of biodiesel by the esterification of fatty acids with methanol in a reactive (DWC).
Results concerning the coupling of the steam reforming (SR) and total oxidation (TOX) of methanol in a two-passage reactor are presented.
The classic method for producing DME is by dehydration of methanol in a catalytic gas-phase reactor, and purification in a direct sequence of two distillation columns.
A purpose-developed theoretical model was used to study the esterification of acetic acid by methanol in a reaction-distillation column.
In the first catalyst bed, the synthesis gas is partly converted to methanol in a water-cooled reactor, which is a fluidized-bed.
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