An adiabatic sump recycle and cooled upper pump-around recover acrylic acid from vapor streams without excessive dilution.
Reactive distillation acetalizes formaldehyde in glycolaldehyde mixtures, preventing catalyst poisoning during subsequent chemical transformations.
Amino acid salt formation enriches curcumin purity beyond 90 wt% through selective precipitation and filtration.
A separation column operating above 1 bar purifies acetone feed streams by altering vapor-liquid equilibrium dynamics.
Replacing water with organic solvents during recrystallization eliminates large solvent consumption and caking issues while maintaining cosmetic-grade purity.
Vacuum distillation in a dividing wall column minimizes thermal isomerization while separating neral from geranial for industrial production.
Three-column rectification with oxidative reagents removes aldehydes to achieve high purity acetone without vacuum operation costs.
Ethanol and ethyl acetate replace water to purify crude 4-hydroxyacetophenone, reducing solvent consumption while maintaining product purity.
Recrystallizing bis(benzoyl)benzene monomers in a binary solvent system reduces metal concentrations by up to 75% while maintaining yields above 90%.
A vanillin purification process uses fractional crystallization to separate impurities from organic streams.
pH-dependent solubility shifts separate asymmetric from symmetric β-diketones, reducing metal loss in chemical vapor deposition.