Disclosed is a method for crystallizing molecules having a molecular weight equal to or lower than about 500 Dalton in a gravity below about 0.01 g to about 0.000001 g as well as to crystalline molecules having a molecular weight equal to, or lower than, about 500 Dalton, prepared under microgravity conditions.

Disclosed is a method for crystallizing molecules having a molecular weight equal to or lower than about 500 Dalton in a gravity below about 0.01 g to about 0.000001 g as well as to crystalline molecules having a molecular weight equal to, or lower than, about 500 Dalton, prepared under microgravity conditions.

Disclosed is a method for crystallizing molecules having a molecular weight equal to or lower than about 500 Dalton in a gravity below about 0.01 g to about 0.000001 g as well as to crystalline molecules having a molecular weight equal to, or lower than, about 500 Dalton, prepared under microgravity conditions.

A method for purifying ethanolamine from a fermentation composition and products thereof.

A method for purifying ethanolamine from a fermentation composition and products thereof.

A method for purifying ethanolamine from a fermentation composition and products thereof.

Disclosed are an amino alcohol-boron-binol complex as an intermediate, including Complex 3-1-1 shown below, and a method for preparing an optically active amino alcohol by using the same, wherein a racemic amino alcohol is resolved in an enationselective manner using a boron compound and a (R)- or (S)-binol, whereby an amino alcohol derivative with high optical purity can be prepared at high yield. ##STR00001##

Disclosed are an amino alcohol-boron-binol complex as an intermediate, including Complex 3-1-1 shown below, and a method for preparing an optically active amino alcohol by using the same, wherein a racemic amino alcohol is resolved in an enationselective manner using a boron compound and a (R)- or (S)-binol, whereby an amino alcohol derivative with high optical purity can be prepared at high yield. ##STR00001##

Process for the production of 2-dimethylaminoethyl (meth)acrylate in multiple stage batch reactions involving the recycling of the catalyst (DBTO) in subsequent reaction, the addition a certain amount of fresh catalyst to the recycled catalyst, the use of said catalysts in the subsequent reaction, and wherein the volume decrease due to azeotropic distillation is compensate in order to keep the volume constant in the reactor during the reaction by the continuous addition of a composition comprising methyl(meth)acrylate and dimethylaminoethanol.

Process for the production of 2-dimethylaminoethyl (meth)acrylate in multiple stage batch reactions involving the recycling of the catalyst (DBTO) in subsequent reaction, the addition a certain amount of fresh catalyst to the recycled catalyst, the use of said catalysts in the subsequent reaction, and wherein the volume decrease due to azeotropic distillation is compensate in order to keep the volume constant in the reactor during the reaction by the continuous addition of a composition comprising methyl(meth)acrylate and dimethylaminoethanol.