The present invention provides processes for preparing a prostacyclin analogue of Formula (I) or a pharmaceutically acceptable salt thereof, wherein R.sup.10 is a linear or branched C.sub.1-6 alkyl. The processes of the present invention comprise steps that generate improved yields and fewer byproducts than traditional methods. The processes of the present invention employ reagents (e.g., the oxidizing reagent) that are less toxic that those used in the traditional methods (e.g., oxalyl chloride). Many of the processes of the present invention generate intermediates with improved e.e. and chemical purity; thereby eliminating the need of additional chromatography steps. And, the processes of the present invention are scalable to generate commercial quantities of the final compound.

The present invention provides processes for preparing a prostacyclin analogue of Formula (I) or a pharmaceutically acceptable salt thereof, wherein R.sup.10 is a linear or branched C.sub.1-6 alkyl. The processes of the present invention comprise steps that generate improved yields and fewer byproducts than traditional methods. The processes of the present invention employ reagents (e.g., the oxidizing reagent) that are less toxic that those used in the traditional methods (e.g., oxalyl chloride). Many of the processes of the present invention generate intermediates with improved e.e. and chemical purity; thereby eliminating the need of additional chromatography steps. And, the processes of the present invention are scalable to generate commercial quantities of the final compound.

Distillative process for obtaining ditrimethylolpropane from solutions includes separating ditrimethylolpropane from the solution in a first distillation unit into a first tops fraction comprising low-boiling compounds having a lower boiling point than ditrimethylolpropane and a first bottoms fraction; introducing the first bottoms fraction into a second distillation unit having at least 5 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment and drawing off a second tops fraction comprising intermediate-boiling compounds having a lower boiling point than ditrimethylolpropane as well as withdrawing a second bottoms fraction from the second distillation unit and introducing the second bottoms fraction into a third distillation unit having at least 4 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment, such that ditrimethylolpropane is obtained as a third tops fraction and high boilers are removed as a third bottoms fraction.

Distillative process for obtaining ditrimethylolpropane from solutions includes separating ditrimethylolpropane from the solution in a first distillation unit into a first tops fraction comprising low-boiling compounds having a lower boiling point than ditrimethylolpropane and a first bottoms fraction; introducing the first bottoms fraction into a second distillation unit having at least 5 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment and drawing off a second tops fraction comprising intermediate-boiling compounds having a lower boiling point than ditrimethylolpropane as well as withdrawing a second bottoms fraction from the second distillation unit and introducing the second bottoms fraction into a third distillation unit having at least 4 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment, such that ditrimethylolpropane is obtained as a third tops fraction and high boilers are removed as a third bottoms fraction.

Distillative process for obtaining ditrimethylolpropane from solutions includes separating ditrimethylolpropane from the solution in a first distillation unit into a first tops fraction comprising low-boiling compounds having a lower boiling point than ditrimethylolpropane and a first bottoms fraction; introducing the first bottoms fraction into a second distillation unit having at least 5 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment and drawing off a second tops fraction comprising intermediate-boiling compounds having a lower boiling point than ditrimethylolpropane as well as withdrawing a second bottoms fraction from the second distillation unit and introducing the second bottoms fraction into a third distillation unit having at least 4 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment, such that ditrimethylolpropane is obtained as a third tops fraction and high boilers are removed as a third bottoms fraction.

Problem The present invention is to provide a generation method that can generate 3,5-dihydroxy-4-methoxybenzyl alcohol, which was not found at all from raw oyster meat originally, at an extraction phase of oyster meat essence. Solution The present invention heats raw oyster meat from which 3,5-dihydroxy-4-methoxybenzyl alcohol is not detected in a raw state at 98° C. to 100° C. for six hours or more to generate 3,5-dihydroxy-4-methoxybenyl alcohol from oyster meat liquid on which the heating process has been performed.

Problem The present invention is to provide a generation method that can generate 3,5-dihydroxy-4-methoxybenzyl alcohol, which was not found at all from raw oyster meat originally, at an extraction phase of oyster meat essence. Solution The present invention heats raw oyster meat from which 3,5-dihydroxy-4-methoxybenzyl alcohol is not detected in a raw state at 98° C. to 100° C. for six hours or more to generate 3,5-dihydroxy-4-methoxybenyl alcohol from oyster meat liquid on which the heating process has been performed.

A process for cleaning contaminated fluid includes combining the contaminated fluid with an acid and water to yield a mixture in which at least some contaminants in the contaminated fluid are insoluble. The insoluble contaminants precipitate to yield precipitated contaminants. At least a portion of the precipitated contaminants are separated from the mixture. At least a portion of the acid and a portion of the water in the mixture are separated from the glycol in the mixture to yield cleaned fluid.

A process for cleaning contaminated fluid includes combining the contaminated fluid with an acid and water to yield a mixture in which at least some contaminants in the contaminated fluid are insoluble. The insoluble contaminants precipitate to yield precipitated contaminants. At least a portion of the precipitated contaminants are separated from the mixture. At least a portion of the acid and a portion of the water in the mixture are separated from the glycol in the mixture to yield cleaned fluid.

The present invention relates generally to the generation of bio-products from organic matter feedstocks. More specifically, the present invention relates to the use of pulping liquors in the hydrothermal/thermochemical conversion of lignocellulosic and/or fossilised organic feedstocks into biofuels (e.g. bio-oils) and/or chemical products (e.g. platform chemicals).