C07C29/88

RECYCLE CONTENT PROPANOL

A recycle content propanol and method of making a recycle content propanol wherein the recycle content is derived directly or indirectly from the cracking of recycle content pyrolysis oil and/or gas. The cracking of the pyrolysis oil can be conducted in a gas furnace or a split furnace.

RECYCLE CONTENT PROPANOL

A recycle content propanol and method of making a recycle content propanol wherein the recycle content is derived directly or indirectly from the cracking of recycle content pyrolysis oil and/or gas. The cracking of the pyrolysis oil can be conducted in a gas furnace or a split furnace.

Systems for converting light paraffins to alcohols

Systems for the catalytic activation and/or dehydrogenation of a paraffin feed stream that is enriched in C5 alkanes to produce olefins that are then hydrated in the presence of water to produce C5 alcohols. Optionally, paraffin isomers are separated and the n-paraffins isomerized prior to catalytic activation and/or dehydrogenation.

Systems for converting light paraffins to alcohols

Systems for the catalytic activation and/or dehydrogenation of a paraffin feed stream that is enriched in C5 alkanes to produce olefins that are then hydrated in the presence of water to produce C5 alcohols. Optionally, paraffin isomers are separated and the n-paraffins isomerized prior to catalytic activation and/or dehydrogenation.

REMOVING ORGANIC ACIDS IN MONOETHYLENE GLYCOL RECOVERY
20220380281 · 2022-12-01 ·

Embodiments described herein provide a method, comprising reducing pH of a glycol vaporization separator purge stream to form an acid stream; distilling the acid stream to form an overhead stream and a bottoms stream; and recycling the bottoms stream to the vaporization separator.

REMOVING ORGANIC ACIDS IN MONOETHYLENE GLYCOL RECOVERY
20220380281 · 2022-12-01 ·

Embodiments described herein provide a method, comprising reducing pH of a glycol vaporization separator purge stream to form an acid stream; distilling the acid stream to form an overhead stream and a bottoms stream; and recycling the bottoms stream to the vaporization separator.

Method for Separation of Close-Boiling Mixture of Polyols

This invention discloses an approach for the separation of the close-boiling mixture of polyols. The raw material is ethylene glycol containing miscellaneous polyols (such as 1,2-propylene glycol and 1,2-butanediol). Over an acid catalyst, these miscellaneous polyols, through (1) a dehydration reaction, (2) pinacol rearrangement, and (3) acetalization or ketalization reaction, are converted into aldehydes (small amounts), acetals, and ketals (trace amount), which are simultaneously and readily separated via distillation. Meanwhile, after the reaction, the mixture is further separated to obtain an ethylene glycol product at a high purity. The invention provides a technique to remove the miscellaneous polyols from ethylene glycol via liquid-phase dehydration reactions under mild conditions, with low energy consumption. In particular, this approach is markedly effective for the removal of 1,2-butanediol that is difficult to be removed via conventional techniques. The purity of the resulting ethylene glycol product is high, and value-added acetals or ketals are co-produced.

Method for Separation of Close-Boiling Mixture of Polyols

This invention discloses an approach for the separation of the close-boiling mixture of polyols. The raw material is ethylene glycol containing miscellaneous polyols (such as 1,2-propylene glycol and 1,2-butanediol). Over an acid catalyst, these miscellaneous polyols, through (1) a dehydration reaction, (2) pinacol rearrangement, and (3) acetalization or ketalization reaction, are converted into aldehydes (small amounts), acetals, and ketals (trace amount), which are simultaneously and readily separated via distillation. Meanwhile, after the reaction, the mixture is further separated to obtain an ethylene glycol product at a high purity. The invention provides a technique to remove the miscellaneous polyols from ethylene glycol via liquid-phase dehydration reactions under mild conditions, with low energy consumption. In particular, this approach is markedly effective for the removal of 1,2-butanediol that is difficult to be removed via conventional techniques. The purity of the resulting ethylene glycol product is high, and value-added acetals or ketals are co-produced.

PROCESS FOR CLEANING CONTAMINATED FLUID
20170233320 · 2017-08-17 ·

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.

PROCESS FOR CLEANING CONTAMINATED FLUID
20170233320 · 2017-08-17 ·

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.