C07C51/14

Process for the sustainable production of acrylic acid

A process for the production of organic acids having at least three carbon atoms comprises the steps of forming an amount of carbon monoxide and reacting the amount of carbon monoxide with an amount of an unsaturated hydrocarbon. The reaction is preferably carried out in the presence of a supported palladium catalyst, a strong acid, and a phosphine. In some embodiments, the unsaturated hydrocarbon is one of acetylene and methylacetylene, and the organic acid is one of acrylic acid and methyl acrylic acid. The reacting step is preferably performed with carbon monoxide produced from carbon dioxide.

Process for the sustainable production of acrylic acid

A process for the production of organic acids having at least three carbon atoms comprises the steps of forming an amount of carbon monoxide and reacting the amount of carbon monoxide with an amount of an unsaturated hydrocarbon. The reaction is preferably carried out in the presence of a supported palladium catalyst, a strong acid, and a phosphine. In some embodiments, the unsaturated hydrocarbon is one of acetylene and methylacetylene, and the organic acid is one of acrylic acid and methyl acrylic acid. The reacting step is preferably performed with carbon monoxide produced from carbon dioxide.

Neo-acids and process for making the same

This disclosure relates to neo-acids and processes for making neo-acids from a vinylidene olefin.

Neo-acids and process for making the same

This disclosure relates to neo-acids and processes for making neo-acids from a vinylidene olefin.

Neo-acids and process for making the same

This disclosure relates to neo-acids and processes for making neo-acids from a vinylidene olefin.

Continuous process for the conversion of olefins and carbon dioxide to acrylates via solution phase reactor

Disclosed is a continuous process for producing ,-unsaturated carboxylic acids or salts thereof, comprising: 1) in a first stage, contacting (a) a transition metal precursor compound comprising at least one first ligand, (b) optionally, at least one second ligand, (c) an olefin, (d) carbon dioxide (CO.sub.2), and (e) a diluent to form a first composition; 2) in a second stage, contacting a polyanionic solid with the first composition to form a second composition; and 3) in a third stage, (a) contacting the second composition with a polar solvent to release a metal salt of an ,-unsaturated carboxylic acid and form a reacted solid. Methods of regenerating the polyanionic solid are described.

SYSTEMS AND PROCESSES FOR POLYACRYLIC ACID PRODUCTION
20200002446 · 2020-01-02 · ·

Disclosed are systems and methods for the production of polyacrylic acid and superabsorbent polymers from ethylene oxidation to form ethylene oxide. Reacting the ethylene oxide with carbon monoxide to form to beta propiolactone (BPL) or polypropiolactone (PPL), or a combination thereof. An outlet configured to provide a carbonylation stream comprising the BPL or PPL, or a combination thereof and using one or more reactors to convert BPL to acrylic acid or to convert at least some of the BPL to PPL, and then to convert PPL to acrylic acid. An outlet configured to provide a PPL stream to a second reactor tm to convert at least some of the PPL to AA or a third reactor to convert at least some of the PPL to AA. The outlet configured to provide an AA stream to a fourth reactor to convert the AA to polyacrylic acid.

SYSTEMS AND PROCESSES FOR POLYACRYLIC ACID PRODUCTION
20200002446 · 2020-01-02 · ·

Disclosed are systems and methods for the production of polyacrylic acid and superabsorbent polymers from ethylene oxidation to form ethylene oxide. Reacting the ethylene oxide with carbon monoxide to form to beta propiolactone (BPL) or polypropiolactone (PPL), or a combination thereof. An outlet configured to provide a carbonylation stream comprising the BPL or PPL, or a combination thereof and using one or more reactors to convert BPL to acrylic acid or to convert at least some of the BPL to PPL, and then to convert PPL to acrylic acid. An outlet configured to provide a PPL stream to a second reactor tm to convert at least some of the PPL to AA or a third reactor to convert at least some of the PPL to AA. The outlet configured to provide an AA stream to a fourth reactor to convert the AA to polyacrylic acid.

Process for Pd-catalyzed hydroxycarbonylation of diisobutene: ligand/Pd ratio

Process for Pd-catalyzed hydroxycarbonylation of diisobutene:ligand/Pd ratio.

Process for Pd-catalyzed hydroxycarbonylation of diisobutene: ligand/Pd ratio

Process for Pd-catalyzed hydroxycarbonylation of diisobutene:ligand/Pd ratio.