Patent classifications
C07C51/145
PLATINUM COMPLEXES HAVING FERROCENE DIPHOSPHINE LIGANDS FOR CATALYSIS OF THE HYDROXYCARBONYLATION OF ETHYLENICALLY UNSATURATED COMPOUNDS
Platinum complexes having ferrocene-diphosphine ligands for catalysis of the hydroxycarbonylation of ethylenically unsaturated compounds.
PLATINUM COMPLEXES HAVING FERROCENE DIPHOSPHINE LIGANDS FOR CATALYSIS OF THE HYDROXYCARBONYLATION OF ETHYLENICALLY UNSATURATED COMPOUNDS
Platinum complexes having ferrocene-diphosphine ligands for catalysis of the hydroxycarbonylation of ethylenically unsaturated compounds.
PLATINUM COMPLEXES HAVING BINAPHTHYL-BASED DIPHOSPHINE LIGANDS FOR THE SELECTIVE CATALYSIS OF THE HYDROXYCARBONYLATION OF ETHYLENICALLY UNSATURATED COMPOUNDS
Platinum complexes having binaphthyl-based diphosphine ligands for the selective catalysis of the hydroxycarbonylation of ethylenically unsaturated compounds.
PLATINUM COMPLEXES HAVING BINAPHTHYL-BASED DIPHOSPHINE LIGANDS FOR THE SELECTIVE CATALYSIS OF THE HYDROXYCARBONYLATION OF ETHYLENICALLY UNSATURATED COMPOUNDS
Platinum complexes having binaphthyl-based diphosphine ligands for the selective catalysis of the hydroxycarbonylation of ethylenically unsaturated compounds.
A PROCESS FOR THE CONTINUOUS PRODUCTION OF EITHER ACROLEIN OR ACRYLIC ACID AS THE TARGET PRODUCT FROM PROPENE
A process for the continuous production of either acrolein or acrylic acid as the target product from propene comprising a catalyzed gas phase partial oxidation of propene to yield a product gas containing the target product, transferring the target product in a separating zone from the product gas into the liquid phase and conducting out of the separating zone a stream of residual gas the major portion of which is returned into the partial oxidation and the remaining portion of said stream is purged from the process as off-gas from which synthesis gas can be produced or which can be added to synthesis gas produced otherwise.
A PROCESS FOR THE CONTINUOUS PRODUCTION OF EITHER ACROLEIN OR ACRYLIC ACID AS THE TARGET PRODUCT FROM PROPENE
A process for the continuous production of either acrolein or acrylic acid as the target product from propene comprising a catalyzed gas phase partial oxidation of propene to yield a product gas containing the target product, transferring the target product in a separating zone from the product gas into the liquid phase and conducting out of the separating zone a stream of residual gas the major portion of which is returned into the partial oxidation and the remaining portion of said stream is purged from the process as off-gas from which synthesis gas can be produced or which can be added to synthesis gas produced otherwise.
Method for producing alpha-fluoroacrylic acid
An object of the present invention is to provide a novel method for producing an α-fluoroacrylic acid ester compound. ##STR00001##
This problem is solved by a method for producing a compound represented by formula (1), wherein R.sup.1 and R.sup.2 are identical or different, and each represents an alkyl group or the like; and R.sup.3 is an alkyl group or the like, the method comprising step A of reacting a compound represented by formula (2) with R.sup.3—OH (3) and carbon monoxide in the presence of palladium, a double bond-containing compound (α), a diphosphine compound (β), and a base, to obtain the compound represented by formula (1) above.
Method for producing alpha-fluoroacrylic acid
An object of the present invention is to provide a novel method for producing an α-fluoroacrylic acid ester compound. ##STR00001##
This problem is solved by a method for producing a compound represented by formula (1), wherein R.sup.1 and R.sup.2 are identical or different, and each represents an alkyl group or the like; and R.sup.3 is an alkyl group or the like, the method comprising step A of reacting a compound represented by formula (2) with R.sup.3—OH (3) and carbon monoxide in the presence of palladium, a double bond-containing compound (α), a diphosphine compound (β), and a base, to obtain the compound represented by formula (1) above.
Method of converting ethylene to polyacrylic acid (PAA) and superabsorbent polymer (SAP) within an integrated system
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.
Method of converting ethylene to polyacrylic acid (PAA) and superabsorbent polymer (SAP) within an integrated system
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.