C07C1/30

PROCESS FOR DECHLORINATION OF WASTE PLASTICS
20240376025 · 2024-11-14 ·

A process involving the steps in this order of: providing a waste plastics stream (A) comprising polyvinyl chloride (PVC); (i) supplying the waste plastics stream (A) to a reactor vessel; (ii) subjecting the waste plastics in the reactor vessel to a temperature of 250 C. and 350 C., preferably of 275 C. and 325 C., preferably for a period of 5-30 minutes, under applying a vacuum, preferably of 35 mbar, or using an inert gas sweep, and evacuating the generated hydrogen chloride (B) from the vessel, wherein the PVC is partially dechlorinated to form a waste plastics stream (C) comprising partially unsaturated PVC; (iii) removing the waste plastics stream (C) comprising partially unsaturated PVC from the reaction vessel; and (iv) separating the partially unsaturated PVC from the waste plastics stream to form a dechlorinated waste plastics stream (D).

1-HALO-2,6,14-TRIMETHYLOCTADECANE COMPOUND AND PROCESS FOR PREPARING 5,13,17-TRIMETHYLALKANE COMPOUND THEREFROM
20240368061 · 2024-11-07 ·

The present invention relates to a 1-halo-2,6,14-trimethyloctadecane compound of the following general formula (1), wherein X.sup.1 represents a halogen atom. The present invention further relates to a process for preparing a 5,13,17-trimethylalkane compound of the following general formula (4), wherein n represents an integer of 14 to 18, the process comprising converting the aforesaid 1-halo-2,6,14-trimethyloctadecane compound (1) into a nucleophilic reagent, 2,6,14-trimethyloctadecyl, of the following general formula (2), wherein M.sup.1 represents Li or MgZ.sup.1, and Z.sup.1 represents a halogen atom or a 2,6,14-trimethyloctadecyl group, and subsequently subjecting the nucleophilic reagent, 2,6,14-trimethyloctadecyl compound (2), to a coupling reaction with an electrophilic alkyl reagent (3) of the following general formula (3), wherein X.sup.2 represents a halogen atom or a p-toluenesulfonyloxy group, and n is as defined above, to obtain the aforesaid 5,13,17-trimethylalkane compound (4).

##STR00001##

1-HALO-2,6,14-TRIMETHYLOCTADECANE COMPOUND AND PROCESS FOR PREPARING 5,13,17-TRIMETHYLALKANE COMPOUND THEREFROM
20240368061 · 2024-11-07 ·

The present invention relates to a 1-halo-2,6,14-trimethyloctadecane compound of the following general formula (1), wherein X.sup.1 represents a halogen atom. The present invention further relates to a process for preparing a 5,13,17-trimethylalkane compound of the following general formula (4), wherein n represents an integer of 14 to 18, the process comprising converting the aforesaid 1-halo-2,6,14-trimethyloctadecane compound (1) into a nucleophilic reagent, 2,6,14-trimethyloctadecyl, of the following general formula (2), wherein M.sup.1 represents Li or MgZ.sup.1, and Z.sup.1 represents a halogen atom or a 2,6,14-trimethyloctadecyl group, and subsequently subjecting the nucleophilic reagent, 2,6,14-trimethyloctadecyl compound (2), to a coupling reaction with an electrophilic alkyl reagent (3) of the following general formula (3), wherein X.sup.2 represents a halogen atom or a p-toluenesulfonyloxy group, and n is as defined above, to obtain the aforesaid 5,13,17-trimethylalkane compound (4).

##STR00001##

Processes and catalysts for converting alkanes to alkenes

Generally, regenerable, encapsulated metal oxide catalysts comprising a ceramic matrix and metal catalysts may be used to convert alkanes to alkenes. The encapsulated metal oxide catalyst may be tailored to produce a variety of alkenes including ethylene, butylene, and propylene. Further, the encapsulated metal oxide catalysts advantageously allow for regeneration and reactant recovery for cost effective and environmentally friendly processes.

Processes and catalysts for converting alkanes to alkenes

Generally, regenerable, encapsulated metal oxide catalysts comprising a ceramic matrix and metal catalysts may be used to convert alkanes to alkenes. The encapsulated metal oxide catalyst may be tailored to produce a variety of alkenes including ethylene, butylene, and propylene. Further, the encapsulated metal oxide catalysts advantageously allow for regeneration and reactant recovery for cost effective and environmentally friendly processes.

Phosphine ligands for catalytic reactions

The disclosure is directed to: (a) phosphacycle ligands; (b) catalyst compositions comprising phosphacycle ligands; and (c) methods of using such phosphacycle ligands and catalyst compositions in bond forming reactions.

Phosphine ligands for catalytic reactions

The disclosure is directed to: (a) phosphacycle ligands; (b) catalyst compositions comprising phosphacycle ligands; and (c) methods of using such phosphacycle ligands and catalyst compositions in bond forming reactions.

Phosphine ligands for catalytic reactions

The disclosure is directed to: (a) phosphacycle ligands; (b) catalyst compositions comprising phosphacycle ligands; and (c) methods of using such phosphacycle ligands and catalyst compositions in bond forming reactions.

Coupling of light alkanes to liquid fuels
09663421 · 2017-05-30 · ·

A method can include reacting a stream including one or more C.sub.3 to C.sub.10 alkanes with bromine in a bromination reactor to form a bromination reactor discharge stream that includes alkylbromides and HBr. The method further includes coupling the alkylbromides in a coupling reactor to form a coupling reactor effluent comprising alkylbromides having between 5 and about 1000 carbon atoms, olefins having between 5 and about 1000 carbon atoms and HBr. The method also includes hydrogenating the alkylbromides having between 5 and about 1000 carbon atoms and olefins having between 5 and about 1000 carbon atoms to form alkanes having between 5 and about 1000 carbon atoms and HBr.

Coupling of light alkanes to liquid fuels
09663421 · 2017-05-30 · ·

A method can include reacting a stream including one or more C.sub.3 to C.sub.10 alkanes with bromine in a bromination reactor to form a bromination reactor discharge stream that includes alkylbromides and HBr. The method further includes coupling the alkylbromides in a coupling reactor to form a coupling reactor effluent comprising alkylbromides having between 5 and about 1000 carbon atoms, olefins having between 5 and about 1000 carbon atoms and HBr. The method also includes hydrogenating the alkylbromides having between 5 and about 1000 carbon atoms and olefins having between 5 and about 1000 carbon atoms to form alkanes having between 5 and about 1000 carbon atoms and HBr.