This describes homogeneous catalysts that are recoverable from solution by being phase selective and through host-guest interactions. An example of a method includes separating a water soluble N-heterocyclic carbene homogeneous catalyst from a solution by: (a) forming a host-guest compound between the catalyst and an inclusion compound in the solution; and (b) isolating the host-guest compound from the solution.

This describes homogeneous catalysts that are recoverable from solution by being phase selective and through host-guest interactions. An example of a method includes separating a water soluble N-heterocyclic carbene homogeneous catalyst from a solution by: (a) forming a host-guest compound between the catalyst and an inclusion compound in the solution; and (b) isolating the host-guest compound from the solution.

A method for separating a homogeneous catalyst from a solution includes forming a host-guest compound between a first isomer of the catalyst and inclusion compound in the solution and isolating the host-guest compound from the solution. The catalyst may be released from the inclusion compound by converting the first isomer of the catalyst to a second isomer of the catalyst.

This describes homogeneous catalysts that are recoverable from solution by being phase selective and through host-guest interactions. An example of a method includes separating a water soluble N-heterocyclic carbene homogeneous catalyst from a solution by: (a) forming a host-guest compound between the catalyst and an inclusion compound in the solution; and (b) isolating the host-guest compound from the solution.

This describes homogeneous catalysts that are recoverable from solution by being phase selective and through host-guest interactions. An example of a method includes separating a water soluble N-heterocyclic carbene homogeneous catalyst from a solution by: (a) forming a host-guest compound between the catalyst and an inclusion compound in the solution; and (b) isolating the host-guest compound from the solution.

The present invention relates to a process for efficiently synthesizing highly optically active 1,3-disubstituted allenes, i.e., a one-step process for preparing highly optically active 1,3-disubstituted allenes by using a functionalized terminal alkyne, an aldehyde and a chiral ,-diphenyl prolinol as reactants under the catalysis of a divalent copper salt. The operation of the process is simple, and the raw materials and reagents are readily available. The process has a broad-spectrum of substrates and a good compatibility for a wide variety of functional groups such as glycosidic units, primary alcohols, secondary alcohols, tertiary alcohols, amides, malonates, etc., and does not require the protection for the functional groups. The obtained axially chiral allene has a moderate to high yield and a good diastereoselectivity or enantioselectivity.

The present invention relates to a process for efficiently synthesizing highly optically active 1,3-disubstituted allenes, i.e., a one-step process for preparing highly optically active 1,3-disubstituted allenes by using a functionalized terminal alkyne, an aldehyde and a chiral ,-diphenyl prolinol as reactants under the catalysis of a divalent copper salt. The operation of the process is simple, and the raw materials and reagents are readily available. The process has a broad-spectrum of substrates and a good compatibility for a wide variety of functional groups such as glycosidic units, primary alcohols, secondary alcohols, tertiary alcohols, amides, malonates, etc., and does not require the protection for the functional groups. The obtained axially chiral allene has a moderate to high yield and a good diastereoselectivity or enantioselectivity.

A method for producing 2,7-octadien-1-ol, that includes feeding a raw material mixture liquid containing butadiene, a Group 6 to 11 transition metal catalyst containing a Group 6 to 11 transition metal, a tertiary phosphorus compound, an amine compound, and water to a telomerization reactor, and reacting butadiene and water in a carbon dioxide atmosphere in the telomerization reactor to obtain a reaction mixture liquid containing 2,7-octadien-1-ol, in which a residence time of the raw material mixture liquid in the telomerization reactor is 1.3 to 3.0 hours.

A method for producing 2,7-octadien-1-ol, that includes feeding a raw material mixture liquid containing butadiene, a Group 6 to 11 transition metal catalyst containing a Group 6 to 11 transition metal, a tertiary phosphorus compound, an amine compound, and water to a telomerization reactor, and reacting butadiene and water in a carbon dioxide atmosphere in the telomerization reactor to obtain a reaction mixture liquid containing 2,7-octadien-1-ol, in which a residence time of the raw material mixture liquid in the telomerization reactor is 1.3 to 3.0 hours.