Abstract An improved process for the continuous preparation of polycaprolactam, in which ε-caprolactam is partially polymerized, with the addition of a water-containing agent and acetic acid or propionic acid as a chain regulator, at a nylon-forming temperature, in a mechanically mixed zone in a vertical tubular reactor through which the reaction mixture flows downwards, and is then polymerized further, in additional heat exchange zones, until the desired degree of polymerization is reached, and polycaprolactam is then discharged as a melt, wherein a gaseous mixture of caprolactam, water and acetic acid or propionic acid is removed at the top of the tubular reactor and is fed to the middle of a column, water is removed at the top of the column, the bottom of the column is maintained at from 125° to 145° C., and the mixture obtained at the bottom of the column, and comprising caprolactam, acetic acid or propionic acid and a small amount of water, is recycled to the top of the tubular reactor.
An improved process for the continuous polymerization of ε-caprolactam which comprises: polymerizing partially an ε-caprolactam composition at a nylon-forming temperature, in a mechanical mixing zone in a vertical tubular reactor through which the caprolactam composition flows downwardly, said composition comprising ε-caprolactam, a water-containing agent, and acetic acid or propionic acid as chain regulator; polymerizing further said composition in additional heat exchange zones in said reactor until polymerization is completed and thereupon discharging polycaprolactam from the reactor as a melt; removing from the tubular reactor a vapor mixture of water, caprolactam, and acetic acid or propionic acid which has formed in the gas space at the top of the tubular reactor; feeding the vapor mixture of caprolactam, water, and acetic acid or propionic acid to the middle of a fractionating column; removing water from the top of said column; maintaining the temperature at the bottom of said column at 125° C. to 145° C.; and recycling the mixture obtained at the bottom of the column to the top of the tubular reactor, said mixture comprising caprolactam, acetic acid or propionic acid, and a small amount of water; whereby the polymerizing caprolactam composition and polycaprolactam melt maintain a constant composition.
Claim 2
Dependent Claim
198 words
An improved process for the continuous polymerization of ε-caprolactam which comprises: polymerizing partially an ε-caprolactam composition at a nylon-forming temperature, in a mechanical mixing zone in a vertical tubular reactor through which the caprolactam composition flows downwardly, said composition comprising ε-caprolactam, a water-containing agent, and acetic acid or propionic acid as chain regulator; polymerizing further said composition in additional heat exchange zones in said reactor until polymerization is completed and thereupon discharging polycaprolactam from the reactor as a melt; removing from the tubular reactor a vapor mixture of water, caprolactam, and acetic acid or propionic acid which has formed in the gas space at the top of the tubular reactor; feeding the vapor mixture of caprolactam, water, and acetic acid or propionic acid to the middle of a fractionating column; removing water from the top of said column; maintaining the temperature at the bottom of said column at 125° C. to 145° C.; and recycling the mixture obtained at the bottom of the column to the top of the tubular reactor, said mixture comprising caprolactam, acetic acid or propionic acid, and a small amount of water; whereby the polymerizing caprolactam composition and polycaprolactam melt maintain a constant composition.
Claim 3
Dependent Claim
21 words
A process as set forth in claim 1, wherein the bottom of the column is maintained at a selected constant temperature.