US 12,359,021 B1
High-viscosity PBT polymerization reactor and method for preparing direct melt-spun high-viscosity PBT/low-viscosity PET two-component elastic fiber
Shuchang Bian, Suzhou (CN); and Rui Wang, Suzhou (CN)
Assigned to JIANGSU GANGHONG FIBER CO., LTD., Suzhou (CN)
Filed by JIANGSU GANGHONG FIBER CO., LTD., Suzhou (CN)
Filed on Nov. 22, 2024, as Appl. No. 18/956,721.
Application 18/956,721 is a continuation in part of application No. PCT/CN2024/093558, filed on May 16, 2024.
Claims priority of application No. 202410046154.8 (CN), filed on Jan. 12, 2024.
Int. Cl. C08G 63/78 (2006.01); C08G 63/183 (2006.01); D01D 5/32 (2006.01); D01F 8/14 (2006.01)
CPC C08G 63/785 (2013.01) [C08G 63/183 (2013.01); D01D 5/32 (2013.01); D01F 8/14 (2013.01)] 19 Claims
OG exemplary drawing
 
1. A high-viscosity PBT polymerization reactor, used to prepare a high-viscosity PBT melt for preparing a high-viscosity PBT/low-viscosity PET two-component elastic fiber, wherein, the high-viscosity PBT polymerization reactor is a horizontal polymerization reactor, and comprises a main body containing a chamber internally, the main body comprises a low viscosity zone, a med-high viscosity zone, and a high viscosity zone arranged in sequence along the axial direction of the high-viscosity PBT polymerization reactor, the viscosity of the PBT melt in the low viscosity zone, the med-high viscosity zone and the high viscosity zone increases in sequence; the high-viscosity PBT polymerization reactor further comprises two agitating shafts, one of which is disposed in the low viscosity zone and part of the med-high viscosity zone, and the other one is disposed in the high viscosity zone and the remaining med-high viscosity zone; a plurality of disc reactors is disposed on each of the agitating shafts, and the disc reactors in the low viscosity zone are three- to ten-disc combination; the disc reactors in the med-high viscosity zone are two-disc combination; the disc reactors in the high viscosity zone are single-disc; a plurality of homogenizers is arranged at intervals on an outer edge of each disc combination along its circumferential direction in the low viscosity zone of the high-viscosity PBT polymerization reactor and the homogenizers extend along the axial direction of the high-viscosity PBT polymerization reactor and are used to pour the PBT melt from the low viscosity zone onto the surfaces of the disc reactors.