The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
May. 27, 2025

Filed:

Dec. 06, 2024
Applicant:

Jiangsu Ganghong Fiber Co., Ltd., Suzhou, CN;

Inventors:

Rui Wang, Suzhou, CN;

Shuchang Bian, Suzhou, CN;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01F 27/191 (2022.01); B01F 27/23 (2022.01); B01F 27/2322 (2022.01); B01F 27/73 (2022.01); B01J 19/00 (2006.01); B01J 19/18 (2006.01); B29B 7/48 (2006.01); B29B 7/64 (2006.01); C08F 2/00 (2006.01); C08G 63/16 (2006.01); C08G 63/183 (2006.01); C08G 63/82 (2006.01); C08G 63/85 (2006.01); C08G 85/00 (2006.01); C08L 67/02 (2006.01); D01D 1/04 (2006.01); D01D 5/08 (2006.01); D01D 5/32 (2006.01); D01F 6/84 (2006.01); D01F 8/14 (2006.01);
U.S. Cl.
CPC ...
D01F 8/14 (2013.01); B01F 27/731 (2022.01); B01J 19/0066 (2013.01); B01J 19/1862 (2013.01); B29B 7/481 (2013.01); C08F 2/001 (2013.01); C08G 85/006 (2013.01); D01D 5/08 (2013.01); C08L 2203/12 (2013.01); D10B 2331/04 (2013.01); D10B 2401/061 (2013.01);
Abstract

A method for preparing direct melt-spun high-viscosity PBAT/low-viscosity PET two-component elastic fiber and a high-viscosity PBAT polymerization reactor. This method uses two production lines respectively used to produce a high-viscosity PBT melt and a low-viscosity PET melt, which are then spun. The high-viscosity PBAT production line comprises a first esterification reactor, a second esterification reactor, a first prepolymerization reactor, a second prepolymerization reactor, and a high-viscosity PBAT polymerization reactor. The polymerization reactor is designed with a special disc structure in a parallel two-shaft disc reactor, and the two shafts are rotated in opposite directions, improving the devolatilization effect and self-cleaning, significantly increasing the viscosity. By using this method, the cost is low and the production capacity is high, the process flow is shortened, the fiber strength can reach 2.55˜2.85 cN/dtex, the crimp shrinkage rate can reach 25%˜60%, and the crimp stability can reach 58%˜70%.


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