Method for recovering useful components from dyed polyester fiber

• US 7,959,807 B2
• Filed: 07/31/2006
• Issued: 06/14/2011
• Est. Priority Date: 08/05/2005
• Status: Expired due to Fees

• Current Assignee: Teijin Fibers Limited (Teijin Limited)
• Original Assignee: Teijin Fibers Limited (Teijin Limited)
• Inventors: Mukai, Kouji, Nakashima, Minoru
• Primary Examiner(s): Drodge; Joseph W
• Application Number:
  US11/996,229
• Publication Number:
  US 20090133200A1
• Time in Patent Office: 1,779 Days
• Field of Search: 810/2, 844/0, 203/28.29, 203/39, 203/47, 210/634, 210/638, 210/639, 210/749, 210/774, 210/805, 210/806, 264/36.1, 264/37.1, 521/48, 521/48.5, 560/76, 560/78, 560/96, 560/98, 528/272, 528/274, 528/480, 528/491, 528/502.R, 528/502.A, 528/503
• US Class Current: 210/634
• CPC Class Codes: B01D 11/0223 Moving bed of solid material see also B01D11/0261
• CPC Class Codes: B01D 11/0288 Applications, solvents
• CPC Class Codes: C07C 67/03 by reacting an ester group with a hydroxy group
• CPC Class Codes: C07C 69/82 Terephthalic acid esters
• CPC Class Codes: C08J 11/24 containing hydroxyl groups
• CPC Class Codes: C08J 2367/02 Polyesters derived from dicarboxylic acids and dihydroxy compounds; C08J2367/06 takes precedence
• CPC Class Codes: C09B 67/0096 Purification; Precipitation; Filtration
• CPC Class Codes: D06P 5/137 with other compounds
• CPC Class Codes: Y02W 30/62 Plastics recycling; Rubber recycling

Abstract

To establish an efficient and economical useful component recovery method capable of recovering high purity useful components from a dyed polyester fiber.

A method for recovering useful components from a dyed polyester fiber, includes a dye extraction step, a solid liquid separation step, a depolymerization reaction step, an ester interchange reaction step, and a useful component separation step, for recovering useful components from the dyed polyester fiber, wherein the dye extraction step includes a step of extracting and removing a dye at the glass transition temperature of the polyester or higher and at 220° C. or less with a xylene extracting solvent and an alkylene glycol extracting solvent in combination.

Claims

1. A method for recovering useful components from a dyed polyester fiber, comprising a dye extraction step, a solid liquid separation step, a depolymerization reaction step, an ester interchange reaction step, and a useful component separation step, the dye extraction step being a step of extracting and removing a dye at the glass transition temperature of the polyester or higher and at 220°

C. or less by an extracting solvent including xylene and alkylene glycol from the dyed polyester fiber, the solid liquid separation step being a step of separating a dye-extracted polyester fiber and a dye-containing extracting solvent after the dye extraction step, the depolymerization reaction step being a step of allowing the dye-extracted polyester fiber to undergo a depolymerization reaction with alkylene glycol in the presence of a depolymerization catalyst, thereby to obtain a depolymerized solution containing bis-ω

-hydroxy alkylene terephthalate, the ester interchange reaction step being a step of allowing the depolymerized solution to undergo an ester interchange reaction by an ester interchange catalyst and methanol, and the useful component separation step being a step of separating and recovering dimethyl terephthalate and alkylene glycol from the ester interchange reaction product mixture obtained in the ester interchange reaction step.

2. The method for recovering useful components according to claim 1, comprising at least one step selected from a group consisting of a solid matter removing step of removing solid matters during the process or after the process of the depolymerization reaction step, a depolymerized solution concentration step of distilling or evaporating a part of xylene and/or alkylene glycol from the depolymerized solution during the process or after the process of the depolymerization reaction step, and a polyamide dissolution and removal step of dissolving and removing polyamide.

3. The method for recovering useful components according to claim 1, comprising an extracting solvent recovery step of recovering xylene and/or alkylene glycol from the dye-containing extracting solvent by distillation.

4. The method for recovering useful components according to claim 1, wherein the polyester fiber is a polyester fiber formed of polyester formed from a repeating unit formed from an alkylene glycol as a raw material, and the alkylene glycol in the dye extraction step is the same compound as the alkylene glycol which is a raw material for forming the repeating unit of the polyester forming the polyester fiber.

5. The method for recovering useful components according to claim 1, wherein the alkylene glycol in the dye extraction step is the same compound as the alkylene glycol in the depolymerization reaction step.

6. The method for recovering useful components according to claim 1, wherein xylene for use in the dye extraction step is at least one xylene selected from a group consisting of mixed xylene, paraxylene, metaxylene, and orthoxylene, and alkylene glycol for use in the dye extraction step is at least one alkylene glycol selected from a group consisting of ethylene glycol, diethylene glycol, 1,3-propanediol, and 1,4-butanediol.

7. The method for recovering useful components according to claim 1, wherein the dye extraction step is carried out in a batch type reaction tank or a countercurrent continuous reaction tank.

8. The method for recovering useful components according to claim 1, wherein the polyester fiber is a fiber including polyethylene terephthalate.

9. The method for recovering useful components according to claim 1, comprising at least one method selected from a group consisting of a method using alkylene glycol and xylene in mixture, a method using alkylene glycol after using xylene, and a method using xylene after using alkylene glycol, in the dye extraction step.

10. The method for recovering useful components according to claim 1, wherein in the dye extraction step, the extraction temperature for using alkylene glycol is the glass transition temperature of the polyester to 200°

C., the extraction temperature for using xylene is the glass transition temperature of the polyester to 144°

C., and the pressure in the dye extraction step is atmospheric pressure when the dye extraction step comprises one or more steps selected from the group consisting of applying alkylene glycol and xylene in a mixture, applying xylene, and applying alkylene glycol.

11. The method for recovering useful components according to claim 1, wherein the amount of alkylene glycol for use in the dye extraction step is 4 parts by weight to 10 parts by weight per 1 part by weight of the dyed polyester.

12. The method for recovering useful components according to claim 1, wherein the amount of xylene for use in the dye extraction step is 4 parts by weight to 12 parts by weight per 1 part by weight of the dyed polyester.