WO2006036823A2 - Colorant removal from polymeric fibers - Google Patents

Colorant removal from polymeric fibers Download PDF

Info

Publication number
WO2006036823A2
WO2006036823A2 PCT/US2005/034242 US2005034242W WO2006036823A2 WO 2006036823 A2 WO2006036823 A2 WO 2006036823A2 US 2005034242 W US2005034242 W US 2005034242W WO 2006036823 A2 WO2006036823 A2 WO 2006036823A2
Authority
WO
WIPO (PCT)
Prior art keywords
ester
stripping composition
composition
fibers
polyamide
Prior art date
Application number
PCT/US2005/034242
Other languages
French (fr)
Other versions
WO2006036823A3 (en
Inventor
Lloyd Ballard Mauldin
Jerry Allen Cook
Original Assignee
Chemical Products Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chemical Products Corporation filed Critical Chemical Products Corporation
Publication of WO2006036823A2 publication Critical patent/WO2006036823A2/en
Publication of WO2006036823A3 publication Critical patent/WO2006036823A3/en

Links

Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P5/00Other features in dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form
    • D06P5/13Fugitive dyeing or stripping dyes
    • D06P5/137Fugitive dyeing or stripping dyes with other compounds

Definitions

  • Articles produced from virgin polymers are typically colored for both practical and aesthetic reasons.
  • Articles other than fibers typically have colorants dispersed throughout the article.
  • poly olefin fibers have colorants dispersed throughout the fiber because surface dyeing techniques have proven unsuccessful.
  • Polyester, Nylon 6, and Nylon 6,6 fibers are typically colored by dyeing the surface of the already-formed fibers.
  • recycled polymer derived from post-consumer fibers One significant limitation to the utility of recycled polymer derived from post-consumer fibers is the color difference between virgin polymer and recycled polymer.
  • the dyes on the surface of recycled polymeric fibers may significantly decrease the suitability of the constituent polymer for reuse because color is not necessarily removed during conventional recycling processes.
  • a process directed to the removal of surface colorants is applicable only to certain polymeric fibers.
  • a substantial quantity of polyamide fiber from post consumer carpet is potentially available for recycle.
  • Approximately 40% of the face fibers in post residential carpet waste in the United States is surface dyed Nylon 6, while another 40% is surface dyed Nylon 6,6.
  • Processes for stripping dyes from fabric include U.S. 4. ,227,881 (Fono) which discloses a process for stripping dyes from textile fabric which involving heating an aqueous solution of an ammonium salt, a sulfite salt and an organic sulfonate, such as sodium hydroxymethane sulfonate, to at least 60 degrees Celsius and adding the dyed fabric to the heated solution while maintaining the temperature of the solution. This process is believed to result in less that satisfactory colorant removal.
  • Patent Application Laida teaches a process for stripping color- from synthetic polymer products by contacting the colored polymer with a chemical system including unstable dispersions of alkyl halides and aqueous solutions of bleaching/oxidizing agents to which specified quantities of acids and surfactant/wetting agents are added.
  • a chemical system including unstable dispersions of alkyl halides and aqueous solutions of bleaching/oxidizing agents to which specified quantities of acids and surfactant/wetting agents are added.
  • the use of this chemical system may restrict the recyclability of the decolorized polymeric materials.
  • U.S. Pat. No. 5,989,296 teaches a process for removing indigo dye from denim scrap by extracting the fabric with an organic solvent such as 1,1,2- trichloroethane in which the indigo dye is soluble at elevated temperatures, the solvent is cooled and extracted with an aqueous phase containing a reducing agent, and the aqueous phase is treated to oxidize and recover the indigo dye.
  • an organic solvent such as 1,1,2- trichloroethane in which the indigo dye is soluble at elevated temperatures
  • the solvent is cooled and extracted with an aqueous phase containing a reducing agent, and the aqueous phase is treated to oxidize and recover the indigo dye.
  • This process is applicable only to indigo dyes.
  • U.S. Patent No. 6,083,283 (Berkstresser, IV) teaches a process for removing color and extracting dyes from polymeric materials by contacting them with a swelling agent under conditions such that the swelling agent interrupts the molecular forces within the polymer matrix and opens the polymer structure sufficiently to remove natural and synthetic pigments dispersed throughout a polymeric article, thus it has wide applicability for colored polymeric articles other than surface dyed fibers.
  • the use of swelling agents which penetrate throughout the polymer matrix to remove surface dyes is potentially undesirable because completely removing them after decolorization of the fiber would be expected to involve extensive washing.
  • the present invention is directed to a method for removing surface dyes and colorants from polymeric materials. More particularly, the present invention is directed to a method for decolorizing Nylon 6, and Nylon 6,6 fibers for the purpose of increasing the suitability of the constituent polymers for subsequent reuse. The present invention is directed to a cost-effective and environmentally friendly process for removing surface stains and dye-imparted color from colored polymeric fibers.
  • the process and composition of the present invention are particularly useful in the recycling of thermoplastic materials.
  • Materials decolorized by the process of the present invention may be utilized in place of or blended with virgin thermoplastics in any known thermoplastics applications including extruding the melted material to form fiber which may be dyed.
  • a dye or other colorant can be substantially removed from the surface of polymeric materials, particularly fibers, by contacting the materials with an organic ester solvent stripping composition containing a cyclic ester, particularly ethylene carbonate, propylene carbonate, or butylene carbonate, at a temperature below the boiling temperature of the ester solvent stripping composition to effect the release of dye or other colorant from the surface of the polymer.
  • an organic ester solvent stripping composition containing a cyclic ester, particularly ethylene carbonate, propylene carbonate, or butylene carbonate
  • the process of the present invention includes contacting colored polyamide fibers with at least one ester solvent stripping composition under conditions sufficient to effect release of the colorant from the surface of the fibers.
  • the process is especially useful for quickly and thoroughly removing colorants from surface dyed polyamide fibers as part of a recycling process for such fibers.
  • Colorants are considered to be any dye, pigment or colored composition or combinations thereof that may intentionally or accidentally color or stain polymeric materials, while dyes are considered to be organic materials which impart color to a polymer and which chemically bond to the polymer surface primarily by ionic mechanisms.
  • the process of the present invention removes colorants from the surface of polyamide fibers without substantially degrading Nylon 6 or Nylon 6,6 polyamide polymers, thus allowing for their recovery and reuse.
  • a process for recycling colored polyamide fibers comprises the steps of shearing or cutting Nylon 6 or Nylon 6,6 face fibers from post consumer carpet waste, then contacting the colored polyamide fibers with an ester stripping solvent solution at a temperature effective to remove colorant from the surface of the polymeric material.
  • a process for recycling colored polyamide fibers comprises the steps of shredding the entire carpet and grinding the face fibers and backing components to yield individual fibers commingled with discrete particles of backing materials, then separating the fibers from the non-fibrous components before contacting the colored polyamide fibers with an ester stripping solvent solution at a temperature effective to remove colorant from the surface of the polymeric material.
  • Another embodiment of the process of the present invention which can allow recycling of the ester solvent stripping composition used to decolorize colored polyamide material comprising: (a) removal of colorant from colored polyamide fibers utilizing an ester solvent stripping composition further containing an alcohol that separates as an immiscible liquid phase as the ester solvent stripping composition is cooled to ambient temperature; (b) cooling the ester solvent stripping composition to a temperature between about 20 degrees and about 90 degrees Celsius, whereby the solution separates into an ester phase and an alcohol phase containing colorant; and (c) removing colorant from the alcohol phase through further separate processing while the ester phase is immediately available for reuse as a component of the ester solvent stripping composition.
  • United States patent application 10/708,479 discloses that polyester polymer is decomposed when heated in the presence of a cyclic ester such as propylene carbonate to form an admixture having utility as an industrial solvent.
  • This novel solvent composition is also suitable for the practice of the present invention, hi this embodiment of the invention, the colored polyamide fibers are contacted with the ester solvent stripping composition at a temperature between about 90 degrees Celsius and about 220 degrees Celsius.
  • the process of decolorization should preferably be preceded by one or more of the preliminary steps of (a) physically segregating carpet pieces having Nylon 6, or Nylon 6,6 face fibers; (b) cleaning the group of carpet pieces containing only one of Nylon 6 or Nylon 6,6 face fibers from step (a) by mechanically separating dirt and other loosely- attached foreign materials; (c) separating the Nylon 6 or Nylon 6,6 face fibers from the backing of the carpet by a method selected from the group consisting of mechanical shearing, melt-cutting with a hot wire, melt-cutting with a laser, shredding followed by grinding and air elutriation, and combinations thereof; and (d) cutting, shearing, or grinding the colored fibers into fibrous particles having reduced size.
  • the decolored polymeric material can be subsequently washed with a polar cyclic ester such as ethylene carbonate, propylene carbonate, butylene carbonate, and mixtures thereof, containing no dissolved colorant.
  • a polar cyclic ester such as ethylene carbonate, propylene carbonate, butylene carbonate, and mixtures thereof.
  • the present invention has a number of advantages over prior art decolorization methods.
  • the present invention does not substantially degrade the polymer and therefore recovered polymer can be used in new polymeric materials or articles in place of virgin polymer.
  • the stripping solvents of the present invention laden with colorants can be thoroughly removed from the surface of the fibers with relative ease because the stripping agent does not penetrate into the fibers and disrupt the molecular forces within the polymer matrix sufficiently to result in an opening of the polymer structure.
  • the process of the present invention includes contacting colored polymeric fibers with at least one ester solvent stripping composition under conditions so as to effect the release of a dye or other colorant from the surface of the polymeric material.
  • the amount of the ester solvent stripping composition and the conditions under which the contacting takes place are selected so that the polymeric material does not undergo substantial destruction or degradation.
  • the contacting step is most preferably performed at ambient pressure.
  • the combined effect of temperature and the formulation of a suitable contacting composition can be used to control the processes of the present invention.
  • variation and optimization of the contacting composition, and the temperature, time, and repetition conditions of the contacting process in order to maximize the decolorizing effect of the contacting composition are considered to be within the scope of the present invention.
  • ester solvent stripping compositions containing esters and alcohols that boil at relatively high temperatures can be used.
  • a preferred practice of this invention utilizes the temperature dependence of the solubility of dyes in the ester solvent stripping compositions to effect separation of dyes from the ester solvent stripping compositions.
  • the dyes are removed as particulate precipitates, thus allowing recycling of the ester solvent stripping compositions.
  • the dissolved dyes can be removed from the ester solvent stripping compositions by prior art techniques such as adsorption onto activated carbon or some other solid surface, chemical destruction, or electrolytic coagulation.
  • the residence time for contacting the colored polymeric material with the contacting composition during the contacting step may be controlled to ensure the desired degree of color removal. Suitable residence times for the contacting step will depend upon the conditions of the contacting step. The preferred residence time is at least about 1/2 minute and no greater than about 20 minutes, more preferably about 3 to 10 minutes.
  • the contacting step in these embodiments may include a plurality of contacting stages wherein the colored polymeric material is contacted with an ester solvent stripping composition at each stage.
  • the residence time varies depending on the temperature and other conditions in order to achieve the results of the present invention.
  • the process of the present invention may further include a washing step, wherein any residual dye, colorant, or ester solvent stripping composition is removed.
  • Suitable washing agents should at least partially solubilize residual dye, colorant or ester solvent stripping composition without harming the decolorized polymeric material. Washing agents should be polar liquids and preferably are selected from the group including ethylene carbonate and propylene carbonate. Water, C.sub.l to C. sub.4 aliphatic alcohols, and mixtures thereof may also be used. An after treatment wash with an aqueous 0.1% to 0.3% sodium hydrosulf ⁇ te solution may also be employed to enhance final polymer color.
  • the contacting step may be performed using a variety of techniques that will be apparent to one of ordinary skill in the art. Such techniques include immersing the colored polymeric material in the ester solvent stripping composition, spraying an effective amount of ester solvent stripping composition onto the polymeric material, and other similar such techniques. Further the contacting step may be carried out in lots in a batch-wise manner or it may be carried out in a continuous manner.
  • dyed nylon fiber is contacted with the solvent composition disclosed in copending patent application 10/708,479 (Mauldin) at a temperature of at least about 130 degrees Celsius for a period of about 0.5 to 5 minutes. A series of two or three sequential treatments can be employed to improve the final polymer product color.
  • EXAMPLE 1 A deep red surface-dyed Nylon 6 yarn was cut into about 1 inch lengths and
  • Nylon 6 carpet fibers recovered from industrial commercial carpet waste were obtained from a commercial carpet manufacturer.
  • the fibers were deep blue in color.
  • Ten grams of these fibers were placed into an Erlenmeyer flask with 100 grams of solvent composed of 80 grams of Propylene Carbonate and 20 grams of 2-Octanol.
  • the fibers were immersed in the solvent and heated to a temperature of 130 degrees Celsius, whereupon the solvent was separated from the Nylon 6 fibers by filtration.
  • the fibers had assumed an off-white color.
  • the solvent was observed to have a blue color.
  • the 2-Octanol phase was substantially darker blue in color than the Propylene Carbonate phase.

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

Novel organic compositions for removing dyes from the surface of polymeric fibers are disclosed. The method for dye removal from the surface of fibers includes contacting the fibers with a non-aqueous ester stripping composition preferably containing at least one cyclic ester and optionally containing a surfactant, an alcohol, or both. The process of the present invention is especially useful for removing color from dyed polyamide fibers as part of a recycling process for such materials.

Description

COLORANT REMOVAL FROM POLYMERIC FIBERS
CROSS REFERENCE TO RELATED APPLICATIONS This application claims priority to and the benefit of U.S. Application Serial No. 10/708,623 filed September 27, 2004.
BACKGROUNDOF INVENTION
Articles produced from virgin polymers are typically colored for both practical and aesthetic reasons. Articles other than fibers typically have colorants dispersed throughout the article. In addition, poly olefin fibers have colorants dispersed throughout the fiber because surface dyeing techniques have proven unsuccessful. Polyester, Nylon 6, and Nylon 6,6 fibers are typically colored by dyeing the surface of the already-formed fibers.
One significant limitation to the utility of recycled polymer derived from post-consumer fibers is the color difference between virgin polymer and recycled polymer. The dyes on the surface of recycled polymeric fibers may significantly decrease the suitability of the constituent polymer for reuse because color is not necessarily removed during conventional recycling processes.
A process directed to the removal of surface colorants is applicable only to certain polymeric fibers. However, a substantial quantity of polyamide fiber from post consumer carpet is potentially available for recycle. Approximately 40% of the face fibers in post residential carpet waste in the United States is surface dyed Nylon 6, while another 40% is surface dyed Nylon 6,6.
Processes for stripping dyes from fabric include U.S. 4. ,227,881 (Fono) which discloses a process for stripping dyes from textile fabric which involving heating an aqueous solution of an ammonium salt, a sulfite salt and an organic sulfonate, such as sodium hydroxymethane sulfonate, to at least 60 degrees Celsius and adding the dyed fabric to the heated solution while maintaining the temperature of the solution. This process is believed to result in less that satisfactory colorant removal. U.S. Pat. No. 4,783,193 (Pensa) teaches a process for stripping color- from synthetic polymer products by contacting the colored polymer with a chemical system including unstable dispersions of alkyl halides and aqueous solutions of bleaching/oxidizing agents to which specified quantities of acids and surfactant/wetting agents are added. The use of this chemical system may restrict the recyclability of the decolorized polymeric materials.
U.S. Pat. No. 5,989,296 (Patton) teaches a process for removing indigo dye from denim scrap by extracting the fabric with an organic solvent such as 1,1,2- trichloroethane in which the indigo dye is soluble at elevated temperatures, the solvent is cooled and extracted with an aqueous phase containing a reducing agent, and the aqueous phase is treated to oxidize and recover the indigo dye. This process is applicable only to indigo dyes.
U.S. Patent No. 6,083,283 (Berkstresser, IV) teaches a process for removing color and extracting dyes from polymeric materials by contacting them with a swelling agent under conditions such that the swelling agent interrupts the molecular forces within the polymer matrix and opens the polymer structure sufficiently to remove natural and synthetic pigments dispersed throughout a polymeric article, thus it has wide applicability for colored polymeric articles other than surface dyed fibers. The use of swelling agents which penetrate throughout the polymer matrix to remove surface dyes is potentially undesirable because completely removing them after decolorization of the fiber would be expected to involve extensive washing.
Thus an unmet need exists for a cost-effective and environmentally friendly process for removing surface colorant from synthetic polymeric fibers without degrading the fiber, or otherwise compromising the polymeric material's suitability for recycling and re-use. This unmet need exists particularly for a process to remove surface colorants from the substantial surface dyed Nylon 6 and Nylon 6,6 fiber component of post-residential waste carpet. A process that can be conducted at atmospheric pressure is most attractive. SUMMARY OF INVENTION
The present invention is directed to a method for removing surface dyes and colorants from polymeric materials. More particularly, the present invention is directed to a method for decolorizing Nylon 6, and Nylon 6,6 fibers for the purpose of increasing the suitability of the constituent polymers for subsequent reuse. The present invention is directed to a cost-effective and environmentally friendly process for removing surface stains and dye-imparted color from colored polymeric fibers.
The process and composition of the present invention are particularly useful in the recycling of thermoplastic materials. Materials decolorized by the process of the present invention may be utilized in place of or blended with virgin thermoplastics in any known thermoplastics applications including extruding the melted material to form fiber which may be dyed.
It was unexpectedly discovered that a dye or other colorant can be substantially removed from the surface of polymeric materials, particularly fibers, by contacting the materials with an organic ester solvent stripping composition containing a cyclic ester, particularly ethylene carbonate, propylene carbonate, or butylene carbonate, at a temperature below the boiling temperature of the ester solvent stripping composition to effect the release of dye or other colorant from the surface of the polymer. Thus the process can be carried out at ambient pressure.
The process of the present invention includes contacting colored polyamide fibers with at least one ester solvent stripping composition under conditions sufficient to effect release of the colorant from the surface of the fibers. The process is especially useful for quickly and thoroughly removing colorants from surface dyed polyamide fibers as part of a recycling process for such fibers.
Colorants are considered to be any dye, pigment or colored composition or combinations thereof that may intentionally or accidentally color or stain polymeric materials, while dyes are considered to be organic materials which impart color to a polymer and which chemically bond to the polymer surface primarily by ionic mechanisms. The process of the present invention removes colorants from the surface of polyamide fibers without substantially degrading Nylon 6 or Nylon 6,6 polyamide polymers, thus allowing for their recovery and reuse.
In one embodiment of the present invention, a process for recycling colored polyamide fibers comprises the steps of shearing or cutting Nylon 6 or Nylon 6,6 face fibers from post consumer carpet waste, then contacting the colored polyamide fibers with an ester stripping solvent solution at a temperature effective to remove colorant from the surface of the polymeric material. In another embodiment, a process for recycling colored polyamide fibers comprises the steps of shredding the entire carpet and grinding the face fibers and backing components to yield individual fibers commingled with discrete particles of backing materials, then separating the fibers from the non-fibrous components before contacting the colored polyamide fibers with an ester stripping solvent solution at a temperature effective to remove colorant from the surface of the polymeric material. These two embodiments are especially useful in recycling the surface dyed polyamide face fiber component of post-consumer carpet.
Another embodiment of the process of the present invention which can allow recycling of the ester solvent stripping composition used to decolorize colored polyamide material comprising: (a) removal of colorant from colored polyamide fibers utilizing an ester solvent stripping composition further containing an alcohol that separates as an immiscible liquid phase as the ester solvent stripping composition is cooled to ambient temperature; (b) cooling the ester solvent stripping composition to a temperature between about 20 degrees and about 90 degrees Celsius, whereby the solution separates into an ester phase and an alcohol phase containing colorant; and (c) removing colorant from the alcohol phase through further separate processing while the ester phase is immediately available for reuse as a component of the ester solvent stripping composition.
United States patent application 10/708,479 (Mauldin) discloses that polyester polymer is decomposed when heated in the presence of a cyclic ester such as propylene carbonate to form an admixture having utility as an industrial solvent. This novel solvent composition is also suitable for the practice of the present invention, hi this embodiment of the invention, the colored polyamide fibers are contacted with the ester solvent stripping composition at a temperature between about 90 degrees Celsius and about 220 degrees Celsius.
In practicing the present invention to decolorize the colored polymeric face fiber component of post consumer carpet waste, the process of decolorization should preferably be preceded by one or more of the preliminary steps of (a) physically segregating carpet pieces having Nylon 6, or Nylon 6,6 face fibers; (b) cleaning the group of carpet pieces containing only one of Nylon 6 or Nylon 6,6 face fibers from step (a) by mechanically separating dirt and other loosely- attached foreign materials; (c) separating the Nylon 6 or Nylon 6,6 face fibers from the backing of the carpet by a method selected from the group consisting of mechanical shearing, melt-cutting with a hot wire, melt-cutting with a laser, shredding followed by grinding and air elutriation, and combinations thereof; and (d) cutting, shearing, or grinding the colored fibers into fibrous particles having reduced size. Optionally, the decolored polymeric material can be subsequently washed with a polar cyclic ester such as ethylene carbonate, propylene carbonate, butylene carbonate, and mixtures thereof, containing no dissolved colorant. The present invention has a number of advantages over prior art decolorization methods. The present invention does not substantially degrade the polymer and therefore recovered polymer can be used in new polymeric materials or articles in place of virgin polymer. The stripping solvents of the present invention laden with colorants can be thoroughly removed from the surface of the fibers with relative ease because the stripping agent does not penetrate into the fibers and disrupt the molecular forces within the polymer matrix sufficiently to result in an opening of the polymer structure.
DETAILED DESCRIPTION The process of the present invention includes contacting colored polymeric fibers with at least one ester solvent stripping composition under conditions so as to effect the release of a dye or other colorant from the surface of the polymeric material. The amount of the ester solvent stripping composition and the conditions under which the contacting takes place are selected so that the polymeric material does not undergo substantial destruction or degradation. The contacting step is most preferably performed at ambient pressure.
As will be apparent to one skilled in the art, the combined effect of temperature and the formulation of a suitable contacting composition can be used to control the processes of the present invention. Thus variation and optimization of the contacting composition, and the temperature, time, and repetition conditions of the contacting process in order to maximize the decolorizing effect of the contacting composition are considered to be within the scope of the present invention. It should be noted that since the process is conducted at ambient pressure, only ester solvent stripping compositions containing esters and alcohols that boil at relatively high temperatures can be used.
A preferred practice of this invention utilizes the temperature dependence of the solubility of dyes in the ester solvent stripping compositions to effect separation of dyes from the ester solvent stripping compositions. The dyes are removed as particulate precipitates, thus allowing recycling of the ester solvent stripping compositions.
Alternatively, the dissolved dyes can be removed from the ester solvent stripping compositions by prior art techniques such as adsorption onto activated carbon or some other solid surface, chemical destruction, or electrolytic coagulation. The residence time for contacting the colored polymeric material with the contacting composition during the contacting step may be controlled to ensure the desired degree of color removal. Suitable residence times for the contacting step will depend upon the conditions of the contacting step. The preferred residence time is at least about 1/2 minute and no greater than about 20 minutes, more preferably about 3 to 10 minutes. The contacting step in these embodiments may include a plurality of contacting stages wherein the colored polymeric material is contacted with an ester solvent stripping composition at each stage. One skilled in the art would appreciate that the residence time varies depending on the temperature and other conditions in order to achieve the results of the present invention.
The process of the present invention may further include a washing step, wherein any residual dye, colorant, or ester solvent stripping composition is removed. Suitable washing agents should at least partially solubilize residual dye, colorant or ester solvent stripping composition without harming the decolorized polymeric material. Washing agents should be polar liquids and preferably are selected from the group including ethylene carbonate and propylene carbonate. Water, C.sub.l to C. sub.4 aliphatic alcohols, and mixtures thereof may also be used. An after treatment wash with an aqueous 0.1% to 0.3% sodium hydrosulfϊte solution may also be employed to enhance final polymer color.
The contacting step may be performed using a variety of techniques that will be apparent to one of ordinary skill in the art. Such techniques include immersing the colored polymeric material in the ester solvent stripping composition, spraying an effective amount of ester solvent stripping composition onto the polymeric material, and other similar such techniques. Further the contacting step may be carried out in lots in a batch-wise manner or it may be carried out in a continuous manner. In an especially preferred embodiment, dyed nylon fiber is contacted with the solvent composition disclosed in copending patent application 10/708,479 (Mauldin) at a temperature of at least about 130 degrees Celsius for a period of about 0.5 to 5 minutes. A series of two or three sequential treatments can be employed to improve the final polymer product color.
The following examples are included to demonstrate preferred embodiments of the invention. Those skilled in the art should, in light of the present disclosure, appreciate that many changes can be made in the specific embodiments which are disclosed and still obtain a like or similar result without departing from the spirit and scope of the invention.
EXAMPLE 1 A deep red surface-dyed Nylon 6 yarn was cut into about 1 inch lengths and
10 grams of the yarn was placed into an Erlenmeyer flask with 100 grams of solvent prepared by admixing 100 grams of Propylene Carbonate with 20 grams of Poly(ethylene terephthalate) yarn and heating the admixture to 230 degrees Celsius for 15 minutes. The Nylon 6 yarn pieces were immersed in the ester solvent composition, heated to a temperature of 160 degrees Celsius, whereupon the solvent was separated from the Nylon 6 fibers by filtration. The Nylon 6 yarn pieces were visibly lighter in color and the ester solvent composition was observed have a strong red color. EXAMPLE 2 Colored Nylon 6,6 carpet fibers recovered from post-residential carpet waste were obtained from a commercial broker of recycled thermoplastic materials. Ten grams of these fibers were selected to obtain fibers of at least four distinct colors including red, blue, beige, and brown; the fibers were placed into an Erlenmeyer flask with 100 grams of solvent composed of 70 grams of Propylene Carbonate and 30 grams of "Soygold 1000" methyl ester of soybean oil. The fibers were immersed in the ester solvent and heated to a temperature of 200 degrees Celsius, whereupon the solvent was separated from the Nylon 6,6 fibers by filtration. The fibers had assumed a uniform light gray appearance while the ester solvent composition was observed to have a brown coloration. EXAMPLE 3
Surface-dyed Nylon 6 carpet fibers recovered from industrial commercial carpet waste were obtained from a commercial carpet manufacturer. The fibers were deep blue in color. Ten grams of these fibers were placed into an Erlenmeyer flask with 100 grams of solvent composed of 80 grams of Propylene Carbonate and 20 grams of 2-Octanol. The fibers were immersed in the solvent and heated to a temperature of 130 degrees Celsius, whereupon the solvent was separated from the Nylon 6 fibers by filtration. The fibers had assumed an off-white color. The solvent was observed to have a blue color. Upon cooling below 55 degrees Celsius, the solvent separated into 2 liquid phases with the greatest volume represented by the lower phase. The 2-Octanol phase was substantially darker blue in color than the Propylene Carbonate phase. While the compositions and methods of this invention have been described in terms of preferred embodiments, the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof, and accordingly, reference should be made to the appended claims, rather than to the foregoing specification, as indicating the scope of the invention.

Claims

Cl aim s
1. A process for removing colorants from surface-dyed polyamide fibers comprising:
(a) contacting said fibers with an organic solvent stripping composition containing at least one cyclic ester at an elevated temperature; and (b) separating the fibers from at least a portion of the solvent stripping composition containing dissolved dye.
2. The process of claim 1 wherein the solvent stripping composition containing at least one cyclic ester is ethylene carbonate, propylene carbonate, butylenes carbonate, or mixtures thereof.
3. The process of claim 1 wherein the solvent stripping composition further contains an alcohol from the group of C. sub.7 to C.sub.12 alcohols, or mixtures thereof, in addition to at least one cyclic ester.
4. The process of claim 1 wherein the solvent stripping composition is present in an amount of at least about 200% by weight of the polyamide fibers.
5. The process of claim 2 wherein the solvent stripping composition is propylene carbonate.
6. The process of claim 1 wherein the solvent stripping composition is substantially non-reactive with the dyes.
7. The process of claim 1 wherein the solvent stripping composition further comprises a surfactant.
8. The process of claim 5 wherein the contacting is conducted at a temperature between about 130 degrees Celsius and about 220 degrees Celsius.
9. The process of claim 1 wherein the stripping composition contains decomposition products of poly (ethylene terephthalate) formed by heating poly(ethylene terephthalate) in the presence of a cyclic ester to a temperature above about 21 5 degrees Celsius.
10. The process of claim 1 wherein the stripping composition contains poly(ethylene terephthalate).
11. A process for removing colorants from the surface of a polyamide material comprising:
(a) contacting the polyamide material with a first ester stripping composition at a temperature up to about the boiling temperature of the first ester stripping composition but without substantial dissolution or degradation of the polyamide material;
(b) separating the polyamide material from at least a portion of the first ester stripping composition; and
(c) contacting the polyamide material with a second ester stripping composition at a temperature up to about the boiling temperature of the second stripping composition.
12. The process of claim 11 wherein in step (a) the first ester stripping composition is composed exclusively of ethylene carbonate, propylene carbonate, butylenes carbonate, or mixtures thereof.
13. The process of claim 11 wherein in step (c) the second ester stripping composition is composed exclusively of ethylene carbonate, propylene carbonate, butylene carbonate, or mixtures thereof.
14. The process of claim 12 wherein the first ester stripping composition is present in an amount of at least about 200% by weight of the polyamide material.
1 5. The process of claim 11 wherein in step (a) the first ester stripping composition contains a cyclic ester and decomposition products of poly (ethylene terephthalate) formed by heating poly(ethylene terephthalate) in the presence of a cyclic ester to a temperature above about 215 degrees Celsius.
16. The process of claim 13 wherein the second ester stripping composition is composed exclusively of propylene carbonate.
17. The process of claim 11 wherein in step (a) the first ester stripping composition further comprises a surfactant.
18. The process of claim 11 wherein in step (a) the polyamide material is contacted with the first ester stripping composition at a temperature between about 130 degrees Celsius and about 200 degrees Celsius.
19. The process of claim 11 wherein in step (a) the first ester stripping composition contains propylene carbonate and the methyl ester of soybean oil.
20. The process of claim 11 wherein in step (c) the second ester stripping composition contains a cyclic ester and decomposition products of poly(ethylene terephthalate) formed by heating poly(ethylene terephthalate) in the presence of a cyclic ester to a temperature above about 215 degrees Celsius.
21. The process of claim 11 wherein in step (a) the first ester stripping composition contains poly(ethylene terephthalate).
22. A process for removing a colorant from the surface of polyamide material comprising:
(a) contacting the polyamide material with an ester composition under conditions sufficient to promote substantial release of the colorant from the surface of the polyamide material into the ester composition; and (b) separating the polyamide material from at least a portion of the ester composition containing released colorant through centrifugation, sedimentation, filtration, or combinations thereof.
23. The process of claim 22 wherein in step (a) the ester composition contains ethylene carbonate, propylene carbonate, butylene carbonate, or mixtures thereof.
24. The process of claim 23 wherein in step (a) the ester composition further contains one or more C.sub.7 to C. sub.12 alcohols.
25. The process of claim 22 wherein the ester composition is present in an amount of at least about 400% by weight of the polyamide.
26. The process of claim 23 wherein the ester composition further contains decomposition products of poly(ethylene terephthalate) formed by heating poly(ethylene terephthalate) in the presence of propylene carbonate to a temperature above about 215 degrees Celsius.
27. The process of claim 22 wherein the ester composition further contains a methyl ester of a vegetable oil.
28. The process of claim 22 wherein in step (a) the contacting is conducted at a temperature up to the boiling temperature of the ester composition.
29. The process of claim 22 further comprising: (a) cooling the ester composition containing released colorant to precipitate the released colorant from the ester composition; and (b) separating the precipitated colorant from the ester composition through centrifugation, sedimentation, filtration, or combinations thereof.
30. A process for recycling colored polyamide fibers from post consumer carpet comprising:
(a) separating polyamide face fibers from carpet backing by shearing, cutting with a hot wire, cutting with a laser, or other means;
(b) contacting said face fibers with an organic ester composition containing at least one cyclic ester under conditions sufficient to substantially remove the colorant from the surface of the polyamide fibers without substantial dissolution or degradation of the polyamide; and (c) separating the polyamide fibers from at least a portion of the ester composition containing colorant.
31. The process of claim 30 wherein in step (b) the contacting is carried out at a temperature of between about 130 degrees Celsius and about 220 degrees Celsius. > 32. The process of claim 30 wherein in step (b) the ester composition containing at least one cyclic ester contains propylene carbonate and the decomposition products of poly(ethylene terephthalate) formed by heating poly(ethylene terephthalate) in the presence of propylene carbonate to a temperature above about 215 degree Celsius.
PCT/US2005/034242 2004-09-27 2005-09-23 Colorant removal from polymeric fibers WO2006036823A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/708,623 2004-09-27
US10/708,623 US20060070188A1 (en) 2004-09-27 2004-09-27 Colorant Removal from Polymeric Fibers

Publications (2)

Publication Number Publication Date
WO2006036823A2 true WO2006036823A2 (en) 2006-04-06
WO2006036823A3 WO2006036823A3 (en) 2008-09-04

Family

ID=36119467

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2005/034242 WO2006036823A2 (en) 2004-09-27 2005-09-23 Colorant removal from polymeric fibers

Country Status (2)

Country Link
US (1) US20060070188A1 (en)
WO (1) WO2006036823A2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008125465A1 (en) * 2007-04-11 2008-10-23 Basf Se Method for removing color from polymeric material

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8110131B1 (en) * 2006-12-06 2012-02-07 Dell Orco Sergio Carpet reclamation system
WO2023117882A1 (en) * 2021-12-20 2023-06-29 Basf Se Process for discoloration of a colored polymeric material
TWI809793B (en) * 2022-03-30 2023-07-21 財團法人工業技術研究院 Decolorization method for polyester textile

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4003880A (en) * 1975-05-19 1977-01-18 Monsanto Company Fabric dye stripping, separation and recovery of polyester
US6036726A (en) * 1995-10-27 2000-03-14 Solutia Inc. Process for separating polyamide from colorant
US6540791B1 (en) * 2000-03-27 2003-04-01 The Procter & Gamble Company Stable alkaline hair bleaching compositions and method for use thereof

Family Cites Families (87)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2639278A (en) * 1950-12-22 1953-05-19 Polymer Corp Method of preparing finely divided nylon powder
US2958677A (en) * 1955-05-10 1960-11-01 Phillips Petroleum Co Purification of polymers of the polyamide type
US3006867A (en) * 1958-01-31 1961-10-31 Gen Plastics Corp Method of reconstituting nylon by solution in formic acid and distillation with hydrocarbon
US3996058A (en) * 1974-07-12 1976-12-07 Bechtel International Corporation Inhibition of corrosion in a pipeline carrying a slurry
FI752346A (en) * 1974-09-13 1976-03-14 Ciba Geigy Ag
US4003881A (en) * 1975-02-24 1977-01-18 Monsanto Company Polyester polymer recovery from dyed polyester fabrics
CA1052048A (en) * 1975-04-25 1979-04-03 Monsanto Company Polyester polymer recovery
CH671575A4 (en) * 1975-05-26 1976-12-31
US4207184A (en) * 1975-06-17 1980-06-10 Ciba-Geigy Ag Process for the purification of industrial effluents
US4146704A (en) * 1976-09-24 1979-03-27 Kabushiki Kaisha Maruki Shokai Method for manufacture of finely powdered polyamide resin
US4137393A (en) * 1977-04-07 1979-01-30 Monsanto Company Polyester polymer recovery from dyed polyester fibers
US4165288A (en) * 1977-07-05 1979-08-21 Riegel Textile Corporation Process of treating waste water from a textile vat dyeing operation to produce a concentrate for reuse
US4227881A (en) * 1978-11-17 1980-10-14 Royce Chemical Company New process of color stripping dyed textile fabric
US4316005A (en) * 1979-06-28 1982-02-16 Ciba-Geigy Corporation Cationic adsorption agent
US4416936A (en) * 1980-07-18 1983-11-22 Phillips Petroleum Company Nonwoven fabric and method for its production
JPS59207966A (en) * 1983-05-13 1984-11-26 Mikuni Seisakusho:Kk Composite material composition utilizing synthetic fiber scrap
US4581144A (en) * 1984-09-07 1986-04-08 American Color And Chemical Corporation Method for treatment of impounded material (sludges) from the chemical treatment of spent sulfuric acid with lime
US4613664A (en) * 1984-12-28 1986-09-23 Toyo Boseki Kabushiki Kaisha Process for production of polyester
US4809397A (en) * 1986-01-21 1989-03-07 Edic Rug and carpet cleaner
US4880510A (en) * 1988-02-16 1989-11-14 Andco Environmental Processes, Inc. Method for removing dye stuffs from wastewater
US5198471A (en) * 1989-09-11 1993-03-30 Rensselaer Polytechnic Institute Polymer recycling by selective dissolution
DE69112401T2 (en) * 1990-06-15 1996-02-01 Crosfield Joseph & Sons TEXTILE TREATMENT.
AU2298392A (en) * 1991-07-01 1993-02-11 Fiber Industries Inc. Recovery of polyester from spent film
US5370757A (en) * 1991-08-30 1994-12-06 Basf Corporation Process for manufacturing substantially 100% nylon 6 carpet
DE4137744C2 (en) * 1991-11-15 1996-10-31 Kuesters Eduard Maschf Process for producing a layered material using plastic waste and inherently rigid layered material containing plastic waste
US5240530A (en) * 1992-02-10 1993-08-31 Tennessee Valley Performance Products, Inc. Carpet and techniques for making and recycling same
US5236959A (en) * 1992-03-12 1993-08-17 Hoechst Celanese Corporation Process for recycling polyester/cotton blends
ZA933072B (en) * 1992-05-01 1994-10-30 Hoechst Celanese Corp A tufted fabric.
US5241066A (en) * 1992-06-25 1993-08-31 Basf Corporation Method of recovering caprolactam from mixed waste
US5472763A (en) * 1992-11-04 1995-12-05 Hoechst Aktiengesellschaft Recyclable carpet floor covering
DE4241176B4 (en) * 1992-12-08 2005-12-22 Focke & Co.(Gmbh & Co. Kg) Apparatus for applying glue to blanks for folding boxes
EP0604897A1 (en) * 1992-12-28 1994-07-06 Hoechst Celanese Corporation Carpet containing a holt melt polyester layer
US5280105A (en) * 1993-01-14 1994-01-18 E. I. Du Pont De Nemours And Company Separation of nylon 6 from mixtures with nylon 6,6
US5294384A (en) * 1993-03-25 1994-03-15 Monsanto Company Thermoplastic composition and method for producing thermoplastic composition by melt blending carpet
US5360551A (en) * 1993-04-01 1994-11-01 Crompton & Knowles Corporation Process for color reduction of dye wastewater
US5453202A (en) * 1993-04-29 1995-09-26 American Color & Chemical Corporation Method for treatment of impounded sludges, soils and other contaminated solid materials
US5342854A (en) * 1993-07-28 1994-08-30 Hoechst Celanese Corporation Polyester dissolution for polyester/cotton blend recycle
US5481786A (en) * 1993-11-03 1996-01-09 Spartan Mills Method of manufacturing a recyclable carpet
US5430068A (en) * 1993-11-24 1995-07-04 E. I. Du Pont De Nemours And Company Recovery of polyamide using a solution process
US5914353A (en) * 1995-08-21 1999-06-22 Collins & Aikman Floorcoverings, Inc. Process of recycling waste polymeric material and an article utilizing the same
DE4416466A1 (en) * 1994-05-10 1995-11-16 Zimmer Ag Separation method for carpets
US5786280A (en) * 1994-06-23 1998-07-28 Eduard Kusters Maschinenfabrik Gmbh & Co. Kg Molded part and method of its production
US5497949A (en) * 1994-06-30 1996-03-12 Jps Automotive Products Corp. Apparatus for reclaiming waste carpeting
US5556158A (en) * 1994-07-19 1996-09-17 L&P Property Management Co. Mechanism for reclining furniture
SE503272C2 (en) * 1994-08-22 1996-04-29 Moelnlycke Ab Nonwoven material prepared by hydroentangling a fiber web and method for making such nonwoven material
US5824709A (en) * 1994-11-16 1998-10-20 Suka; Motoshi Method for recycling waste plastic material containing styrene polymer
US5604009A (en) * 1994-12-02 1997-02-18 Synthetic Industries, Inc. Non-adhesive bonded tufted carpet and method for making the same
DE59503020D1 (en) * 1994-12-13 1998-09-03 Hp Chemie Pelzer Res & Dev RECYCLABLE TEXTILE TOP FLOORS
TW328542B (en) * 1995-02-09 1998-03-21 Eastman Chem Co Process for recycling polyesters
US5516050A (en) * 1995-02-27 1996-05-14 Basf Corporation Industrial Rotary Shredder
US5849804A (en) * 1995-06-29 1998-12-15 Basf Corporation Recovery of polyamides from composite articles
US5952660A (en) * 1995-07-06 1999-09-14 Dsm N.V. & Institut Fur Chemo Method of identifying post consumer or post industrial waste carpet utilizing a hand-held infrared spectrometer
BE1009547A3 (en) * 1995-08-23 1997-05-06 Dsm Nv Process for reprocessing polyamide INTO CARPET WASTE.
US5626939A (en) * 1995-09-05 1997-05-06 Georgia Tech Synthetic wood from waste fibrous waste products
US5792336A (en) * 1995-09-18 1998-08-11 Elif Technologies Ltd. Method for purification of wastewater from soluble substances
US5704104A (en) * 1995-12-27 1998-01-06 Bacon; Forrest C. Method and machine for recycling discarded carpets
US5912062A (en) * 1996-01-26 1999-06-15 Georgia Tech Research Corporation Utilization of waste fibers in laminates
DE69708056T2 (en) * 1996-01-31 2002-06-20 Du Pont METHOD FOR CENTRIFUGAL SEPARATION OF MATERIALS
US5859071A (en) * 1996-04-15 1999-01-12 Lear Corporation Recycling of carpet scrap
US5994417A (en) * 1996-06-04 1999-11-30 Auburn University Process for recovering polymers from commingled materials
US5829690A (en) * 1996-06-07 1998-11-03 Sudrohrbau Gmbh & Co. Shredding apparatus with shearing action
US5639379A (en) * 1996-07-08 1997-06-17 Environmental Wastewater Services, Inc. Process for removing color and odor from aqueous effluent contaminated with textile dye
US6083283A (en) * 1996-10-24 2000-07-04 Solutia Inc. Method for removing color from ionically dyeable polymeric materials
DE19700155A1 (en) * 1997-01-07 1998-07-09 Henkel Kgaa Continuous washing process with waste water recirculation
US5769335A (en) * 1997-01-31 1998-06-23 Tennessee Technological University Method and apparatus for shear pulverization of polymer materials
US5919717A (en) * 1997-02-07 1999-07-06 Wallick; Judith L. Recycled fiber yarn and method for making same
US5898063A (en) * 1997-02-18 1999-04-27 Stefandl; Roland E. Carpet recycling process for nylon containing carpeting
US6140463A (en) * 1997-02-18 2000-10-31 Stefandl; Roland E. Process for recycling and recovery of purified nylon polymer
US6180192B1 (en) * 1997-03-24 2001-01-30 Wood Waste Energy, Inc. Solids produced from ash and process for producing the same
US5897066A (en) * 1997-04-07 1999-04-27 Forrest C. Bacon Claw drum for shredding used carpet
US5889142A (en) * 1997-04-21 1999-03-30 Alliedsignal Inc. Selective polyamide recovery from multi-component materials
US6061876A (en) * 1997-06-11 2000-05-16 John D. Hollingsworth On Wheels, Inc. Textile recycling machine
CA2295117A1 (en) * 1997-06-27 1999-01-07 The Procter & Gamble Company Non-aqueous, fatty acid-containing structured liquid detergent compositions
US5989296A (en) * 1998-02-02 1999-11-23 American Renewable Resources Llc Solvent process for recovering indigo dye from textile scrap
US6213557B1 (en) * 1998-05-12 2001-04-10 Johnson Controls Technology Company Vehicle seat assembly with thermoformed fibrous suspension panel
US6126096A (en) * 1998-06-24 2000-10-03 Robinson; Forrest L. Method and apparatus for separating and recovering fractional components of carpet
US6155020A (en) * 1998-08-27 2000-12-05 Deem; Thomas Shredded carpet insulation
US6211275B1 (en) * 1998-11-10 2001-04-03 New Jersey Institute Of Technology Wood substitute composition and process for producing same
US6291048B1 (en) * 1999-02-16 2001-09-18 Eastman Chemical Company Polymeric based carpet
US6503595B1 (en) * 2000-02-22 2003-01-07 Aristech Chemical Company Carpet having syndiotactic polypropylene backing and technique for making same
US6610769B1 (en) * 2000-06-30 2003-08-26 Basf Corporation Carpet backing adhesive and its use in recycling carpet
US7252691B2 (en) * 2001-03-06 2007-08-07 John Philipson Conversion of municipal solid waste to high fuel value
EP1444077A1 (en) * 2001-10-24 2004-08-11 Infiltrator Systems, Inc. A method for recycling carpet and articles made therefrom
SG125919A1 (en) * 2002-06-24 2006-10-30 Kuraray Co Apparatus and method for treating wastewater containing nitrogen-containing dyes
US20040001934A1 (en) * 2002-06-28 2004-01-01 Lear Corporation Recyclable carpet products and method of making
US20040048035A1 (en) * 2002-09-06 2004-03-11 Racemark International, Inc. Recyclable floor mats, methods and systems for recycling floor mats
US20040086682A1 (en) * 2002-11-05 2004-05-06 Rice Jeffrey L. Recyclable, rubber-like thermoplastic backing material used in a throw-in mat for a vehicle floor

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4003880A (en) * 1975-05-19 1977-01-18 Monsanto Company Fabric dye stripping, separation and recovery of polyester
US6036726A (en) * 1995-10-27 2000-03-14 Solutia Inc. Process for separating polyamide from colorant
US6540791B1 (en) * 2000-03-27 2003-04-01 The Procter & Gamble Company Stable alkaline hair bleaching compositions and method for use thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008125465A1 (en) * 2007-04-11 2008-10-23 Basf Se Method for removing color from polymeric material
JP2010523781A (en) * 2007-04-11 2010-07-15 ビーエーエスエフ ソシエタス・ヨーロピア Method for removing color from polymeric materials
CN101675102B (en) * 2007-04-11 2012-05-09 巴斯夫欧洲公司 Method for removing color from polymeric material

Also Published As

Publication number Publication date
US20060070188A1 (en) 2006-04-06
WO2006036823A3 (en) 2008-09-04

Similar Documents

Publication Publication Date Title
US6036726A (en) Process for separating polyamide from colorant
AU738052B2 (en) Biodegradable dry cleaning solvent
US5898063A (en) Carpet recycling process for nylon containing carpeting
EP2922905B1 (en) Processing of cotton-polyester waste textile
US7947750B2 (en) Method for removing color from polymeric material
AU2001275510A1 (en) Biodegradable ether dry cleaning solvent
EP1294841A1 (en) Biodegradable ether dry cleaning solvent
US6083283A (en) Method for removing color from ionically dyeable polymeric materials
US6140463A (en) Process for recycling and recovery of purified nylon polymer
WO2006036823A2 (en) Colorant removal from polymeric fibers
JP2008179816A (en) Recycling method for nylon 6 product
CA2261304C (en) Process for separating polyamide from colorant
JP2023041597A (en) Method for recovering polyester fabric
US10640914B2 (en) Method for decolorizing textile materials
US20180171539A1 (en) Oxidative Method for Decolorizing Textile Materials
CA2261303C (en) Method for removing color from ionically dyeable polymeric materials
JP2023551806A (en) Raw material engineering of polyester waste for recycling process
US20150031778A1 (en) Process and system for recovering polyamides and polymers from composite articles
Fei et al. Towards Closed Loop Recycling of Polyester Fabric: 3) Reuse of Decolorization Bath and Decolorized Polyester Fabrics

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A2

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KM KP KR KZ LC LK LR LS LT LU LV LY MA MD MG MK MN MW MX MZ NA NG NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A2

Designated state(s): BW GH GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU LV MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase