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US3640942A - Manufacture of delustred nylon filaments - Google Patents

Manufacture of delustred nylon filaments Download PDF

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Publication number
US3640942A
US3640942A US821464A US3640942DA US3640942A US 3640942 A US3640942 A US 3640942A US 821464 A US821464 A US 821464A US 3640942D A US3640942D A US 3640942DA US 3640942 A US3640942 A US 3640942A
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US
United States
Prior art keywords
polyamide
filaments
delustred
chips
substituted
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
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US821464A
Inventor
Edward Crampsey
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Akzo Nobel UK PLC
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Courtaulds PLC
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Publication of US3640942A publication Critical patent/US3640942A/en
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/04Pigments
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • General Chemical & Material Sciences (AREA)
  • Textile Engineering (AREA)
  • Artificial Filaments (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

POLYAMIDE FILAMENTS WHICH ARE BOTHE DELUSTRED AND RESISTANT TO ACID DYES, COMPRISING AN INTIMATE BLEND OF A SUBSTITUTED CO-POLYAMIDE HAVING COVALENTLY BOUND ANIONIC SULPHONATE GROUPS AND A POLYAMIDE, IN WHICH IS DISPERSED TITANIUM DIOXIDE PARTICLES.

Description

United States Patent Office 3,640,942 Patented Feb. 8, 1972 US. Cl. 260-37 N 5 Claims ABSTRACT OF THE DISCLOSURE Polyamide filaments which are both delustred and resistant to acid dyes, comprising an intimate blend of a substituted co-polyamide having covalently bound anionic sulphonate groups and a polyamide, in which is dispersed titanium dioxide particles.
This invention is concerned with the manufacture of polyamide filaments delustred with titanium dioxide particles and resistant to acid dyes.
The manufacture of delustred polyamide filaments conventionally includes the step of dispersing titanium dioxide particles in the relatively fluid melt of the polyamide-forming reactants for example caprolactam and hexamethylene adipamide, the precursors of nylon 6 and nylon 66 respectively. The fluidity of the initial melt, or of the molten oligomers formed at an early stage in the polymerisation, aids the dispersion of the titanium dioxide. If the particles were added at a later stage, say when the polymerisation was near or at completion, the difficulties of obtaining a uniform dispersion would be greatly increased.
A more recent development in polyamide technology is the proposal to incorporate covalently bound anionic sulphonate groups in a substituted co-polyamide, to improve the afiinity of the filaments for basic dyes and at the same time render the filaments resistant to acid dyes. Such a process is described in US. patent specification No. 3,142,662.
However, substituted co-polyamides containing covalently bound anionic suphonate groups, that is sulphonic acid groups of their metal or ammonium salts, are not adequately delustred by the process evolved for simple polyamides. In the presence of the sulphonate ion and the fluid melt of the co-polyamide forming reactants, the titanium dioxide particles tend to flocculate, lessening their effect.
The present invention is concerned with a method of overcoming this difliculty.
According to the present invention a method of making polyamide filaments which are both delustred and resistant to acid dyes, comprises blending chips of a substituted co-polyamide containing covalently bound anionic sulphonate groups 'With chips of a polyamide containing a dispersion of titanium dioxide particles, melting the blended chips and extruding the molten blend to form filaments.
The sulphonate content of the filaments is preferably at least 60 microequivalents per gram. The acid dye resistance of the filaments may be increased by increasing the sulphonate content beyond this preferred minimum amount, but there is no advantage in practice in going beyond about 150 microequivalents per gram of filament.
Whilst the chips may be blended in any proportions so long as the sulphonate and titanium dioxide contents of the filaments are adequate and well dispersed in the filaments, the difiiculty of blending the chips is least when the chips are of approximately equal size and each of the two kinds of chips is present to the extent of at least 40% of the total 'weight of the blend. Thus the preferred ranges of concentration of sulphonate groups in the substituted co-polyamide will vary depending on the contribution of the substituted co-polyamide to the weight of the blend, as the following examples show.
(a) At 60% by weight of the blend, the substituted co-polyamide contains from to 250 microequivalents per gram, of anionic sulphonate.
(b) At 50% by weight of the blend, the substituted co-polyamide contains from to 300 microequivalents per gram, of anionic sulphonate.
(c) At 40% by weight of the blend, the substituted co-polyamide contains to 375 microequivalents pergram, of anionic sulphonate.
Equally the total titanium dioxide requirements of the filaments are contained in the complementary chips of the polyamide and the concentration of the particles therein is dictated by the weight contribution to the blend made by those chips. The complementary chips contain 1.7 times the required percentage of TiO in the filaments when those chips contribute 60 percent to the weight of the blend 2 times the percentage of TiO in the filaments when blended in equal weights with the substituted copolyamide and 2.5 times the percentage TiO in the filaments when the chips are only 40 percent weight of the blend.
The success of the present invention in overcoming the flocculation problems of the straightforward addition of titanium dioxide particles to the polymerisable antecedents of substituted co-polyamide, is due, in the main, to avoiding contact of the particles with the strongly acid sulphonic acid groups until the polymer matrix has a viscosity which hinders the gathering together of those particlesit is the viscosity of the blended polymers which reduces the opportunity for flocculation.
The molten blend of polymers is subject to a further blending by the inevitable mechanical mixing occurring in the spinning head, ensuring an adequate dispersion of the titanium dioxide particles throughout the blend.
The process in one form includes the steps of:
(i) 'Forming a molten polyamide delustred with titanium dioxide particles and extruding the polymer to form chips,
(ii) Forming a substituted co-polyamide containing sulphonate groups, and extruding it to form chips,
(iii) Blending the chips from (i) and (ii), melting them and extruding the melt to form delustred filaments which are resistant to dyeing with acid dyes.
Suitable materials which are difunctional in a polyamidepolymerisation process and carry sulphonic acid groups have been adequately disclosed in the aforesaid US. patent specification No. 3,142,662.
The invention includes delustred filaments resistant to acid dyes composed essentially of an intimate blend of a polyamide with a substituted co-polyamide having covalently bound anionic sulphonate groups, in which particles of titanium dioxide are dispersed.
The invention is illustrated in the following example in which parts and percentages are by weight.
EXAMPLE A polymerisation charge was made up to 400 parts caprolactam, 18.5 parts of sulpho-isophthalic acid, 2.72 parts of lithium carbonate, 7.1 parts hexamethylene diamine and 16 parts of water. The charge was heated for 18 hours at 260 C. during which time a viscous substituted co-polyamide was formed. The co-polyamide had a relative viscosity of 2.26 and an amine group content of 38.8 micro-equivalent/gram (meq./gm.), a carboxyl-ic acid group content of 103 meq./ gm. and a sulphonic acid group content of 180 meq./gm. The molten polymer was extruded to form rods of the co-polyamide which were cut Analysis NH2 COH, SO3H, Relative Yarn Source meq./gm. meqJgm. meqJgm. viscosity Screw extruder 33. 7 70. 7 90 2. 41 Melt-pool machine 26. 6 63. 4 90 2. 79
Samples of yarn from both sources were knitted into sock panels and severally dyed with Astrazone Blue and Solway Blue EN. The panels dyed with the basic dye Astrazone Blue were uniformly deeply coloured and there was no evidence of heterogenity in the filaments. Equally the filaments showed an excellent and uniform resistance to dyeing with the acid dye Solway Blue BN.
What is claimed is:
1. A method of making delustred polyamide filaments which are resistant to acid dyes, comprising blending chips of a first polymer consisting of a substituted co-polyamide containing covalently bound anionic sulphonate groups with chips of a second polymer different from said first consisting of a polyamide containing a dispersion of titanium dioxide particles, melting the blended chips and extruding the molten blend to form filaments.
2. A method as claimed in claim- 1 in which the sulphonate content of the filaments is at least 60 microequivalents per gram.
3. A method as claimed in claim 1 in which the sulphonate content of the filaments is at most 150 microequivalents per gram.
4. A method as claimed in claim 1 in which the chips of the co-polyamide contribute between and weight percent of the blend, the balance being the chips of the polyamide.
5. A method as claimed in claim 1 in which the sulphonate content of the substituted co-polyamide is between 100 and 375 micro-equivalents per gram.
References Cited UNITED STATES PATENTS 3,142,662 6/1964 Hulfman 26078 3,184,436 3/1965 Magat 26078 3,321,566 3/1967 Whitman 264210 3,403,200 8/1968 Randall 260-857 3,505,165 4/1970 Kubitzek 161-173 MORRIS LIEBMAN, Primary Examiner R. ZAITLEN, Assistant Examiner US. Cl. X.R. 260 7 I P0405) UN ITEDSTATES PATENT OFFICE (569 CERTIFICATE OF CORRECTION Patent'No. 3,640,942 I Dated bruary 8, 1972 Inventor) EDWARD CRAMPSEY It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
I v Col. 3, line 14, in Example, under "relative viscosity",
"2.41" should be 2.49
line 15, under "Relative viscosity", "2.79"
should be 2.71
Signed and sealed this 25th day of July 1972.
( SEAL) Attest: EDWARD M.FLETCHER, JR. ROBERT GOTTSCHALK Attesting Officer Commissioner of Patents
US821464A 1968-05-24 1969-05-02 Manufacture of delustred nylon filaments Expired - Lifetime US3640942A (en)

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GB2483168 1968-05-24

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FR (1) FR2010480A1 (en)
GB (1) GB1258756A (en)

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2308266A1 (en) * 1972-02-21 1973-09-13 Union Carbide Canada Ltd FIBER-MAKING POLYAMIDE, ITS USE AND MANUFACTURING
US3846507A (en) * 1972-04-06 1974-11-05 Union Carbide Canada Ltd Polyamide blends with one polyamide containing phthalate sulfonate moieties and terphthalate on isophthalate residues
WO1989005214A2 (en) * 1987-11-25 1989-06-15 Haytayan Harry M Powder-actuated fastener driving tool
EP0421971A2 (en) * 1989-10-05 1991-04-10 Monsanto Company Pigmented stain resistant nylon fiber
US5108684A (en) * 1988-12-14 1992-04-28 E. I. Du Pont De Nemours And Company Process for producing stain-resistant, pigmented nylon fibers
US5141692A (en) * 1990-11-20 1992-08-25 E. I. Du Pont De Nemours And Company Processing of pigmented nylon fibers
US5155178A (en) * 1990-08-08 1992-10-13 E. I. Du Pont De Nemours And Company Antistain block copolymer compositions of modified nylon copolymers and high carbon nylons
US5164261A (en) * 1990-08-08 1992-11-17 E. I. Du Pont De Nemours And Company Dyed antistain nylon with cationic dye modifier
EP0517203A2 (en) * 1991-06-06 1992-12-09 Basf Corporation Acid-dye resistant polyamide products and process for preparation
US5223196A (en) * 1990-11-20 1993-06-29 E. I. Du Pont De Nemours And Company Processing of pigmented nylon fibers using modified polymers
US5242733A (en) * 1990-08-08 1993-09-07 E. I. Du Pont De Nemours And Company Carpets and fabrics of antistain block copolymer compositions of modified nylon copolymers and high carbon nylons
US5340886A (en) * 1989-07-17 1994-08-23 Basf Corporation Acid-dye resistant polyamide products and process for preparation
US5422420A (en) * 1990-11-20 1995-06-06 E. I. Du Pont De Nemours And Company Terpolyamides and multipolyamides containing amide units of 2-methylpentamethylenediamine and products prepared therefrom
US5889138A (en) * 1996-11-27 1999-03-30 Solutia Inc. Process for making stain resistant nylon fibers from highly sulfonated nylon copolymers
US6117550A (en) * 1997-10-22 2000-09-12 Prisma Fibers, Inc. Acid dye stain-resistant fiber-forming polyamide composition containing masterbatch concentrate containing reagent and carrier
US6133382A (en) * 1995-08-31 2000-10-17 Prisma Fibers, Inc. Fiber-forming polyamide composition containing polyamide and a sulfonated polyester concentrate
US6433107B1 (en) 1995-08-31 2002-08-13 Prisma Fibers, Inc. Fiber-forming polyamide with concentrate of polyamide and sulfonated aromatic acid
US20030146536A1 (en) * 2001-12-07 2003-08-07 General Electric Company Color enhancement for resin blends
US20040133997A1 (en) * 2003-01-15 2004-07-15 Kelly David R. Fiber reactive dyeing system
US20080206559A1 (en) * 2007-02-26 2008-08-28 Yunjun Li Lubricant enhanced nanocomposites
WO2021167913A1 (en) * 2020-02-18 2021-08-26 Advansix Resins & Chemicals Llc Polyamide-based masterbatch formulation
WO2021167912A1 (en) * 2020-02-19 2021-08-26 Advansix Resins & Chemicals Llc Stain-resistant branched polyamides
US12146029B1 (en) 2022-02-07 2024-11-19 Futurefuel Chemical Company Polymers enhanced with hydrated sodium sulfoisophthalic acid salts

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2791906B1 (en) * 1999-04-12 2001-05-18 Rhodia Chimie Sa SOLID ACTIVE MATERIAL VECTOR SYSTEM
CN115418118B (en) * 2022-09-26 2023-03-28 福建乐钛科技有限公司 Preparation method of titanium dioxide for nylon color master batch

Cited By (48)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2308266A1 (en) * 1972-02-21 1973-09-13 Union Carbide Canada Ltd FIBER-MAKING POLYAMIDE, ITS USE AND MANUFACTURING
US3846507A (en) * 1972-04-06 1974-11-05 Union Carbide Canada Ltd Polyamide blends with one polyamide containing phthalate sulfonate moieties and terphthalate on isophthalate residues
WO1989005214A2 (en) * 1987-11-25 1989-06-15 Haytayan Harry M Powder-actuated fastener driving tool
WO1989005214A3 (en) * 1987-11-25 1989-08-10 Harry M Haytayan Powder-actuated fastener driving tool
US5830572A (en) * 1988-12-14 1998-11-03 E. I. Du Pont De Nemours And Company Stain-resistant, pigmented nylon fibers
US5108684A (en) * 1988-12-14 1992-04-28 E. I. Du Pont De Nemours And Company Process for producing stain-resistant, pigmented nylon fibers
US5340886A (en) * 1989-07-17 1994-08-23 Basf Corporation Acid-dye resistant polyamide products and process for preparation
EP0421971A3 (en) * 1989-10-05 1991-07-17 Monsanto Company Pigmented stain resistant nylon fiber
EP0421971A2 (en) * 1989-10-05 1991-04-10 Monsanto Company Pigmented stain resistant nylon fiber
US5242733A (en) * 1990-08-08 1993-09-07 E. I. Du Pont De Nemours And Company Carpets and fabrics of antistain block copolymer compositions of modified nylon copolymers and high carbon nylons
US5468554A (en) * 1990-08-08 1995-11-21 E. I. Du Pont De Nemours And Company Dyed antistain nylon with cationic dye modifier
AU633753B2 (en) * 1990-08-08 1993-02-04 E.I. Du Pont De Nemours And Company Antistain composition of nylon-cationic dye modifier copolymers melt blended with high carbon nylons
US5164261A (en) * 1990-08-08 1992-11-17 E. I. Du Pont De Nemours And Company Dyed antistain nylon with cationic dye modifier
US5155178A (en) * 1990-08-08 1992-10-13 E. I. Du Pont De Nemours And Company Antistain block copolymer compositions of modified nylon copolymers and high carbon nylons
US5223196A (en) * 1990-11-20 1993-06-29 E. I. Du Pont De Nemours And Company Processing of pigmented nylon fibers using modified polymers
US5141692A (en) * 1990-11-20 1992-08-25 E. I. Du Pont De Nemours And Company Processing of pigmented nylon fibers
US5391703A (en) * 1990-11-20 1995-02-21 E. I. Du Pont De Nemours And Company Polyamide pigment dispersion
US5422420A (en) * 1990-11-20 1995-06-06 E. I. Du Pont De Nemours And Company Terpolyamides and multipolyamides containing amide units of 2-methylpentamethylenediamine and products prepared therefrom
EP0517203A3 (en) * 1991-06-06 1993-08-04 Basf Corporation Acid-dye resistant polyamide products and process for preparation
US5545363A (en) * 1991-06-06 1996-08-13 Basf Corporation Process for forming melt-spun carpet fiber
US5548037A (en) * 1991-06-06 1996-08-20 Basf Corporation Acid dye resistant pigmented polymer
US5562871A (en) * 1991-06-06 1996-10-08 Basf Corporation Acid-dye resistant polyamide products and process for preparation
EP0517203A2 (en) * 1991-06-06 1992-12-09 Basf Corporation Acid-dye resistant polyamide products and process for preparation
US20040154110A1 (en) * 1995-08-31 2004-08-12 Matthew Studholme Stain-resistant polyamide composition and fibers
US6133382A (en) * 1995-08-31 2000-10-17 Prisma Fibers, Inc. Fiber-forming polyamide composition containing polyamide and a sulfonated polyester concentrate
US6433107B1 (en) 1995-08-31 2002-08-13 Prisma Fibers, Inc. Fiber-forming polyamide with concentrate of polyamide and sulfonated aromatic acid
US6537475B1 (en) 1995-08-31 2003-03-25 Prisma Fibers, Inc. Melt extrusion spinning polyamide fibers with sulfonated reagent
US20030138625A1 (en) * 1995-08-31 2003-07-24 Studholme Matthew Benjamin Stain-resistant polyamide composition and fibers
US6680018B2 (en) * 1995-08-31 2004-01-20 Prisma Fibers, Inc. Melt extrusion spinning polyamide fibers with sulfonated reagent and thermoplastic carrier
US6753385B2 (en) * 1995-08-31 2004-06-22 Prisma Fibers, Inc. Fiber-forming polyamide and sulfonated acid for disabling acid dye sites
US6861480B2 (en) * 1995-08-31 2005-03-01 Prisma Fibers, Inc. Yarn-forming composition of polyamide and sulfonated acid dye disabler
US5889138A (en) * 1996-11-27 1999-03-30 Solutia Inc. Process for making stain resistant nylon fibers from highly sulfonated nylon copolymers
US6420044B1 (en) 1997-10-22 2002-07-16 Prisma Fibers, Inc. Stain-resistant polyamide composition and fibers and method of production thereof
US6117550A (en) * 1997-10-22 2000-09-12 Prisma Fibers, Inc. Acid dye stain-resistant fiber-forming polyamide composition containing masterbatch concentrate containing reagent and carrier
US6635346B2 (en) 1997-10-22 2003-10-21 Prisma Fibers, Inc. Stain-resistant polyamide composition and fibers and method of production thereof
US20040152840A1 (en) * 1997-10-22 2004-08-05 Studholme Matthew Benjamin Stain resistant polyamide composition and fibers and method of production thereof
US20030146536A1 (en) * 2001-12-07 2003-08-07 General Electric Company Color enhancement for resin blends
US20040133997A1 (en) * 2003-01-15 2004-07-15 Kelly David R. Fiber reactive dyeing system
US20080206559A1 (en) * 2007-02-26 2008-08-28 Yunjun Li Lubricant enhanced nanocomposites
WO2021167913A1 (en) * 2020-02-18 2021-08-26 Advansix Resins & Chemicals Llc Polyamide-based masterbatch formulation
CN115427481A (en) * 2020-02-18 2022-12-02 艾德凡斯化学公司 Polyamide-based masterbatch formulation
JP2023514775A (en) * 2020-02-18 2023-04-10 アドバンシックス・レジンズ・アンド・ケミカルズ・リミテッド・ライアビリティ・カンパニー Polyamide-based masterbatch formulation
US11920009B2 (en) 2020-02-18 2024-03-05 Advansix Resins & Chemicals Llc Polyamide-based masterbatch formulation
CN115427481B (en) * 2020-02-18 2024-05-31 艾德凡斯化学公司 Masterbatch formulations based on polyamides
WO2021167912A1 (en) * 2020-02-19 2021-08-26 Advansix Resins & Chemicals Llc Stain-resistant branched polyamides
CN115103870A (en) * 2020-02-19 2022-09-23 艾德凡斯化学公司 Stain-resistant branched polyamides
CN115103870B (en) * 2020-02-19 2023-08-25 艾德凡斯化学公司 Stain resistant branched polyamides
US12146029B1 (en) 2022-02-07 2024-11-19 Futurefuel Chemical Company Polymers enhanced with hydrated sodium sulfoisophthalic acid salts

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FR2010480A1 (en) 1970-02-20
GB1258756A (en) 1971-12-30

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