US3085987A - Linear polyester containing a diaryl ether and process of producing same - Google Patents

Linear polyester containing a diaryl ether and process of producing same Download PDF

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Publication number
US3085987A
US3085987A US841010A US84101059A US3085987A US 3085987 A US3085987 A US 3085987A US 841010 A US841010 A US 841010A US 84101059 A US84101059 A US 84101059A US 3085987 A US3085987 A US 3085987A
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polyester
ether
dye
aromatic
glycol
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Abashian Steven
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EIDP Inc
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EI Du Pont de Nemours and Co
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Priority to NL256036D priority Critical patent/NL256036A/xx
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Priority to US841010A priority patent/US3085987A/en
Priority to US20281A priority patent/US3058987A/en
Priority to GB32264/60A priority patent/GB898289A/en
Priority to FR839051A priority patent/FR1267725A/fr
Priority to DEP25723A priority patent/DE1152257B/de
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/04Oxygen-containing compounds
    • C08K5/06Ethers; Acetals; Ketals; Ortho-esters
    • 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
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/78Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
    • D01F6/86Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from polyetheresters
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S8/00Bleaching and dyeing; fluid treatment and chemical modification of textiles and fibers
    • Y10S8/92Synthetic fiber dyeing
    • Y10S8/922Polyester fiber

Definitions

  • This invention relates to fiberand film-forming synthetic linear condensation polyesters and shaped articles which are produced therefrom. More particularly, it is concerned with a synthetic linear condensation polyester composition from which readily dyeable shaped articles may be prepared, and to a process for producing such shaped articles.
  • Synthetic linear condensation polyesters and particularly the linear terephthalate polyesters, have attracted high commercial interest for many uses owing to their high tenacity, flexibility, crease resistance, low mois ture absorption, and other valuable properties.
  • polyesters are polyethylene terephthalate and poly- (p-hexahydroxylylene terephthalate).
  • One of the chief disadvantages associated with the polyesters has been the difficulty in dyeing fabrics and other shaped articles composed thereof with commercially available dyes.
  • polyester filaments by treating them with various reagents to create sites receptive to dyes on or in the filaments; however, such treatments have usually been effective only for modifying the surface of the fiber, and in many cases the physical properties of the fibers are adversely affected by the treatment. It has also been proposed to prepare copolyesters containing substituents which would tend to serve as sites receptive to dyes. Even with the use of such methods, however, it has been necessary in general to employ elevated pressures and temperatures to obtain deep shades in the dyeing of polyester articles. These requirements have placed restrictions on the commercial dyeing of polyester articles owing to the need for costly pressure equipment and special methods. In contrast, the natural fibers such as cotton and wool are customarily dyed at the boil at atmospheric pressure.
  • filaments having greatly enhanced rates of dyeability can be melt spun from linear condensation polyesters having dissolved therein an aromatic ether of the formula Ar(OC H OAr', where Ar and Ar are the same or different radicals containing an aromatic nucleus, and n and x are integers within the range of 2 to 4.
  • aromatic ether of the formula Ar(OC H OAr', where Ar and Ar are the same or different radicals containing an aromatic nucleus, and n and x are integers within the range of 2 to 4.
  • 1,2-diphenoxyethane is employed as the aromatic ether.
  • a solution of the aromatic ether in the molten polyester is prepared and the molten mixture is spun into filaments and drawn in the usual manner to form continuous filament or staple yarns, as desired.
  • the resulting yarns are tenacious and exhibit the desirable properties usually found in polyester yarns.
  • fabric prepared from the modified yarns are highly receptive to dyes and may be dyed to any desired depth of color from aqueous dye baths at the boil using conventional equipment at atmospheric pressure. Films or other shaped structures which are highly receptive to dyes may likewise be extruded from the molten linear condensation polyester having the aromatic ether dissolved therein.
  • the amount of aromatic ether which is added to the polyester is usually in the range of about 3 to about 20% of the weight of the polyester, the optimum usually being considered to be about 10%.
  • the aromatic ethers falling within the class defined by the formula Ar(OC H OAr' are soluble in the molten polyester to form viscous melts which may be extruded into filaments in the same manner as unmodified polymer.
  • the aromatic ethers are stable at the spinning temperature, which is usually about the same as or slightly lower than the normal spinning temperature of the unmodified polymer, e.g., in the range of about 250 C. to 295 C. in the case of polyethylene terephthalate containing about 10% of the aromatic ether.
  • the aromatic ethers are also inert with respect to the polyester and do not promote polymer degradation, either during spinning or while remaining in the yarn over a long period of. time;
  • the solution of the aromatic ether in the molten polyester may be prepared in any of various ways.
  • the solid polyester in flake or other finely divided form may be blended with the aromatic ether and then melted.
  • the ether may also be mixed in the proper proportions with molten polymer, either in a batch manner or by metering the ether into a continuous stream of the polymer.
  • An excess of the ether may also be used as the solvent in a solvent polymerization process, followed by stripping off the ether to the desired concentration in the finished polymer.
  • delusterants or other additives may also be added during polymerization or just prior to spinning.
  • the presence of the aromatic ether in the polymer does not alter the ability of the polyester filaments to become oriented and highly tenacious in the drawing step. Surprisingly, the initial modulus and yield point of the corresponding modified and unmodified yarns are quite comparable.
  • the tenacity of ether-containing drawn yarns while slightly lower than that of similar yarns containing no additive, also remains at a high level as contrasted with the natural fibers. 'However, the dyeability of the modified filaments is outstandingly superior to that of the unmodified filaments.
  • the improvement is not restricted to any particular type of dye, but applies to all classes of dyes customarily employed with the various types of polyester fibers. In general, the rate of dyeing of the ether-containing fibers is at least several times faster than that of the corresponding unmodified polyesters.
  • a small amount of the aromatic ether may evaporate from the filaments during spinning.
  • An additional 2-3% of the ether, based on the weight of the polyester, may be lost if the fabric is subjected to a scour at the boil during processing.
  • an amount on the order of about two-thirds of the aromatic ether originally introduced into the polyester remains in the fiber prior to the dyeing step, during which there is usually a small additional loss of the ether from the fiber.
  • the ether may be removed by scouring with hot solvent or, in the case of the more volatile aromatic ethers, by heating the fabric to an elevated temperature.
  • a liquid or mixed liquid which is a solvent for the ether but not also a solvent elfective for removing the adsorbed dye should be employed, of course.
  • carbon tetrachloride or a benzeneethanol mixture can frequently be used, either at the boil under atmospheric pressure or at elevated temperature and pressure. Removal of the aromatic ether by heat setting is preferably effected at about 190 C., where practicable, although temperatures up to about 230 C. or higher may be used if required.
  • any of the various aromatic ethers having the formula Ar(OC H OAr', wherein Ar and Ar are the same or different aryl-containing radicals and n and x are integers within the range of 2 to 4, may be employed as additives for enhanced dyeability in accordance with the present invention.
  • the carbon atom in the Ar radical (or Ar radical) adjacent to the ether linkage is attached, except for the ether linkage, solely to atoms from the group consisting of carbon and hydrogen and is located in an aromatic nucleus or a side chain of an aromatic nucleus.
  • the Ar radical may contain halogen substituents, ether substituents such as methoxy groups, or other substantially non-reactive substituents; but reactive substituents will generally be avoided, especially ester-forming substituents such as carboxyl groups, hydroxyalkyl groups, etc.
  • the use of aromatic ethers of the type for improving the rate of dyeing is applicable in general to the class of synthetic organic linear condensation polyester fibers.
  • synthetic organic linear condensation polyester comprehends a substantially linear polymer of fiber-forming molecular weight comprising a series of predominantly carbon atom chains joined by recurring divalent ester radicals, each of said ester radicals comprising a carbonyl .group attached on at least one side to an oxygen atom.
  • the divalent ester radicals may be represented by the general formula (a) Poly(ethylene p-oxybeuzoate) (b) P0ly(ethylene terephthalate) i r @aQ OH;
  • m represents a number sufficiently great that the polyesters are of fiber-forming molecular weight; i.e., having a relative viscosity of at least about 10.
  • Poly(ethylene p-oxybenzoate) is an example of a synthetic organic linear condensation polyester in which each repeating unit contains only one ester linkage.
  • Each of the ester linkages is a carboxylate radical oriented in the same direction; i.e., the chain of atoms between successive carboxylate radicals is attached at one end to an oxygen atom of a carboxylate radical and at the other end to the carbon atom of the next carboxylate radical.
  • This polyester is conveniently prepared by the polycondensation of methyl p-(Z-hydroxyethoxy)benzoate at elevated temperature and reduced pressure.
  • Poly(ethylene terephthalate) which is usually designated simply as polyethyelne terephthalate, is an example of a polyester in which each repeating unit contains two ester linkages, i.e., carboxylate radicals. In this polyester successive carboxylate radicals are oriented in the opposite direction, so that the ethylene radicals are attached at each end to the oxygen atoms of carboxyls and the phenylene radicals are attached at each end to the carbon atoms of carboxyls.
  • Polyethylene terephthalate may be prepared by reacting terephthalic acid with ethylene glycol to form bis-(Z-hydroxyethyl) terephthalate, followed by polycondensation at elevated temperature and reduced pressure with elimination of excess glycol.
  • ester-forming derivatives may be used, i.e. derivatives which readily undergo polyesterification with ethylene glycol or a derivative thereof.
  • the acid chloride or a lower alkyl ester, such as dimethyl terephthalate may be used.
  • an ester-forming derivative of the glycol may be used in place of the glycol, i.e. a derivative of the glycol which readily undergoes polyesterification with dicarboxylic acids or derivatives thereof.
  • a cyclic oxide from which the corresponding glycol can be derived by hydrolysis may be used.
  • Poly(p,p'-isopropylidenediphenyl carbonate) is an example of a synthetic organic linear condensation polyester in which each repeating unit contains a carbonate ester linkage. Since the carbonate radical is symmetrical, the chain of atoms between successive carbonate radicals is attached at each end to an oxygen atom.
  • This polycarbonate polyester is readily prepared by the reaction of 2,2-bis-(p-hydroxyphenyl)propane with an equimolar quantity of phosgene.
  • Poly(decamethylene oxalate) is a polyester of the polyethylene terephthalate type, in which each repeating unit contains two ester linkages, being the limiting case in which the two carboxylate radicals are linked together between the two carbon atoms without any intervening chain of atoms. It may be prepared by reacting diethyl oxalate with deeamethylene glycol.
  • Copolyesters derived from a glycol and a mixture of acids or from an acid and a mixture of glycols, etc., may be prepared in accordance with any of the above types or a mixture of them.
  • synthetic organic linear condensation polyesters can be formed by the polycondensation of bifunctional monomers which are capable of undergoing condensation with elimination of small molecules such as H O, HCl, NaCl, CH O H, l-l-OCH CH OH, or the like.
  • the synthetic organic linear condensation polyesters are also characterized in that the monomers from which they are derived can be regenerated from the polymer under suitable conditions by hydrolysis, alcoholysis, or other reactions in which small molecules react to split the polymer chain at the ester linkages.
  • small amounts of monomers having three or more functional groups may be employed to promote a limited amount of cross-linking.
  • monofunctional reagents may be employed in small quantities to control the degree of polymerization.
  • alternative routes employing various types of monomers are usually available for the preparation of any given polyester.
  • the polymer in which the ether is incorporated is a linear glycol terephthalate polyester.
  • linear glycol terephthalate polyester is meant a linear condensation polyester comprising recurring glycol dicarboxylate structural units in which at least about 75% of the recurring structural units are units of the formula wherein --G represents a divalent organic radical containing from 2 to about 18 carbon atoms and attached to the adjacent oxygen atoms by saturated carbon atoms.
  • the radical -G- contains from 2 to about carbon atoms.
  • the terephthalate radical may be the sole dicarboxylate constituent of the recurring structural units, or up to about 25% of the recurring structural units may contain other dicarboxylate radicals, such as the adipate, sebacate, isophthalate, 'bibenzoate, hexahydroterephthalate, diphenoxyethane-4,4-dicarboxylate, p,p'- carbonyldibenzoate, and p,p'-sulfonyldibenzoate radicals.
  • dicarboxylate radicals such as the adipate, sebacate, isophthalate, 'bibenzoate, hexahydroterephthalate, diphenoxyethane-4,4-dicarboxylate, p,p'- carbonyldibenzoate, and p,p'-sulfonyldibenzoate radicals.
  • the glycol, G(OH) from which the polyester is prepared may be any suitable dihydroxy compound containing from 2 to 18 carbon atoms, preferably from 2 to 10 carbon atoms, in which the hydroxyl groups are attached to saturated carbon atoms.
  • the radical G- may be of the form (C H2p+2 Y where p and q are positive integers and Y is a cycloaliphatic group, an aromatic group, an oxy group, or an arylenedioxy group.
  • polymethylene glycols such as ethylene glycol, tetramethylene glycol, hexa-methylene glycol, and decamethylene glycol
  • branched chain glycols such as 2,2-dimethy1-1,3-propanediol and 2,2-dimethyl-1,4-butanediol.
  • glycols such as tetraethylene glycol may be used. Mixtures of the glycols may be used. If desired small amounts, e.g., up to about 15 weight percent, of a higher glycol such as a polyethylene glycol of high molecular Weight may be added.
  • Polyethylene terephthalate may be prepared from ethylene glycol and dimethyl tereph-thalate in accordance with the procedures outlined by Whinfield and Dickson in US. Patent 2,465,319, and polyethylene terephthalate/S-(sodiu m sulfo)-isophthalate (98/2) is prepared in similar fashion by reacting ethylene glycol with a mixture of 98 mol percent dimethyl terephthalate and 2 mol percent sodium 3,5-dicarbomethoxybenzenesulfonate.
  • Poly(trans-p-hexahydroxylylene terephthalate) from dimethyl terephthalate and trans-p-hexahydroxylylene glycol and to prepare polyhexamethylene bibenzoate from hexamethylene glycol and dimethyl bibenzoate.
  • Poly(p,p-isopropylidenediphenyl isophthalate) may be prepared from isophthaloyl chloride and 2,2-bis-(p-hydroxyphenyl)propane in accordance with the procedure described by Wagner in U.S. Patent 2,035,578.
  • Poly(p,p'-isopropylidenediphenyl carbonate) may be prepared from phosgene and 2,2-bis- (p-hydroxyphenyl)-propane in accordance with the procedure described in British Patent 772,627.
  • EXAMPLE 1 In a series of experiments for which the results are recorded in Table I, molten mixtures of polyethylene terephthalate and 10% (based on the weight of the polyethylene terephthalate) of the indicated organic compound are prepared and melt-spun at the indicated spinning temperature from a spinneret containing 34 holes, each 0.009 inch in diameter. A control sample of unmodified polyethylene terephthala-te is included. The yarns are Wound up at 1206 yards per minute and then dra-Wn 3.2x from a feed roll maintained at C. to a draw roll operated at a peripheral speed of 454 yards per minute. The physical properties of the resulting yarns are as shown in the table. A series of 1.0-gram skeins of each of the yarns is then dyed at 100 C. in separate vessels,
  • a dispersing agent comprising the sodium salt of an unsaturated long chain alcohol sulfate such as Du Ponts Duponol D.
  • the time required for adsorption of 4.0% dye by the fibers containing aromatic ethers of the type Ar(OC H OAr', listed under B, is far lower than the time required for the control sample, A.
  • the required time is also markedly lower than the time required for adsorption of the same amount of dye for the fibers of group C, containing the same amounts by weight of other aromatic ethers, such as diphenyl ether, or other typical aromatic compounds such as benzophenone and diphenyl.
  • EXAMPLE 2 A sample of polyethylene terephthalate yarn containing 1,2-diphenoxyethane, spun and drawn as described in Example 1, and a sample of the unmodified polyethylene terephthalate control yarn of Example 1 are woven separately into 104 X 76 taffeta fabrics and dyed with the dye of Example 1 (4% dye on fabric). The dyed fabrics are then heated at 190 C. for one minute. Prior to heat treatment, the unmodified control fabric has a soft, limp hand and the fabric made of polyethylene terephthalate containing diphenoxyethane has a substantially identical hand.
  • the unmodified control fabric After heat treatment, the unmodified control fabric has a smooth, boardy hand, while the fabric made of polyethylene terephthalate containing diphenoxyethane has a soft, supple, silk-like hand.
  • the fabric made from polyethylene terephthalate containing diphenoxyethane shows no loss in weight when treated with 50% ethanol-50% benzene, indicating that no more diphenoxyethane remains in the fabric.
  • the properties of yarn taken from this fabric are listed in Table I.
  • EXAMPLE 3 A quantity of polyethylene terephthalate/S-(sodium sulfo)isophthalate (98/2) is blended with 10% (based on the weight of the polymer) of 1,2-diphenoxyethane and melt-spun at 275 C. from a spinneret containing 34 holes, each 0.009 inch in diameter. The yarn is Wound up at 1206 yards per minute and is then drawn 2.9x from a feed roll maintained at 90 C. to a draw roll operated at a peripheral speed of 454 yards per minute.
  • the yarn has a tenacity of 2.4 g.p.d., an el0ngation of 21%, an initial modulus of 42 g.p.d., and a yield point of 0.87 g.p.d.
  • a 5.0-gram skein of the yarn containing the diphenoxyethane is then dyed at C. in 500 ml. of a dye bath containing 0.10 g. of a basic dye of blue color having the structure together with 0.30 g. of a retarding agent comprising a long-chain alkyl trimethyl ammonium chloride such as Armour & Companys Arquad C.
  • a retarding agent comprising a long-chain alkyl trimethyl ammonium chloride such as Armour & Companys Arquad C.
  • small samples of the dye bath are removed and analyzed spectrophotometrically for the for the amount of dye remaining in the bath.
  • the resulting dye concentrations are then used to calculate the percentage dye adsorbed by the fiber at the measured time intervals and the percentage dye adsorption is plotted against the square root of the time.
  • the time required for adsorption of 1.5% dye, as determined by the resulting plots, is 1.7 hours.
  • the time required for adsorption of 1.5% dye by control samples of unmodified polyethylcne terephthalate/S-(sodium sulfo)- isophthalate fibers dyed under the same conditions, as determined by a similar plot is 93.8 hours.
  • Samples of similarly prepared fibers made from polyethylene terephthalate/S-(sodium sulfo)isophthalate containing 10% diphenyl ether, when dyed under the same conditions, require 6.5 hours to adsorb 1.5% dye, as determined by the plots.
  • EXAMPLE 4 A quantity of polyethylene terephthalate/S-(sodium sulfo)isophthalate (98/2) is blended with 10% (based on the weight of the polymer) of 1,2-di-fi-naphthoxyethane and melt-spun at 275 C. from a spinneret containing 5 holes, each 0.007 inch in diameter.
  • the yarn is wound up at 240 yards per minute and is then drawn 4.6x from a feed roll maintained at 100 C. to a draw roll operated at a peripheral speed of 75 yards per minute.
  • the yarn has a tenacity of 1.7 g.p.d. at an elongation of 25%.
  • a skein of the yarn containing the dinaphthoxyethane is dyed at the boil in a bath (pH 4.5) containing 3% (based on the weight of the yarn) of the dye of Example 3 together with 1% (based on the weight of the yarn) of Arquad C retarding agent.
  • the dye is dyed to a medium shade of blue, whereas a sample of the unmodified control yarn is colored only a light shade of blue.
  • EXAMPLE 5 An intimate blend of 2.0 g. of poly(trans-p-hexahydroxylylene tercphthalate) and 0.20 g. of 1,2-diphenoxyethane is pressed into a film under 6000 p.s.i. pressure at 320 C. When dyed for 90 minutes at the boil in a bath (pH 4.5) containing 2% (based on the weight of the film) of 1,4-diamino-2,3-dichloroanthraquinone together with 2% (based on the weight of the film) of an anionic hydrocarbon sodium sulfonate such as Du Ponts Avitone T, the film is colored a deep shade of violet. A control film of unmodified poly(trans-p-hexahydroxylylene terephthalate), pressed and dyed under the same conditions, is dyed only to a light shade of violet.
  • EXAMPLE 6 An intimate blend of 2.0 g. of polyhexamethylene bibenzoate and 0.20 g. of 1,2-diphenoxyethane is pressed into a film under 6000 p.s.i. pressure at 275 C. When dyed with the dye of Example under the given conditions, the film is colored a deep shade of violet. A control film of unmodified polyhexamethylene b-ibenzoate, pressed and dyed under the same conditions, is dyed only a medium shade of violet.
  • EXAMPLE 8 An intimate blend of 2.0 g. of poly(p,p-isopropylidene diphenyl carbonate) and 0.20 g. of 1,2-diphenoxyethane is pressed into a film under 6000 p.s.i. pressure at 320 C. When dyed with the dye of Example 5 under the given conditions, the film is colored a medium shade of violet. A control film of unmodified poly(p,p'-isopropylidenediphenyl carbonate), pressed and dyed under the same conditions, is dyed only a very light shade of violet.
  • a synthetic linear glycol dicarboxylate condensation polyester having dissolved-therein from 3% to 20% by weight of an aromatic ether of the formula n zn)x 1 in which Ar and Ar are radicals containing an aromatic nucleus selected from the class consisting of hydrocarbon alkoxy substituted and halogen substituted aromatic nuclei and n and x are integers within the range of 2 to 4.
  • a filament made from a synthetic linear glycol dicarboxylate condensation polyester of a glycol and a terephthalic acid having dissolved therein from about 3% to 20% by weight of an aromatic ether of the formula in which Ar and Ar are radicals containing an aromatic nucleus selected from the class consisting of hydrocarbon alkoxy substituted and halogen substituted aromatic nuclei and n and x are integers within the range of 2 to 4.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Artificial Filaments (AREA)
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US841010A 1959-09-21 1959-09-21 Linear polyester containing a diaryl ether and process of producing same Expired - Lifetime US3085987A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
NL256036D NL256036A (en)) 1959-09-21
US841010A US3085987A (en) 1959-09-21 1959-09-21 Linear polyester containing a diaryl ether and process of producing same
US20281A US3058987A (en) 1959-09-21 1960-04-06 3-amino-2-aminomethyl-1-phenyl-1-propanols
GB32264/60A GB898289A (en) 1959-09-21 1960-09-20 Polyesters and shaped articles produced therefrom
FR839051A FR1267725A (fr) 1959-09-21 1960-09-20 Perfectionnement aux polyesters, en particulier pour l'obtention de fibres textiles
DEP25723A DE1152257B (de) 1959-09-21 1960-09-21 Thermoplastische Formkoerper, die synthetische, lineare Polyester und einen Zusatz enthalten

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3516239A (en) * 1966-03-15 1970-06-23 Teijin Ltd Artificial fiber having voids and method of manufacture thereof
US3619124A (en) * 1968-11-04 1971-11-09 Hoechst Ag Process for the dyeing or printing of fibrous materials
US4318787A (en) * 1980-02-22 1982-03-09 Conoco Inc. Sacrificial anode composition in cathodic protection process
US4983660A (en) * 1987-12-25 1991-01-08 Mitsubishi Rayon Company Ltd. Polyethylene terephthalate resin composition

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1282842B (de) * 1963-04-11 1969-02-20 Bayer Ag Feinkristalline verstreckbare Faeden oder Folien aus hochmolekularen linearen Polycarbonaten und Verfahren zu deren Herstellung

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2263444A (en) * 1941-11-18 - trichlorophenoxy
US2329033A (en) * 1939-06-05 1943-09-07 Dow Chemical Co Styrene copolymer plastic composition
US2710849A (en) * 1951-07-05 1955-06-14 Siggel Erhard Process of dyeing aromatic polyesters
GB801065A (en) * 1955-06-30 1958-09-10 Goodyear Tire & Rubber Aromatic polyester compositions

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2263444A (en) * 1941-11-18 - trichlorophenoxy
US2329033A (en) * 1939-06-05 1943-09-07 Dow Chemical Co Styrene copolymer plastic composition
US2710849A (en) * 1951-07-05 1955-06-14 Siggel Erhard Process of dyeing aromatic polyesters
GB801065A (en) * 1955-06-30 1958-09-10 Goodyear Tire & Rubber Aromatic polyester compositions

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3516239A (en) * 1966-03-15 1970-06-23 Teijin Ltd Artificial fiber having voids and method of manufacture thereof
US3619124A (en) * 1968-11-04 1971-11-09 Hoechst Ag Process for the dyeing or printing of fibrous materials
US4318787A (en) * 1980-02-22 1982-03-09 Conoco Inc. Sacrificial anode composition in cathodic protection process
US4983660A (en) * 1987-12-25 1991-01-08 Mitsubishi Rayon Company Ltd. Polyethylene terephthalate resin composition

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NL256036A (en))
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