JP2008111088A - Polyester production method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a polyester production method reducing the formation of foreign matter originated in a catalyst and mold fouling during molding and producing a polymer having heat resistance and hue more markedly excellent than those of a conventional product. <P>SOLUTION: The polyester production method comprises subjecting a dicarboxylic acid or an esterifiable derivative thereof and a diol or an esterifiable derivative thereof to esterification or transesterification and thereafter polycondensing the product in the presence of a titanium polycondensation catalyst, wherein a specified biphenyl group-containing phosphorus compound is added. <P>COPYRIGHT: (C)2008,JPO&amp;INPIT

Description

  The present invention relates to a method for producing a polyester excellent in color tone and thermal stability. More specifically, the generation of foreign substances due to the catalyst used during polymerization and mold contamination during molding are reduced, the polymer has better thermal stability and color tone than conventional products, and color tone deterioration at high temperature melting is dramatic. The present invention relates to an improved polyester production method.

  Polyester is used for various purposes because of its useful functionality, and is used for clothing, materials, and medical use, for example. Among them, polyethylene terephthalate is excellent in terms of versatility and practicality and is preferably used.

  In general, polyethylene terephthalate is produced from terephthalic acid or an ester-forming derivative thereof and ethylene glycol. In a commercial process for producing a high molecular weight polymer, an antimony compound is widely used as a polycondensation catalyst. However, polymers containing antimony compounds have some undesirable properties as described below.

  For example, when a polymer obtained using an antimony catalyst is melt-spun into a fiber, it is known that an antimony catalyst residue is deposited around the die hole. As this deposition progresses, it becomes a cause of defects in the filament, so that it needs to be removed in a timely manner. The deposition of the antimony catalyst residue is considered to be due to the antimony compound in the polymer being transformed in the vicinity of the die and partially vaporizing and dissipating, and then a component mainly composed of antimony remains in the die. In addition, the antimony catalyst residue in the polymer tends to be relatively large particles, and it becomes a foreign substance, causing an increase in the filtration pressure of the filter during molding, causing yarn breakage during spinning or film tearing during film formation, etc. It has undesirable characteristics and contributes to a decrease in operability.

  In view of the above background, there is a demand for polyesters that do not contain antimony. Therefore, germanium compounds are known when the role of the polycondensation catalyst is required for compounds other than antimony compounds, but germanium compounds are difficult to use for general purposes because they have a small reserve and rare value.

  In order to solve this problem, studies using a titanium compound as a polymerization catalyst have been actively conducted. Since the titanium compound has a higher catalytic activity than the antimony compound, the desired catalytic activity can be obtained with a small amount of addition, and generation of foreign particles and contamination of the base can be suppressed. However, when a titanium compound is used as a polymerization catalyst, side reactions such as a thermal decomposition reaction and an oxidative decomposition reaction are promoted due to its high activity, resulting in a problem that the thermal stability is deteriorated and the polymer is colored yellow. It is not preferable that the polymer is yellowish, for example, when polyester is used as the fiber, since the commercial value of the fiber for clothing is impaired. In order to solve such a problem, studies have been widely made to improve the heat resistance and color tone of a polymer by adding a phosphorus compound together with a titanium compound. This method is to suppress the activity of titanium that is too high by the phosphorus compound and improve the heat resistance and color tone of the polymer. For example, in a method for producing polyester using a titanium compound as a catalyst, a method of adding phosphoric acid or phosphorous acid as a phosphorus compound (Patent Document 1), a phosphinic acid compound, a phosphine oxide compound, or phosphonous acid as a phosphorus compound The method of adding a phosphinic compound, a phosphinic acid compound, or a phosphine compound (Patent Documents 2 and 3) is clearly shown. However, when these methods are used, a certain improvement in the heat resistance of the polymer can be seen. However, when a certain amount or more of the phosphorus compound is added, the polymerization activity of the titanium compound is excessively suppressed, and the target degree of polymerization is reached. Or the polymerization reaction time is delayed, resulting in a problem that the color tone of the polymer deteriorates. In contrast, a method (Patent Document 4) in which the molar ratio of titanium compound to phosphorus compound (Ti / P) is within a certain range has been studied. Although life can be prevented, it is impossible to obtain polyester having a heat resistance and color tone above a certain level. Further, although a method of separating the addition interval between the titanium compound and the phosphorus compound has been studied (Patent Document 5), the deactivation of the titanium compound by the phosphorus compound proceeds in the polymerization reaction system, and the addition amount of the phosphorus compound still remains. When there is a large amount of catalyst, the catalyst is deactivated. As described above, it was necessary to solve the contradictory problem of suppressing the side reaction without impairing the polymerization reaction activity of the titanium compound.

Therefore, as a result of intensive studies on improving the above-described problems in the present invention, the object of the present invention can be achieved by adding a specific phosphorus compound in the process of producing a polyester using a titanium compound as a polymerization catalyst. Obtained knowledge.
JP-A-6-100680 (Claims) JP 2004-292657 A (Claims) Japanese Patent Laying-Open No. 2005-15630 (Claims) JP 2005-25630 A (Claims) Japanese Patent Application Laid-Open No. 2004-124067 (Claims)

  The object of the present invention is to solve the above-mentioned conventional problems, that is, the generation of foreign matters due to the catalyst and the mold contamination during molding are reduced, and the thermal stability and color tone of the polymer are remarkably superior to those of conventional products. It is providing the manufacturing method of polyester.

  The object of the present invention is to esterify or transesterify a dicarboxylic acid or an ester-forming derivative thereof and a diol or an ester-forming derivative thereof, and then perform a polycondensation reaction in the presence of a titanium-based polycondensation catalyst. In the method for producing the obtained polyester, it can be achieved by a method for producing a polyester characterized by adding a phosphorus compound represented by the following formula 1 or formula 2.

(In the above formulas 1 and 2, R _{1 to} R ₄ each independently represent a hydroxyl group or a hydrocarbon group having 1 to 20 carbon atoms. The hydrocarbon group is an alicyclic structure or an aliphatic branch. It may contain one or more structures, aromatic ring structures, hydroxyl groups and double bonds.)

  In the method for obtaining a polyester by polycondensation in the presence of a titanium-based polycondensation catalyst of the present invention, by adding a phosphorus compound represented by Formula 1 or Formula 2, the color tone can be drastically improved compared to conventional products. A polyester having improved heat resistance can be obtained. This polyester can solve problems such as deterioration in color tone, base stain, increased filtration pressure, and thread breakage in the production of molded articles for fibers, films and bottles.

  The polyester production method of the present invention is a method in which dicarboxylic acid or an ester-forming derivative thereof and diol or an ester-forming derivative thereof are esterified or transesterified and then polycondensed.

  Specific examples of the polyester obtained by such a production method include polyethylene terephthalate, polytrimethylene terephthalate, polytetramethylene terephthalate, polycyclohexylene dimethylene terephthalate, polyethylene-2,6-naphthalene dicarboxylate, polyethylene. -1,2-bis (2-chlorophenoxy) ethane-4,4′-dicarboxylate and the like. The present invention is suitable for polyethylene terephthalate or polyester copolymers mainly containing ethylene terephthalate units, which are most commonly used.

  In the method for producing the polyester of the present invention, it is essential to add the phosphorus compound represented by the formula 1 or 2 as a phosphorus compound at an arbitrary time.

  In the method of obtaining a polyester by polycondensation in the presence of a titanium-based polycondensation catalyst, when the phosphorus compound represented by Formula 1 or Formula 2 is added, surprisingly the color tone and heat resistance of the resulting polymer are dramatically increased. To be improved. The coloring of the polyester and the deterioration of the heat resistance are caused by a side reaction of polyester polymerization as specified in the saturated polyester resin handbook (Nikkan Kogyo Shimbun, first edition, pages 178 to 198). In the side reaction of this polyester, carbonyl oxygen is activated by a metal catalyst, and β hydrogen is extracted, thereby generating a vinyl end group component and an aldehyde component. As a result of such a side reaction, the polymer is colored yellow, and since an aldehyde component is generated, the main chain ester bond is cleaved, resulting in a polymer having poor heat resistance. In particular, when a titanium compound is used as a polymerization catalyst, a side reaction caused by heat is strongly activated, so that many vinyl end group components and aldehyde components are generated, resulting in a yellow colored polymer having poor heat resistance. The conventional phosphorus compound has adjusted the activity of the titanium catalyst by allowing the phosphorus compound to appropriately interact with the titanium compound. However, with conventional phosphorus compounds, it is inevitable that the polymerization activity is reduced as well as the side reaction activity of the titanium compound. However, in the phosphorus compound represented by Formula 1 or Formula 2 of the present invention, only the side reaction activity can be suppressed to a very small value while sufficiently maintaining the polymerization activity of the titanium compound. The mechanism of this effect is not completely clear at present, but this is essentially different from the effect of conventional phosphorus compounds on titanium compounds, or at least well achieved with conventional phosphorus compounds. It was not possible.

  Among these, when a phosphorus compound represented by Formula 3 is used, it is preferably used in polymerization of polyester because the phosphorus compound has high heat resistance and hydrolysis resistance.

(In the above formula 3, R _{5 to} R ₇ each independently represents a hydroxyl group or a hydrocarbon group having 1 to 10 carbon atoms. The hydrocarbon group is an alicyclic structure, an aliphatic branched structure, an aromatic group. (It may contain one or more ring structures, hydroxyl groups and double bonds, and a + b + c = 0 to 5 is an integer.)
Examples of the phosphorus compound represented by the above formula 3 include, for example, a compound having a = 2, b = 0, c = 0, R ₅ = tert-butyl group, R ₅ = 2,4-position, tetrakis (2,4- Di-t-butylphenyl) [1,1-biphenyl] -4,4′-diylbisphosphonite, which is IRGAFOS P-EPQ (Ciba Specialty Chemicals) or Sandostab P-EPQ (Clariant). (Available from Japan).

  Among these, the phosphorus compound represented by Formula 4 is preferable because the color tone and heat resistance of the obtained polyester are particularly good.

(In the above formula 4, R _{8 to} R ₁₀ each independently represents a hydroxyl group or a hydrocarbon group having 1 to 10 carbon atoms. The hydrocarbon group represents an alicyclic structure, an aliphatic branched structure, and an aromatic group. (It may contain one or more ring structures, hydroxyl groups and double bonds.)
As a phosphorus compound represented by the above formula 4, tetrakis (2,4-di-t-butyl-5 is used as a compound of R ₈ = tert-butyl group, R ₉ = tert-butyl group, R ₁₀ = methyl group. -Methylphenyl) [1,1-biphenyl] -4,4'-diylbisphosphonite, and this compound is available as GSY-P101 (Osaki Kogyo Co., Ltd.). These compounds may be used alone or in combination.

  The phosphorus compound of the polyester of the present invention may be added alone or in a state dissolved or dispersed in a diol component such as ethylene glycol.

  In the method for producing a polyester of the present invention, it is preferable to add a titanium compound excluding titanium oxide particles added for the purpose of a matting agent so as to be 1 to 20 ppm in terms of titanium atom with respect to the obtained polymer. When it is 3 to 15 ppm, the thermal stability and color tone of the polymer become better, more preferably 5 to 10 ppm. Moreover, it is preferable that the manufacturing method of the polyester of this invention adds a phosphorus compound with a titanium compound so that it may become 1-500 ppm in conversion of a phosphorus atom with respect to polyester. The amount of phosphorus added is preferably 5 to 250 ppm, more preferably 10 to 100 ppm from the viewpoint of thermal stability and color tone of the polyester during yarn production and film formation. Moreover, when the titanium atom of a titanium compound is Ti / P = 0.01-1.5 by a molar ratio as a phosphorus atom in a phosphorus compound, the thermal stability and color tone of polyester are good, which is preferable. More preferably, Ti / P = 0.03 to 0.75, and further preferably Ti / P = 0.05 to 0.5.

  Addition of at least one selected from the group consisting of magnesium compounds, manganese compounds, calcium compounds, and cobalt compounds is preferable because the reaction activity and the color tone of the polymer are improved. It is preferable to add at least one selected from the group consisting of a magnesium compound, a manganese compound, a calcium compound, and a cobalt compound so that the total is 1 to 100 ppm in terms of atoms with respect to the polyester of magnesium, manganese, calcium, and cobalt. If the total in terms of atoms of magnesium, manganese, calcium, and cobalt is less than 1 ppm, the effect is not sufficient, and if it exceeds 100 ppm, the thermal stability and the color tone are not sufficiently improved. More preferably, it is 3-75 ppm, Most preferably, it is 5-50 ppm. At this time, the molar ratio (Mg + Mn + Ca + Co) / P of the total amount of magnesium, manganese, calcium, and cobalt in terms of atoms and the phosphorus atom of the phosphorus compound is preferably 0.01 to 5 from the viewpoints of color tone and thermal stability. More preferably, it is 0.1-4, More preferably, it is 0.3-3. In particular, when the atomic conversion amount of magnesium to polyester is 5 to 25 ppm, and when the molar ratio Mg / P of the phosphorus atom of the phosphorus compound to the total of magnesium atoms is 0.3 to 3, both the color tone and thermal stability are good. It is. Specific examples of the magnesium compound used in this case include magnesium oxide, magnesium hydroxide, magnesium alkoxide, magnesium acetate, and magnesium carbonate. Specific examples of the manganese compound include manganese chloride, manganese bromide, manganese nitrate, manganese carbonate, manganese acetylacetonate, and manganese acetate. Specific examples of the calcium compound include calcium oxide, calcium hydroxide, calcium alkoxide, calcium acetate, and calcium carbonate. Specific examples of the cobalt compound include cobalt chloride, cobalt nitrate, cobalt carbonate, cobalt acetylacetonate, cobalt naphthenate, and cobalt acetate tetrahydrate. Among these, a magnesium compound is preferable in terms of color tone and polymerization activity, and magnesium acetate is particularly preferable.

  The polyester production method comprising the titanium compound of the present invention and the phosphorus compound represented by Formula 1 or Formula 2, wherein the titanium compound of the polymerization catalyst is a polyvalent carboxylic acid and / or a hydroxycarboxylic acid and It is preferable from the viewpoint of the thermal stability and color tone of the polymer that the nitrogen complex containing nitrogen / carboxylic acid is a chelating agent. Examples of chelating agents for titanium compounds include polyvalent carboxylic acids such as phthalic acid, trimellitic acid, trimesic acid, hemititic acid, pyromellitic acid, and hydroxycarboxylic acids such as lactic acid, malic acid, tartaric acid, and citric acid. As the nitrogen-containing carboxylic acid, ethylenediaminetetraacetic acid, nitrilotripropionic acid, carboxyiminodiacetic acid, carboxymethyliminodipropionic acid, diethylenetriaminopentaacetic acid, triethylenetetraminohexaacetic acid, iminodiacetic acid, iminodipropionic acid Hydroxyethyliminodiacetic acid, hydroxyethyliminodipropionic acid, methoxyethyliminodiacetic acid and the like. These titanium compounds may be used alone or in combination.

  The polycondensation catalyst of the present invention is generally a series of reactions for synthesizing polyester from dicarboxylic acid or its ester-forming derivative and diol or its ester-forming derivative. (1) Dicarboxylic acid component and diol component Or (2) an ester exchange reaction that is a reaction between an ester-forming derivative component of a dicarboxylic acid and a diol component, and (3) the ester reaction or the ester exchange reaction is substantially completed. It refers to those having the effect of contributing to at least one of the polycondensation reactions in which the obtained polyethylene terephthalate low polymer has a high degree of polymerization by dediol reaction. Therefore, titanium oxide particles generally used as inorganic particles in fiber matting agents and the like have substantially no catalytic effect on the above reaction and should be used as the polycondensation catalyst of the present invention. It is different from the titanium compound that can be used.

  In the polyester production method of the present invention, the polymerization catalyst and additives may be added as they are to the polyester reaction system, but the compound contains a diol component that forms a polyester such as ethylene glycol or propylene glycol in advance. Is added to the reaction system after removing low-boiling components such as alcohol used at the time of synthesizing the compound, if necessary, and it is preferable because foreign matter formation in the polymer is further suppressed. The addition time includes a method of adding a catalyst immediately after the addition of the raw material as an esterification reaction catalyst or a transesterification reaction catalyst, and a method of adding the catalyst together with the raw material. When added as a polycondensation reaction catalyst, it may be substantially before the start of the polycondensation reaction, added before the esterification reaction or transesterification reaction, or after the completion of the reaction, before the start of the polycondensation reaction catalyst. May be. The order of addition to the reaction system of at least one compound selected from the group consisting of titanium compounds, phosphorus compounds, magnesium compounds, manganese compounds, calcium compounds, and cobalt compounds is not particularly limited. It is preferable to add to. By mixing the catalyst additive in advance, the thermal stability and the color tone can be improved, and the amount of carboxyl end groups can be suppressed. The above mixing conditions are carried out by stirring at a temperature of 0 to 200 ° C. for 1 minute or longer, preferably at a temperature of 10 to 100 ° C. for 5 minutes to 300 minutes. The reaction pressure at this time is not particularly limited, and may be normal pressure.

  In addition, in the method for producing a polyester of the present invention, the addition of the phosphorus compound represented by Formula 1 or Formula 2 is performed after the polycondensation catalyst is added and then the pressure in the reactor is reduced to initiate the polycondensation reaction. By carrying out until the degree of polymerization is reached, a polyester having good color tone and excellent heat resistance can be obtained. In the case of adding a phosphorus compound by the above method, if a large amount of a diol component such as ethylene glycol is brought in and added, depolymerization of the polyester (polyester main chain cleavage reaction) proceeds. A method of adding alone or adding a master pellet containing phosphorus at a high concentration is preferable. At this time, the phosphorus compound may be added in several portions, or may be continuously added with a feeder or the like. In addition, the above-described method for adding a phosphorus compound is preferably added in a container that can be dissolved or melted in a polymerization system and is made of a polymer having substantially the same component as the polymer obtained in the present invention. . When the phosphorus compound is added to the container as described above and added, the addition of the polymerization reactor under the reduced pressure condition may cause the phosphorus compound to scatter and prevent the phosphorus compound from flowing out to the reduced pressure line. In addition, a desired amount of phosphorus compound can be added to the polymer. The container referred to in the present invention is not limited as long as it contains phosphorus compounds, and includes, for example, an injection-molded container having a lid or a stopper, or a sheet or film formed into a bag shape by sealing or sewing. More preferably, the container described above creates an air vent. When a phosphorus compound is added to a container that has been vented, even if it is added to the polymerization reactor under vacuum conditions, the container bursts due to air expansion and the phosphorus compound flows out to the decompression line, or the upper part of the polymerization reactor. The phosphorus compound can be added to the polymer in a desired amount without adhering to the wall surface. If the container is too thick, it takes longer to dissolve and melt, so it is better to make the container thinner. However, the container should be thick enough not to rupture when the phosphorus compound is sealed or added. For this purpose, a material having a thickness of 10 to 500 μm and uniform thickness is preferable. In particular, before starting depressurization in the polymerization reactor, the phosphorus compound of formula 1 or formula 2 is added to the obtained polyester in an amount of 1 to 50 ppm in terms of phosphorus atoms, and depressurization in the polymerization reactor is started. When the phosphorus compound of formula 1 or formula 2 is added to 10 to 500 ppm with respect to the obtained polyester until the polyester reaches the target degree of polymerization, the color tone is particularly good and the polymerization delay is extremely reduced. Can do.

  Moreover, in the manufacturing method of polyester of this invention, you may add a blue-type regulator and / or a red-type regulator as a color tone regulator.

  The color tone adjusting agent of the present invention is a dye used for a resin or the like. Specifically, in the COLOR INDEX GENERIC NAME, blue color tone adjusting agents such as SOLVENT BLUE 104, SOLVENT BLUE 122, SOLVENT BLUE 45, SOLVENT RED 111, SOLVENT RED 179, SOLVENT RED 195, SOLVENT RED 135, PIGMENT RED 263, VAT RED 41, etc. Examples thereof include system color adjusting agents. Among them, SOLVENT BLUE 104, SOLVENT BLUE 45, SOLVENT RED 179, SOLVENT RED 195, SOLVENT RED 135, which do not contain halogen that is likely to cause corrosion of equipment, have relatively good heat resistance at high temperatures and excellent color developability, SOLVENT VIOLET 49 is preferably used.

  Further, one or more of these color tone adjusting agents can be used depending on the purpose. In particular, it is preferable to use one or more blue-type adjusting agents and red-type adjusting agents, since the color tone can be finely controlled. Furthermore, in this case, the color tone of the resulting polyester is particularly preferable when the ratio of the blue-based regulator is 50% by weight or more with respect to the total amount of the color-tone regulator to be added.

  Finally, the content of the color tone adjusting agent with respect to the polyester is preferably 30 ppm or less in total. If it exceeds 30 ppm, the transparency of the polyester may be lowered or the color may become dull.

The polyester obtained by the method for producing a polyester of the present invention preferably has an intrinsic viscosity ([η]) of 0.4 to 1.0 dlg ⁻¹ when measured at 25 ° C. using orthochlorophenol as a solvent. More preferably from 0.5~0.8dlg ^-1, particularly preferably from 0.6~0.7dlg ^-1.

  Moreover, in order to improve the thermal stability which is the object of the present invention, the terminal carboxyl group concentration of the polyester is preferably in the range of 1 to 30 equivalents / ton. As the terminal carboxyl group concentration is lower, the thermal stability is improved, and the dirt adhering to the mold during molding and the dirt adhering to the die during yarn production are significantly reduced. When the terminal carboxyl group concentration exceeds 30 equivalents / ton, the effect of reducing dirt adhering to the mold or die may be reduced. The terminal carboxyl group concentration is preferably 25 equivalent / ton or less, particularly preferably 20 equivalent / ton or less.

  The polyester obtained by the method for producing a polyester of the present invention preferably has a diethylene glycol content of 0.1 to 1.5% by weight or less due to less mold contamination during molding. More preferably, it is 1.3 weight% or less, Most preferably, it is 1.1 weight% or less.

  Moreover, since the polyester obtained by the manufacturing method of the polyester of this invention is 1-15 ppm or less in content of acetaldehyde, since the bad influence to the flavor in a molded object and a fragrance is suppressed, it is preferable. More preferably, it is 13 ppm or less, Most preferably, it is 11 ppm or less.

  The color tone of the chip shape is a hunter value, and the L value is in the range of 60 to 95, the a value is in the range of -6 to 2, and the b value is in the range of -5 to 5. To preferred. More preferably, the L value ranges from 70 to 90, the a value ranges from -5 to 1, and the b value ranges from -3 to 3.

  The polyester obtained by the method for producing a polyester of the present invention was dried under reduced pressure at 150 ° C. for 12 hours and then increased in carboxyl end groups after being melted at 290 ° C. for 60 minutes in a nitrogen atmosphere. It is preferably in the range of tons. The smaller this value is, the higher the thermal stability is, and the dirt that adheres to the mold during molding and the dirt that adheres to the die during yarn production are reduced. If this value exceeds 18 equivalents / ton, the thermal stability is inferior and the amount of deposits on the mold or die increases. Preferably it is 13 equivalent / ton or less, Most preferably, it is 8 equivalent / ton or less.

  The polyester obtained by the method for producing a polyester of the present invention has a change in color tone b value Δb value 290 of −6 to 6 after being dried under reduced pressure at 150 ° C. for 12 hours and then melted at 290 ° C. for 60 minutes in a nitrogen atmosphere. It is preferable that it is the range of these. The smaller this value, the less the decomposition and coloring due to thermal deterioration, and the better the thermal stability. If this value exceeds 5, the polymer will be discolored during spinning or molding, which will have a significant effect on quality. Preferably it is 4 or less, particularly preferably 3 or less.

  The polyester obtained by the method for producing a polyester of the present invention is useful as a fiber by forming into a filament shape by, for example, melt extrusion molding or the like and then stretching or spinning.

  A method for producing the polyester of the present invention will be described. Although the example of a polyethylene terephthalate is described as a specific example, it is not limited to this.

Polyethylene terephthalate is usually produced by one of the following processes.
That is, (A) a process in which terephthalic acid and ethylene glycol are used as raw materials, a low polymer is obtained by direct esterification reaction, and a high molecular weight polymer is obtained by subsequent polycondensation reaction, and (B) dimethyl terephthalate and ethylene glycol are used as raw materials. In this process, a low polymer is obtained by a transesterification reaction, and a high molecular weight polymer is obtained by a subsequent polycondensation reaction. Here, the esterification reaction proceeds even without a catalyst, but the aforementioned titanium compound may be added as a catalyst. In the transesterification reaction, a compound such as magnesium, manganese, calcium, cobalt, zinc, lithium, or the above-described titanium compound is used as a catalyst, and after the transesterification reaction is substantially completed, it is used for the reaction. In order to inactivate the catalyst, the phosphorus compound is added.

  The polyester of the present invention can be used as a polycondensation catalyst for the low polymer obtained in any stage of the series of reactions (A) or (B), preferably in the first half of the series of reactions (A) or (B). After adding at least one compound selected from the above-mentioned titanium compound, phosphorus compound, magnesium compound, manganese compound, calcium compound, cobalt compound, titanium oxide particles, and, if necessary, a color adjusting agent, a polycondensation reaction is performed, The high molecular weight polyethylene terephthalate is obtained.

  Further, the above reaction can be applied to a batch, semi-batch, or continuous system.

  The color tone adjusting agent is preferably added to the polyester at any time after completion of the esterification reaction or transesterification reaction until the polycondensation reaction is completed. In particular, it is preferably added after completion of the esterification reaction or transesterification reaction and before the start of the polycondensation reaction, because the dispersion in the polyester is good.

  It is also possible to add the color tone adjusting agent to the polyester after the polycondensation reaction is substantially completed. In this case, a method of directly melting and kneading the color tone adjusting agent on the chip using a single screw or twin screw extruder, or preparing a polyester containing the color tone adjusting agent at a high concentration separately in advance, You may blend with the chip which does not contain.

Hereinafter, the present invention will be described in more detail with reference to examples. In addition, the physical-property value in an Example was measured by the method described below.
(1) Intrinsic viscosity of polymer IV
Measurement was performed at 25 ° C. using orthochlorophenol as a solvent.
(2) Carboxyl terminal group amount of polymer The measurement was carried out by titrating with an automatic titrator (Hiranuma Sangyo Co., Ltd., COM-550) using orthocresol as a solvent and a 0.02 N aqueous NaOH solution at 25 ° C.
(3) Color tone of polymer Using a color difference meter (SM color computer model SM-T45, manufactured by Suga Test Instruments Co., Ltd.), it was measured as a Hunter value (L, a, b value).
(4) Diethylene glycol content of polymer Using monoethanolamine as a solvent, a 1,6-hexanediol / methanol mixed solution was added, cooled, neutralized and centrifuged, and then the supernatant was gas chromatographed (manufactured by Shimadzu Corporation) GC-14A).
(5) Polymer acetaldehyde content Polyester and pure water were heated and extracted at 160 ° C. for 2 hours under a nitrogen seal, and the amount of acetaldehyde in the extract was gas chromatographed using isobutyl alcohol as an internal standard (manufactured by Shimadzu Corporation “ GC-14A ").
(6) Δ carboxyl end group 290, Δb value 290
After the polyester was dried under reduced pressure at 150 ° C. for 12 hours and then heated and melted at 290 ° C. for 60 minutes in a nitrogen atmosphere, the amount of carboxyl end groups and the color tone were measured by the methods (2) and (3) and heated. Differences before and after melting were measured as Δ carboxyl end group 290 and Δb value 290, respectively.
(7) Observation of deposits in the die The amount of deposits around the die holes 72 hours after spinning of the fibers was observed using a long focus microscope. The state in which deposits were hardly recognized was judged as ◯, the state in which deposits were recognized but operable was judged as Δ, and the state in which deposits were found and yarn breakage frequently occurred was judged as ×.

Example 1
About 100 kg of bis (hydroxyethyl) terephthalate is charged in advance, 82.5 kg of high-purity terephthalic acid (manufactured by Mitsui Chemicals) and ethylene glycol are added to an esterification reaction tank maintained at a temperature of 250 ° C. and a pressure of 1.2 × 10 ⁵ Pa. (Manufactured by Nippon Shokubai Co., Ltd.) 35.4 kg of slurry was sequentially supplied over 4 hours, and after completion of the supply, an esterification reaction was carried out over an additional hour, and 101.5 kg of the resulting esterification reaction product was polycondensed. Transferred to.

  To the esterification reaction product, 7.6 g of cobalt acetate (20 ppm in terms of cobalt atom relative to the polymer), 12.0 g of magnesium acetate (15 ppm in terms of magnesium atom relative to the polymer) ethylene glycol solution, and the polymer Citrate chelate titanium compound equivalent to 5 ppm in terms of titanium atom, tetrakis (2,4-di-t-butyl-5-methylphenyl) [1,1-biphenyl equivalent to 289 ppm (15 ppm in terms of phosphorus atom) relative to the polymer ] -4,4'-diylbisphosphonite (Osaki Kogyo Co., Ltd., GSY-P101) 30 minutes before adding in a separate mixing tank and stirring at room temperature for 30 minutes, the mixture is Added. After 5 minutes, an ethylene glycol slurry of titanium oxide particles was added to the polymer in an amount of 0.3% by weight in terms of titanium oxide particles. After another 5 minutes, the reaction system was decompressed to initiate the reaction. The reactor was gradually heated from 250 ° C. to 290 ° C., and the pressure was reduced to 40 Pa. The time to reach the final temperature and final pressure was both 60 minutes. When the predetermined stirring torque was reached, the reaction system was purged with nitrogen and returned to normal pressure to stop the polycondensation reaction, discharged into a strand, cooled, and immediately cut to obtain polymer pellets. The time from the start of decompression to the arrival of the predetermined stirring torque was 2 hours and 45 minutes.

  The obtained polymer was excellent in color tone and heat resistance.

  The polyester was vacuum-dried at 150 ° C. for 12 hours, then subjected to a spinning machine, melted by a melter, discharged from the spinning pack portion, and taken up at a speed of 1000 m / min. In the melt spinning process, almost no deposits around the nozzle holes and no increase in filtration pressure were observed during spinning.

Examples 2-9
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that the addition amounts of the magnesium compound, manganese compound, calcium compound, cobalt compound, and color tone modifier (Solvent Blue 104) were changed. In Example 9, although the color tone b value was slightly poor, the obtained polymer was excellent in color tone and thermal stability was also excellent. In addition, almost no deposits and increase in filtration pressure around the nozzle holes during spinning were observed.

Examples 10-15
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that the addition amounts of the titanium compound and the magnesium compound were changed. In Example 15, the color tone was slightly poor, and in Examples 12, 13, and 15, the heat resistance was slightly poor, but it was at a level with no problem in terms of product. In other examples, both the color tone and heat resistance were good. Further, the deposit around the base hole and the increase in the filtration pressure during spinning were slightly contaminated and broken in Example 13, but at a level that does not interfere with the operation. In the other examples, almost no deposits around the nozzle holes and no increase in filtration pressure were observed during spinning.

Examples 16-18
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that the addition amount of the phosphorus compound was changed. In Example 16, although the color tone and heat resistance were slightly poor, they were at a level with no problem on the product. In other examples, both the color tone and heat resistance were good. In addition, almost no deposits and increase in filtration pressure around the nozzle holes during spinning were observed.

Examples 19-20
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that the mixing time of the titanium compound and phosphorus compound was changed. The obtained polymer was excellent in color tone and excellent in thermal stability. In addition, almost no deposits and increase in filtration pressure around the nozzle holes during spinning were observed.

Example 21
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that the titanium compound and the phosphorus compound were not premixed. The titanium compound and the phosphorus compound were added to the reaction system by first adding the phosphorus compound to the polycondensation reaction tank after the esterification reaction product was transferred, and adding the magnesium compound 5 minutes later. Titanium compound was added after minutes. The obtained polymer was excellent in color tone and excellent in thermal stability. In addition, almost no deposits and increase in filtration pressure around the nozzle holes during spinning were observed.

Examples 22-23
In Example 22, after the polycondensation catalyst was added, the inside of the reactor was depressurized to start the polycondensation reaction, and then the phosphorus compound was further added until the polymerization reached the target degree of polymerization. Polyester was polymerized and melt-spun as in Example 1. The phosphorus compound was added to the reaction system at a time when 85% of the predetermined stirring torque was reached (at 2 hours 30 minutes after the start of decompression), and a thickness prepared by injection molding a polyethylene terephthalate sheet. Tetrakis (2,4-di-t-butyl-5-methylphenyl) [1,1-biphenyl]-674 ppm (35 ppm in terms of phosphorus atom) with respect to the polymer in a container having a thickness of 0.2 mm and an internal volume of 500 cm ³ 4,4′-Diylbisphosphonite (Osaki Kogyo Co., Ltd., GSY-P101) was packed and added from the top of the reaction can. Further, in Example 23, the addition of the phosphorus compound before starting the polycondensation was not performed, and the period from when the inside of the reactor was depressurized to start the polycondensation reaction until the polymerization reached the target degree of polymerization. (When 85% of the predetermined stirring torque is reached: 2 hours and 20 minutes after depressurization is started) 963 ppm (50 ppm in terms of phosphorus atom) of tetrakis (2,4-di-t) with respect to the polymer -Butyl-5-methylphenyl) [1,1-biphenyl] -4,4'-diylbisphosphonite (Osaki Kogyo Co., Ltd., GSY-P101) was added to polymerize the polyester in the same manner as in Example 22, Melt spun.
The obtained polymer was excellent in color tone and excellent in thermal stability. In addition, almost no deposits and increase in filtration pressure around the nozzle holes during spinning were observed.

Examples 24-25
In Example 24, tetrakis (2,4-di-t-butylphenyl) [1,1-biphenyl] -4,4′-diylbisphosphonite (manufactured by Ciba Specialty Chemicals, IRGAFOS P— EPQ), Example 25, except that bis (2,4-di-t-butyl-5-methylphenyl) [1,1-biphenyl] -4-ylphosphonite was used as the phosphorus compound. Polyester was polymerized and melt-spun in the same manner as described above. The obtained polymer was excellent in color tone and excellent in thermal stability. In addition, almost no deposits and increase in filtration pressure around the nozzle holes during spinning were observed.

Examples 26-28
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that ethylenediaminetetraacetic acid chelate titanium, trimellitic acid chelate titanium, and tetrabutoxytitanium were used instead of the citric acid chelate titanium compound. In Example 28, the heat resistance was slightly poor, but it was at a level that was not a problem on the product at all. In other examples, both the color tone and heat resistance were good. In addition, almost no deposits and increase in filtration pressure around the nozzle holes during spinning were observed.

Examples 29-30
Except for changing the setting of the predetermined agitation torque (in Example 29, the intrinsic viscosity of the resulting polyester is lowered, in Example 30, the intrinsic viscosity of the obtained polyester is increased), the same as in Example 1. Polyester was polymerized and melt spun. The obtained polyester had good color tone and heat resistance, and almost no deposits around the nozzle holes and no increase in filtration pressure were observed during spinning.

Comparative Example 1
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that no phosphorus compound was added. The color tone was strongly yellowish, and contained a lot of DEG and acetaldehyde, and was a polymer with poor heat resistance.

Comparative Examples 2-4
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that a phosphoric acid compound was added as the phosphorus compound.

  Comparative Examples 2 and 3 did not reach the predetermined stirring torque. Moreover, in Comparative Example 4, the time until it reached significantly increased, and the polymer was inferior in color tone. Further, the polymer was a polymer having a large Δ carboxyl end group 290 and Δb value 290 and inferior heat resistance.

Comparative Examples 5-7
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that a phosphonic acid compound was added as the phosphorus compound. Comparative Examples 5 and 6 did not reach the predetermined stirring torque. Moreover, in Comparative Example 7, the time until it was significantly increased, and the polymer was inferior in color tone. Further, the polymer was a polymer having a large Δ carboxyl end group 290 and Δb value 290 and inferior heat resistance.

Comparative Examples 8-10
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that a phosphinic acid compound was added as the phosphorus compound. Comparative Examples 8 and 9 did not reach the predetermined stirring torque. Moreover, in Comparative Example 10, the time to reach was significantly increased, resulting in a polymer with poor color tone. Further, the polymer was a polymer having a large Δ carboxyl end group 290 and Δb value 290 and inferior heat resistance.

Comparative Examples 11-12
A polyester was polymerized in the same manner as in Example 1 except that a phosphine oxide compound was added as the phosphorus compound. Neither Comparative Example 11 nor 12 reached the predetermined stirring torque.

Comparative Examples 13-15
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that a phosphorous compound was added as the phosphorus compound. In any level, the time until the predetermined stirring torque was reached was significantly increased, and the polymer was inferior in color. Further, the polyester had a large Δ carboxyl end group 290 and Δb value 290, and was inferior in thermal stability.

Comparative Examples 16-17
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that a phosphonous acid compound not having the structure represented by Formula 1 was added as the phosphorus compound. In any level, the time until the predetermined stirring torque was reached was significantly increased, and the polymer was inferior in color. Further, the polyester had a large Δ carboxyl end group 290 and Δb value 290, and was inferior in thermal stability.

Comparative Examples 18-19
A polyester was polymerized and melt-spun in the same manner as in Example 1 except that a phosphinic acid compound was added as the phosphorus compound. In any level, the time until the predetermined stirring torque was reached was significantly increased, and the polymer was inferior in color. Further, it was a polyester having a large Δ carboxyl end group 290 and a large Δb value 290 and inferior thermal stability.

Comparative Examples 20-21
A polyester was polymerized and melt-spun as in Example 1 except that a phosphine compound was added as the phosphorus compound. In any level, the time until the predetermined stirring torque was reached was significantly increased, and the polymer was inferior in color. Further, it was a polyester having a large Δ carboxyl end group 290 and a large Δb value 290 and inferior thermal stability.

Comparative Example 22
Polyester was polymerized and melt-spun as in Example 1 except that antimony oxide, an antimony compound, was added as a polycondensation catalyst instead of the titanium compound. Although the polymer had good time, polymer color tone and heat resistance until reaching a predetermined stirring torque, deposits were observed around the mouthpiece holes during melt spinning, and the filtration pressure increased and yarn breakage occurred.

Claims (8)

A method for producing a polyester obtained by esterifying or transesterifying dicarboxylic acid or an ester-forming derivative thereof with diol or an ester-forming derivative thereof and then polycondensing in the presence of a titanium-based polycondensation catalyst In addition, at least 1 sort (s) is added among the phosphorus compounds represented by following formula 1 or formula 2. The manufacturing method of polyester characterized by the above-mentioned.

(In Formula 1 and Formula 2, R _{1 to} R ₄ each independently represent a hydroxyl group or a hydrocarbon group having 1 to 20 carbon atoms.) The molar ratio Ti / P of the titanium atom in the titanium-based polycondensation catalyst and the phosphorus atom in the phosphorus compound represented by Formula 1 or Formula 2 is 0.01 to 1.5. Polyester production method.   At least one compound selected from the group consisting of a magnesium compound, a manganese compound, a calcium compound, and a cobalt compound is added, and the total in terms of atoms in the magnesium compound, the manganese compound, the calcium compound, and the cobalt compound and Formula 1 or Formula 2 3. The method for producing a polyester according to claim 1, wherein a molar ratio (Mg + Mn + Ca + Co) / P of a phosphorus atom in the represented phosphorus compound is 0.1 to 5. 5. The method for producing a polyester according to claim 1, wherein the phosphorus compound is a compound represented by Formula 3.

(In the above formula _3, R 5 to R ₇ each independently represents a hydroxyl group or a hydrocarbon group having 1 to 10 carbon atoms, a + b + c is an integer of 0-5.) The method for producing a polyester according to claim 1, wherein the phosphorus compound is a compound represented by Formula 4.

(In the above formula 4, R _{8 to} R ₁₀ each independently represents a hydroxyl group or a hydrocarbon group having 1 to 10 carbon atoms.)   The production of polyester, wherein the titanium-based polymerization catalyst according to claim 1 is a titanium complex having at least one selected from the group consisting of polyvalent carboxylic acid, hydroxycarboxylic acid and nitrogen-containing carboxylic acid as a chelating agent. Method.   The polymer color tone change after being dried under reduced pressure at 150 ° C for 12 hours and then melted at 290 ° C for 60 minutes in a nitrogen atmosphere is -5 to 5. A polyester produced by the method described in 1. In the process for producing a polyester obtained by polycondensation reaction of a dicarboxylic acid or an ester-forming derivative thereof with a diol or an ester-forming derivative thereof in the presence of a polycondensation catalyst, before starting the pressure reduction in the polymerization reactor The phosphorus compound of Formula 1 or Formula 2 is added to the obtained polyester in an amount of 0 to 50 ppm in terms of phosphorus atom, and the pressure reduction in the polymerization reactor is started until the polyester reaches the target degree of polymerization. A method for producing a polyester, characterized in that 10 to 500 ppm of the phosphorus compound of formula 1 or formula 2 is added to the polyester obtained.

(In Formula 1 and Formula 2, R _{1 to} R ₄ each independently represent a hydroxyl group or a hydrocarbon group having 1 to 20 carbon atoms.)