JP2002220448A - Polymerization catalyst for polyester, polyester produced by using the same and method for producing polyester - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a polymerization catalyst for a polyester, which comprises a main component other than an antimony or germanium compound, and is excellent in catalytic activity giving a polyester excellent in thermal stability, thermal oxidation stability and hydrolysis resistance and to provide the polyester excellent in thermal stability, thermal oxidation stability and hydrolysis resistance. SOLUTION: The polymerization catalyst for the polyester, which is characterized by containing at least one compound selected from aluminum and its compounds as a metal-containing component and at least one compound selected from metallic salts of a phosphorus compound, is used.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyester polymerization catalyst, a polyester produced using the same, and a method for producing the polyester. More specifically, the present invention relates to a novel polyester which does not use a germanium or antimony compound as a main component of the catalyst. The present invention relates to a polymerization catalyst, a polyester produced using the same, and a method for producing the polyester.

[0002]

2. Description of the Related Art Polyester, especially polyethylene terephthalate (hereinafter abbreviated as PET) has excellent mechanical properties and chemical properties, and is applicable to various uses such as fibers for clothing and industrial materials, and packaging. It is applied to various films and sheets for tapes and magnetic tapes, and molded products such as bottles and engineering plastics.

[0003] In the industrial production of PET, bis (2-hydroxyethyl) terephthalate is produced by esterification or transesterification of terephthalic acid or dimethyl terephthalate with ethylene glycol. Obtained by polycondensation.

As a catalyst used in the polycondensation, antimony trioxide is widely used. Antimony trioxide is a catalyst that is inexpensive and has excellent catalytic activity.
Since metal antimony precipitates during polycondensation, there is a problem that darkening and foreign matter are generated in PET. Under such circumstances, a polyester containing no or only a very small amount of antimony has been desired.

[0005] Attempts have been made to use antimony trioxide as a polycondensation catalyst and to suppress the occurrence of darkening and foreign matter in PET. For example, in Japanese Patent No. 2666502, the use of a compound of antimony trioxide, bismuth and selenium as a polycondensation catalyst suppresses the formation of black foreign substances in PET. JP-A-9-291141 states that the use of antimony trioxide containing sodium and iron oxides as a polycondensation catalyst suppresses the deposition of antimony metal. However, these polycondensation catalysts cannot achieve the purpose of a polyester containing no antimony after all.

[0006] Studies have been made on polycondensation catalysts that can replace antimony trioxide. In particular, titanium compounds typified by tetraalkoxy titanates have already been proposed. However, PET produced using such compounds has problems that it is significantly colored and that thermal decomposition easily occurs.

As an attempt to overcome such problems when using a tetraalkoxy titanate as a polycondensation catalyst, for example, in Japanese Patent Application Laid-Open No. 55-116722, tetraalkoxy titanate is used simultaneously with a cobalt salt and a calcium salt. A method has been proposed. Also, JP-A-8-7358
No. 1 proposes a method in which a tetraalkoxy titanate is used simultaneously with a cobalt compound as a polycondensation catalyst, and a fluorescent brightener is used. However, in these proposals, although the coloring of PET is reduced when tetraalkoxy titanate is used as a polycondensation catalyst, on the other hand,
Effective suppression of thermal decomposition of PET has not been achieved.

Germanium compounds have been put into practical use as polycondensation catalysts which can substitute for antimony trioxide and which overcome problems such as the use of tetraalkoxytitanate. It has a problem that it is very expensive and a problem that the catalyst concentration in the reaction system changes due to easy distilling out of the reaction system during the polymerization, making it difficult to control the polymerization.

It is known that aluminum compounds generally have poor catalytic activity. Among the aluminum compounds,
It has been reported that aluminum chelate compounds have higher catalytic activity as polycondensation catalysts than other aluminum compounds, but that they have sufficient catalytic activity compared to the above-mentioned antimony compounds and titanium compounds. In addition, polyester which is polymerized over a long period of time using an aluminum compound as a catalyst has a problem in that it has poor thermal stability and the like.

[0010]

DISCLOSURE OF THE INVENTION The present invention comprises an antimony compound or a germanium compound as a main component of a catalyst, aluminum as a main metal component, excellent catalytic activity, and without deactivation or removal of the catalyst. Provided is a polyester polymerization catalyst which effectively suppresses thermal deterioration during melt molding and gives a polyester having excellent thermal stability. The present invention also provides a film using the catalyst,
Improved thermal stability when performing melt molding of hollow molded products such as bottles and fibers, etc., and excels in quality even when using virgin resin or reusing waste generated during molding. And a method for producing a polyester using the polyester polymerization catalyst.

Another object of the present invention is to provide a polyester polymerization catalyst which gives a polyester excellent in heat aging resistance and hydrolysis resistance, a polyester excellent in heat aging resistance and hydrolysis resistance, and the use of the polyester polymerization catalyst. To provide a polyester production method.

[0012]

Means for Solving the Problems The inventors of the present invention have conducted intensive studies aiming at solving the above-mentioned problems, and as a result, although aluminum compounds are originally inferior in catalytic activity, they use aluminum compounds and specific phosphorus compounds. As a result, it has been found that a polyester excellent in catalytic activity and excellent in thermal stability, thermal oxidation stability and hydrolysis resistance can be obtained.

That is, the present invention provides a polyester polymerization catalyst comprising at least one selected from aluminum and its compounds as a metal-containing component, and at least one metal salt compound of phosphorus. And a polyester produced using the same, and a method for producing the polyester.

[0014]

BEST MODE FOR CARRYING OUT THE INVENTION The metal salt compound of phosphorus constituting the polymerization catalyst of the present invention is not particularly limited as long as it is a metal salt of a phosphorus compound. The effect of improvement is large and preferable. Examples of the metal salt of a phosphorus compound include a monometal salt, a dimetal salt, and a trimetal salt.

The phosphonic acid compound as referred to in the present invention refers to a compound having a structure represented by the following formula (3).

[0016]

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Of the above-mentioned phosphorus compounds, the use of a compound having an aromatic ring structure is preferred because the effect of improving the catalytic activity is large.

Further, among the above phosphorus compounds, the metal portion of the metal salt is Li, Na, K, Be, Mg, Sr,
It is preferable to use one selected from Ba, Mn, Ni, Cu, and Zn because the effect of improving the catalytic activity is large. Of these, Li, Na, and Mg are particularly preferred.

As the phosphorus metal salt compound constituting the polymerization catalyst of the present invention, it is preferable to use at least one selected from the compounds represented by the following general formula (1) because the effect of improving the catalytic activity is large.

[0020]

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(In the formula (1), R ¹ is hydrogen and has 1 to 5 carbon atoms.
And represents a hydrocarbon group having 1 to 50 carbon atoms including 0 hydrocarbon group, hydroxyl group, halogen group, alkoxyl group or amino group. R ² is hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group having 1 to 50 carbon atoms.
Represents a hydrocarbon group. R ³ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group or a hydrocarbon group having 1 to 50 carbon atoms including carbonyl. l is 1
M is an integer of 0 or 1 or more, and l + m is 4
It is as follows. M represents a (l + m) -valent metal cation. n is 1
Represents the above integer. The hydrocarbon group may contain an alicyclic structure or branched structure such as cyclohexyl or an aromatic ring structure such as phenyl or naphthyl. As the above R ¹ , for example, phenyl, 1-naphthyl, 2-naphthyl, 9-anthryl, 4-biphenyl,
2-biphenyl and the like. Examples of R ² include hydrogen, methyl, ethyl, propyl, isopropyl, n-butyl, sec-butyl, ter
t- butyl group, an aliphatic group of a long chain, a phenyl group, a naphthyl group, a substituted phenyl group or a naphthyl group, -CH ₂ CH ₂
And a group represented by OH. Examples of R ³ O ⁻ include a hydroxide ion, an alcoholate ion, an acetate ion and an acetylacetone ion.

Among the compounds represented by the general formula (1), it is preferable to use at least one selected from the compounds represented by the following general formula (2).

[0023]

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(In the formula (2), R ¹ is hydrogen and has 1 to 5 carbon atoms.
And represents a hydrocarbon group having 1 to 50 carbon atoms including 0 hydrocarbon group, hydroxyl group, halogen group, alkoxyl group or amino group. R ³ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group or a hydrocarbon group having 1 to 50 carbon atoms including carbonyl. l is an integer of 1 or more, m is 0 or an integer of 1 or more, and l + m is 4 or less. M represents a (l + m) -valent metal cation. The hydrocarbon group may contain an alicyclic structure or branched structure such as cyclohexyl or an aromatic ring structure such as phenyl or naphthyl. As the above R ¹ , for example, phenyl, 1-naphthyl, 2-naphthyl, 9-anthryl, 4-biphenyl,
2-biphenyl and the like. Examples of R ³ O ⁻ include a hydroxide ion, an alcoholate ion, an acetate ion and an acetylacetone ion. Among the above-mentioned phosphorus compounds, the use of a compound having an aromatic ring structure is preferable because the effect of improving the catalytic activity is large.

In the above formula (2), M is Li, N
a, K, Be, Mg, Sr, Ba, Mn, Ni, Cu,
It is preferable to use a material selected from Zn because the effect of improving the catalytic activity is large. Of these, Li, Na, and Mg are particularly preferred. Examples of the phosphorus metal salt compound of the present invention include lithium [ethyl (1-naphthyl) methylphosphonate], sodium [ethyl (1-naphthyl) methylphosphonate], magnesium bis [(1-naphthyl) methylphosphonate], potassium [ (2-naphthyl) ethyl methyl phosphonate], magnesium bis [(2-naphthyl) methyl ethyl phosphonate], lithium [ethyl benzyl phosphonate], sodium [ethyl benzyl phosphonate], magnesium bis [ethyl benzyl phosphonate], beryllium bis [Ethyl benzylphosphonate],
Strontium bis [ethyl benzylphosphonate], manganese bis [ethyl benzylphosphonate], sodium benzylphosphonate, magnesium bis [benzylphosphonic acid], sodium [ethyl (9-anthryl) methylphosphonate], magnesium bis [(9-anthryl) ) Ethyl methyl phosphonate], sodium [ethyl 4-hydroxybenzyl phosphonate], magnesium bis [ethyl 4-hydroxybenzyl phosphonate], sodium [phenyl chlorophenyl phosphonate], magnesium bis [4-chlorobenzyl phosphonate ethyl] ], Sodium [methyl 4-aminobenzylphosphonate], magnesium bis [methyl 4-aminobenzylphosphonate], sodium phenylphosphonate, magnesium bis [phenylphosphonate] Ethyl phosphate], zinc bis [phenylphosphonic acid ethyl] and the like. Among these, lithium [ethyl (1-naphthyl) methylphosphonate], sodium [ethyl (1-naphthyl) methylphosphonate], magnesium bis [(1-naphthyl) methylphosphonate], lithium [ethyl benzylphosphonate], Sodium [ethyl benzylphosphonate],
Magnesium bis [ethyl benzylphosphonate], sodium benzylphosphonate and magnesium bis [benzylphosphonic acid] are particularly preferred.

By using a phosphorus compound having such a specific structure, an antimony compound or a germanium compound is not included as a main component of the catalyst, aluminum is used as a main metal component, and excellent catalytic activity is obtained. Without removal, a polyester polymerization catalyst is obtained, which effectively suppresses thermal degradation during melt molding and provides a polyester having excellent thermal stability, thermal oxidation stability and hydrolysis resistance.

When the phosphorus compound of the present invention is used in combination, a catalyst exhibiting a sufficient catalytic effect can be obtained even if the amount of aluminum added in the polyester polymerization catalyst is small.

The amount of the phosphorus compound of the present invention to be used is preferably 0.0001 to 0.1 mol% based on the total number of moles of all constituent units of the polycarboxylic acid component of the obtained polyester.
More preferably, it is 0.005 to 0.05 mol%. When the addition amount of the phosphorus compound is less than 0.0001 mol%, the effect of addition may not be exhibited. When the addition amount exceeds 0.1 mol%, on the contrary, the catalytic activity as a polyester polymerization catalyst may decrease. The tendency changes depending on the amount of aluminum used and the like.

This is a technology using an aluminum compound as a main catalyst component without using a phosphorus compound. This technology reduces the amount of the aluminum compound used, and furthermore adds a cobalt compound to make the heat stable when the aluminum compound is used as the main catalyst. Although there is a technique for preventing coloration due to a decrease in the property, if the cobalt compound is added to such an extent that it has a sufficient catalytic activity, the thermal stability also decreases. Therefore, it is difficult to achieve both using this technique.

According to the present invention, the use of the phosphorus compound having the above-mentioned specific chemical structure does not cause problems such as a decrease in thermal stability and the generation of foreign matter, and the addition amount of the metal-containing component as aluminum is small. However, a polymerization catalyst having a sufficient catalytic effect can be obtained, and by using this polymerization catalyst, the thermal stability at the time of melt molding of hollow molded articles such as polyester films and bottles, and fibers and engineering plastics can be improved. Even if a phosphoric acid ester such as phosphoric acid or trimethyl phosphoric acid is added in place of the phosphorus compound of the present invention, the effect of addition is not seen and it is not practical. Further, even when the phosphorus compound of the present invention is used in combination with a conventional antimony compound, a titanium compound, a tin compound, a metal-containing polyester polymerization catalyst such as a germanium compound in the range of the addition amount of the present invention, the melt polymerization reaction is promoted. No effect is observed.

As the aluminum or aluminum compound constituting the polycondensation catalyst of the present invention, known aluminum compounds can be used without limitation in addition to metallic aluminum.

Specific examples of the aluminum compound include aluminum formate, aluminum acetate, basic aluminum acetate, aluminum propionate, aluminum oxalate, aluminum acrylate, aluminum laurate, aluminum stearate, aluminum benzoate, and aluminum trichloroacetate. , Aluminum lactate,
Carboxylates such as aluminum tartrate, aluminum citrate, and aluminum salicylate; inorganics such as aluminum chloride, aluminum hydroxide, aluminum hydroxide chloride, polyaluminum chloride, aluminum nitrate, aluminum sulfate, aluminum carbonate, aluminum phosphate, and aluminum phosphonate Acid salts, aluminum methoxide, aluminum ethoxide, aluminum n-propoxide, aluminum iso-propoxide, aluminum n-butoxide, aluminum t-butoxide, and other aluminum alkoxides, aluminum acetylacetonate, aluminum acetyl acetate,
It consists of aluminum chelates such as aluminum ethyl acetoacetate and aluminum ethyl acetoacetate di-iso-propoxide, organic aluminum compounds such as trimethyl aluminum and triethyl aluminum or partial hydrolysates thereof, aluminum alkoxides and aluminum chelates and hydroxycarboxylic acids. Reaction products, aluminum oxide, ultrafine aluminum oxide, aluminum silicate, and a composite oxide of aluminum with titanium, silicon, zirconium, an alkali metal, an alkaline earth metal, or the like can be given. Of these, carboxylate, inorganic acid salt and chelate compound are preferable, and among these, basic aluminum acetate, aluminum chloride, aluminum hydroxide, aluminum hydroxide chloride and aluminum acetylacetonate are particularly preferable. As the basic aluminum acetate, one stabilized with an additive such as boric acid may be used.

The amount of the aluminum or aluminum compound used in the present invention is 0.001 to 0.05 mol per mol of all the constituent units of the carboxylic acid component such as dicarboxylic acid and polycarboxylic acid of the obtained polyester. %, More preferably 0.005 to 0.0%
2 mol%. If the amount used is less than 0.001 mol%, the catalytic activity may not be sufficiently exhibited. If the amount used is more than 0.05 mol%, the thermal stability and thermo-oxidation stability decrease, and aluminum is caused. In some cases, the generation of foreign matter and the increase in coloring may become a problem. As described above, even when the addition amount of the aluminum component is small, the polymerization catalyst of the present invention is greatly characterized in that it exhibits a sufficient catalytic activity. As a result, thermal stability and thermal oxidation stability are excellent, and foreign matter and coloring due to aluminum are reduced.

The polyester polymerization catalyst of the present invention has an activity parameter (AP) satisfying the following formula (1). Polyethylene terephthalate (PET) polymerized using this polyester polymerization catalyst has a thermal stability parameter (TS).
Converts the following equation (2) into a thermal oxidation stability parameter (TO
S) preferably satisfies the following formula (3), and the hydrolysis resistance parameter (HS) desirably satisfies the following formula (4).

(1) AP (min) <2T (min) (wherein the activity parameter AP is the intrinsic viscosity (IV) at 275 ° C. and a reduced pressure of 13.3 Pa (0.1 Torr) using a predetermined amount of catalyst. ) Indicates the time (min) required to polymerize 0.65 dl / g of polyethylene terephthalate, and T indicates the AP when antimony trioxide is used as a catalyst, where antimony trioxide is contained in the produced polyethylene terephthalate. The antimony atom is added as an antimony atom in an amount of 0.05 mol% with respect to the acid component.) In the present invention, antimony trioxide having a purity of 99% or more is used for comparison. For example, Antidony (III) oxide manufactured by ALDRICH, purity 99.999% is used.

(2) TS <0.30 (where TS is a melt-polymerized polyethylene terephthalate (PE) having an intrinsic viscosity (IV) of about 0.65 dl / g)
T) 1 g of a resin chip was placed in a glass test tube, vacuum-dried at 130 ° C. for 12 hours, and then dried under a non-circulating nitrogen atmosphere.
The IV after maintaining at 2 ° C. for 2 hours in a molten state is measured and can be determined by the following formula. TS = 0.245 ｛[IV] _f2 ^-1.47 − [IV] _i
^-1.47 ｝ [IV] _i and [IV] _f2 indicate the IV (dl / g) before and after the melting test, respectively. )

The non-circulating nitrogen atmosphere means a non-circulating nitrogen atmosphere. For example, a glass test tube containing a resin chip is connected to a vacuum line, and the pressure is reduced and nitrogen is sealed.
This is a state in which nitrogen is sealed and sealed so that the pressure becomes 100 Torr after the repetition is repeated at least 100 times.

(3) TOS <0.10 (in the above formula, TOS has a melt-polymerized IV of about 0.65 d
1 / g PET resin chip was freeze-pulverized to powder having a size of 20 mesh or less, which was vacuum-dried at 130 ° C. for 12 hours. 0.3 g was placed in a glass test tube and vacuum-dried at 70 ° C. for 12 hours. 230 under dry air
The IV after heating at 15 ° C. for 15 minutes is measured and can be determined using the following formula. TOS = 0.245 ｛[IV] _f1 ^-1.47 − [IV] _i
^-1.47 ｝ [IV] _i and [IV] _f1 indicate the IV (dl / g) before and after the heating test, respectively. )

As a method of heating under air dried with silica gel, for example, a method of attaching a drying tube containing silica gel to the upper part of a glass test tube and heating under dry air can be used.

(4) HS <0.10 (HS has an intrinsic viscosity of about 0.65 d obtained by melt polymerization.
1 / g (before the test; [IV] _i ) PET chips were frozen and pulverized into powder having a size of 20 mesh or less, and dried in vacuum at 130 ° C. for 12 hours. Intrinsic viscosity ([IV] _f2 ) after stirring at 130 ° C. for 6 hours under pressure and pressure
Is a numerical value calculated by the following equation. HS = 0.245 ｛[IV] _f2 ^-1.47- [IV] _i
^-1.47 ｝)

The beaker used for measuring the HS was
Use one that does not elute acid or alkali. Specifically, it is preferable to use a stainless beaker or a quartz beaker.

With this configuration, thermal degradation during melt molding is effectively suppressed without deactivating or removing the catalyst, resulting in excellent thermal stability, excellent thermal oxidation stability, and hydrolysis resistance. Polyester polymerization catalysts which give excellent polyesters, have excellent catalytic activity, and therefore have high polyester productivity, and polyesters polymerized using the catalysts are preferred.

The AP is preferably 1.5T or less, more preferably 1.3T or less, more preferably 1.
It is particularly preferable that it is 0T or less. TS is more preferably 0.25 or less, particularly preferably 0.20 or less. TOS is more preferably 0.09 or less, and particularly preferably 0.08 or less.
Further, HS is more preferably 0.09 or less,
It is particularly preferably 0.085 or less.

The method for measuring AP is specifically as follows. 1) (BHET production process) Terephthalic acid and a 2-fold molar amount of ethylene glycol were used, and the esterification rate was 95%.
% Bis (2-hydroxyethyl) terephthalate (B
HET) and a mixture of oligomers (hereinafter, referred to as a BHET mixture). 2) (Catalyst addition step) A predetermined amount of a catalyst is added to the above BHET mixture, and the mixture is stirred at 245 ° C. for 10 minutes under a normal pressure under a nitrogen atmosphere, and then heated to 275 ° C. in 50 minutes. Is gradually reduced to 0.1 Torr. 3) (Polycondensation step) 275 ° C, 13.3 Pa (0.1 T
(orr) to carry out a polycondensation reaction and polymerize until the IV of polyethylene terephthalate reaches 0.65 dl / g. 4) The polymerization time required for the polycondensation step is defined as AP (min).

These are performed using a batch-type reaction apparatus.

The production of the BHET mixture is performed by a known method. For example, terephthalic acid and a 2-fold molar amount of ethylene glycol are charged into a batch type autoclave equipped with a stirrer, and an esterification reaction is performed while distilling water out of the system at 245 ° C. under a pressure of 0.25 MPa. Manufactured.

The "predetermined amount of catalyst" means the amount of the catalyst used in a variable amount according to the activity of the catalyst. The amount of the catalyst is small for a highly active catalyst and large for a low active catalyst. . The amount of the catalyst used is at most 0.1 mol% as an aluminum compound based on the number of moles of terephthalic acid. If more is added, the residual amount in the polyester is large,
It is no longer a practical catalyst.

As the PET resin chip used for measuring the above-mentioned TS, TOS, and HS, the one produced by quenching from a molten state after the above steps 1) to 3) is used. As the shape of the resin chip used for these measurements, for example, a cylindrical resin chip having a length of about 3 mm and a diameter of about 2 mm is used.

In the present invention, in addition to aluminum or its compound, a small amount of at least one selected from the group consisting of alkali metals, alkaline earth metals and compounds thereof is used as a secondary metal.
It is a preferred embodiment to coexist as a metal-containing component. The coexistence of such a second metal-containing component in the catalyst system increases the catalytic activity in addition to the effect of suppressing the production of diethylene glycol, and thus provides a catalyst component with a higher reaction rate, which is effective for improving productivity. . As these alkali metals and alkaline earth metals, Li, Na, K, R
It is preferably at least one selected from b, Cs, Be, Mg, Ca, Sr, and Ba, and more preferably an alkali metal or a compound thereof. When an alkali metal or a compound thereof is used, it is particularly preferable to use Li, Na, and K.

Examples of the compound of an alkali metal or an alkaline earth metal include, for example, saturated aliphatic carboxylate such as formic acid, acetic acid, propionic acid, butyric acid and oxalic acid, and unsaturated fatty acid such as acrylic acid and methacrylic acid. Aromatic carboxylate, aromatic carboxylate such as benzoic acid, halogen-containing carboxylate such as trichloroacetic acid, lactic acid, citric acid,
Hydroxycarboxylic acid salts such as salicylic acid, carbonic acid, sulfuric acid, nitric acid, phosphoric acid, phosphonic acid, hydrogen carbonate, hydrogen phosphate, hydrogen sulfate, sulfurous acid, thiosulfuric acid, hydrochloric acid, hydrobromic acid,
Chloric acid, inorganic acid salts such as bromic acid, 1-propanesulfonic acid, 1-pentanesulfonic acid, organic sulfonates such as naphthalenesulfonic acid, organic sulfates such as lauryl sulfate,
Methoxy, ethoxy, n-propoxy, iso-propoxy,
Examples thereof include alkoxides such as n-butoxy and t-butoxy, chelate compounds such as acetylacetonate, oxides and hydroxides.

When a strong alkali such as hydroxide is used among these alkali metals, alkaline earth metals or compounds thereof, they are hardly dissolved in an organic solvent such as diol such as ethylene glycol or alcohol. Because of the tendency, it must be added to the polymerization system in an aqueous solution, which may cause a problem in the polymerization step. Furthermore, when a strong alkali such as a hydroxide is used, the polyester is liable to undergo side reactions such as hydrolysis during polymerization, and the polymerized polyester tends to be colored, and the hydrolysis resistance is also reduced. Tend. Therefore,
Suitable alkali metals or compounds thereof or alkaline earth metals or compounds thereof of the present invention are alkali metal or alkaline earth metal saturated aliphatic carboxylate, unsaturated aliphatic carboxylate, aromatic carboxylate. Acid salts, halogen-containing carboxylate salts, hydroxycarboxylate salts, inorganic acid salts, organic sulfates, alkoxides,
Chelate compounds and oxides. Of these, alkali metal or alkaline earth metal saturated aliphatic carboxylate salts are preferable, and acetate salts are particularly preferable from the viewpoints of ease of handling and availability.

When an alkali metal, an alkaline earth metal and a compound thereof are added, the amount M (mol%) used is
It is preferably 1 × 10 ⁻⁶ or more and less than 0.1 mol%, more preferably 5 × 10 ^{−6 to} 0.05 mol%, further preferably, 5 × 10 ^{−6 to} less than 0.1 mol%, based on the number of moles of all the polycarboxylic acid units constituting the polyester. It is 1 × 10 ^{−5 to} 0.03 mol%, particularly preferably 1 × 10 ^{−5 to} 0.01 mol%. Since the added amount of the alkali metal and the alkaline earth metal is small, the reaction rate can be increased without causing problems such as a decrease in thermal stability, generation of foreign matter, and coloring. The amount of alkali metal, alkaline earth metal and compound used is M
When the content is 0.1 mol% or more, there may be a case where the heat stability and the hydrolysis resistance decrease, the generation of foreign matter and the increase in coloring become a problem in product processing. If M is less than 1 × 10 ⁻⁶ , the effect is not clear even if added.

In a preferred embodiment, the polyester polymerization catalyst of the present invention is further added with a cobalt compound as a cobalt atom in an amount of less than 10 ppm based on the polyester. It is more preferably less than 5 ppm, and further preferably 3 ppm or less.

It is known that the cobalt compound itself has a certain degree of polymerization activity, but when added to such an extent that a sufficient catalytic effect is exhibited as described above, the thermal stability decreases. The polyester obtained according to the present invention has good thermal stability, but the cobalt compound is added in such a small amount as described above in an amount such that the catalytic effect is not clear, so that the obtained polyester is colored. It can be erased more effectively. The purpose of the cobalt compound in the present invention is to eliminate coloration, and the timing of addition may be at any stage of the polymerization or after the end of the polymerization reaction.

The cobalt compound is not particularly limited, but specifically, for example, cobalt acetate, cobalt nitrate,
Cobalt chloride, cobalt acetylacetonate, cobalt naphthenate, and hydrates thereof are exemplified. Among them, cobalt acetate tetrahydrate is particularly preferred.

The production of the polyester according to the present invention can be carried out by a method including conventionally known steps except that the polyester polymerization catalyst of the present invention is used as a catalyst. For example, when producing PET, after esterification of terephthalic acid and ethylene glycol, a method of polycondensation, or after performing an ester exchange reaction between an alkyl ester of terephthalic acid such as dimethyl terephthalate and ethylene glycol, Any of the polycondensation methods can be used. Also, the polymerization apparatus is a batch type,
It may be a continuous type.

The catalyst of the present invention has catalytic activity not only in polymerization but also in esterification and transesterification. For example, polymerization by transesterification of an alkyl ester of a dicarboxylic acid such as dimethyl terephthalate with a glycol such as ethylene glycol is usually carried out in the presence of a transesterification catalyst such as a titanium compound or a zinc compound. Alternatively, or in combination with these catalysts, the catalyst of the present invention can be used. Further, the catalyst of the present invention has catalytic activity not only in melt polymerization but also in solid phase polymerization and solution polymerization, and it is possible to produce polyester by any method.

The polymerization catalyst of the present invention can be added to the reaction system at any stage of the polymerization reaction. For example, it can be added to the reaction system before the start of the esterification reaction or transesterification reaction and at any stage during the reaction, immediately before the start of the polycondensation reaction, or at any stage during the polycondensation reaction. In particular, it is preferable to add aluminum or its compound immediately before the start of the polycondensation reaction.

The method for adding the polycondensation catalyst of the present invention may be a powdery or neat addition, or a slurry or solution addition of a solvent such as ethylene glycol. Not limited. Further, a mixture of aluminum metal or a compound thereof and another component, preferably the phosphorus compound of the present invention, may be added in advance, or they may be added separately. In addition, the aluminum metal or its compound and another component, preferably a phosphorus compound, may be added to the polymerization system at the same addition time, or they may be added at different addition times. Further, the whole amount of the catalyst may be added at once, or may be added in plural times.

The polymerization catalyst of the present invention comprises an antimony compound,
Other polymerization catalysts such as titanium compounds, germanium compounds, and tin compounds are allowed to coexist within the range of the addition amount in which the addition of these components does not cause a problem in the properties of the polyester, processability, color tone, etc. as described above. The use is advantageous and preferable in improving productivity by shortening the polymerization time.

However, the antimony compound is used as an antimony atom with respect to a polyester obtained by polymerization.
Preferably, it is added in an amount of 50 ppm or less. More preferably, it is added in an amount of 30 ppm or less. If the added amount of antimony is more than 50 ppm, precipitation of metallic antimony occurs, which is not preferable because blackening and foreign matter are generated in the polyester.

The titanium compound is preferably added in a range of 10 ppm or less based on the polymer obtained by polymerization. More preferably 5ppm or less, more preferably 2ppm
It is to be added in the following amount. Add 10ppt titanium
If it is larger than m, the thermal stability of the obtained resin is significantly reduced.

The germanium compound is preferably added to the polyester obtained by polymerization in an amount of 20 ppm or less as a germanium atom. More preferably 10pp
m or less. If the amount of germanium added is more than 20 ppm, it is not preferable because it is disadvantageous in terms of cost.

When polymerizing a polyester using the polymerization catalyst of the present invention, one or more of an antimony compound, a titanium compound, a manium compound, and a tin compound can be used.

The antimony compound, titanium compound, germanium compound and tin compound used in the present invention are not particularly limited.

Specifically, as the antimony compound,
Examples include antimony trioxide, antimony pentoxide, antimony acetate, antimony glycooxide, and the like. Of these, antimony trioxide is preferable.

As the titanium compound, tetra-n-
Propyl titanate, tetraisopropyl titanate,
Tetra-n-butyl titanate, tetraisobutyl titanate, tetra-tert-butyl titanate, tetracyclohexyl titanate, tetraphenyl titanate, tetrabenzyl titanate, lithium titanate, potassium titanate, ammonium titanate, ammonium titanate, titanium oxide, titanium and Complex oxides with silicon, zirconium, alkali metals, alkaline earth metals, etc., orthoesters or condensed orthoesters of titanium, reaction products consisting of orthoesters or condensed orthoesters of titanium and hydroxycarboxylic acids, orthoesters of titanium or Reaction products comprising condensed orthoesters, hydroxycarboxylic acids and phosphorus compounds, titanium orthoesters or condensed orthoesters and polyvalent compounds having at least two hydroxyl groups And a reaction product comprising 2-hydroxycarboxylic acid and a base, among which titanium-silicon composite oxide, titanium-magnesium composite oxide, titanium orthoester or condensed orthoester and hydroxycarboxylic acid. Reaction products consisting of phosphorus compounds are preferred.

Examples of the germanium compound include germanium dioxide and germanium tetrachloride. Of these, germanium dioxide is preferable. Both germanium dioxide and crystalline one can be used.

Examples of the tin compound include dibutyltin oxide, methylphenyltin oxide, tetraethyltin, hexaethylditin oxide, triethyltin hydroxide, monobutylhydroxytin oxide, triisobutyltin acetate, diphenyltin dilaurate and monobutyltin trilaurate. Examples thereof include chloride, dibutyltin sulfide, dibutylhydroxytin oxide, methylstannoic acid, and ethylstannoic acid, and the use of monobutylhydroxytin oxide is particularly preferable.

The polyester referred to in the present invention is one or more selected from polycarboxylic acids containing dicarboxylic acids and their ester-forming derivatives and one or more selected from polyhydric alcohols containing glycol. Or those composed of hydroxycarboxylic acids and their ester-forming derivatives, or those composed of cyclic esters.

As the dicarboxylic acid, oxalic acid, malonic acid,
Succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, decanedicarboxylic acid, dodecanedicarboxylic acid, tetradecanedicarboxylic acid, hexadecanedicarboxylic acid, 1,3-cyclobutanedicarboxylic acid, 1,3-cyclocyclohexane Pentanedicarboxylic acid,
Saturated aliphatic dicarboxylic acids exemplified by 1,2-cyclohexanedicarboxylic acid, 1,3-cyclohexanedicarboxylic acid, 1,4-cyclohexanedicarboxylic acid, 2,5-norbornanedicarboxylic acid, dimer acid, and the like, and their ester-forming properties Derivatives, unsaturated aliphatic dicarboxylic acids exemplified by fumaric acid, maleic acid, itaconic acid and the like and ester-forming derivatives thereof, orthophthalic acid, isophthalic acid, terephthalic acid, 5- (alkali metal) sulfoisophthalic acid, diphenic acid 1,3 naphthalenedicarboxylic acid, 1,4 naphthalenedicarboxylic acid, 1,5 naphthalenedicarboxylic acid, 2,6 naphthalenedicarboxylic acid, 2,7 naphthalenedicarboxylic acid, 4,4′-biphenyldicarboxylic acid, 4,4'-biphenylsulfone dicarboxylic acid, 4,4'-biphe Aromatic dicarboxylic acids exemplified by enyl ether dicarboxylic acid, 1,2-bis (phenoxy) ethane-p, p'-dicarboxylic acid, pamoic acid, anthracene dicarboxylic acid and the like, and ester-forming derivatives thereof are exemplified.

Of these dicarboxylic acids, terephthalic acid and naphthalenedicarboxylic acid, particularly 2,6-naphthalenedicarboxylic acid, are preferred in view of the physical properties of the resulting polyester, and other dicarboxylic acids may be used if necessary.

Examples of polycarboxylic acids other than these dicarboxylic acids include ethanetricarboxylic acid, propanetricarboxylic acid, butanetetracarboxylic acid, pyromellitic acid, trimellitic acid, trimesic acid, 3,4,3 ′, 4′-biphenyltetracarboxylic acid. Examples include carboxylic acids and their ester-forming derivatives.

As the glycol, ethylene glycol,
1,2-propylene glycol, 1,3-propylene glycol, diethylene glycol, triethylene glycol, 1,2 butylene glycol, 1,3 butylene glycol, 2,3 butylene glycol, 1,4 butylene glycol, 1,5-pentanediol, neopentyl glycol, 1,6-hexanediol, 1,
2-cyclohexanediol, 1,3-cyclohexanediol, 1,4-cyclohexanediol, 1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol, 1,4-cyclohexanedimethanol, 1,
Aliphatic glycols exemplified by 4-cyclohexanediethanol, 1,10-decamethylene glycol, 1,12-dodecanediol, polyethylene glycol, polytrimethylene glycol, polytetramethylene glycol, etc., hydroquinone, 4,4'-dihydroxybisphenol 1,4-bis (β-hydroxyethoxy) benzene, 1,4-bis (β-hydroxyethoxyphenyl) sulfone, bis (p-hydroxyphenyl) ether, bis (p-hydroxyphenyl) sulfone, bis (p-hydroxy Phenyl) methane, 1,2-bis (p
-Hydroxyphenyl) ethane, bisphenol A, bisphenol C, 2,5 naphthalene diol, and aromatic glycols exemplified by ethylene glycol added to these glycols.

Of these glycols, ethylene glycol, 1,3-propylene glycol, 1,4-butylene glycol, and 1,4-cyclohexanedimethanol are preferred.

As the polyhydric alcohols other than these glycols, trimethylolmethane, trimethylolethane,
Trimethylolpropane, pentaerythritol, glycerol, hexanetriol and the like.

The hydroxycarboxylic acids include lactic acid, citric acid, malic acid, tartaric acid, hydroxyacetic acid, 3-hydroxybutyric acid, p-hydroxybenzoic acid, p- (2-hydroxyethoxy) benzoic acid, 4-hydroxycyclohexanecarboxylic acid, Or, an ester-forming derivative thereof and the like.

Examples of the cyclic ester include ε-caprolactone, β-propiolactone, β-methyl-β-propiolactone, δ-valerolactone, glycolide, lactide and the like.

The ester-forming derivatives of polycarboxylic acids or hydroxycarboxylic acids include these alkyl esters, acid chlorides, acid anhydrides and the like.

The polyester used in the present invention is preferably a polyester whose main acid component is terephthalic acid or its ester-forming derivative or naphthalenedicarboxylic acid or its ester-forming derivative, and whose main glycol component is an alkylene glycol.

The polyester in which the main acid component is terephthalic acid or its ester-forming derivative or naphthalenedicarboxylic acid or its ester-forming derivative refers to terephthalic acid or its ester-forming derivative and naphthalenedicarboxylic acid or It is preferable that the polyester is a polyester containing at least 70 mol% of the ester-forming derivative in total, more preferably a polyester containing at least 80 mol%, more preferably
It is a polyester containing 90 mol% or more.

The polyester in which the main glycol component is an alkylene glycol is preferably a polyester containing alkylene glycol in a total amount of 70 mol% or more based on all glycol components, and more preferably.
It is a polyester containing 80 mol% or more, and more preferably a polyester containing 90 mol% or more. The alkylene glycol mentioned here may contain a substituent or an alicyclic structure in the molecular chain.

The naphthalenedicarboxylic acid or ester-forming derivative thereof used in the present invention includes 1,3 naphthalenedicarboxylic acid, 1,4 naphthalenedicarboxylic acid, 1,5 naphthalenedicarboxylic acid, and 2,6 naphthalenedicarboxylic acid Acid, 2,7 naphthalene dicarboxylic acid,
Alternatively, these ester-forming derivatives are preferred.

The alkylene glycol used in the present invention includes ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,2-butylene glycol, 1,3-butylene glycol,
3-butylene glycol, 1,4-butylene glycol, 1,5-pentanediol, neopentyl glycol, 1,6-hexanediol, 1,2-cyclohexanediol, 1,3-cyclohexanediol, 1,4-cyclohexanediol, 1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol, 1.4
-Cyclohexanedimethanol, 1,4-cyclohexanediethanol, 1,10-decamethylene glycol,
1,12-dodecanediol and the like. Two or more of these may be used simultaneously.

The polyester of the present invention includes polyethylene terephthalate, polybutylene terephthalate, polypropylene terephthalate, poly (1,4-cyclohexane dimethylene terephthalate), polyethylene naphthalate, polybutylene naphthalate, polypropylene naphthalate, and copolymers thereof. Of these, polyethylene terephthalate and its copolymer are particularly preferred.

The polyester of the present invention can contain a known phosphorus compound as a copolymer component. As the phosphorus compound, a bifunctional phosphorus compound is preferable, for example, (2-carboxylethyl) methylphosphinic acid,
(2-carboxyethyl) phenylphosphinic acid, 9,
10-dihydro-10-oxa- (2,3-carboxypropyl) -10-phosphaphenanthrene-10-oxide and the like. By including these phosphorus compounds as copolymer components, it is possible to improve the flame retardancy and the like of the obtained polyester.

As the constituent components of the polyester of the present invention,
In a preferred embodiment, a polycarboxylic acid having a sulfonate alkali metal base is used as a copolymer component in order to improve dyeability when polyester is used as a fiber.

The metal sulfonate group-containing compound used as the copolymerizable monomer is not particularly limited, but may be 5-sodium sulfoisophthalic acid, 2-sodium sulfoterephthalic acid, 5-lithium sulfoisophthalic acid, or 2-lithium sulfoisophthalic acid. Examples thereof include terephthalic acid, 5-potassium sulfoisophthalic acid, 2-potassium sulfoterephthalic acid, and lower alkyl ester derivatives thereof. In the present invention, use of 5-sodium sulfoisophthalic acid or an ester-forming derivative thereof is particularly preferred.

The amount of the metal sulfonate group-containing compound to be copolymerized is 0.3 to 10.0 with respect to the acidic component constituting the polyester.
Mol% is preferred, and more preferably 0.80 to 5.0 mol%. If the copolymerization amount is too small, the dyeability of the basic dye is inferior. If the copolymerization amount is too large, not only the spinning properties are poor, but also the fiber does not have sufficient strength due to the thickening phenomenon. The metal sulfonate-containing compound was 2.0 mol%
By copolymerizing as described above, it is also possible to impart normal pressure dyeability to the obtained modified polyester fiber. It is possible to appropriately reduce the amount of the metal sulfonate group-containing compound by selecting an appropriate dye for facilitating dyeing. Examples of the easily dyeable monomer include, but are not particularly limited to, long-chain glycol compounds represented by polyethylene glycol and polytetramethylene glycol, and aliphatic dicarboxylic acids represented by adipic acid, sebacic acid, and azelaic acid.

After the polyester polymerization according to the method of the present invention, the thermal stability of the polyester can be further enhanced by removing the catalyst from the polyester or deactivating the catalyst by adding a phosphorus compound or the like. .

The polyester of the present invention may contain an organic, inorganic, or organometallic toner, a fluorescent whitening agent, and the like. Coloring such as yellowing can be suppressed to a more excellent level. In addition, any other polymer, antistatic agent, defoamer, dyeability improver, dye,
Pigments, matting agents, optical brighteners, stabilizers, antioxidants and other additives may be included. As the antioxidant, an antioxidant such as an aromatic amine type or a phenol type can be used, and as the stabilizer, a phosphoric acid type such as phosphoric acid or a phosphoric acid ester type, a sulfur type or an amine type stabilizer can be used. Can be used.

[0092]

EXAMPLES The present invention will be described below with reference to examples, but the present invention is not limited to these examples. The evaluation method used in each of the examples and comparative examples will be described below.

(1) Intrinsic viscosity (IV) Polyester is dissolved in a 6/4 mixed solvent (weight ratio) of phenol / 1,1,2,2-tetrachloroethane and measured at a temperature of 30 ° C. did.

(2) Acid value 0.1 g of polyester was dissolved by heating in 10 ml of benzyl alcohol, and the acid value was determined by titration using a solution of 0.1N NaOH in methanol / benzyl alcohol = 1/9.

(3) Differential Scanning Calorimetry (DSC) Measurement was performed using a DSC 2920 manufactured by TA Instruments. Put 10.0mg of polyester in an aluminum pan, 50 ℃
The temperature was raised to 280 ° C. at a heating rate of / min, and after reaching 280 ° C., the temperature was maintained for 1 minute, and immediately after that, quenched in liquid nitrogen. Thereafter, the temperature is increased from room temperature by 20 ° C./min.
℃, the crystallization temperature Tc1 and the melting point T
m was determined. After the temperature was maintained at 300 ° C. for 2 minutes, the temperature was lowered at a rate of 10 ° C./minute, and the crystallization temperature Tc2 at the time of temperature decrease was determined. Tc1, Tm, and Tc2 were the temperatures of the local maximums of the respective peaks.

(4) Hue At the time when a predetermined stirring torque was reached in the melt polymerization, nitrogen was introduced into the autoclave, the pressure was returned to normal pressure, and the polycondensation reaction was stopped. Thereafter, the polymer was discharged into cold water in the form of strands under slight pressure and rapidly cooled. After that, the polymer was held in cold water for about 20 seconds and then cut to obtain a cylindrical resin tip having a length of about 3 mm and a diameter of about 2 mm. The resin chip thus obtained was air-dried on a filter paper at room temperature for about 24 hours, and then used for color measurement. The color measurement was performed using a PET resin chip having an IV of about 0.65 dl / g obtained by melt polymerization using a color difference meter (MODEL TC-150 manufactured by Tokyo Denshoku Co., Ltd.).
0MC-88) was used to measure the hunter's L value, a value, and b value.

(5) Thermal stability parameter (TS) The melt-polymerized IV was about 0.65 dl / g (before the melt test;
[IV] 1 g of PET resin chip of _i ) is about 14 m in inner diameter
m, placed in a glass test tube, vacuum-dried at 130 ° C. for 12 hours, set in a vacuum line, and repeatedly vacuumed and filled with nitrogen five times or more, sealed with 100 mmHg of nitrogen, and sealed.
After being immersed in a salt bath at 300 ° C. and maintained in a molten state for 2 hours, the sample was taken out, freeze-crushed and vacuum-dried.
V (after the melting test; IV) _f2 ) was measured and determined by the following formula. The ceremony is already published (Kamiyama et al .: The Japan Rubber Association Journal No. 6
3, No. 8, p. 497, 1990). TS = 0.245 ｛[IV] _f2 ^-1.47 − [IV] _i
^-1.47 ｝

(6) Thermal Oxidation Stability Parameter (TOS) A melt-polymerized PET resin chip having an IV of about 0.65 dl / g was freeze-pulverized into a powder having a mesh size of 20 mesh or less, which was vacuum-dried at 130 ° C. for 12 hours. 300 mg is placed in a glass test tube having an inner diameter of about 8 mm and a length of about 140 mm.
After vacuum drying at 0 ° C. for 12 hours, a drying tube containing silica gel was placed on the upper portion of the test tube, and dried under air at 230 ° C.
IV after being immersed in a salt bath and heated for 15 minutes, was determined using the same formula as that for TS described above. Here, [IV] _i and [IV] _f1 indicate the IV (dl / g) before and after the heating test, respectively. For freezing and pulverization, use a freezer mill (Type 6750 manufactured by Spex, USA)
This was performed using After putting about 2 g of resin chip and dedicated impactor in the dedicated cell, set the cell in the device, fill the device with liquid nitrogen and hold for about 10 minutes, then
Milling was performed for 5 minutes with ATE10 (impacter moves around 20 times per second). TOS = 0.245 ｛[IV] _f1 ^-1.47 − [IV] _i
^-1.47 ｝

(7) Hydrolysis resistance parameter (HS) The intrinsic viscosity obtained by melt polymerization is about 0.65 dl / g.
(Before the test; [IV] _i ) The PET resin chip was frozen and pulverized in the same manner as in the above 6) to obtain a powder having a size of 20 mesh or less, which was vacuum-dried at 130 ° C. for 12 hours. The hydrolysis test was performed using a mini color device (TypeMC12.EL manufactured by Texam Giken Co., Ltd.).
B). 1 g of the above-mentioned powder was put into a special stainless beaker together with 100 ml of pure water, a special stirring blade was further put therein, and a closed system was set.
The mixture was stirred for 6 hours while heating and pressurizing to 30 ° C. The PET after the test was collected by filtration with a glass filter, dried under vacuum, and then measured for IV ([IV] _f2 ), and the hydrolysis resistance parameter (HS) was determined by the following equation. HS = 0.245 ｛[IV] _f2 ^-1.47- [IV] _i
^-1.47 ｝

(8) Film Formation In each of the examples and comparative examples, the PET resin chips before the melting test were vacuum-dried at 135 ° C. for 6 hours. Then, it was supplied to an extruder, melt-extruded into a sheet at 280 ° C., and quenched and solidified on a metal roll maintained at a surface temperature of 20 ° C. to obtain a cast film having a thickness of 1400 μm.

Next, this cast film was heated to 100 ° C. by a heated roll group and an infrared heater, and then stretched 3.5 times in the longitudinal direction by a roll group having a peripheral speed difference to obtain a uniaxially oriented PET film. Was. Subsequently, the film was stretched 4.0 times in the width direction at 120 ° C. with a tenter, and the film was heated with an infrared heater at 260 ° C. for 0.5 second with the film width fixed, and further 3% at 200 ° C. for 23 seconds. To obtain a biaxially oriented PET film having a thickness of 100 μm.

(9) Preparation of Recovered Pellets The PET film obtained by the above method was cut into strips, vacuum-dried, put into an extruder, and extruded at a temperature of 280 ° C. from a nozzle having a diameter of 5 mm. Thereafter, the pellets were obtained by cooling and cutting with water.

(10) Film Formation with Collected Pellets The PET resin chip before the melting test and the above-mentioned collected pellets were mixed at a weight ratio of 50:50, and vacuum-dried at 135 ° C. for 6 hours. Then, it was supplied to an extruder, melt-extruded into a sheet at 280 ° C., and quenched and solidified on a metal roll maintained at a surface temperature of 20 ° C. to obtain a cast film having a thickness of 1400 μm.

Next, the cast film was heated to 100 ° C. by a heated roll group and an infrared heater, and then stretched 3.5 times in the longitudinal direction by a roll group having a peripheral speed difference to obtain a uniaxially oriented PET film. Was. Then, in the tenter,
Stretched 4.0 times in the width direction at 120 ° C, thickness 100 μm
Was obtained.

(11) Thermal Stability of Film The appearance of the obtained films was visually observed and ranked. ◎: no coloring ○: slightly colored △: colored ×: markedly colored

(12) Heat aging resistance of film The film obtained by the method of the above (8) was prepared by subjecting the film to a length of 10 cm and a width of 10 cm.
A 5 cm test piece was cut out, and the test piece was treated at 200 ° C. for 100 hours using a gear hot air drier, and the film was evaluated for ease of cutting when pulled in the length direction. ：: Strength is sufficiently high and cutting is not easy. △: Strength is slightly reduced and cutting is easy. ×: Strength is reduced and cutting is easy.

(13) Water resistance of the film The film obtained by the method of the above (8) was used to prepare a film having a length of 8 cm and a width of 4 cm.
The test pieces were cut into cm test pieces, and the test pieces were boiled in boiling water for 5 days. The films after boiling were ranked according to their ease of cutting when pulled in the length direction. ：: Strength is sufficiently high and cutting is not easy. △: Strength is slightly reduced and cutting is easy. ×: Strength is reduced and cutting is easy.

(14) ¹ H-NMR Measurement The compound was dissolved in CDCl ₃ or DMSO-d6, and
Measured using an GEMINI-200.

(15) Melting point measurement The compound was placed on a cover glass, and the sample was placed on a Yanaco MICRO MELTING.
Measurement was performed at a heating rate of 1 ° C./min using POINT APPARATUS.

(16) Elemental Analysis Phosphorus was analyzed by molybdenum blue colorimetry after wet decomposition of a PET resin chip. Other metals were subjected to high-frequency plasma emission analysis and atomic absorption analysis after incineration / acid dissolution.

Example 1 Synthesis Example of Phosphorus Compound Synthesis of sodium salt of phosphorus compound (phosphorus compound A) represented by the following formula (4)

[0112]

Embedded image

Synthesis of O-Ethyl (1-naphtyl) methylphosphonate Under a nitrogen atmosphere, 8.31 g (50 mmol) of triethyl phosphite and 1-
A mixture of 8.83 g (50 mmol) of chloromethylnaphthalene at 200 ° C
The mixture was heated at (external temperature) for about 30 minutes until the generation of gas (C ₂ H ₅ Cl) was completed. After cooling to room temperature, NMPA, a colorless oily liquid,
10.38 g (crude yield 75%) was obtained. _{^{1 H-NMRCDCl 3, δ)}} : 1.151 (6H, t), 3.641 (2H, d), 3.948
(4H, m), 7.381-7.579 (4H, m), 7.749-7.867 (2H, m),
8.088-8.133 (1H, d) Synthesis of Sodium [O-ethyl (1-naphtyl) methylphosphonate] (phosphorus compound A) The above-mentioned O was added to a mixed solution of 6.5 g (84 mmol) of a 50% aqueous sodium hydroxide solution and 6.1 ml of methanol. -Ethyl (1-naphtyl) methy
A solution of 5 g (18 mmol) of lphosphonate in 6.1 ml of methanol was added, and the mixture was heated and refluxed for 24 hours under a nitrogen atmosphere. After the reaction, 6.59 g (63 mmol) of concentrated hydrochloric acid was added while cooling the reaction mixture, the precipitate was collected by filtration, washed with isopropanol, and the filtrate was distilled off under reduced pressure. The obtained residue was dissolved in hot isopropanol, the insoluble matter was collected by filtration, and isopropanol was distilled off under reduced pressure. The residue was washed with hot n-heptane, recrystallized from isopropanol, dried, and dried with Sodium [O-ethyl (1-naphtyl) meth
ylphosphonate] (3.8 g, 78%). Shape: needle crystal Melting point: 277-281 ° C (decomposition) ¹ H-NMR (DMSO, δ): 0.961 (3H, t, J = 7 Hz), 3.223 (2H, d),
3.589 (2H, m), 7.365-7.468 (4H, m, J = 7Hz), 7.651-8.
314 (3H, m)

(Polyester polymerization example) A mixture of bis (2-hydroxyethyl) terephthalate and an oligomer prepared from a high-purity terephthalic acid and ethylene glycol by a conventional method was used as a catalyst at 2.5 g / l of aluminum acetylacetonate in ethylene glycol. The solution was added to the acid component in the polyester in an amount of 0.01 as aluminum atoms.
4 mol%, and then the above-mentioned phosphorus compound A was added at 0.01 mol% to the acid component in the polyester.
Stirred for 0 minutes. Then, over 50 minutes, the temperature of the reaction system was gradually lowered while the temperature was raised to 275 ° C. to 0.1 mmHg, and the polycondensation reaction was further performed at the same temperature and pressure for 3 hours. IV of the obtained polymer was 0.54.

Comparative Example 1 A polyester was polymerized in exactly the same manner as in Example 1 except that the above-mentioned phosphorus compound A was not used. IV of the obtained polymer was 0.33.

As is clear from the above Examples and Comparative Examples, when the aluminum compound alone was used as a catalyst, the polymerization activity was inferior. However, when the phosphorus compound of the present invention was used in combination, the polymerization activity was greatly improved. You can see that

[0117]

According to the present invention, there is provided a novel polycondensation catalyst other than an antimony compound, a polyester produced using the same, and a method for producing a polyester. The polyester of the present invention, for example, clothing fibers,
Interior and bedding fibers represented by curtains, carpets, futon, etc., fibers for industrial materials represented by tire cords, ropes, etc., various fabrics, various knits, short fiber nonwoven fabrics, fibers such as long fiber nonwoven fabrics, and packaging Films, films for industrial use, films for optics, films for magnetic tapes, films for photographs, films for can lamination, films for contensors, heat shrink films, gas barrier films, white films, films such as easy-cut films, non-heat-resistant stretched bottles, Hollow molded products such as heat-resistant stretched bottles, direct blow bottles, gas barrier bottles, pressure-resistant bottles, heat-resistant pressure bottles, sheets such as A-PET and C-PET, engineering plastics represented by glass fiber reinforced polyester and elastomers, etc. For moldings and paints and adhesives It is possible.

Continued on the front page F-term (reference) 4J029 BA03 CB06A HA01 HB01 HB03A JA061 JA091 JA121 JA161 JA201 JA261 JA281 JB131 JB151 JB171 JB271 JC571 JF021 JF031 JF041 JF121 JF131 JF151 JF161 JF181 JF551 JF561 KE02

Claims (12)

[Claims] 1. A polyester polymerization catalyst comprising at least one selected from aluminum and its compounds as a metal-containing component, and at least one metal salt compound of phosphorus. 2. The polyester polymerization catalyst according to claim 1, wherein the metal salt compound of phosphorus is one or more compounds selected from the group consisting of metal salts of phosphonic acid compounds. 3. The polyester polymerization catalyst according to claim 1, wherein the phosphorus metal salt compound is a compound having an aromatic ring structure. 4. The method according to claim 1, wherein the metal portion of the metal salt compound of phosphorus is Li,
Na, K, Be, Mg, Sr, Ba, Mn, Ni, C
4. A material selected from u and Zn.
The polyester polymerization catalyst according to any one of the above. 5. A phosphorous metal salt compound represented by the following general formula (1):
The polyester polymerization catalyst according to claim 1, which is at least one selected from compounds represented by the following formula: Embedded image (In the formula (1), R ¹ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or a halogen group, or a hydrocarbon group having 1 to 50 carbon atoms including an alkoxyl group or an amino group.
R ² represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydrocarbon group having 1 to 50 carbon atoms including a hydroxyl group or an alkoxyl group. R ³ is hydrogen, a hydrocarbon group having 1 to 50 carbon atoms,
Represents a hydrocarbon group having 1 to 50 carbon atoms including a hydroxyl group, an alkoxyl group or a carbonyl. l is an integer of 1 or more, m
Represents 0 or an integer of 1 or more, and l + m is 4 or less. M
Represents a (l + m) -valent metal cation. n represents an integer of 1 or more. The hydrocarbon group may have an alicyclic structure, a branched structure, or an aromatic ring structure. ) 6. The polyester polymerization catalyst according to claim 5, wherein the phosphorus compound represented by the general formula (1) is at least one selected from compounds represented by the following general formula (2). Embedded image (In the formula (2), R ¹ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or a halogen group, or a hydrocarbon group having 1 to 50 carbon atoms including an alkoxyl group or an amino group.
R ³ is hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group or a carbon atom having 1 to 5 carbon atoms including carbonyl.
Represents 50 hydrocarbon groups. l is an integer of 1 or more, m is 0 or an integer of 1 or more, and l + m is 4 or less. M is (l + m)
Represents a valent metal cation. The hydrocarbon group may have an alicyclic structure, a branched structure, or an aromatic ring structure. ) 7. M in the general formula (2) is Li, Na,
K, Be, Mg, Sr, Ba, Mn, Ni, Cu, Zn
The polyester polymerization catalyst according to claim 6, which is selected from the group consisting of: 8. A polyester produced using the polyester polymerization catalyst according to claim 1. 9. A method for producing a polyester, comprising using the polyester polymerization catalyst according to any one of claims 1 to 7. 10. A polyester polymerization catalyst, comprising at least one selected from the phosphorus compounds represented by the general formula (1). 11. A polyester comprising at least one selected from the phosphorus compounds represented by the general formula (1). 12. M in the general formula (1) is Li, Na,
K, Be, Mg, Sr, Ba, Mn, Ni, Cu, Zn
The polyester according to claim 11, which is selected from the group consisting of: