JP2005320302A - Method for producing dicarboxylic acid diester - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a dicarboxylic acid diester having a good hue from a dicarboxylic acid or a dicarboxylic acid anhydride and a low-quality raw material alcohol. <P>SOLUTION: The method for producing the dicarboxylic acid diester comprises carrying out an esterification reaction of the dicarboxylic acid or its anhydride with the alcohol in the presence of an esterification catalyst. The method for producing the dicarboxylic acid diester is characterized as using the alcohol obtained by carrying out a flash treatment of the raw material alcohol. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a method for producing a dicarboxylic acid diester, and more particularly to a method for producing a dicarboxylic acid diester having a good hue from dicarboxylic acid or dicarboxylic acid anhydride and a low-quality raw material alcohol.

  A linear or branched saturated alcohol having about 4 to 12 carbon atoms is used as a raw material alcohol for dicarboxylic acid diesters that are widely used as plasticizers for vinyl chloride resins. It contains trace amounts of impurities such as unsaturated hydrocarbons, ethers, carbonyl compounds such as aldehydes and ketones, and peroxides.

  The impurities in these raw material alcohols are coloring cause components or coloring cause components (hereinafter abbreviated as “coloration cause components”) that deteriorate the hue of the diester, and serve as an index of the content of these color cause components. Is a carbonyl value (hereinafter abbreviated as “COV”), a peroxide value (hereinafter abbreviated as “POV”), sulfuric acid coloration, and the like. Abbreviated as “low-quality alcohol”) the hue of the diester gets worse.

  The content of the above color-causing component is usually very small immediately after distillation because it is purified by distillation in the final step of alcohol production, but increases due to heat and / or oxidative degradation due to long-term storage and transportation. To do. For this reason, COV, POV, hue (Hazen), etc. of alcohol showed a high value compared with immediately after distillation, and there was a problem that a product with good hue could not be obtained from such low quality raw material alcohol.

  As a method for suppressing the progress of heat and / or oxidative deterioration over time during such long-term storage and transportation, methods such as addition of an antioxidant and replacement with an inert gas are generally performed. ing. However, the method by adding an antioxidant has problems in terms of the final quality and cost of the diester, and any method has a good hue when used as a raw alcohol because the quality deteriorates when stored for a long time. There is a problem that a diester cannot be obtained.

  Further, since the recovered alcohol generated during the production of the diester is also subjected to heat and / or oxidative degradation in the production process, there is a problem that a product having a good hue cannot be obtained when used as a raw material alcohol.

  As methods for regenerating these low-quality raw material alcohols, methods such as distillation purification (see Patent Documents 1 and 2), methods using a treating agent (see Patent Documents 3 and 4), hydrogen reduction methods (see Patent Document 5), and the like Although a method has been proposed, it has many problems in terms of manufacturing and economy such as a complicated manufacturing process, and the current situation is that the above problem has not yet been sufficiently solved.

JP-A-6-122638 JP-A-7-278032 Japanese Patent Laid-Open No. 11-43452 JP 2003-12582 A Japanese Patent Publication No. 6-69974

  An object of the present invention is to provide a method for producing a dicarboxylic acid diester having a good hue from dicarboxylic acid or dicarboxylic acid anhydride and a low-quality raw material alcohol.

  As a result of intensive studies to solve the above problems, the present inventors have been able to significantly reduce the content of impurities that cause coloration by flashing low-quality raw material alcohol, and from the obtained alcohol It was found that a dicarboxylic acid diester having a good hue was obtained, and the present invention was completed based on such knowledge.

  That is, the present invention provides the following method for producing a dicarboxylic acid diester.

  Item 1 A method for producing a dicarboxylic acid diester by subjecting a dicarboxylic acid or an anhydride thereof and an alcohol to an esterification reaction in the presence of an esterification catalyst, wherein the alcohol obtained by flashing a raw material alcohol is used. A method for producing a dicarboxylic acid diester.

  Item 2 The method for producing a dicarboxylic acid diester according to Item 1, wherein the raw material alcohol has a carbonyl value of 0.1 to 1.0 mgKOH / g and a peroxide value of 0.5 to 10.0 meq / kg.

  Item 3 The raw material alcohol has a carbonyl value of 0.1 to 1.0 mg KOH / g, a peroxide value of 0.5 to 10.0 meq / kg, and a sulfuric acid coloration of Hazen 30 to 250. The manufacturing method of dicarboxylic acid diester as described in any one of.

  Item 4 The method according to any one of Items 1 to 3, wherein the raw material alcohol contains a recovered alcohol generated during the production of the dicarboxylic acid diester.

  Item 5 The method according to any one of Items 1 to 4, wherein the raw material alcohol is flushed immediately before the esterification reaction.

Item 6 The production according to any one of Items 1 to 5, wherein the raw material alcohol heated to a temperature of 80 to 165 ° C. is flashed at a can internal pressure of 4.0 × 10 ^{3 to} 13.3 × 10 ³ Pa. Method.

  Item 7. The method according to any one of Items 1 to 6, wherein the raw alcohol is flash-treated so that the evaporation amount in the flash treatment step is 0.5 to 5% by weight with respect to the raw alcohol.

  Item 8 The dicarboxylic acid diester is di-2-ethylhexyl phthalate, diisononyl phthalate, diisodecyl phthalate, isobutyl 2-ethylhexyl phthalate, isobutyl isononyl phthalate, di-2-ethylhexyl tetrahydrophthalate, diisononyl tetrahydrophthalate, tetrahydrophthalate Diisodecyl acid, isobutyl 2-ethylhexyl tetrahydrophthalate, isobutyl isononyl tetrahydrophthalate, di-2-ethylhexyl hexahydrophthalate, diisononyl hexahydrophthalate, diisodecyl hexahydrophthalate, isobutyl 2-ethylhexyl hexahydrophthalate, or hexa Item 8. The method for producing a dicarboxylic acid diester according to any one of Items 1 to 7, which is isobutyl isononyl hydrophthalate.

  Item 9 A plasticizer for a vinyl chloride resin, comprising a dicarboxylic acid diester obtained by the production method according to Item 8.

  According to the method of the present invention, an alcohol in which the content of impurities that cause coloration is greatly reduced can be efficiently obtained by a simple method of introducing a low quality raw material alcohol into a flash can kept under reduced pressure and flushing it. From this alcohol, a dicarboxylic acid diester having a good hue can be produced. Further, complicated processing is not necessary.

Hereinafter, the present invention will be described in detail.
The raw material alcohol used in the present invention is exemplified by heat and / or oxidatively deteriorated low-quality raw material alcohol that does not yield a dicarboxylic acid diester excellent in hue even when used as an alcohol raw material.

  As such raw material alcohol, a low quality alcohol having a carbonyl value of about 0.1 to 1.0 mg KOH / g and a peroxide value of about 0.5 to 10.0 meq / kg can be used. In the range, the effects of the present invention can be sufficiently exhibited.

  Furthermore, if the sulfuric acid coloration of the raw material alcohol is too bad, the color-causing component cannot be sufficiently removed even after flash treatment, and a dicarboxylic acid diester having an excellent hue may not be obtained. Is about 0.1 to 1.0 mgKOH / g, a peroxide value is about 0.5 to 10.0 meq / kg, and low-quality alcohol having a sulfuric acid coloration of about Hazen 30 to 250 can be used. Within these ranges, the effects of the present invention can be sufficiently exerted.

  Specific examples of such raw material alcohols include alcohol deteriorated by long-term storage and transportation, recovered alcohol generated during the production of dicarboxylic acid diesters, etc., and used alone or as a mixture of two or more of them. You can also. These raw material alcohols are preferably flashed immediately before the esterification reaction in view of the effect of improving the hue.

  In the flash evaporation of the color-causing component in the raw alcohol, the raw alcohol is preferably heated in advance in order to increase the evaporation efficiency of the color-causing component. The heating temperature of the raw material alcohol may be any temperature that can efficiently remove the color-causing component, and can usually be selected from the range of about 80 to 165 ° C., preferably about 100 to 140 ° C., more preferably about 120 to 135 ° C. It is. If the heating temperature is too low, removal of the color-causing component by flash evaporation is not sufficient, and it becomes difficult to obtain the effect of improving the hue of the dicarboxylic acid diester, and if it is too high, the raw alcohol is likely to be thermally deteriorated. Moreover, the raw material alcohol in the pipe immediately before the introduction of the flash can is heated as necessary so that the heating temperature can be maintained.

  The apparatus for heating the raw alcohol is not particularly limited, and various heating means can be used. However, as an apparatus for heating continuously and efficiently, a tubular heater that can be heated by steam, a heating medium, or the like. Examples thereof include a coil heater and a double tube heater. The residence time (heating time) in the heater is preferably about 1 to 10 minutes within the above heating temperature. If it is less than 1 minute, a heating device having a large heat conduction area is required, and if it exceeds 10 minutes, thermal degradation of the raw material alcohol tends to occur. In order to avoid such thermal deterioration in the heater, the raw material alcohol may be heated in a state maintained at a pressure lower than atmospheric pressure.

In the flash treatment step, the heated raw material alcohol is introduced into a container or an evaporator maintained at a pressure lower than atmospheric pressure, and the color-causing component is flash evaporated. In order to increase the separation efficiency of the color-causing component, it is preferable to use a vacuum can or a flash can such as a vacuum container or an evaporator, in which flash evaporation increases the separation efficiency of the color-causing component instantaneously. The internal pressure of the flash can can be appropriately selected depending on the heating temperature and type of the raw alcohol, and is 4.0 × 10 ^{3 to} 13.3 × 10 ³ Pa, preferably 6.6 × 10 ^{3 to} 10.7 × 10. It is about ³ Pa. When the pressure is less than 4.0 × 10 ³ Pa, the alcohol evaporation tends to increase. When the pressure exceeds 13.3 × 10 ³ Pa, the color-causing component is not sufficiently removed and the dicarboxylic acid diester It becomes difficult to obtain the effect of improving the hue.

  At this time, the evaporation amount of impurities in the flash treatment step is not particularly limited as long as the effect of improving the hue of the dicarboxylic acid diester is obtained, but as a total weight of the color-causing component and the alcohol, It is preferably about 0.5 to 5% by weight. If the evaporation amount is less than 0.5% by weight, removal of the color-causing component is not sufficient, and it is difficult to obtain the effect of improving the hue of the dicarboxylic acid diester. In addition, the burden on the manufacturing cost is large and not economical.

  In general, the raw alcohol is preferably introduced into the flash can continuously or intermittently by a method such as jetting or spraying. The introduction rate of the raw alcohol can be appropriately selected according to the temperature and pressure, and for example, about 1000 to 5000 g / hr, preferably about 2000 to 3000 g / hr is recommended per 1 L of the volume of the flash can.

  As the flash can used in the above flash processing step, a conventional evaporator such as a long tube type or a forced circulation type can be used, and if necessary, a jacket capable of indirect heating by heating, a heating medium or steam is provided. You may use what is.

  An example of a schematic diagram of a flash processing step and apparatus used in the manufacturing method of the present invention is shown in FIG. This apparatus includes a heating unit 1 for heating the raw alcohol, a unit 9 for separating the coloring cause component from the heated raw alcohol, collecting the coloring cause component, and a recovery unit 5 for recovering the separated alcohol. It has.

  The heating unit 1 includes a coil-type heating tube 4 disposed in the heating chamber 3. In this example, raw alcohol is quantitatively supplied to the heating tube 4 by the pump 2. The heated raw material alcohol is supplied to the reduced-pressure raw material alcohol recovery unit 5 to separate the color-causing component and to recover the alcohol. The raw alcohol recovery unit 5 includes a decompression chamber 6 to which the heating pipe is connected, and a pan-type dispersion plate 7 in the chamber. Further, an alcohol recovery storage tank 8 for recovering alcohol is connected to the lower part of the decompression chamber 6. Furthermore, a supply line leading to the esterification reaction apparatus is connected to the alcohol recovery storage tank 8.

  The coloring cause component separated in the decompression chamber 6 is a coloring cause component collection unit 9 including a condenser 10 for condensing the component and a coloring component collection storage tank 11 for collecting the condensed component. It is collected by.

  The decompression chamber 6 and the vacuum pump 12 are connected via the capacitor 10.

  The alcohol obtained by the flash treatment in this way is preferably used immediately for the esterification reaction. Moreover, what was stored for a long time in inert gas atmosphere, such as nitrogen, can also be used in the range which does not impair the effect of this invention.

  The production method of the dicarboxylic acid diester according to the present invention is not particularly limited, but the dicarboxylic acid or dicarboxylic acid anhydride of the acid component and the alcohol component obtained by the above flash treatment, preferably an inert gas such as nitrogen A conventionally known production method in which esterification is carried out under heating and stirring in the presence of an esterification catalyst in the presence of an atmosphere can be used. The esterification reaction according to the present invention can be carried out under atmospheric pressure, reduced pressure or increased pressure.

  Examples of the acid component used in the present invention include aliphatic dicarboxylic acids having 4 to 18 carbon atoms, preferably 6 to 12 carbon atoms, and aromatic dicarboxylic acids having 8 to 18 carbon atoms, preferably 8 to 12 carbon atoms. .

  Specific examples of the aliphatic dicarboxylic acid and the aliphatic dicarboxylic acid anhydride include succinic acid, succinic anhydride, glutaric acid, glutaric anhydride, adipic acid, adipic anhydride, pimelic acid, pimelic anhydride, azelaic acid, Sebacic acid, decane-1,10-dicarboxylic acid, octadecane-1,18-dicarboxylic acid, and tetrahydrophthalic acid, tetrahydrophthalic anhydride, hexahydrophthalic acid, hexahydrophthalic anhydride, methyltetrahydrophthalic acid, methyl Diels-Alder adducts such as tetrahydrophthalic anhydride, methylhexahydrophthalic acid, methylhexahydrophthalic anhydride, nadic acid, nadic acid anhydride, methylnadic acid, methylnadic acid anhydride, and hydrogenated products thereof Among these, in particular, tetrahydrophthalic acid Tetrahydrophthalic acid anhydride, hexahydrophthalic acid, hexahydrophthalic anhydride, nadic, nadic anhydride, methyl nadic acid, Diels-Alder adducts and hydrogenated products thereof such as methylnadic anhydride are preferred.

  Specific examples of the aromatic dicarboxylic acid and the aromatic dicarboxylic acid anhydride include phthalic acid, phthalic anhydride, isophthalic acid, terephthalic acid, naphthalene-1,5-dicarboxylic acid, and naphthalene-2,8-dicarboxylic acid. Of these, phthalic acid, phthalic anhydride, isophthalic acid, and terephthalic acid are particularly preferable.

  These dicarboxylic acids and dicarboxylic anhydrides can be used alone or in admixture of two or more.

  Examples of the alcohol component used in the present invention include aliphatic linear or branched alcohols having 4 to 20 carbon atoms, preferably 6 to 18 carbon atoms, and more preferably 8 to 13 carbon atoms.

  Specific examples of the aliphatic linear or branched alcohol include n-butanol, isobutanol, sec-butanol, n-pentanol, n-hexanol, n-heptanol, n-octanol, and 2-ethylhexanol. , Isooctanol, n-nonanol, isononanol, 3,5,5-trimethylhexanol, n-decanol, isodecanol, n-undecanol, n-dodecanol, n-tridecanol, isotridecanol, tetradecanol, octadecanol, etc. Of these, n-octanol, 2-ethylhexanol, isononanol, 3,5,5-trimethylhexanol, and isodecanol are particularly preferable. These alcohols can be used alone or in admixture of two or more.

  When performing esterification reaction, the usage-amount of an alcohol component is 2.0-3.0 mol with respect to 1 mol of acid components, for example, Preferably 2.1-2.5 mol is used.

  As the esterification catalyst, Lewis acids, alkali metals, sulfonic acids and the like are used. Specifically, examples of the Lewis acid include aluminum derivatives, tin derivatives and titanium derivatives. Examples of the alkali metals include sodium alkoxides. Potassium alkoxides and the like, and examples of the sulfonic acids include p-toluenesulfonic acid, methanesulfonic acid, sulfuric acid, etc. Among them, Lewis acids are particularly preferable in that coloring and side reactions can be suppressed. Specific examples of such Lewis acids include titanium compounds such as tetramethyl titanate, tetraethyl titanate, tetra-n-propyl titanate, tetraisopropyl titanate, tetra-n-butyl titanate, dibutyltin dilaurate, dibutyltin oxide, Examples thereof include tin compounds such as dibutyltin diacetate, tin octylate and tin oxide. The amount used is, for example, about 0.05 to 1.0% by weight based on the total weight of the acid component and the alcohol component.

  The esterification reaction is preferably carried out at a reaction temperature of usually 100 to 250 ° C., preferably 130 to 230 ° C. in the presence of an inert gas. The reaction time is usually 3 to 30 hours. If necessary, the water produced may be distilled off azeotropically outside the system using a water-insoluble solvent such as benzene, toluene, xylene, cyclohexane or the like.

  The esterification reaction is carried out by reacting an alcohol component 2.1 to 2.5 mol with 1 mol of an acid component (particularly dicarboxylic acid anhydride) to prepare a monoester, and then adding the above-mentioned catalyst. It can also be carried out at a temperature of This monoesterification reaction is preferably performed, for example, in the presence of an inert gas at a reaction temperature of 120 to 135 ° C.

  After completion of the ester reaction, excess unreacted alcohol is recovered under reduced pressure or normal pressure as necessary. After cooling, the catalyst is decomposed, neutralized and washed with water or an aqueous alkali solution. Thereafter, if necessary, excess unreacted alcohol is distilled off under reduced pressure or atmospheric pressure, and then the alcohol is completely removed by steam stripping, followed by dehydration. Furthermore, purification with an adsorbent such as activated carbon, activated clay, activated alumina, and filtration using a filter aid can yield the desired dicarboxylic acid diester. The recovered alcohol can be effectively used as an alcohol component by flashing again.

  In addition, as a manufacturing method of the dicarboxylic acid diester which concerns on this invention, any reaction system of a batch type or a continuous type is employable.

  Examples of the aliphatic dicarboxylic acid diester to which the method of the present invention is suitably used include di-n-butyl adipate, n-butyl 2-ethylhexyl adipate, di-2-ethylhexyl adipate, n-butyl n-octyl adipate, Di-n-octyl adipate, n-butyl n-nonyl adipate, di-n-nonyl adipate, n-butylisononyl adipate, diisononyl adipate, n-butyl 3,5,5-trimethylhexyl adipate, adipine Di-3,5,5-trimethylhexyl acid, n-butyl n-decyl adipate, di n-decyl adipate, n-butylisodecyl adipate, diisodecyl adipate, n-butylundecyl adipate, diundecyl adipate , N-butyldodecyl adipate, didodecyl adipate, n adipate Butyltridecyl, ditridecyl adipate, n-butyltetradecyl adipate, ditetradecyl adipate, n-butyloctadecyl adipate, dioctadecyl adipate, diisobutyl adipate, isobutyl 2-ethylhexyl adipate, isobutyl n-octyl adipate, Isobutyl n-nonyl adipate, isobutyl isononyl adipate, isobutyl 3,5,5-trimethylhexyl adipate, isobutyl n-decyl adipate, isobutyl isodecyl adipate, isobutyl undecyl adipate, isobutyl dodecyl adipate, adipine Isobutyltridecyl acid, isobutyltetradecyl adipate, isobutyloctadecyl adipate, n-octyl n-nonyl adipate, n-octyl isonoxy adipate N-octyl 3,5,5-trimethylhexyl adipate, n-octyl n-decyl adipate, n-octylisodecyl adipate, n-octylundecyl adipate, n-octyldodecyl adipate, adipic acid n-octyltridecyl, n-octyltetradecyl adipate, n-octyloctadecyl adipate, n-nonylisononyl adipate, n-nonyl 3,5,5-trimethylhexyl adipate, n-nonyl n-decyl adipate, N-nonylisodecyl adipate, n-nonylundecyl adipate, n-nonyldodecyl adipate, n-nonyltridecyl adipate, n-nonyltetradecyl adipate, n-nonyloctadecyl adipate, n-nonylisononyl adipate, n-adipate Nonyl 3,5 , 5-trimethylhexyl, n-nonyl n-decyl adipate, n-nonyl isodecyl adipate, n-nonyl undecyl adipate, n-nonyl dodecyl adipate, n-nonyl tridecyl adipate, n-nonyl tetradecyl adipate, adipic acid n-nonyloctadecyl, isononyl adipate 3,5,5-trimethylhexyl, isononyl n-decyl adipate, isononyl isodecyl adipate, isononyl undecyl adipate, isononyl dodecyl adipate, isononyl tridecyl adipate , Isononyl tetradecyl adipate, isononyl octadecyl adipate, 3,5,5-trimethylhexyl n-decyl adipate, 3,5,5-trimethylhexylisodecyl adipate, 3,5,5-trimethyl adipate Xylundecyl, 3,5,5-trimethylhexyldecyl adipate, 3,5,5-trimethylhexyltridecyl adipate, 3,5,5-trimethylhexyltetradecyl adipate, 3,5,5-trimethylhexyl adipate Octadecyl, n-decylisodecyl adipate, n-decylundecyl adipate, n-decyldodecyl adipate, n-decyltridecyl adipate, n-decyltetradecyl adipate, n-decyloctadecyl adipate, isodecylundecyl adipate, adipine Isodecyl dodecyl adipate, Isodecyl tridecyl adipate, Isodecyl tetradecyl adipate, Isodecyl octadecyl adipate, Undecyl dodecyl adipate, Undecyl tridecyl adipate, Undecyl adipate Linear aliphatic dicarboxylics such as tetradecyl, undecyl octadecyl adipate, dodecyl tridecyl adipate, dodecyl tetradecyl adipate, dodecyl octadecyl adipate, tridecyl tetradecyl adipate, tridecyl octadecyl adipate, tetradecyl octadecyl adipate, etc. An acid diester is mentioned.

Di-n-butyl tetrahydrophthalate, n-butyl tetrahydrophthalate, 2-ethylhexyl tetrahydrophthalate, di-2-ethylhexyl tetrahydrophthalate, n-butyl tetrahydrophthalate, di-n-octyl tetrahydrophthalate, n-butyl tetrahydrophthalate n-nonyl, di-n-nonyl tetrahydrophthalate, n-butylisononyl tetrahydrophthalate, diisononyl tetrahydrophthalate, n-butyl tetrahydrophthalate 3,5,5-trimethylhexyl, dihydrotetrahydrophthalate 3,5,5 -Trimethylhexyl, n-butyl n-butyl tetrahydrophthalate, di-n-decyl tetrahydrophthalate, n-butylisodecyl tetrahydrophthalate, diisodecyl tetrahydrophthalate, n-butylundecyl tetrahydrophthalate Dihydrodecyl tetrahydrophthalate, n-butyldodecyl tetrahydrophthalate, didodecyl tetrahydrophthalate, n-butyltridecyl tetrahydrophthalate, ditridecyl tetrahydrophthalate, n-butyltetradecyl tetrahydrophthalate, ditetradecyl tetrahydrophthalate, tetrahydrophthalic acid n -Butyloctadecyl, dioctadecyl tetrahydrophthalate, diisobutyl tetrahydrophthalate, 2-butylhexyl tetrahydrophthalate, isobutyl n-octyl tetrahydrophthalate, isobutyl n-nonyl tetrahydrophthalate, isobutyl isononyl tetrahydrophthalate, isobutyl tetrahydrophthalate 3,5,5-trimethylhexyl, isobutyl n-decyl tetrahydrophthalate, tetra Isobutyl isodecyl drophthalate, isobutyl undecyl tetrahydrophthalate, isobutyl dodecyl tetrahydrophthalate, isobutyl tridecyl tetrahydrophthalate, isobutyl tetradecyl tetrahydrophthalate, isobutyl octadecyl tetrahydrophthalate, n-octyl n-octyl tetrahydrophthalate, tetrahydro N-octyl isononyl phthalate, n-octyl tetrahydrophthalate 3,5,5-trimethylhexyl, n-octyl tetrahydrophthalate, n-decyl tetrahydrophthalate, n-octylisodecyl tetrahydrophthalate, n-octyl undecyl tetrahydrophthalate N-octyldodecyl tetrahydrophthalate, n-octyltridecyl tetrahydrophthalate, n-octyltetradecyl tetrahydrophthalate, teto N-octyl octadecyl lahydrophthalate, n-nonyl isononyl tetrahydrophthalate, n-nonyl tetrahydrophthalate 3,5,5-trimethylhexyl, n-nonyl n-decyl tetrahydrophthalate, n-nonylisodecyl tetrahydrophthalate, tetrahydrophthalic acid n -Nonyl undecyl, n-nonyl dodecyl tetrahydrophthalate, n-nonyl tridecyl tetrahydrophthalate, n-nonyl tetradecyl tetrahydrophthalate, n-nonyl octadecyl tetrahydrophthalate, n-nonyl isononyl tetrahydrophthalate, n-nonyl tetrahydrophthalate 3, 5,5-trimethylhexyl, n-nonyl tetrahydrophthalate, n-decyl tetrahydrophthalate, n-nonyl isodecyl tetrahydrophthalate, n-nonyl tetrahydrophthalate , N-nonyldodecyl tetrahydrophthalate, n-nonyl tridecyl tetrahydrophthalate, n-nonyl tetradecyl tetrahydrophthalate, n-nonyl octadecyl tetrahydrophthalate, isononyl tetrahydrophthalate 3,5,5-trimethylhexyl, tetrahydrophthalic acid Isononyl n-decyl, isononyl isodecyl tetrahydrophthalate, isononyl undecyl tetrahydrophthalate, isononyl dodecyl tetrahydrophthalate, isononyl tridecyl tetrahydrophthalate, isononyl tetradecyl tetrahydrophthalate, isononyl octadecyl tetrahydrophthalate 3,5,5-trimethylhexyl n-decyl tetrahydrophthalate, 3,5,5-trimethylhexylisodecyl tetrahydrophthalate, 3,5,5-trimethylhexyl undecyl lophthalate, 3,5,5-trimethylhexyl dodecyl tetrahydrophthalate, 3,5,5-trimethylhexyl tridecyl tetrahydrophthalate, 3,5,5-trimethyl tetrahydrophthalate Hexyltetradecyl, tetrahydrophthalate 3,5,5-trimethylhexyloctadecyl, tetrahydrophthalate n-decylisodecyl, tetrahydrophthalate n-decylundecyl, tetrahydrophthalate n-decyldodecyl, tetrahydrophthalate n-decyltridecyl, tetrahydrophthalate n -Decyltetradecyl, n-decyl octadecyl tetrahydrophthalate, isodecyl tetradecyl tetrahydrophthalate, isodecyl tetrahydrophthalate, isodecyl tetrahydrophthalate Rutridecyl, isodecyl tetrahydrophthalate, tetradecyl tetrahydrophthalate, octadecyl tetrahydrophthalate, undecyl dodecyl tetrahydrophthalate, undecyl tetrahydrophthalate, tridecyl tetrahydrophthalate, tetradecyl tetrahydrophthalate, undecyl tetradecyl tetrahydrophthalate, tetrahydrophthalic acid Dodecyl tridecyl, dodecyl tetrahydrophthalate, tetradecyl tetrahydrophthalate, octadecyl tetrahydrophthalate, tetradecyl tetrahydrophthalate, tridecyl tetradecyl tetrahydrophthalate, tetradecyl tetradecyl tetrahydrophthalate, di-n-butyl hexahydrophthalate, hexahydro N-butyl 2-ethylhexyl phthalate, di-2-ethylhexyl hexahydrophthalate, hexahydride N-butyl n-octyl phthalate, di-n-octyl hexahydrophthalate, n-butyl n-butyl hexahydrophthalate, di-n-nonyl hexahydrophthalate, n-butyl isononyl hexahydrophthalate, hexahydro Diisononyl phthalate, n-butyl hexahydrophthalate 3,5,5-trimethylhexyl, di3,5,5-trimethylhexyl hexahydrophthalate, n-butyl hexahydrophthalate, n-decyl hexahydrophthalate, dihydrohexahydrophthalate n-decyl, n-butylisodecyl hexahydrophthalate, diisodecyl hexahydrophthalate, n-butylundecyl hexahydrophthalate, diundecyl hexahydrophthalate, n-butyldodecyl hexahydrophthalate, didodecyl hexahydrophthalate , N-butyhexahydrophthalic acid Tridecyl, ditridecyl hexahydrophthalate, n-butyltetradecyl hexahydrophthalate, ditetradecyl hexahydrophthalate, n-butyloctadecyl hexahydrophthalate, dioctadecyl hexahydrophthalate, diisobutyl hexahydrophthalate, hexahydrophthalic acid Isobutyl 2-ethylhexyl, isobutyl n-octyl hexahydrophthalate, isobutyl n-nonyl hexahydrophthalate, isobutyl isononyl hexahydrophthalate, isobutyl hexahydrophthalate 3,5,5-trimethylhexyl, isobutyl hexahydrophthalate n-decyl, isobutylisodecyl hexahydrophthalate, isobutylundecyl hexahydrophthalate, isobutyldodecyl hexahydrophthalate, hexahydrophthalic acid Isobutyltridecyl, isobutyltetradecyl hexahydrophthalate, isobutyloctadecyl hexahydrophthalate, n-octyl n-nonyl hexahydrophthalate, n-octylisononyl hexahydrophthalate, n-octyl hexahydrophthalate 3,5 , 5-trimethylhexyl, n-octyl n-decyl hexahydrophthalate, n-octylisodecyl hexahydrophthalate, n-octyl undecyl hexahydrophthalate, n-octyldodecyl hexahydrophthalate, hexahydrophthalic acid n-octyltridecyl, n-octyltetradecyl hexahydrophthalate, n-octyloctadecyl hexahydrophthalate, n-nonylisononyl hexahydrophthalate, n-nonyl hexahydrophthalate 3,5,5-trimethyl Xyl, n-nonyl n-decyl hexahydrophthalate, n-nonyl isodecyl hexahydrophthalate, n-nonyl undecyl hexahydrophthalate, n-nonyl dodecyl hexahydrophthalate, n-nonyl tridecyl hexahydrophthalate, hexahydrophthalic acid n-nonyltetradecyl, n-nonyloctadecyl hexahydrophthalate, n-nonylisononyl hexahydrophthalate, n-nonyl hexahydrophthalate 3,5,5-trimethylhexyl, n-nonyl hexahydrophthalate, n-decyl hexahydrophthalate, N-nonylisodecyl hexahydrophthalate, n-nonyl undecyl hexahydrophthalate, n-nonyl dodecyl hexahydrophthalate, n-nonyl tridecyl hexahydrophthalate, n-nonyl tetradecyl hexahydrophthalate, hexyl N-nonyloctadecyl hydrophthalate, isononyl 3,5,5-trimethylhexyl hexahydrophthalate, isononyl n-decyl hexahydrophthalate, isononyl isodecyl hexahydrophthalate, isononyl undecyl hexahydrophthalate, hexahydro Isononyl dodecyl phthalate, isononyl tridecyl hexahydrophthalate, isononyl tetradecyl hexahydrophthalate, isononyl octadecyl hexahydrophthalate, 3,5,5-trimethylhexyl n-decyl hexahydrophthalate, hexahydro 3,5,5-trimethylhexylisodecyl phthalate, 3,5,5-trimethylhexylundecyl hexahydrophthalate, 3,5,5-trimethylhexyl dodecyl hexahydrophthalate, 3,3 5,5-trimethylhexyltridecyl, 3,5,5-trimethylhexyltetradecyl hexahydrophthalate, 3,5,5-trimethylhexyloctadecyl hexahydrophthalate, n-decylisodecyl hexahydrophthalate, hexahydrophthalic acid n-decylundecyl, n-decyl dodecyl hexahydrophthalate, n-decyl tridecyl hexahydrophthalate, n-decyl tetradecyl hexahydrophthalate, n-decyl octadecyl hexahydrophthalate, isodecyl undecyl hexahydrophthalate, hexa Isodecyl dodecyl hydrophthalate, Isodecyl tridecyl hexahydrophthalate, Isodecyl tetradecyl hexahydrophthalate, Isodecyl octadecyl hexahydrophthalate, Undecyl hexahydrophthalate , Undecyl tridecyl hexahydrophthalate, undecyl tetradecyl hexahydrophthalate, undecyl hexadecyl hexahydrophthalate, dodecyl tridecyl hexahydrophthalate, dodecyl hexadecyl hexahydrophthalate, dodecyl octadecyl hexahydrophthalate , Tridecyl tetradecyl hexahydrophthalate, tridecyl octadecyl hexahydrophthalate, tetradecyl octadecyl hexahydrophthalate, di-n-butyl methyltetrahydrophthalate, n-butyl 2-ethylhexyl methyltetrahydrophthalate, methyltetrahydrophthalic acid Di-2-ethylhexyl, n-butyl n-butyl methyl tetrahydrophthalate, di-n-octyl methyl tetrahydrophthalate, n-butyl methyl tetrahydrophthalate Nonyl, di-n-nonyl methyltetrahydrophthalate, n-butylisononyl methyltetrahydrophthalate, diisononyl methyltetrahydrophthalate, n-butyl methyltetrahydrophthalate 3,5,5-trimethylhexyl, dimethyltetrahydrophthalate di-3 , 5,5-trimethylhexyl, n-butyl n-butyl methyl tetrahydrophthalate, di-n-decyl methyl tetrahydrophthalate, n-butyl isodecyl methyl tetrahydrophthalate, diisodecyl methyl tetrahydrophthalate, n-methyl tetrahydrophthalate Butyl undecyl, diundecyl methyl tetrahydrophthalate, n-butyl dodecyl methyl tetrahydrophthalate, didodecyl methyl tetrahydrophthalate, n-butyl tridecyl methyl tetrahydrophthalate, methyl Ditetradecyl tetrahydrophthalate, n-butyltetradecyl methyltetrahydrophthalate, ditetradecyl methyltetrahydrophthalate, n-butyloctadecyl methyltetrahydrophthalate, dioctadecyl methyltetrahydrophthalate, diisobutyl methyltetrahydrophthalate, isobutyl methyltetrahydrophthalate 2 -Ethylhexyl, isobutyl n-octyl methyl tetrahydrophthalate, isobutyl n-nonyl methyl tetrahydrophthalate, isobutyl isononyl methyl tetrahydrophthalate, isobutyl 3,5,5-trimethylhexyl methyl tetrahydrophthalate, isobutyl methyl tetrahydrophthalate n- Decyl, isobutyl isobutyl methyltetrahydrophthalate, isobutylunmethyl tetrahydrophthalate Sil, methyltetrahydrophthalate isobutyldodecyl, methyltetrahydrophthalate isobutyltridecyl, methyltetrahydrophthalate isobutyltetradecyl, methyltetrahydrophthalate isobutyloctadecyl, methyltetrahydrophthalate n-octyl n-nonyl, methyltetrahydrophthalate n-octyl Isononyl, n-octyl 3,5,5-trimethylhexyl methyltetrahydrophthalate, n-octyl n-decyl methyltetrahydrophthalate, n-octylisodecyl methyltetrahydrophthalate, n-octylundecyl methyltetrahydrophthalate, N-octyldodecyl methyltetrahydrophthalate, n-octyltridecyl methyltetrahydrophthalate, n-octyltetradecyl methyltetrahydrophthalate , N-octyloctadecyl methyltetrahydrophthalate, n-nonylisononyl methyltetrahydrophthalate, n-nonyl methyltetrahydrophthalate 3,5,5-trimethylhexyl, n-nonyl n-decyl methyltetrahydrophthalate, methyltetrahydrophthalic acid n-nonylisodecyl, n-nonylundecyl methyltetrahydrophthalate, n-nonyldodecyl methyltetrahydrophthalate, n-nonyltridecyl methyltetrahydrophthalate, n-nonyltetradecyl methyltetrahydrophthalate, n-nonyloctadecyl methyltetrahydrophthalate, methyltetrahydro N-nonyl isononyl phthalate, n-nonyl methyl tetrahydrophthalate 3,5,5-trimethylhexyl, n-nonyl n-methyl tetrahydrophthalate Decyl, n-nonylisodecyl methyltetrahydrophthalate, n-nonylundecyl methyltetrahydrophthalate, n-nonyldodecyl methyltetrahydrophthalate, n-nonyltridecyl methyltetrahydrophthalate, n-nonyltetradecyl methyltetrahydrophthalate, methyltetrahydrophthalic acid n -Nonyl octadecyl, isononyl methyl tetrahydrophthalate 3,5,5-trimethylhexyl, isononyl n-decyl methyl tetrahydrophthalate, isononyl isodecyl methyl tetrahydrophthalate, isononyl undecyl methyl tetrahydrophthalate, iso-methyl tetrahydrophthalate Nonyldodecyl, isononyltridecyl methyltetrahydrophthalate, isononyltetradecyl methyltetrahydrophthalate, methyltetrahydro Isononyl octadecyl drophthalate, 3,5,5-trimethylhexyl n-decyl methyltetrahydrophthalate, 3,5,5-trimethylhexylisodecyl methyltetrahydrophthalate, 3,5,5-trimethylhexylunmethyltetrahydrophthalate Decyl, 3,5,5-trimethylhexyldecyl methyltetrahydrophthalate, 3,5,5-trimethylhexyltridecyl methyltetrahydrophthalate, 3,5,5-trimethylhexyltetradecyl methyltetrahydrophthalate, methyltetrahydrophthalic acid 3,5,5-trimethylhexyl octadecyl, n-decylisodecyl methyltetrahydrophthalate, n-decylundecyl methyltetrahydrophthalate, n-decyldodecyl methyltetrahydrophthalate, N-decyltridecyl lahydrophthalate, n-decyltetradecyl methyltetrahydrophthalate, n-decyloctadecyl methyltetrahydrophthalate, isodecyl undecyl methyltetrahydrophthalate, isodecyldodecyl methyltetrahydrophthalate, isodecyltridecyl methyltetrahydrophthalate , Isodecyl tetradecyl methyl tetrahydrophthalate, isodecyl octadecyl methyl tetrahydrophthalate, undecyl dodecyl methyl tetrahydrophthalate, undecyl tridecyl methyl tetrahydrophthalate, undecyl tetradecyl methyl tetrahydrophthalate, undecyl methyl tetrahydrophthalate Octadecyl, tridecyl methyltetrahydrophthalate, dodecyltetradecyl methyltetrahydrophthalate , Dodecyl octadecyl methyl tetrahydrophthalate, tridecyl tetradecyl methyl tetrahydrophthalate, tridecyl octadecyl methyl tetrahydrophthalate, tetradecyl octadecyl methyl tetrahydrophthalate, di-n-butyl methyl hexahydrophthalate, n-methyl hexahydrophthalate Butyl 2-ethylhexyl, di-2-ethylhexyl methyl hexahydrophthalate, n-butyl n-octyl methyl hexahydrophthalate, di n-octyl methyl hexahydrophthalate, n-butyl n-nonyl methyl hexahydrophthalate, methyl Di-n-nonyl hexahydrophthalate, n-butyl isononyl methyl hexahydrophthalate, diisononyl methyl hexahydrophthalate, n-butyl methyl hexahydrophthalate 3,5,5-tri Tilhexyl, di3,5,5-trimethylhexyl methylhexahydrophthalate, n-butyl n-decyl methylhexahydrophthalate, di-n-decyl methylhexahydrophthalate, n-butylisodecyl methylhexahydrophthalate, Diisodecyl methyl hexahydrophthalate, n-butylundecyl methyl hexahydrophthalate, diundecyl methyl hexahydrophthalate, n-butyl dodecyl methyl hexahydrophthalate, didodecyl methyl hexahydrophthalate, n-butyl methyl hexahydrophthalate Tridecyl, ditridecyl methylhexahydrophthalate, n-butyltetradecyl methylhexahydrophthalate, ditetradecyl methylhexahydrophthalate, n-butyloctadecyl methylhexahydrophthalate, methylhexa Dioctadecyl drophthalate, diisobutyl methylhexahydrophthalate, isobutyl 2-ethylhexyl methylhexahydrophthalate, isobutyl n-octyl methylhexahydrophthalate, isobutyl n-nonyl methylhexahydrophthalate, isobutylisononyl methylhexahydrophthalate , Isobutyl 3,5,5-trimethylhexyl methyl hexahydrophthalate, isobutyl n-decyl methyl hexahydrophthalate, isobutyl isodecyl methyl hexahydrophthalate, isobutyl undecyl methyl hexahydrophthalate, isobutyl methyl hexahydrophthalate Dodecyl, isobutyl tridecyl methyl hexahydrophthalate, isobutyl tetradecyl methyl hexahydrophthalate, isobutyl octyl methyl hexahydrophthalate Tadecyl, n-octyl n-octyl methylhexahydrophthalate, n-octylisononyl methylhexahydrophthalate, n-octyl methylhexahydrophthalate 3,5,5-trimethylhexyl, n-octyl methylhexahydrophthalate n-decyl, n-octylisodecyl methylhexahydrophthalate, n-octylundecyl methylhexahydrophthalate, n-octyldodecyl methylhexahydrophthalate, n-octyltridecyl methylhexahydrophthalate, methylhexahydro N-octyltetradecyl phthalate, n-octyloctadecyl methylhexahydrophthalate, n-nonylisononyl methylhexahydrophthalate, n-nonyl methylhexahydrophthalate 3,5,5-trimethylhexyl, methylhexahydro N-nonyl n-decyl tartrate, n-nonyl isodecyl methyl hexahydrophthalate, n-nonyl undecyl methyl hexahydrophthalate, n-nonyl dodecyl methyl hexahydrophthalate, n-nonyl tridecyl methyl hexahydrophthalate, methyl hexahydrophthal N-nonyl tetradecyl acid, n-nonyl octadecyl methyl hexahydrophthalate, n-nonyl isononyl methyl hexahydrophthalate, n-nonyl methyl hexahydrophthalate 3,5,5-trimethylhexyl, n-methyl hexahydrophthalate Nonyl n-decyl, n-nonyl isodecyl methyl hexahydrophthalate, n-nonyl undecyl methyl hexahydrophthalate, n-nonyl dodecyl methyl hexahydrophthalate, n-nonyl trimethyl hexahydrophthalate Sil, n-nonyltetradecyl methylhexahydrophthalate, n-nonyloctadecyl methylhexahydrophthalate, isononyl 3,5,5-trimethylhexylmethylhexahydrophthalate, isononyl n-decyl methylhexahydrophthalate, methylhexa Isononyl isodecyl hydrophthalate, isononyl undecyl methyl hexahydrophthalate, isononyl dodecyl methyl hexahydrophthalate, isononyl tridecyl methyl hexahydrophthalate, isononyl tetradecyl methyl hexahydrophthalate, methyl hexahydro Isononyl octadecyl phthalate, 3,5,5-trimethylhexyl n-decyl methylhexahydrophthalate, 3,5,5-trimethylhexylisodecyl methylhexahydrophthalate, methylhexahydro 3,5,5-trimethylhexylundecyl phthalate, 3,5,5-trimethylhexyldodecyl methylhexahydrophthalate, 3,5,5-trimethylhexyltridecyl methylhexahydrophthalate, methylhexahydrophthalic acid 3 , 5,5-trimethylhexyltetradecyl, 3,5,5-trimethylhexyloctadecyl methylhexahydrophthalate, n-decylisodecyl methylhexahydrophthalate, n-decylundecyl methylhexahydrophthalate, n-methylhexahydrophthalate Decyl dodecyl, n-decyl tridecyl methyl hexahydrophthalate, n-decyl tetradecyl methyl hexahydrophthalate, n-decyl octadecyl methyl hexahydrophthalate, isodecyl undecyl methyl hexahydrophthalate, methyl Isodecyl dodecyl hexahydrophthalate, isodecyl tridecyl methyl hexahydrophthalate, isodecyl tetradecyl methyl hexahydrophthalate, isodecyl octadecyl methyl hexahydrophthalate, undecyl dodecyl methyl hexahydrophthalate, methyl hexahydrophthal Undecyl tridecyl acid, undecyl tetradecyl methyl hexahydrophthalate, undecyl octadecyl methyl hexahydrophthalate, dodecyl tridecyl methyl hexahydrophthalate, tetradecyl methyl hexahydrophthalate, dodecyl octadecyl methyl hexahydrophthalate , Tridecyl tetradecyl methyl hexahydrophthalate, tridecyl octadecyl methyl hexahydrophthalate, tetradecyl methyl hexahydrophthalate Alicyclic dicarboxylic acid diester such as Tadeshiru like.

  Examples of aromatic dicarboxylic acid diesters include di-n-butyl phthalate, n-butyl 2-ethylhexyl phthalate, di-2-ethylhexyl phthalate, n-butyl n-octyl phthalate, di-n-octyl phthalate, phthalate N-butyl n-nonyl phthalate, di-n-nonyl phthalate, n-butyl isononyl phthalate, diisononyl phthalate, n-butyl phthalate 3,5,5-trimethylhexyl, di-3,5,5-phthalate Trimethylhexyl, n-butyl n-decyl phthalate, di-n-decyl phthalate, n-butyl isodecyl phthalate, diisodecyl phthalate, n-butyl undecyl phthalate, diundecyl phthalate, n-butyl dodecyl phthalate, Didodecyl phthalate, n-butyltridecyl phthalate, ditridecyl phthalate, n-butyltetradecyl phthalate , Ditetradecyl phthalate, n-butyloctadecyl phthalate, dioctadecyl phthalate, diisobutyl phthalate, isobutyl 2-ethylhexyl phthalate, isobutyl n-octyl phthalate, isobutyl n-nonyl phthalate, isobutyl isononyl phthalate, phthalate Isobutyl 3,5,5-trimethylhexyl, isobutyl n-decyl phthalate, isobutyl isodecyl phthalate, isobutyl undecyl phthalate, isobutyl dodecyl phthalate, isobutyl tridecyl phthalate, isobutyl tetradecyl phthalate, isobutyl phthalate Octadecyl, n-octyl n-nonyl phthalate, n-octyl isononyl phthalate, n-octyl phthalate 3,5,5-trimethylhexyl, n-octyl n-decyl phthalate, n-octyl phthalate Isodecyl, n-octyl undecyl phthalate, n-octyl dodecyl phthalate, n-octyl tridecyl phthalate, n-octyl tetradecyl phthalate, n-octyl octadecyl phthalate, n-nonyl isononyl phthalate, n-phthalate Nonyl 3,5,5-trimethylhexyl, n-nonyl n-decyl phthalate, n-nonyl isodecyl phthalate, n-nonyl undecyl phthalate, n-nonyl dodecyl phthalate, n-nonyl tridecyl phthalate, n-nonyl tetraphthalate Decyl, n-nonyl octadecyl phthalate, n-nonyl isononyl phthalate, n-nonyl phthalate 3,5,5-trimethylhexyl, n-nonyl n-decyl phthalate, n-nonyl isodecyl phthalate, n-nonyl undecyl phthalate, N-nonyldodecyl phthalate, phthalate N-nonyl tridecyl tartrate, n-nonyl tetradecyl phthalate, n-nonyl octadecyl phthalate, isononyl 3,5,5-trimethylhexyl phthalate, isononyl n-decyl phthalate, isononyl isodecyl phthalate, isophthalic acid iso Nonyl undecyl, isononyl dodecyl phthalate, isononyl tridecyl phthalate, isononyl tetradecyl phthalate, isononyl octadecyl phthalate, 3,5,5-trimethylhexyl n-decyl phthalate, 3, 5, phthalate 5-trimethylhexylisodecyl, 3,5,5-trimethylhexylundecyl phthalate, 3,5,5-trimethylhexyldecyl phthalate, 3,5,5-trimethylhexyltridecyl phthalate, 3,5 phthalate , 5-Trimethylhexyltetradecyl phthalate 3, , 5-trimethylhexyl octadecyl, n-decylisodecyl phthalate, n-decyl undecyl phthalate, n-decyl dodecyl phthalate, n-decyl tridecyl phthalate, n-decyl tetradecyl phthalate, n-decyl octadecyl phthalate, isophthalic acid Decyl undecyl, isodecyl dodecyl phthalate, isodecyl tridecyl phthalate, isodecyl tetradecyl phthalate, isodecyl octadecyl phthalate, undecyl dodecyl phthalate, undecyl tridecyl phthalate, undecyl tetradecyl phthalate, Undecyl octadecyl phthalate, dodecyl tridecyl phthalate, dodecyl tetradecyl phthalate, dodecyl octadecyl phthalate, tridecyl tetradecyl phthalate, tridecyl octadecyl phthalate, tetradecyl phthalate Octadecyl, and the like.

  Among these, in particular, di-2-ethylhexyl phthalate, diisononyl phthalate, diisodecyl phthalate, isobutyl 2-ethylhexyl phthalate, isobutyl isononyl phthalate, di-2-ethylhexyl tetrahydrophthalate used as plasticizers for vinyl chloride resins, Dihydrononyl tetrahydrophthalate, diisodecyl tetrahydrophthalate, isobutyl 2-ethylhexyl tetrahydrophthalate, isobutyl isononyl tetrahydrophthalate, di-2-ethylhexyl hexahydrophthalate, diisononyl hexahydrophthalate, diisodecyl hexahydrophthalate, hexahydrophthalic acid Isobutyl 2-ethylhexyl, isobutyl isononyl hexahydrophthalate and the like are preferable.

  EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples. However, the present invention is not limited to these examples. In addition, COV, POV, sulfuric acid coloration, and hue in each Example and Comparative Example were measured by the following methods.

(1) Carbonyl value (COV)
Measurement was performed according to the method described in JIS K 1525.
(2) Peroxide value (POV)
It measured based on the method as described in a reference | standard oil-and-fat analysis test method.
(3) Coloration with sulfuric acid Wash with concentrated sulfuric acid, rinse with distilled water, put 200 ml sample into a 300 ml flat-bottomed flask with a stopper after drying, and stir with a magnetic stirrer at a temperature of 30 ° C or lower in an ice bath. Add 17.5 ml of 98 wt% concentrated sulfuric acid in a 25 ml burette at a rate of 3.5 ml / min. Put a stopper and immerse in an oil bath at 98 ± 2 ° C for 1 hour. After cooling, the hue (Hazen) of the sample was measured according to the method of JIS K-0071.
(4) Hue
The hue of the dicarboxylic acid diester was measured by the method of JIS K-0071.

The flash apparatus shown in FIG. 1 was used to perform an alcohol flash process under the following conditions. As the raw material alcohol, COV of 0.20 mgKOH / g, POV of 2.31 meq / kg, sulfuric acid coloration of Hazen and 50 kg of 2-ethylhexanol was used, and the outlet temperature of the heating unit 1 was 130 ° C. The pump 2 was charged at a flow rate of 3 kg / h so that the time would be 1 minute. The temperature of the heating chamber 3 at this time was 188 ° C. The alcohol heated to 130 ° C. was charged into the decompression chamber 6 having an internal volume of 5 L, which was decompressed to 8.0 × 10 ³ Pa, at a flow rate of 6 kg / h, and flushed. The 2-ethylhexanol obtained in the alcohol recovery storage tank 8 was 2.96 kg, the coloring component recovery storage tank 11 was 0.06 kg, and the yield was 98.0%.

Next, a 500 ml four-necked flask equipped with a water separator, a nitrogen inlet tube, and a thermometer was replaced with nitrogen gas, and 156 g (1.2 mol) of 2-ethylhexanol in the alcohol recovery tank 8 and anhydrous phthalate were added to the flask. 74 g (0.5 mol) of acid and 0.12 g of tetra n-butyl titanate were added, and the reaction was carried out for 6 hours while refluxing 2-ethylhexanol at 180 ° C. under reduced pressure to remove the produced water. The acid value of the reaction mixture after 6 hours was 0.14 mg KOH / g, and the reaction rate of diesterification was 99.9%. Subsequently, most of the alcohol was distilled off under reduced pressure, cooled, added with 5 g of 2% aqueous sodium hydroxide solution, neutralized with stirring at 90 ° C. for 30 minutes, decomposed the catalyst, allowed to stand, and separated water. The layer was extracted, and the upper diester layer was washed with warm water at 70 ° C. until the pH of the washing water became neutral. After washing, steam stripping was performed at 170 ° C. to completely remove and remove residual 2-ethylhexanol, followed by drying under reduced pressure at 0.67 × 10 ³ Pa or less. After cooling, 0.3 g of activated clay, activated carbon and activated alumina were added and stirred for 30 minutes under a reduced pressure of 0.67 × 10 ³ Pa for decolorization and adsorption treatment. Then, the treatment agent was filtered off and dicarboxylic acid diester Got. The hue of the obtained dicarboxylic acid diester was 15.

  In Example 1, when the outlet temperature of the alcohol heating unit 1 was changed to 100 ° C. and flushing was performed, 2-ethylhexanol obtained in the alcohol recovery storage tank 8 was 2.95 kg, and the colored component recovery storage tank 11 was The yield was 98.2% at 0.05 kg. Furthermore, when diesterification was performed in the same manner as in Example 1, the hue of the obtained dicarboxylic acid diester was 10.

  In Example 1, when the outlet temperature of the alcohol heating unit 1 was changed to 165 ° C. and flashing was performed, 2-ethylhexanol obtained in the alcohol recovery tank 8 was 2.91 kg, and the colored component recovery tank 11 was The yield was 97.0% at 0.09 kg. Furthermore, when diesterification was performed in the same manner as in Example 1, the hue of the obtained dicarboxylic acid diester was 10.

In Example 1, when the outlet temperature of the alcohol heating unit 1 was changed to 80 ° C. and the pressure in the decompression chamber 6 was changed to 4.0 × 10 ³ Pa, the flash treatment was performed. -Ethylhexanol was 2.98 kg, the colored component recovery storage tank 11 was 0.02 kg, and the yield was 99.3%. Furthermore, when diesterification was performed in the same manner as in Example 1, the hue of the obtained dicarboxylic acid diester was 10.

In Example 3, when the pressure in the decompression chamber 6 was changed to 8.0 × 10 ³ Pa and flushing was performed, 2-ethylhexanol obtained in the alcohol recovery storage tank 8 was 2.87 kg, and the colored component recovery storage tank 11 was 0.13 kg and the yield was 95.7%. Further, diesterification was carried out in the same manner as in Example 1. As a result, the hue of the obtained dicarboxylic acid diester was 15.

  In Example 1, the raw material alcohol was COV 0.30 mg KOH / g, POV was 5.69 meq / kg, sulfuric acid color wason and isononanol having a color of 100, and the outlet temperature of the alcohol heating unit 1 was changed to 135 ° C. to perform flash processing. As a result, 2.98 kg of isononanol was obtained in the alcohol recovery storage tank 8, 0.02 kg in the colored component recovery storage tank 11, and the yield was 99.3%. Furthermore, when diesterification was performed in the same manner as in Example 1, the hue of the obtained dicarboxylic acid diester was 10.

In Example 6, when the outlet temperature of the alcohol heating unit 1 was changed to 100 ° C. and the pressure in the decompression chamber 6 was changed to 4.0 × 10 ³ Pa to perform flash treatment, isononanol obtained in the alcohol recovery storage tank 8 was obtained. Was 2.97 kg, and the colored component recovery storage tank 11 was 0.03 kg, and the yield was 99.0%. Furthermore, when diesterification was performed in the same manner as in Example 1, the hue of the obtained dicarboxylic acid diester was 10.

In Example 6, the outlet temperature of the alcohol heating unit 1 was changed to 165 ° C., and the pressure in the decompression chamber 6 was changed to 4.0 × 10 ³ Pa to perform flash treatment. As a result, isononanol obtained in the alcohol recovery storage tank 8 was obtained. Was 2.92 kg, and the coloring component recovery storage tank 11 was 0.08 kg, and the yield was 97.3%. Further, diesterification was carried out in the same manner as in Example 1. As a result, the hue of the obtained dicarboxylic acid diester was 15.

In Example 6, when the pressure in the decompression chamber 6 was changed to 4.0 × 10 ³ Pa and flushing was performed, 2.96 kg of isononanol was obtained in the alcohol recovery storage tank 8, and the colored component recovery storage tank 11 had The yield was 98.7% at 0.04 kg. Furthermore, when diesterification was performed in the same manner as in Example 1, the hue of the obtained dicarboxylic acid diester was 10.

In Example 6, when the outlet temperature of the alcohol heating unit 1 was changed to 165 ° C. and the pressure in the decompression chamber 6 was changed to 13.3 × 10 ³ Pa, flushing was performed, and isononanol obtained in the alcohol recovery storage tank 8 Was 2.97 kg, and the colored component recovery storage tank 11 was 0.03 kg, and the yield was 99.0%. Further, diesterification was carried out in the same manner as in Example 1. As a result, the hue of the obtained dicarboxylic acid diester was 15.

  When diesterification was carried out in the same manner as in Example 1 using 76.0 g (0.5 mol) of tetrahydrophthalic anhydride instead of phthalic anhydride in Example 6, the resulting dicarboxylic acid diester had a hue of 15 Met.

  In Example 6, diesterification was carried out in the same manner as in Example 1 using 77.0 g (0.5 mol) of hexahydrophthalic anhydride instead of phthalic anhydride. The resulting dicarboxylic acid diester had a hue of 10.

  When diesterification was carried out in the same manner as in Example 1 using 73.0 g (0.5 mol) of adipic acid instead of phthalic anhydride in Example 6, the hue of the obtained dicarboxylic acid diester was 10. .

In Example 1, instead of the 500 ml four-necked flask, a 5 L four-necked flask was used, and 1560 g (12.0 mol) of 2-ethylhexanol in 10 times the amount of the alcohol recovery storage tank 8 of Example 1 and anhydrous phthalate The same reaction and post-treatment were performed using 740 g (5.0 mol) of acid and 1.20 g of tetra-n-butyl titanate. At this time, the COV of 2-ethylhexanol recovered by distillation after diesterification reaction and steam stripping after washing with water was 0.38 mgKOH / g, and POV was 5.22 meq / kg.
Furthermore, the carboxylic acid diester obtained in the same manner as in Example 1 except that recovered 2-ethylhexanol having a COV of 0.38 mg KOH / g and a POV of 5.22 meq / kg was used in Example 1. The hue of was 15.

In Example 6, instead of the 500 ml four-necked flask, a 5-L four-necked flask was used, and 1728 g (12.0 mol) of isononanol and 740 g of phthalic anhydride (10 times the amount of the alcohol recovery storage tank 8 of Example 6) ( 5.0 mol) and 1.20 g of tetra n-butyl titanate were subjected to the same reaction and post-treatment. At this time, the COV of isononanol recovered by distillation after the diesterification reaction and steam stripping after washing with water was 0.42 mgKOH / g, and POV was 7.44 meq / kg.
Further, in Example 6, except that the recovered isononanol having a COV of 0.42 mg KOH / g and a POV of 7.44 meq / kg was used, the hue of the resulting carboxylic acid diester was as follows. It was 15.

Comparative Example 1
When diesterification was carried out in the same manner as in Example 1 without performing the alcohol flash treatment in Example 1, the hue of the obtained dicarboxylic acid diester was 30.

Comparative Example 2
In Example 1, using CO2-0.04 mg KOH / g as alcohol, PO7 as 0.27 meq / kg, sulfuric acid color of Hazen and 20-ethylhexanol, and diesterifying as in Example 1 without flashing. As a result, the hue of the obtained dicarboxylic acid diester was 10.

Comparative Example 3
In Example 6, only the diesterification was performed in the same manner as in Example 1 without performing the alcohol flash treatment. As a result, the hue of the obtained dicarboxylic acid diester was 40.

Comparative Example 4
In Example 1, the raw material alcohol was COV 0.09 mg KOH / g, POV was 0.78 meq / kg, sulfuric acid wason and isononanol having a color of 10 and flashing was not performed, and only diesterification was performed as in Example 1. As a result, the hue of the obtained dicarboxylic acid diester was 10.

Comparative Example 5
In Example 6, when the outlet temperature of the alcohol heating unit 1 was changed to 180 ° C. and the pressure in the decompression chamber 6 was changed to 4.0 × 10 ³ Pa to perform flash treatment, isononanol obtained in the alcohol recovery storage tank 8 was obtained. Was 2.88 kg, the colored component recovery storage tank 11 was 0.12 kg, and the yield was 96.0%. Further, diesterification was carried out in the same manner as in Example 1. As a result, the hue of the obtained dicarboxylic acid diester was 30.

Comparative Example 6
In Example 6, when the outlet temperature of the alcohol heating unit 1 was changed to 165 ° C. and the pressure in the vacuum chamber 6 was changed to 2.0 × 10 ³ Pa, flushing was performed, and the isononanol obtained in the alcohol recovery storage tank 8 was obtained. Was 2.83 kg, and the colored component recovery storage tank 11 was 0.17 kg, and the yield was 94.3%. Furthermore, when diesterification was performed in the same manner as in Example 1, the hue of the obtained dicarboxylic acid diester was 10.

Comparative Example 7
In Example 6, when the pressure in the decompression chamber 6 was changed to 26.7 × 10 ³ Pa and flushing was performed, 2.99 kg of isononanol was obtained in the alcohol recovery storage tank 8, and the colored component recovery storage tank 11 The yield was 99.7% at 0.01 kg. Furthermore, when diesterification was performed in the same manner as in Example 1, the hue of the obtained dicarboxylic acid diester was 40.

Comparative Example 8
In Comparative Example 3, diesterification was carried out in the same manner as in Example 1 using 76.0 g (0.5 mol) of tetrahydrophthalic anhydride instead of phthalic anhydride. The resulting dicarboxylic acid diester had a hue of 40 Met.

Comparative Example 9
When diesterification was carried out in the same manner as in Example 1 using 77.0 g (0.5 mol) of hexahydrophthalic anhydride instead of phthalic anhydride in Example 3, the hue of the obtained dicarboxylic acid diester was 30.

Comparative Example 10
When diesterification was carried out in the same manner as in Example 1 using 73.0 g (0.5 mol) of adipic acid instead of phthalic anhydride in Example 3, the hue of the obtained dicarboxylic acid diester was 40. .

  According to the present invention, the content of impurities that cause coloration can be significantly reduced by flashing low-quality raw material alcohol, and a dicarboxylic acid diester having a good hue can be produced from the obtained alcohol. .

FIG. 1 is a schematic diagram illustrating an example of a flash processing step and an apparatus.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 ... Heating unit 2 ... Pump 3 ... Heating chamber 4 ... Coil type heating tube 5 ... Raw material alcohol recovery unit 6 ... Depressurization chamber 7 ... Eye plate type dispersion plate 8. ..Alcohol recovery storage phase 9 ... Coloring cause component collection unit 10 ... Capacitor 11 ... Coloration cause component recovery storage tank 12 ... Vacuum pump

Claims (9)

  A method for producing a dicarboxylic acid diester by subjecting a dicarboxylic acid or its anhydride and an alcohol to an esterification reaction in the presence of an esterification catalyst, wherein the alcohol obtained by flashing a raw material alcohol is used. Method for producing acid diester.   The method for producing a dicarboxylic acid diester according to claim 1, wherein the raw material alcohol has a carbonyl value of 0.1 to 1.0 mgKOH / g and a peroxide value of 0.5 to 10.0 meq / kg.   The raw material alcohol has a carbonyl value of 0.1 to 1.0 mgKOH / g, a peroxide value of 0.5 to 10.0 meq / kg, and a sulfuric acid coloration of Hazen 30 to 250. A process for producing a dicarboxylic acid diester.   The manufacturing method in any one of Claims 1-3 in which raw material alcohol contains the collection | recovery alcohol generate | occur | produced in the case of manufacture of dicarboxylic acid diester.   The manufacturing method in any one of Claims 1-4 which flush-processes raw material alcohol just before esterification reaction. The starting alcohol was heated to a temperature eighty to one hundred and sixty-five ° C., The process according to any one of claims 1 to 4 flash process can internal pressure ^{4.0 × 10 3 ~13.3 × 10 3} Pa of flash can.   The manufacturing method according to any one of claims 1 to 6, wherein the raw alcohol is flash-treated so that an evaporation amount in the flash treatment step is 0.5 to 5% by weight with respect to the raw alcohol.   Dicarboxylic acid diesters are di-2-ethylhexyl phthalate, diisononyl phthalate, diisodecyl phthalate, isobutyl 2-ethylhexyl phthalate, isobutyl isononyl phthalate, di-2-ethylhexyl tetrahydrophthalate, diisononyl tetrahydrophthalate, diisodecyl tetrahydrophthalate , Isobutyl 2-ethylhexyl tetrahydrophthalate, isobutyl isononyl tetrahydrophthalate, di-2-ethylhexyl hexahydrophthalate, diisononyl hexahydrophthalate, diisodecyl hexahydrophthalate, isobutyl 2-ethylhexyl hexahydrophthalate, or hexahydrophthal It is isobutyl isononyl acid, The manufacturing method of the dicarboxylic acid diester in any one of Claims 1-7. A plasticizer for vinyl chloride resin comprising a dicarboxylic acid diester obtained by the production method according to claim 8.

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