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WO2003078015A1 - Apparatus and method for purifying easily polymerizable substance - Google Patents

Apparatus and method for purifying easily polymerizable substance Download PDF

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Publication number
WO2003078015A1
WO2003078015A1 PCT/JP2003/003319 JP0303319W WO03078015A1 WO 2003078015 A1 WO2003078015 A1 WO 2003078015A1 JP 0303319 W JP0303319 W JP 0303319W WO 03078015 A1 WO03078015 A1 WO 03078015A1
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WIPO (PCT)
Prior art keywords
polymerizable substance
easily polymerizable
polymerization inhibitor
purification tower
purifying
Prior art date
Application number
PCT/JP2003/003319
Other languages
French (fr)
Japanese (ja)
Inventor
Seiji Miyazaki
Yasuhiro Kabu
Yoshiyuki Taniguchi
Original Assignee
Mitsubishi Rayon Co., Ltd.
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Publication date
Application filed by Mitsubishi Rayon Co., Ltd. filed Critical Mitsubishi Rayon Co., Ltd.
Priority to JP2003576066A priority Critical patent/JPWO2003078015A1/en
Publication of WO2003078015A1 publication Critical patent/WO2003078015A1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/48Separation; Purification; Stabilisation; Use of additives
    • C07C67/52Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation
    • C07C67/54Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation by distillation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/34Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • C07C51/44Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/50Use of additives, e.g. for stabilisation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/48Separation; Purification; Stabilisation; Use of additives
    • C07C67/62Use of additives, e.g. for stabilisation

Definitions

  • the present invention relates to an apparatus and a method for purifying an easily polymerizable substance such as a vinyl-type polymerizable monomer.
  • Proposals for introducing the polymerization inhibitor include a condenser that condenses the vapor of the easily polymerizable substance discharged from the purification tower, a pipe that returns the condensed easily polymerizable substance to the purification tower, and the top of the purification tower. Have been. These methods were very effective in preventing polymerization in the purification tower.
  • the present invention has been made in view of the above circumstances, and when distilling and purifying easily polymerizable substances, it is possible to prevent polymerization in the purification column and to remove the polymerization inhibitor from the purification column more than necessary. It is an object of the present invention to provide an apparatus and a method for purifying an easily polymerizable substance, which can obtain a high-quality product by suppressing the distillation of water.
  • the apparatus for purifying an easily polymerizable substance is an apparatus for purifying an easily polymerizable substance, comprising: a purification tower for continuously distilling and purifying the easily polymerizable substance, wherein the easy polymerizable substance introduction section includes a purification tower. Separately from this, a polymerization inhibitor introducing section for introducing the first polymerization inhibitor into the purification tower is provided in an intermediate portion of the purification tower.
  • the intermediate part of the purification tower is a part from the introduction part of the easily polymerizable substance to the top of the tower.
  • the easily polymerizable substance introduction section is a section for introducing an unpurified easily polymerizable substance into a purification tower.
  • the relationship between the theoretical plate number H1 from the top of the purification tower to the introduction section of the easily polymerizable substance and the theoretical plate number H2 from the top of the purification tower to the polymerization inhibitor introduction section is defined as follows. It is preferable that an easily polymerizable substance introduction part and a polymerization inhibitor introduction part are provided at positions satisfying the following formula (1).
  • the easily polymerizable substance is (meth) acrylic acid or (meth) acrylate.
  • the easily polymerizable substance introduction section is provided in the purification tower, and the polymerization inhibitor introduction section is separately provided in the middle section of the purification tower.
  • the purification tower has a theoretical plate number H 1 from the top of the purification tower to the introduction section of the polymerizable substance and a theoretical plate number H from the top of the purification tower to the polymerization inhibitor introduction section H It is preferable that the purification column is provided with an easily polymerizable substance introduction part and a polymerization inhibitor introduction part at a position where the relationship with 2 satisfies the following formula (1).
  • the easily polymerizable substance is (meth) acrylic acid or (meth) acrylate.
  • the method for purifying an easily polymerizable substance of the present invention may further include a step of adding a second polymerization inhibitor different from the first polymerization inhibitor to the purified easily polymerizable substance obtained from the top of the tower. it can.
  • FIG. 1 is a schematic view showing an example of the apparatus for purifying an easily polymerizable substance of the present invention.
  • the apparatus for purifying an easily polymerizable substance of the present invention will be described with reference to FIG.
  • the apparatus for purifying easily polymerizable substances 10 includes a purification tower 11 for continuously distilling and purifying easily polymerizable substances, and an easily polymerizable substance for supplying unpurified easily polymerizable substances to the purification tower 11.
  • the purification tower 11 has a tower top outlet pipe 16 for discharging the vaporized easily polymerizable substance from the tower top 15, and a reflux pipe 17 for refluxing from the condenser 14 to the tower top 15.
  • a bottom outlet pipe 19 for drawing out the easily polymerizable substance from the bottom 18 of the purification tower 11; and a reboiler 20 for heating a part of the easily polymerizable substance sent through the bottom guide pipe 19.
  • the reintroduction pipe 21 for reintroducing the vapor of the easily polymerizable substance generated in the reboiler 20 into the purification tower 11 and the remaining of the easily polymerizable substance sent through the bottom outlet pipe 18
  • An impurity discharge pipe 22 for discharging a part is attached.
  • the condenser 14 is provided with a next-step liquid sending pipe 23 for sending the liquid to the next step.
  • the purification column 11 is not particularly limited as long as it can purify the easily polymerizable substance by distillation.
  • a tray column type purification column, a packed column type purification column, and the like are used. Further, the pressure in the purification tower 11 can be reduced.
  • An easily polymerizable substance introduction part 25 to which an easily polymerizable substance supply pipe 12 is connected is provided at an appropriate position of the purification tower 11.
  • the position of the easily polymerizable substance introduction section 25 should be determined by calculating the theoretical number of plates HI from the easily polymerizable substance introduction section 25 to the tower top 15 based on the type and amount of impurities to be separated in the easily polymerizable substance.
  • a polymerization inhibitor supply pipe 13 is connected to an intermediate portion 26 of the purification tower 11, A polymerization inhibitor introduction section 27 for introducing the polymerization inhibitor into the purification tower 11 is provided.
  • the position where the polymerization inhibitor introduction section 27 is provided depends on the performance of the purification tower 11, the liquid properties of the easily polymerizable substance to be treated, the distribution of the polymerization inhibitor in the vertical direction of the purification tower 11, and the like. It is appropriately determined within the range of the intermediate part 26 of 1, but it is necessary that the theoretical plate number H 2 from the polymerization inhibitor introduction part 27 to the tower top part 15 satisfies the following formula (1). preferable.
  • HI indicates the number of theoretical plates from the easily polymerizable substance introduction section 25 to the top section 15 of the purification tower 11.
  • the polymerization inhibitor introduction section 27 is preferably provided at a position where the theoretical plate number H 2 from the polymerization inhibitor introduction section 27 to the top 15 of the purification tower satisfies the following formula (2). .
  • the polymerization inhibitor introduction section 27 When the polymerization inhibitor introduction section 27 is provided at a position satisfying 0.1 x H 1> H2, the number of theoretical plates from the polymerization inhibitor introduction section 27 to the tower top 15 is small, and 1 The polymerization inhibitor may be discharged from the purification tower 1 1 and satisfies H 1 ⁇ H 2
  • the top section 15 in the purification column 11 Insufficient amount of polymerization inhibitor in the vicinity may cause polymerization of easily polymerizable substances.
  • An easily polymerizable substance is a substance having a polymerizable functional group.
  • the easily polymerizable substance is not particularly limited as long as it is an easily polymerizable substance that can be purified by distillation.
  • (Meth) acrylic acid or (meth) acrylic acid ester is preferred, and among them, methyl ester of (meth) acrylic acid or (meth) acrylic acid, ethyl ester, n-propynoleesterol, and isopropyl ester are preferable.
  • any known polymerization inhibitor can be used arbitrarily, depending on the type of easily polymerizable substance, the operating conditions of the purification tower 11, and the like. Selected.
  • the first polymerization inhibitor include, for example, hide-mouth quinone, benzoquinone, hydroquinone monomethyl ether, force tecole, 2,4-dimethinole 6-tert-butyl phenol, 2,6-ditertyl butyl Phenols such as 4-methylphenol, N-isopropyl-N'-phenol-para-phenylenediamine, N, N'-diphen-nor-para-phenylenediamine, N, N'-diene Amines such as 2-naphthyl-para-phenylenediamine; N-hydroxyl such as 4-hydroxy 2,2,4,4-tetramethylpiperidine-N-oxyl And phenoxythiazine. These can be used in combination of two or more as necessary.
  • a polymerization inhibitor introduction section 27 for introducing a first polymerization inhibitor is provided in an intermediate section 26 of a purification tower. Since the polymerization inhibitor is introduced into the purification tower 11 from the polymerization inhibitor introduction section 27, the polymerization inhibitor can be present in almost the entire portion of the purification tower 11, and the polymerization of the easily polymerizable substance can be prevented. At the same time, since the polymerization inhibitor introducing section 27 is not provided at the tower top section 15, it is possible to prevent the first polymerization inhibitor from distilling more than necessary from the tower top outlet pipe 16. Therefore, it is possible to prevent the product of the easily polymerizable substance from being colored due to the polymerization inhibitor. In addition, by adding a new polymerization inhibitor to the easily polymerizable substance distilled out of the purification device 10, the concentration of the polymerization inhibitor in the easily polymerizable substance product can be easily made constant, thereby improving the quality. be able to.
  • the polymerization inhibitor introduction section 27 is provided at a position satisfying the above formula (1), polymerization in the purification tower 11 can be prevented and the polymerization inhibitor introduction section 27 is separated from the outlet pipe 16. Distillation of the first polymerization inhibitor from the purification tower 11 more than necessary can be more reliably prevented.
  • the easily polymerizable substance is (meth) acrylic acid or (meth) acrylic acid ester
  • the production amount is large, the effect of suppressing the polymerization and the effect of improving the quality in the purification tower 11 are enormous.
  • the above-described apparatus for purifying an easily polymerizable substance 10 is used.
  • an unpurified easily polymerizable substance is supplied to a purification tower 1 by an easily polymerizable substance supply pipe 12. Introduced into the easily polymerizable substance introduction section 25 of 1.
  • the first polymerization inhibitor is introduced into the polymerization inhibitor introduction section 27 of the purification tower 11 through the polymerization inhibitor supply pipe 13.
  • the first polymerization inhibitor is a solution of an easily polymerizable substance.
  • the first polymerization inhibitor is a solution of an easily polymerizable substance, it can be easily introduced into the purification tower 11.
  • the introduced liquid easily polymerizable substance flows down to the bottom 18 of the purification tower 11, and a part of the easily polymerizable substance reaching the bottom 18 is sent to the reboiler 20 via the bottom outlet pipe 19. Introduced Is heated and vaporized.
  • the easily polymerizable substance vaporized by the reboiler 20 is again introduced into the purification tower 11 through the reintroduction pipe 21 and rises inside the purification tower 11.
  • gas-liquid comes into contact, and mass transfer and heat transfer in gas-liquid are repeated. 5
  • the easily polymerizable substance, which is a low-boiling component, is concentrated.
  • the vapor-like easily polymerizable substance that has reached the tower top 15 is introduced into the condenser 14 via the tower outlet pipe 16, cooled, condensed, and liquefied.
  • a part of the easily polymerizable substance liquefied in the condenser 14 is refluxed to the top 15 through the reflux pipe 17 to flow down the purification tower 11 ⁇ , and liquefied in the condenser 14 ⁇ .
  • the remaining part of the easily polymerizable substance thus obtained is sent to the next step through the next step liquid sending pipe 23 in order to be used as a product.
  • impurities that are high-boiling components are concentrated in the bottom part 18 of the purification tower 11, and these impurities are purified together with some easily polymerizable substances through the bottom outlet pipe 18 and the impurity discharge pipe 22. It is discharged out of the device 10.
  • the easily polymerizable substance discharged from the purification device 1 0, the purpose is to prevent polymerization in during transportation or storage, in which case c it is the addition of a second polymerization inhibitor, the aforementioned purified
  • a different first polymerization inhibitor from the second polymerization inhibitor can be used as the first polymerization inhibitor introduced into the purification tower 11.
  • a polymerization inhibitor suitable for the purpose can be appropriately used.
  • a second polymerization inhibitor added to a product of an easily polymerizable substance may have an insufficient effect of suppressing the polymerization in the purification tower 11. Those having a high suppression effect can be used.
  • the first polymerization inhibitor having a high polymerization inhibitory effect often causes coloring, and as the second polymerization inhibitor, a substance which does not easily color a product of an easily polymerizable substance can be used.
  • the first polymerization inhibitor may be of the same type as the second polymerization inhibitor, but the first polymerization inhibitor may be used as the first polymerization inhibitor. If it is discharged from step 1, it becomes difficult to keep the concentration of the polymerization inhibitor in the product constant, and the quality of the product may deteriorate. It is preferable to distill the first polymerization inhibitor more than necessary from the refining tower even if it is the same. Absent.
  • the purification device 10 since the purification device 10 is used, polymerization of the easily polymerizable substance in the purification tower 11 can be prevented.
  • the first polymerization inhibitor does not distill more than necessary from the purification tower 11, it is possible to prevent the polymerization inhibitor, which causes coloring, from being mixed into the easily polymerizable substance product.
  • the second polymerization inhibitor can be newly added to the purified easily polymerizable substance, the concentration of the polymerization inhibitor in the product of the easily polymerizable substance can be easily made constant. Therefore, the quality of the easily polymerizable substance product can be improved.
  • the present invention will be described more specifically with reference to Examples and Comparative Examples.
  • the embodiment shows one embodiment of the present invention, and does not limit the present invention in any way.
  • the apparatus for purifying easily polymerizable substances shown in FIG. 1 was used.
  • the amount of the polymerization inhibitor was measured by liquid chromatography (quantification limit: 0.5 ppm).
  • Methyl methacrylate (MM A) which is an easily polymerizable substance, was purified using a purification column 11 (10 theoretical plates) having 180 trays and a diameter of 180 O mm.
  • the unpurified MMA used for the purification was synthesized from methacrylic acid and methanol in the presence of a catalyst and hydroquinone, and unreacted methacrylic acid, excess methanol and water were removed in advance.
  • MMA In the purification of MMA, first, under the reduced pressure of 200 hPa, the pressure at the top of the column 15 was not transferred to the 20th tray (counting from the top of the polymerizable substance introduction section 25) counted from the top. Purified MMA was introduced at 8250 L / h. At the same time, a first polymerization inhibitor N- Isopuropi Lou New '-. Hue Nino rate para-Hue two Renjiamin 3 8 mass 0/0 counted from the top of the MM Alpha of 1 0 stage containing trays ( 6.2 L / h was introduced into the polymerization inhibitor introduction section 27).
  • the MMA was allowed to flow down, the MMA was sent to the reboiler 20 from the bottom 18 of the purification tower 11, and MMA vapor was generated in the reboiler 20, and the steam was reintroduced into the purification tower 11 .
  • mass transfer and heat transfer between gas and liquid are repeated, MMA, a low-boiling component, was concentrated at the top 15.
  • the MMA vapor led out through the outlet pipe 16 at the top was introduced into the condenser 14 using water at 4 ° C as a refrigerant, and was condensed.
  • 1000 L / h was returned to the top 15 of the purification tower 11 as a reflux liquid by a reflux pipe 1 ⁇ through a reflux pipe 1 ⁇ , and the remaining liquid was passed through the next-step liquid feed pipe 23. Distilled out of the purification apparatus 10 through the apparatus.
  • MMA was obtained as a distillate from the purification device 10 at a rate of 7950 L / h. No hydroquinone was detected in the distilled MMA.
  • the MMA product was exposed to sunlight for 4 hours, there was no change in appearance, and N-isopropyl-N'-phenyl-/-para-phenylenediamine was not contaminated.
  • Butyl methacrylate (BMA) was purified using a purification column 11 (5.5 theoretical plates) with 70 trays and a diameter of 70 O mm.
  • the unpurified BMA used for the purification was synthesized from ⁇ and butanol in the presence of the catalyst and N-isopropinole ⁇ '-pheninoleparaphenylenediamine, from which excess ⁇ and butanol had been removed in advance. .
  • unpurified BMA was added hourly to the 18th shelf (easy polymerizable substance introduction section 25), counting from the top, under the reduced pressure of 80 hPa at the top of the column at a pressure of 15 hPa. Introduced at 1200 L.
  • 2 first is a polymerization inhibitor, 4-dimethyl one 6 - tertiary butyl and Honoré phenol 0.3 wt 0/0 containing BMA, counted from the top of the 5-stage tray (polymerization inhibitor It was introduced at 5 L / h into the introduction section 27).
  • the BMA was allowed to flow down, the BMA was sent to the reboiler 20 from the bottom 18 of the purification tower 11, and BMA steam was generated in the reboiler 20, and the steam was re-introduced into the purification tower 11. In this way, mass transfer and heat transfer were repeated between gas and liquid, and BMA, which is a low-boiling component, was concentrated at the top 15 of the tower.
  • the BMA vapor led out through the tower top outlet pipe 16 was introduced into a condenser 14 using 4 ° C water as a refrigerant to condense.
  • 150 L / h of the condensed BMA was returned to the top 15 of the purification tower 11 as a reflux liquid by the reflux pipe 17 as a reflux liquid, and the remaining liquid was passed through the next step liquid supply pipe 23. It was distilled out of the purification device 10.
  • BMA could be obtained as a distillate from the purification device 10 at a rate of 950 L / h. 2,4-Dimethyl-6-tert-butylphenol was not detected in the distilled BMA product.
  • the product was exposed to sunlight for 4 hours without any change in appearance.
  • MMA containing 3.8% by weight of N-isopropyl-1-N'-phenylparaphenylenediamine as the first polymerization inhibitor is returned from the condenser 14 to the top 15 of the purification column 11 and refluxed.
  • the MMA was purified in the same manner as in Example 1, except that it was introduced at 6.2 L / h into the reflux liquid in the tube 17.
  • MMA could be obtained as a distillate from the purification device 10 at 7480 L / h. No hydroquinone was detected in the distilled MMA. However, when the MMA product was exposed to sunlight for 1 hour, the colorless and clear liquid turned red, and it was found that N-isopropyl-N'-phenyl-para-phenylenediamine was mixed into the distilled MMA. INDUSTRIAL APPLICABILITY According to the present invention, the polymerization inhibitor introducing section for introducing the first polymerization inhibitor is provided in the middle of the purification tower, and the polymerization inhibitor is introduced into the purification tower from the polymerization inhibitor introducing section.
  • the first polymerization inhibitor Since the first polymerization inhibitor is introduced, the first polymerization inhibitor can be present in almost all parts in the purification tower, and polymerization of the easily polymerizable substance in the purification tower can be prevented. At the same time, since the polymerization inhibitor introduction section is not located at the top of the tower, it is possible to prevent the first polymerization inhibitor from distilling out of the purification tower more than necessary, and to facilitate the polymerization of the polymerization inhibitor, which causes coloring. Can be prevented from being mixed into a product with a chemical substance. Also, by adding a new polymerization inhibitor, the concentration of the polymerization inhibitor in the easily polymerizable substance product can be easily made constant, so that the quality can be improved.

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Abstract

An apparatus (10) and a method for purifying an easily polymerizable substance equipped with a rectifying column (11) for purifying the easily polymerizable substance by continuous distillation thereof, wherein an introduction port for a first polymerization inhibitor (27) is provided in an intermediate portion (26) of the rectifying column (11), preferably at a position such that a theoretical plate number (H2) from the introduction port (27) for the polymerization inhibitor to the top (15) of the column satisfies the formula: 0.1 × H1 ≤ H2 < (H1) wherein (H1) represents the theoretical plate number from an introduction port(25) for the easily polymerizable substance to the top (15) of the column. The apparatus and the method allow the prevention of both the polymerization within the rectifying column and the incorporation of the polymerization inhibitor into a distillate of the rectification, which results in the production of a high quality product.

Description

明細書 易重合性物質の精製装置および精製方法 技術分野 本発明は、 ビニル型重合性単量体などの易重合性物質の精製装置および精製方 法に関する。  TECHNICAL FIELD The present invention relates to an apparatus and a method for purifying an easily polymerizable substance such as a vinyl-type polymerizable monomer.
本出願は、 日本国特許出願 2 0 0 2— 7 9 3 6 9号を基礎としており、 その内 容を本明細書に組み込む。 景技術 ビニル型重合性単量体などの易重合性物質は、 精製塔を用いて蒸留して精製す る際に、 精製塔内で非常に重合しやすいため、 従来から、 精製塔内に各種の重合 防止剤を導入して蒸留精製する方法が提案されている。 例えば、 ハイ ドロキノン や、 フエノール類、 アミン類、 フエノチアジン、 N—ォキシル型化合物などの重 合防止剤を精製塔内に導入する方法が知られており、 さらに上述した重合防止剤 を数種類組み合わせて用いる方法などが提案されている。  This application is based on Japanese Patent Application No. 2002-79369, the contents of which are incorporated herein. BACKGROUND ART When easily polymerizable substances such as vinyl-type polymerizable monomers are purified by distillation in a purification tower, they are very easily polymerized in the purification tower. A method of introducing a polymerization inhibitor to purify by distillation has been proposed. For example, a method is known in which a polymerization inhibitor such as hydroquinone, phenols, amines, phenothiazine, N-oxyl type compound, etc. is introduced into a purification column, and several types of the above-mentioned polymerization inhibitors are used in combination. Methods have been proposed.
重合防止剤を導入する位置としては、 精製塔から排出した易重合性物質の蒸気 を凝縮させる凝縮器、 凝縮させた易重合性物質を精製塔に還流させる配管、 精製 塔の塔頂部などが提案されている。 これらの方法は、 精製塔内の重合防止に対し ては非常に有効であった。  Proposals for introducing the polymerization inhibitor include a condenser that condenses the vapor of the easily polymerizable substance discharged from the purification tower, a pipe that returns the condensed easily polymerizable substance to the purification tower, and the top of the purification tower. Have been. These methods were very effective in preventing polymerization in the purification tower.
しかしながら、 上述したいずれの重合防止剤の導入位置においても、 一部が易 重合性物質とともに精製塔から留出し、 易重合性物質の製品中に重合防止剤が混 入することがあった。 その結果、 重合防止剤が着色の原因となって易重合性物質 の製品を着色させることがあった。 また、 重合防止剤が混入しているために、 易 重合性物質の製品を重合させて重合体とする際の易重合性物質の重合性が変化し て、 安定した重合体を得ることが困難となっていた。 また、 重合防止剤の導入方法としては、 精製塔に導入される未精製の易重合性 物質に重合防止剤を添加する方法が提案されている。 しかしながら、 この方法で は、 重合防止剤の留出を防止できる反面、 精製塔内の塔頂部近傍に重合物が生成 することが観察され、 精製塔内の重合を十分に抑制することができなかった。 ま た、 未精製の易重合性物質を精製塔内に導入する位置に重合防止剤を同時に導入 する方法も考えられるが、 この方法は、 未精製の易重合性物質に重合防止剤を添 加することと実質的に同じであり、 精製塔内での重合を十分に抑制できなかった 発明の開示 However, in any of the above-described positions where the polymerization inhibitor was introduced, a part of the polymerization inhibitor was distilled out of the purification tower together with the easily polymerizable substance, and the polymerization inhibitor was sometimes mixed into the product of the easily polymerizable substance. As a result, the polymerization inhibitor sometimes causes coloring of products of easily polymerizable substances due to coloring. In addition, since the polymerization inhibitor is mixed, the polymerizability of the easily polymerizable substance when a product of the easily polymerizable substance is polymerized into a polymer changes, and it is difficult to obtain a stable polymer. Had become. As a method for introducing a polymerization inhibitor, a method has been proposed in which a polymerization inhibitor is added to an unpurified easily polymerizable substance introduced into a purification tower. However, while this method can prevent the polymerization inhibitor from distilling out, it is observed that a polymer is generated near the top of the purification column, and the polymerization in the purification column cannot be sufficiently suppressed. Was. It is also conceivable to simultaneously introduce a polymerization inhibitor at a position where the unpurified easily polymerizable substance is introduced into the purification tower, but this method adds a polymerization inhibitor to the unpurified easily polymerizable substance. Of the invention, in which polymerization in the purification tower could not be sufficiently suppressed.
本発明は、 前記事情を鑑みてなされたものであり、 易重合性物質を蒸留して精 製する際に、 精製塔内の重合を防止するとともに、 重合防止剤の精製塔からの必 要以上の留出を抑制して品質の高い製品を得ることができる易重合性物質の精製 装置および精製方法を提供することを目的とする。 The present invention has been made in view of the above circumstances, and when distilling and purifying easily polymerizable substances, it is possible to prevent polymerization in the purification column and to remove the polymerization inhibitor from the purification column more than necessary. It is an object of the present invention to provide an apparatus and a method for purifying an easily polymerizable substance, which can obtain a high-quality product by suppressing the distillation of water.
本発明の易重合性物質の精製装置は、 易重合性物質を連続的に蒸留して精製す る精製塔を具備する易重合性物質の精製装置において、 易重合性物質導入部が精 製塔に設けられており、 これとは別に第 1の重合防止剤を精製塔内に導入する重 合防止剤導入部が精製塔の中間部に設けられている。  The apparatus for purifying an easily polymerizable substance according to the present invention is an apparatus for purifying an easily polymerizable substance, comprising: a purification tower for continuously distilling and purifying the easily polymerizable substance, wherein the easy polymerizable substance introduction section includes a purification tower. Separately from this, a polymerization inhibitor introducing section for introducing the first polymerization inhibitor into the purification tower is provided in an intermediate portion of the purification tower.
ここで、 精製塔の中間部とは、 易重合性物質導入部から塔頂部までの部分のこ とである。 また、 易重合性物質導入部とは、 未精製の易重合性物質を精製塔内に 導入する部分のことである。  Here, the intermediate part of the purification tower is a part from the introduction part of the easily polymerizable substance to the top of the tower. The easily polymerizable substance introduction section is a section for introducing an unpurified easily polymerizable substance into a purification tower.
本発明の易重合性物質の精製装置において、 精製塔塔頂部から易重合性物質導 入部までの理論段数 H 1 と精製塔塔頂部から重合防止剤導入部までの理論段数 H 2との関係が下記式 (1 ) を満たす位置に易重合性物質導入部と重合防止剤導入 部が設けられていることが好ましい。  In the apparatus for purifying an easily polymerizable substance of the present invention, the relationship between the theoretical plate number H1 from the top of the purification tower to the introduction section of the easily polymerizable substance and the theoretical plate number H2 from the top of the purification tower to the polymerization inhibitor introduction section is defined as follows. It is preferable that an easily polymerizable substance introduction part and a polymerization inhibitor introduction part are provided at positions satisfying the following formula (1).
0 . 1 X H 1≤H 2 < H 1 ( 1 )  0. 1 X H 1≤H 2 <H 1 (1)
また、 本発明の易重合性物質の精製装置において、 前記易重合性物質が、 (メ タ) アクリル酸または (メタ) アクリル酸エステルであることが好ましい。 また、 本発明の易重合性物質の精製方法は、 易重合性物質導入部が精製塔に設 けられており、 これとは別に重合防止剤導入部が精製塔の中間部に設けられてい る精製塔を使用する易重合性物質の精製方法であって、 易重合性物質導入部から 易重合性物質を連続的に導入し、 重合防止剤導入部から第 1の重合防止剤を精製 塔内に導入する段階を有する。 Further, in the apparatus for purifying an easily polymerizable substance of the present invention, it is preferable that the easily polymerizable substance is (meth) acrylic acid or (meth) acrylate. Further, in the method for purifying an easily polymerizable substance of the present invention, the easily polymerizable substance introduction section is provided in the purification tower, and the polymerization inhibitor introduction section is separately provided in the middle section of the purification tower. A method for purifying an easily polymerizable substance using a purification tower, in which an easily polymerizable substance is continuously introduced from an easily polymerizable substance introduction section, and a first polymerization inhibitor is purified from the polymerization inhibitor introduction section. The step of introducing
本発明の易重合性物質の精製方法において、 精製塔が、 精製塔塔頂部から易重 合性物質導入部までの理論段数 H 1と精製塔塔頂部から重合防止剤導入部までの 理論段数 H 2との関係が下記式 (1 ) を満たす位置に易重合性物質導入部と重合 防止剤導入部が設けられている精製塔であることが好ましい。  In the method for purifying an easily polymerizable substance of the present invention, the purification tower has a theoretical plate number H 1 from the top of the purification tower to the introduction section of the polymerizable substance and a theoretical plate number H from the top of the purification tower to the polymerization inhibitor introduction section H It is preferable that the purification column is provided with an easily polymerizable substance introduction part and a polymerization inhibitor introduction part at a position where the relationship with 2 satisfies the following formula (1).
0 . 1 X H 1 ≤H 2 < H 1 ( 1 )  0. 1 X H 1 ≤H 2 <H 1 (1)
また、 本発明の易重合性物質の精製方法において、 前記易重合性物質が、 (メ タ) アクリル酸または (メタ) アクリル酸エステルであることが好ましい。  In the method for purifying an easily polymerizable substance of the present invention, it is preferable that the easily polymerizable substance is (meth) acrylic acid or (meth) acrylate.
本発明の易重合性物質の精製方法は、 塔頂から取得した精製された易重合性物 質に第 1の重合防止剤と異なる第 2の重合防止剤を添加する段階を更に有するこ とができる。 図面の簡単な説明 図 1は本発明の易重合性物質の精製装置の一例を示す模式図である。 発明を実施するための最良の形態 以下、 本発明について詳細に述べる。  The method for purifying an easily polymerizable substance of the present invention may further include a step of adding a second polymerization inhibitor different from the first polymerization inhibitor to the purified easily polymerizable substance obtained from the top of the tower. it can. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic view showing an example of the apparatus for purifying an easily polymerizable substance of the present invention. BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail.
本発明の易重合性物質の精製装置を、 図 1を参照しながら説明する。 この易重 合性物質の精製装置 1 0は、 易重合性物質を連続的に蒸留して精製する精製塔 1 1 と、 未精製の易重合性物質を精製塔 1 1に供給する易重合性物質供給管 1 2と、 第 1の重合防止剤を精製塔 1 1に供給する重合防止剤供給管 1 3と、 精製塔 1 1 から排出された易重合性物質蒸気を凝縮する凝縮器 1 4とを有して概略構成され る。 The apparatus for purifying an easily polymerizable substance of the present invention will be described with reference to FIG. The apparatus for purifying easily polymerizable substances 10 includes a purification tower 11 for continuously distilling and purifying easily polymerizable substances, and an easily polymerizable substance for supplying unpurified easily polymerizable substances to the purification tower 11. Substance supply pipe 12, polymerization inhibitor supply pipe 13 that supplies the first polymerization inhibitor to purification tower 11, and condenser 1 4 that condenses the easily polymerizable substance vapor discharged from purification tower 11 And has a schematic configuration You.
さらに、 精製塔 1 1には、 蒸気化した易重合性物質を塔頂部 1 5から導出させ る塔頂部導出管 1 6と、 凝縮器 1 4から塔頂部 1 5に還流させる還流管 1 7と、 精製塔 1 1の底部 1 8から易重合性物質を導出させる底部導出管 1 9と、 底部導 出管 1 9を介して送られた易重合性物質の一部を加熱するリボイラ 2 0と、 リボ イラ 2 0で発生した易重合性物質の蒸気を精製塔 1 1内に再導入する再導入管 2 1 と、 底部導出管 1 8を介して送られてきた易重合性物質の残りの一部を排出す る不純物排出管 2 2とが取り付けられている。  Further, the purification tower 11 has a tower top outlet pipe 16 for discharging the vaporized easily polymerizable substance from the tower top 15, and a reflux pipe 17 for refluxing from the condenser 14 to the tower top 15. A bottom outlet pipe 19 for drawing out the easily polymerizable substance from the bottom 18 of the purification tower 11; and a reboiler 20 for heating a part of the easily polymerizable substance sent through the bottom guide pipe 19. The reintroduction pipe 21 for reintroducing the vapor of the easily polymerizable substance generated in the reboiler 20 into the purification tower 11 and the remaining of the easily polymerizable substance sent through the bottom outlet pipe 18 An impurity discharge pipe 22 for discharging a part is attached.
また、 凝縮器 1 4には、 次工程に送液する次工程送液管 2 3が取り付けられて いる。  Further, the condenser 14 is provided with a next-step liquid sending pipe 23 for sending the liquid to the next step.
精製塔 1 1としては、 易重合性物質を蒸留して精製できるものであれば特に制 限されず、 例えば、 棚段塔型精製塔、 充填塔型精製塔などが使用される。 また、 精製塔 1 1は、 減圧可能とすることができる。  The purification column 11 is not particularly limited as long as it can purify the easily polymerizable substance by distillation. For example, a tray column type purification column, a packed column type purification column, and the like are used. Further, the pressure in the purification tower 11 can be reduced.
精製塔 1 1の適切な位置に易重合性物質供給管 1 2が接続された易重合性物質 導入部 2 5が設けられる。 易重合性物質導入部 2 5の位置は、 易重合性物質中の 分離したい不純物の種類や量により易重合性物質導入部 2 5から塔頂部 1 5まで の理論段数 H Iを求め、 決定することができる。 すなわち、 精製塔 1 1には、 易 重合性物質導入部 2 5から塔頂部 1 5までの間に、 不純物を分離するのに必要な 理論段数 H 1を有する棚段もしくは充填層が設けられる。  An easily polymerizable substance introduction part 25 to which an easily polymerizable substance supply pipe 12 is connected is provided at an appropriate position of the purification tower 11. The position of the easily polymerizable substance introduction section 25 should be determined by calculating the theoretical number of plates HI from the easily polymerizable substance introduction section 25 to the tower top 15 based on the type and amount of impurities to be separated in the easily polymerizable substance. Can be. That is, the purification tower 11 is provided with a tray or a packed bed having a theoretical plate number H 1 required for separating impurities between the easily polymerizable substance introduction section 25 and the tower top 15.
この精製塔 1 1には、 精製塔 1 1内での易重合性物質の重合を防止することを 目的として、 その中間部 2 6に、 重合防止剤供給管 1 3が接続され、 第 1の重合 防止剤を精製塔 1 1内に導入する重合防止剤導入部 2 7が設けられる。 重合防止 剤導入部 2 7が設けられる位置は、 精製塔 1 1の性能、 処理する易重合性物質の 液物性、 精製塔 1 1の上下方向における重合防止剤分布のバランスなどにより、 精製塔 1 1の中間部 2 6の範囲内で適宜決定されるが、 重合防止剤導入部 2 7か ら塔頂部 1 5までの理論段数 H 2が下記式 (1 ) を満たすような位置であること が好ましい。  In order to prevent the polymerization of the easily polymerizable substance in the purification tower 11, a polymerization inhibitor supply pipe 13 is connected to an intermediate portion 26 of the purification tower 11, A polymerization inhibitor introduction section 27 for introducing the polymerization inhibitor into the purification tower 11 is provided. The position where the polymerization inhibitor introduction section 27 is provided depends on the performance of the purification tower 11, the liquid properties of the easily polymerizable substance to be treated, the distribution of the polymerization inhibitor in the vertical direction of the purification tower 11, and the like. It is appropriately determined within the range of the intermediate part 26 of 1, but it is necessary that the theoretical plate number H 2 from the polymerization inhibitor introduction part 27 to the tower top part 15 satisfies the following formula (1). preferable.
0 . 1 xH 1≤H 2 < H 1 ( 1 ) (ここで、 H Iは、 易重合性物質導入部 2 5から精製塔 1 1の塔頂部 1 5までの 理論段数を示す。 ) 0. 1 xH 1≤H 2 <H 1 (1) (Here, HI indicates the number of theoretical plates from the easily polymerizable substance introduction section 25 to the top section 15 of the purification tower 11.)
特に、 重合防止剤導入部 2 7は、 重合防止剤導入部 2 7から精製塔塔頂部 1 5 までの理論段数 H 2が下記式 (2 ) を満たすような位置に設けられたことが好ま しい。  In particular, the polymerization inhibitor introduction section 27 is preferably provided at a position where the theoretical plate number H 2 from the polymerization inhibitor introduction section 27 to the top 15 of the purification tower satisfies the following formula (2). .
0 . 2 xH 1≤H 2≤ 0 . 7 xH 1 ( 2 )  0.2 xH 1≤H 2≤ 0.7 .x x 1 (2)
なお、 0 . 1 xH 1 > H 2を満たす位置に、 重合防止剤導入部 2 7を設けた場 合には、 重合防止剤導入部 2 7から塔頂部 1 5までの理論段数が少なく、 第 1の 重合防止剤が精製塔 1 1から排出されることがあり、 H 1≤H 2を満たす位置 When the polymerization inhibitor introduction section 27 is provided at a position satisfying 0.1 x H 1> H2, the number of theoretical plates from the polymerization inhibitor introduction section 27 to the tower top 15 is small, and 1 The polymerization inhibitor may be discharged from the purification tower 1 1 and satisfies H 1 ≤ H 2
(すなわち、 易重合性物質導入部 2 5と同じ高さの位置またはそれより低い位 置) に、 重合防止剤導入部 2 7を設けた場合には、 精製塔 1 1内の塔頂部 1 5近 傍における重合防止剤の量が不足し、 易重合性物質が重合することがある。 When the polymerization inhibitor introduction section 27 is provided at the same level as the easily polymerizable substance introduction section 25 or at a position lower than the same, the top section 15 in the purification column 11 Insufficient amount of polymerization inhibitor in the vicinity may cause polymerization of easily polymerizable substances.
易重合性物質とは、 重合性の官能基を有する物質のことである。 易重合性物質 と しては、 蒸留により精製できる易重合性物質であれば特に制限されないが、 An easily polymerizable substance is a substance having a polymerizable functional group. The easily polymerizable substance is not particularly limited as long as it is an easily polymerizable substance that can be purified by distillation.
(メタ) アク リル酸または (メタ) アク リル酸エステルが好ましく、 それらの中 でも、 (メタ) アク リル酸または (メタ) アク リル酸のメチルエステル、 ェチル エステル、 n—プロピノレエステノレ、 イソプロピノレエステノレ、 n一ブチルエステノレ、 イ ソブチルエステノレ、 t一ブチルエステル、 2 —ェチルへキシルエステル、 シク 口へキシルエステル、 N , N ' -ジメチルァミノェチノレエステルがさらに好ましい c 精製塔 1 1内に供給される第 1の重合防止剤としては、 公知の重合防止剤など を任意に使用することができ、 易重合性物質の種類、 精製塔 1 1の運転条件など により適宜選択される。 第 1の重合防止剤の具体例としては、 例えば、 ハイ ド口 キノン、 ベンゾキノン、 ハイ ドロキノンモノメチルエーテル、 力テコール、 2 , 4ージメチノレー 6—ターシャ リーブチルフエノーノレ、 2 , 6—ジターシャ リーブ チル一 4—メチルフエノール等のフエノール類、 N—イソプロピル一 N'—フエ- ノレ一パラ一フエ二レンジァミン、 N , N '—ジフエ-ノレ一パラ一フエ二レンジアミ ン、 N , N '—ジ一 2—ナフチル一パラーフエ二レンジァミン等のアミン類、 4一 ヒ ドロキシー 2 , 2 , 4 , 4—テ トラメチルピペリ ジン一 N—ォキシル等の N— ォキシル型化合物、 フエノチアジン等を挙げることができる。 これらは、 必要に 応じて 2種類以上組み合わせて使用することもできる。 (Meth) acrylic acid or (meth) acrylic acid ester is preferred, and among them, methyl ester of (meth) acrylic acid or (meth) acrylic acid, ethyl ester, n-propynoleesterol, and isopropyl ester are preferable. Noreesutenore, n one-butyl ester Honoré, Lee Seo-butyl ester Honoré, t one-butyl ester, 2 - Echiru hexyl ester, cyclohexyl ester to consequent opening, n, n '- dimethyl § Mino E Chino les esters are more preferred c As the first polymerization inhibitor to be supplied into the purification tower 11, any known polymerization inhibitor can be used arbitrarily, depending on the type of easily polymerizable substance, the operating conditions of the purification tower 11, and the like. Selected. Specific examples of the first polymerization inhibitor include, for example, hide-mouth quinone, benzoquinone, hydroquinone monomethyl ether, force tecole, 2,4-dimethinole 6-tert-butyl phenol, 2,6-ditertyl butyl Phenols such as 4-methylphenol, N-isopropyl-N'-phenol-para-phenylenediamine, N, N'-diphen-nor-para-phenylenediamine, N, N'-diene Amines such as 2-naphthyl-para-phenylenediamine; N-hydroxyl such as 4-hydroxy 2,2,4,4-tetramethylpiperidine-N-oxyl And phenoxythiazine. These can be used in combination of two or more as necessary.
上述した易重合性物質の精製装置では、 第 1の重合防止剤を導入する重合防止 剤導入部 2 7が、 精製塔の中間部 2 6に設けられており、 第 1の重合防止剤を、 重合防止剤導入部 2 7から精製塔 1 1内に導入するので、 精製塔 1 1内の殆どの 部分に重合防止剤を存在させることができ、 易重合性物質の重合を防止できる。 それとともに、 重合防止剤導入部 2 7は、 塔頂部 1 5にはないので、 塔頂部導出 管 1 6から第 1の重合防止剤が必要以上に留出することを抑制できる。 そのため、 重合防止剤が原因となって易重合性物質の製品を着色させることを防止できる。 また、 精製装置 1 0から留出した易重合性物質に新たに重合防止剤を添加するこ とで、 易重合性物質製品中の重合防止剤濃度を容易に一定にできるので、 品質を 向上させることができる。  In the apparatus for purifying an easily polymerizable substance described above, a polymerization inhibitor introduction section 27 for introducing a first polymerization inhibitor is provided in an intermediate section 26 of a purification tower. Since the polymerization inhibitor is introduced into the purification tower 11 from the polymerization inhibitor introduction section 27, the polymerization inhibitor can be present in almost the entire portion of the purification tower 11, and the polymerization of the easily polymerizable substance can be prevented. At the same time, since the polymerization inhibitor introducing section 27 is not provided at the tower top section 15, it is possible to prevent the first polymerization inhibitor from distilling more than necessary from the tower top outlet pipe 16. Therefore, it is possible to prevent the product of the easily polymerizable substance from being colored due to the polymerization inhibitor. In addition, by adding a new polymerization inhibitor to the easily polymerizable substance distilled out of the purification device 10, the concentration of the polymerization inhibitor in the easily polymerizable substance product can be easily made constant, thereby improving the quality. be able to.
また、 重合防止剤導入部 2 7が、 上記式 ( 1 ) を満たす位置に設けられていれ ば、 精製塔 1 1内での重合を防止できるとともに、 導出管 1 6から離れているの で、 第 1の重合防止剤が精製塔 1 1から必要以上に留出することをより確実に防 止できる。  If the polymerization inhibitor introduction section 27 is provided at a position satisfying the above formula (1), polymerization in the purification tower 11 can be prevented and the polymerization inhibitor introduction section 27 is separated from the outlet pipe 16. Distillation of the first polymerization inhibitor from the purification tower 11 more than necessary can be more reliably prevented.
また、 易重合性物質が (メタ) アクリル酸または (メタ) アクリル酸エステル の場合には、 生産量が多いため、 精製塔 1 1内での重合抑制効果および品質向上 効果が絶大となる。  Further, when the easily polymerizable substance is (meth) acrylic acid or (meth) acrylic acid ester, since the production amount is large, the effect of suppressing the polymerization and the effect of improving the quality in the purification tower 11 are enormous.
次に、 本発明の易重合性物質の精製方法の一例について説明する。 この易重合 性物質の精製方法では、 上述した易重合性物質の精製装置 1 0が使用されており、 まず、 未精製の易重合性物質を易重合性物質供給管 1 2によって、 精製塔 1 1の 易重合性物質導入部 2 5に導入する。 それとともに、 第 1の重合防止剤を重合防 止剤供給管 1 3によって、 精製塔 1 1の重合防止剤導入部 2 7に導入する。 その 際、 第 1の重合防止剤を易重合性物質の溶液とすることが好ましい。 第 1の重合 防止剤を易重合性物質の溶液とすると、 精製塔 1 1内に容易に導入できる。  Next, an example of the method for purifying the easily polymerizable substance of the present invention will be described. In this method for purifying an easily polymerizable substance, the above-described apparatus for purifying an easily polymerizable substance 10 is used. First, an unpurified easily polymerizable substance is supplied to a purification tower 1 by an easily polymerizable substance supply pipe 12. Introduced into the easily polymerizable substance introduction section 25 of 1. At the same time, the first polymerization inhibitor is introduced into the polymerization inhibitor introduction section 27 of the purification tower 11 through the polymerization inhibitor supply pipe 13. At that time, it is preferable that the first polymerization inhibitor is a solution of an easily polymerizable substance. When the first polymerization inhibitor is a solution of an easily polymerizable substance, it can be easily introduced into the purification tower 11.
導入された液状の易重合性物質は、 精製塔 1 1の底部 1 8へと流下し、 底部 1 8に達した易重合性物質の一部は底部導出管 1 9を介してリボイラ 2 0に導入さ れ、 加熱されて蒸気化される。 次いで、 リボイラ 2 0によって蒸気化した易重合 性物質は、 再導入管 2 1を介して再び精製塔 1 1内に導入され、 精製塔 1 1内を 上昇する。 このような、 液状易重合性物質の流下および蒸気状易重合性物質の上 昇に伴って、 気液が接触し、 気液での物質移動と熱移動とが繰り返されることで、 塔頂部 1 5に低沸点成分である易重合性物質が濃縮される。 The introduced liquid easily polymerizable substance flows down to the bottom 18 of the purification tower 11, and a part of the easily polymerizable substance reaching the bottom 18 is sent to the reboiler 20 via the bottom outlet pipe 19. Introduced Is heated and vaporized. Next, the easily polymerizable substance vaporized by the reboiler 20 is again introduced into the purification tower 11 through the reintroduction pipe 21 and rises inside the purification tower 11. As the liquid polymerizable substance flows down and the vapor-like polymerizable substance rises in this manner, gas-liquid comes into contact, and mass transfer and heat transfer in gas-liquid are repeated. 5, the easily polymerizable substance, which is a low-boiling component, is concentrated.
次いで、 塔頂部 1 5に達した蒸気状の易重合性物質を、 塔頂部導出管 1 6を介 して凝縮器 1 4内に導入し、 冷却し、 凝縮して液化する。 次いで、 凝縮器 1 4で 液化された易重合性物質の一部を、 還流管 1 7を介して塔頂部 1 5に還流させて 精製塔 1 1內を流下させるとともに、 凝縮器 1 4で液化された易重合性物質の残 りの一部を、 製品とするために、 次工程送液管 2 3によって次工程に送液する。 一方 精製塔 1 1の底部 1 8には、 高沸点成分である不純物が濃縮されおり、 この不純物は一部の易重合性物質とともに、 底部導出管 1 8および不純物排出管 2 2を介して精製装置 1 0外に排出される。  Next, the vapor-like easily polymerizable substance that has reached the tower top 15 is introduced into the condenser 14 via the tower outlet pipe 16, cooled, condensed, and liquefied. Next, a part of the easily polymerizable substance liquefied in the condenser 14 is refluxed to the top 15 through the reflux pipe 17 to flow down the purification tower 11 內, and liquefied in the condenser 14 內. The remaining part of the easily polymerizable substance thus obtained is sent to the next step through the next step liquid sending pipe 23 in order to be used as a product. On the other hand, impurities that are high-boiling components are concentrated in the bottom part 18 of the purification tower 11, and these impurities are purified together with some easily polymerizable substances through the bottom outlet pipe 18 and the impurity discharge pipe 22. It is discharged out of the device 10.
さらに、 精製装置 1 0から排出された易重合性物質に、 輸送中あるいは貯蔵中 の重合を防止させることを目的として、 第 2の重合防止剤を添加することがある c その場合、 上述した精製方法では、 精製塔 1 1内に導入する第 1の重合防止剤に, 第 2の重合防止剤と異なるものを用いることができる。 第 1の重合防止剤と第 2 の重合防止剤とが異なるものであれば、 目的に応じた重合防止剤を適切に使用す ることができる。 例えば、 易重合性物質の製品に添加される第 2の重合防止剤で は精製塔 1 1内の重合を抑制する効果が不十分なことがあるので、 第 1の重合防 止剤として、 重合抑制効果の高いものを使用することができる。 また、 重合抑制 効果の高い第 1の重合防止剤は着色の原因となるものが多く、 第 2の重合防止剤 として、 易重合性物質の製品を着色させにくいものを使用することができる。 Further, the easily polymerizable substance discharged from the purification device 1 0, the purpose is to prevent polymerization in during transportation or storage, in which case c it is the addition of a second polymerization inhibitor, the aforementioned purified In the method, a different first polymerization inhibitor from the second polymerization inhibitor can be used as the first polymerization inhibitor introduced into the purification tower 11. If the first polymerization inhibitor and the second polymerization inhibitor are different, a polymerization inhibitor suitable for the purpose can be appropriately used. For example, a second polymerization inhibitor added to a product of an easily polymerizable substance may have an insufficient effect of suppressing the polymerization in the purification tower 11. Those having a high suppression effect can be used. In addition, the first polymerization inhibitor having a high polymerization inhibitory effect often causes coloring, and as the second polymerization inhibitor, a substance which does not easily color a product of an easily polymerizable substance can be used.
なお、 精製塔 1 1内の重合を抑制できれば、 第 1の重合防止剤に第 2の重合防 止剤と同じ種類のものを使用してもよいが、 第 1の重合防止剤が精製塔 1 1から 排出されると、 製品中の重合防止剤濃度を一定とするのが困難になり、 製品の品 質が低下するおそれがあるので、 第 1の重合防止剤と第 2の重合防止剤が同じも のであっても第 1の重合防止剤を精製塔から必要以上に留出することは好ましく ない。 If the polymerization in the purification tower 11 can be suppressed, the first polymerization inhibitor may be of the same type as the second polymerization inhibitor, but the first polymerization inhibitor may be used as the first polymerization inhibitor. If it is discharged from step 1, it becomes difficult to keep the concentration of the polymerization inhibitor in the product constant, and the quality of the product may deteriorate. It is preferable to distill the first polymerization inhibitor more than necessary from the refining tower even if it is the same. Absent.
上述した易重合性物質の精製方法では、 精製装置 1 0を用いるので、 精製塔 1 1内での易重合性物質の重合を防止できる。 また、 第 1の重合防止剤は精製塔 1 1から必要以上に留出しないので、 着色の原因となる重合防止剤の易重合性物質 製品への混入を抑制できる。 また、 精製した易重合性物質に新たに第 2の重合防 止剤を添加することができるので、 易重合性物質の製品中の重合防止剤濃度を容 易に一定にできる。 したがって、 易重合性物質の製品の品質を向'上させることが できる。  In the above-described method for purifying an easily polymerizable substance, since the purification device 10 is used, polymerization of the easily polymerizable substance in the purification tower 11 can be prevented. In addition, since the first polymerization inhibitor does not distill more than necessary from the purification tower 11, it is possible to prevent the polymerization inhibitor, which causes coloring, from being mixed into the easily polymerizable substance product. In addition, since the second polymerization inhibitor can be newly added to the purified easily polymerizable substance, the concentration of the polymerization inhibitor in the product of the easily polymerizable substance can be easily made constant. Therefore, the quality of the easily polymerizable substance product can be improved.
実施例 : Example :
以下、 実施例および比較例により本発明をより具体的に説明する。 ただし、 実 施例は本発明の一態様を示すものであって、 本発明を何ら制限するものではない。 なお、 以下の実施例および比較例において、 図 1の易重合性物質の精製装置を 使用した。 また、 重合防止剤の量は、 液体ク口マトグラフィ (定量限界 0 . 5 p p m) により測定した。  Hereinafter, the present invention will be described more specifically with reference to Examples and Comparative Examples. However, the embodiment shows one embodiment of the present invention, and does not limit the present invention in any way. In the following Examples and Comparative Examples, the apparatus for purifying easily polymerizable substances shown in FIG. 1 was used. The amount of the polymerization inhibitor was measured by liquid chromatography (quantification limit: 0.5 ppm).
(実施例 1 )  (Example 1)
塔径 1 8 0 O m mで 3 0段の棚段を持つ精製塔 1 1 (理論段数 1 0段) を用い て、 易重合性物質であるメタクリル酸メチル (MM A ) の精製を行った。 なお、 精製に供した未精製 MMAは、 触媒とハイ ドロキノンの共存下、 メタクリル酸と メタノールより合成し、 あらかじめ未反応のメタクリル酸と過剰のメタノール、 および水を取り除いたものである。  Methyl methacrylate (MM A), which is an easily polymerizable substance, was purified using a purification column 11 (10 theoretical plates) having 180 trays and a diameter of 180 O mm. The unpurified MMA used for the purification was synthesized from methacrylic acid and methanol in the presence of a catalyst and hydroquinone, and unreacted methacrylic acid, excess methanol and water were removed in advance.
この MM Aの精製では、 まず、 塔頂部 1 5の圧力が 2 0 0 h P aの減圧条件下、 上から数えて 2 0段目の棚段 (易重合性物質導入部 2 5 ) に未精製 MM Aを毎時 8 2 5 0 Lで導入した。 それとともに、 第 1の重合防止剤である N—ィソプロピ ルー Ν '—フエニノレーパラーフエ二レンジァミンを 3 . 8質量0 /0含有する MM Αを 上から数えて 1 0段目の棚段 (重合防止剤導入部 2 7 ) に毎時 6 . 2 Lで導入し た。 そして、 MM Aを流下させ、 精製塔 1 1の底部 1 8から MM Aをリボイラ 2 0に送り、 リボイラ 2 0で MM Aの蒸気を発生させ、 その蒸気を精製塔 1 1内に 再導入した。 このよ うにして、 気液間で物質移動と熱移動とを繰り返させて、 塔 頂部 1 5に低沸点成分である MM Aを濃縮させた。 In the purification of MMA, first, under the reduced pressure of 200 hPa, the pressure at the top of the column 15 was not transferred to the 20th tray (counting from the top of the polymerizable substance introduction section 25) counted from the top. Purified MMA was introduced at 8250 L / h. At the same time, a first polymerization inhibitor N- Isopuropi Lou New '-. Hue Nino rate para-Hue two Renjiamin 3 8 mass 0/0 counted from the top of the MM Alpha of 1 0 stage containing trays ( 6.2 L / h was introduced into the polymerization inhibitor introduction section 27). Then, the MMA was allowed to flow down, the MMA was sent to the reboiler 20 from the bottom 18 of the purification tower 11, and MMA vapor was generated in the reboiler 20, and the steam was reintroduced into the purification tower 11 . In this way, mass transfer and heat transfer between gas and liquid are repeated, MMA, a low-boiling component, was concentrated at the top 15.
次いで、 塔頂部導出管 1 6を介して導出された MMA蒸気を、 冷媒として 4°C の水を用いた凝縮器 1 4に導入して凝縮した。 次いで、 凝縮された MMAの内、 毎時 1 0 0 0 0 Lを還流管 1 Ίによって還流液として精製塔 1 1の塔頂部 1 5に 戻し、 残りの液を、 次工程送液管 2 3を介して精製装置 1 0外に留出させた。  Next, the MMA vapor led out through the outlet pipe 16 at the top was introduced into the condenser 14 using water at 4 ° C as a refrigerant, and was condensed. Next, of the condensed MMA, 1000 L / h was returned to the top 15 of the purification tower 11 as a reflux liquid by a reflux pipe 1 Ί through a reflux pipe 1 、, and the remaining liquid was passed through the next-step liquid feed pipe 23. Distilled out of the purification apparatus 10 through the apparatus.
その結果、 精製装置 1 0から留出液として MMAを毎時 7 9 5 0 Lで得ること ができた。 留出した MMA中にはハイ ドロキノンは検出されなかった。 また、 M MA製品を日光に 4時間暴露したが、 外観に変化はなく、 N—イソプロピル一 N' 一フェニ^/—パラ一フエ二レンジァミンは混入していなかった。  As a result, MMA was obtained as a distillate from the purification device 10 at a rate of 7950 L / h. No hydroquinone was detected in the distilled MMA. When the MMA product was exposed to sunlight for 4 hours, there was no change in appearance, and N-isopropyl-N'-phenyl-/-para-phenylenediamine was not contaminated.
(実施例 2)  (Example 2)
塔径 7 0 O mmで 2 0段の棚段を持つ精製塔 1 1 (理論段数 5. 5段) を用い て、 メタク リル酸ブチル (BMA) の精製を行った。 なお精製に供した未精製 B MAは、 触媒と N—ィ ソプロピノレー Ν'—フエニノレーパラーフエ二レンジァミンの 共存下、 ΜΜΑとブタノールより合成し、 あらかじめ過剰の ΜΜΑとブタノール を取り除いたものである。  Butyl methacrylate (BMA) was purified using a purification column 11 (5.5 theoretical plates) with 70 trays and a diameter of 70 O mm. The unpurified BMA used for the purification was synthesized from ΜΜΑ and butanol in the presence of the catalyst and N-isopropinole Ν'-pheninoleparaphenylenediamine, from which excess ΜΜΑ and butanol had been removed in advance. .
この ΒΜΑの精製では、 塔頂部 1 5の圧力が 8 0 h P aの減圧条件下、 上から 数えて 1 8段目の棚段 (易重合性物質導入部 2 5 ) に未精製 BMAを毎時 1 2 0 0 Lで導入した。 それとともに、 第 1の重合防止剤である 2 , 4—ジメチル一 6 —ターシャ リーブチノレフェノールを 0. 3重量0 /0含む BMAを、 上から数えて 5 段目の棚段 (重合防止剤導入部 2 7) に、 毎時 5 Lで導入した。 そして、 BMA を流下させ、 精製塔 1 1の底部 1 8から BMAをリボイラ 2 0に送り、 リボイラ 2 0で BMAの蒸気を発生させ、 その蒸気を精製塔 1 1内に再導入した。 このよ うにして、 気液間で物質移動と熱移動とを繰り返させて、 塔頂部 1 5に低沸点成 分である BM Aを濃縮させた。 In this purification process, unpurified BMA was added hourly to the 18th shelf (easy polymerizable substance introduction section 25), counting from the top, under the reduced pressure of 80 hPa at the top of the column at a pressure of 15 hPa. Introduced at 1200 L. At the same time, 2 first is a polymerization inhibitor, 4-dimethyl one 6 - tertiary butyl and Honoré phenol 0.3 wt 0/0 containing BMA, counted from the top of the 5-stage tray (polymerization inhibitor It was introduced at 5 L / h into the introduction section 27). Then, the BMA was allowed to flow down, the BMA was sent to the reboiler 20 from the bottom 18 of the purification tower 11, and BMA steam was generated in the reboiler 20, and the steam was re-introduced into the purification tower 11. In this way, mass transfer and heat transfer were repeated between gas and liquid, and BMA, which is a low-boiling component, was concentrated at the top 15 of the tower.
次いで、 塔頂部導出管 1 6を介して導出させた BMA蒸気を、 冷媒として 4°C の水を用いた凝縮器 1 4に導入して凝縮した。 次いで、 凝縮された BMAの内、 毎時 1 5 0 Lを還流管 1 7によって還流液として精製塔 1 1の塔頂部 1 5に戻し、 残りの液を、 次工程送液管 2 3を介して精製装置 1 0外に留出させた。 その結果、 精製装置 1 0から留出液として B MAを毎時 9 5 0 Lで得ることが できた。 留出した B M A製品中には 2 , 4—ジメチルー 6 —ターシャリーブチル フエノールは検出されなかった。 また、 製品を日光に 4時間暴露したが、 外観に 変化はなかった。 Next, the BMA vapor led out through the tower top outlet pipe 16 was introduced into a condenser 14 using 4 ° C water as a refrigerant to condense. Next, 150 L / h of the condensed BMA was returned to the top 15 of the purification tower 11 as a reflux liquid by the reflux pipe 17 as a reflux liquid, and the remaining liquid was passed through the next step liquid supply pipe 23. It was distilled out of the purification device 10. As a result, BMA could be obtained as a distillate from the purification device 10 at a rate of 950 L / h. 2,4-Dimethyl-6-tert-butylphenol was not detected in the distilled BMA product. Also, the product was exposed to sunlight for 4 hours without any change in appearance.
(比較例 1 )  (Comparative Example 1)
第 1の重合防止剤として N—イ ソプロピル一 N '—フエ二ルーパラーフエ二レン ジァミンを 3 . 8重量%含有するMM Aを、 凝縮器 1 4から精製塔 1 1の塔頂部 1 5に戻す還流管 1 7の還流液の中に毎時 6 . 2 Lで導入した以外は、 実施例 1 と同じ方法で MM Aを精製した。  MMA containing 3.8% by weight of N-isopropyl-1-N'-phenylparaphenylenediamine as the first polymerization inhibitor is returned from the condenser 14 to the top 15 of the purification column 11 and refluxed. The MMA was purified in the same manner as in Example 1, except that it was introduced at 6.2 L / h into the reflux liquid in the tube 17.
その結果、 精製装置 1 0から留出液として MMAを毎時 7 4 8 0 Lで得ること ができた。 留出した MM A中にはハイ ドロキノンは検出されなかった。 しかし、 MM A製品を日光に 1時間暴露したところ、 無色透明の液が赤く着色し、 留出し た MMA中に N—ィソプロピル一 N'—フエニル一パラーフエ二レンジァミンが混 入したことが判明した。 産業上の利用可能性 本発明によれば、 第 1の重合防止剤を導入する重合防止剤導入部が、 精製塔の 中間部に設けられており、 その重合防止剤導入部から精製塔内に第 1の重合防止 剤を導入するので、 精製塔内の殆どの部分に第 1の重合防止剤を存在させること ができ、 精製塔内での易重合性物質の重合を防止できる。 それとともに、 重合防 止剤導入部は、 塔頂部にはないので、 第 1の重合防止剤を精製塔から必要以上に 留出することを抑制でき、 着色の原因となる重合防止剤の易重合性物質製品への 混入を防止できる。 また、 新たに重合防止剤を添加することで、 易重合性物質製 品中の重合防止剤濃度を容易に一定にできるので、 品質を向上させることができ る。  As a result, MMA could be obtained as a distillate from the purification device 10 at 7480 L / h. No hydroquinone was detected in the distilled MMA. However, when the MMA product was exposed to sunlight for 1 hour, the colorless and clear liquid turned red, and it was found that N-isopropyl-N'-phenyl-para-phenylenediamine was mixed into the distilled MMA. INDUSTRIAL APPLICABILITY According to the present invention, the polymerization inhibitor introducing section for introducing the first polymerization inhibitor is provided in the middle of the purification tower, and the polymerization inhibitor is introduced into the purification tower from the polymerization inhibitor introducing section. Since the first polymerization inhibitor is introduced, the first polymerization inhibitor can be present in almost all parts in the purification tower, and polymerization of the easily polymerizable substance in the purification tower can be prevented. At the same time, since the polymerization inhibitor introduction section is not located at the top of the tower, it is possible to prevent the first polymerization inhibitor from distilling out of the purification tower more than necessary, and to facilitate the polymerization of the polymerization inhibitor, which causes coloring. Can be prevented from being mixed into a product with a chemical substance. Also, by adding a new polymerization inhibitor, the concentration of the polymerization inhibitor in the easily polymerizable substance product can be easily made constant, so that the quality can be improved.

Claims

請求の範囲 The scope of the claims
1 . 易重合性物質を連続的に蒸留して精製する精製塔を具備する易重合性物質 の精製装置において、 易重合性物質導入部が精製塔に設けられており、 これとは 別に第 1の重合防止剤を精製塔内に導入する重合防止剤導入部が精製塔の中間部 に設けられている易重合性物質の精製装置。 1. In an apparatus for purifying an easily polymerizable substance having a purification tower for continuously distilling and purifying the easily polymerizable substance, an easy polymerizable substance introduction section is provided in the purification tower. An apparatus for purifying easily polymerizable substances, wherein a polymerization inhibitor introduction section for introducing the polymerization inhibitor into the purification tower is provided in an intermediate portion of the purification tower.
2 . 請求項 1に記載の易重合性物質の精製装置であって、 精製塔塔頂部から易 重合性物質導入部までの理論段数 H 1と精製塔塔頂部から重合防止剤導入部まで の理論段数 H 2との関係が下記式 (1 ) を満たす位置に易重合性物質導入部と重 合防止剤導入部が設けられている易重合性物質の精製装置。 2. The apparatus for purifying an easily polymerizable substance according to claim 1, wherein the number of theoretical stages H1 from the top of the purification tower to the introduction section of the easily polymerizable substance and the theory from the top of the purification tower to the introduction section of the polymerization inhibitor. An apparatus for purifying an easily polymerizable substance, wherein an easily polymerizable substance introduction section and a polymerization inhibitor introduction section are provided at positions where the relationship with the number of stages H2 satisfies the following formula (1).
0 . 1 X H 1≤H 2 < H 1 ( 1 )  0. 1 X H 1≤H 2 <H 1 (1)
3 . 請求項 1または 2に記載の易重合性物質の精製装置であって、 前記易重合 性物質が、 (メタ) アクリル酸または (メタ) アクリル酸エステルである易重合 性物質の精製装置。 3. The apparatus for purifying an easily polymerizable substance according to claim 1 or 2, wherein the easily polymerizable substance is (meth) acrylic acid or (meth) acrylate.
4 . 易重合性物質導入部が精製塔に設けられており、 これとは別に重合防止剤 導入部が精製塔の中間部に設けられている精製塔を使用する易重合性物質の精製 方法であって、 易重合性物質導入部から易重合性物質を連続的に導入し、 重合防 止剤導入部から第 1の重合防止剤を精製塔内に導入する段階を有する易重合性物 質の精製方法。 4. An easily polymerizable substance introduction section is provided in the purification tower. Separately, a polymerization inhibitor introduction section is provided by a purification tower provided in an intermediate portion of the purification tower. A step of continuously introducing an easily polymerizable substance from the easily polymerizable substance introduction section and introducing the first polymerization inhibitor into the purification tower from the polymerization inhibitor introduction section. Purification method.
5 . 請求項 4に記載の易重合性物質の精製方法であって、 精製塔が、 精製塔塔 頂部から易重合性物質導入部までの理論段数 H 1 と精製塔塔頂部から重合防止剤 導入部までの理論段数 H 2との関係が下記式 (1 ) を満たす位置に易重合性物質 導入部と重合防止剤導入部が設けられている精製塔である易重合性物質の精製方 法。 5. The method for purifying an easily polymerizable substance according to claim 4, wherein the purification tower comprises: a theoretical plate number H 1 from the top of the purification tower to the introduction section of the easily polymerizable substance; and a polymerization inhibitor introduced from the top of the purification tower. A method for purifying an easily polymerizable substance, which is a purification tower provided with an easily polymerizable substance introduction section and a polymerization inhibitor introduction section at a position where the relationship with the theoretical plate number H2 up to the part satisfies the following formula (1).
0. 1 XH 1≤H 2 <H 1 ( 1 ) 0.1 XH 1≤H 2 <H 1 (1)
6. 請求項 4または 5に記載の易重合性物質の精製方法であって、 前記易重合 性物質が、 (メタ) アクリル酸または (メタ) アク リル酸エステルである易重合 性物質の精製方法。 6. The method for purifying an easily polymerizable substance according to claim 4 or 5, wherein the easily polymerizable substance is (meth) acrylic acid or (meth) acrylic acid ester. .
7. 請求項 4〜6に記載の易重合性物質の精製方法であって、 塔頂から取得し た精製された易重合性物質に第 1の重合防止剤と異なる第 2の重合防止剤を添加 する段階を更に有する易重合性物質の精製方法。 7. The method for purifying an easily polymerizable substance according to claim 4, wherein a second polymerization inhibitor different from the first polymerization inhibitor is added to the purified easily polymerizable substance obtained from the tower top. A method for purifying an easily polymerizable substance, further comprising a step of adding.
PCT/JP2003/003319 2002-03-20 2003-03-19 Apparatus and method for purifying easily polymerizable substance WO2003078015A1 (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1044957A1 (en) * 1999-04-16 2000-10-18 Nippon Shokubai Co., Ltd. Process for inhibiting the polymerization of easily-polymerizable compounds
EP1097742A1 (en) * 1999-11-08 2001-05-09 Nippon Shokubai Co., Ltd. Distillation process for easily polymerizable substance-containing solution
JP2002053871A (en) * 2000-08-07 2002-02-19 Nippon Zeon Co Ltd Method for separating and purifying conjugated dienes and apparatus for separating and purification
JP2003103106A (en) * 2001-09-28 2003-04-08 Sumitomo Chem Co Ltd Distillation method for easily polymerizable substance

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1044957A1 (en) * 1999-04-16 2000-10-18 Nippon Shokubai Co., Ltd. Process for inhibiting the polymerization of easily-polymerizable compounds
EP1097742A1 (en) * 1999-11-08 2001-05-09 Nippon Shokubai Co., Ltd. Distillation process for easily polymerizable substance-containing solution
JP2002053871A (en) * 2000-08-07 2002-02-19 Nippon Zeon Co Ltd Method for separating and purifying conjugated dienes and apparatus for separating and purification
JP2003103106A (en) * 2001-09-28 2003-04-08 Sumitomo Chem Co Ltd Distillation method for easily polymerizable substance

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