KR20120128004A - Dimethyl 2-methylenemalonate process - Google Patents

Dimethyl 2-methylenemalonate process Download PDF

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KR20120128004A
KR20120128004A KR1020110045861A KR20110045861A KR20120128004A KR 20120128004 A KR20120128004 A KR 20120128004A KR 1020110045861 A KR1020110045861 A KR 1020110045861A KR 20110045861 A KR20110045861 A KR 20110045861A KR 20120128004 A KR20120128004 A KR 20120128004A
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methylenemalonate
dimethyl
solvent
formaldehyde
malonate
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KR101336774B1 (en
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이춘남
이병화
이중현
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대흥화학공업주식회사
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/465Preparation of carboxylic acid esters by oligomerisation
    • 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
    • B01D3/10Vacuum distillation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/02Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the alkali- or alkaline earth metals or beryllium
    • B01J23/04Alkali metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0234Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
    • B01J31/0235Nitrogen containing compounds
    • B01J31/0237Amines
    • 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
    • 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/34Esters of acyclic saturated polycarboxylic acids having an esterified carboxyl group bound to an acyclic carbon atom
    • C07C69/38Malonic acid esters

Abstract

PURPOSE: A manufacturing method of dimethyl 2-methylenemalonate is provided to manufacture dimethyl 2-methylenemalonate with high stability and low emitting amount of formaldehyde by hydrolysis, to have excellent solubility and thermal stability, and moderate hardness and flexibility. CONSTITUTION: A manufacturing method of dimethyl 2-methylenemalonate comprises a step of synthesizing a polymer through a condensation of formaldehyde and malonate, and conducting heat depolymerization in a vacuum state. When polymerizing, a solvent with a density lower than water and a boiling point of 74-177°C is used. The solvent is one selected from methyl isobutyl ketone, acetic acid and ethylacetate. The comprised amount of the solvent is 200-300 parts by weight based on 100.0 parts by weight of the formaldehyde and malonate. [Reference numerals] (AA) Estimated value 72g(0.5mol); (BB) Estimated value 9g(0.5mol)

Description

디메틸 2-메틸렌말로네이트의 제조방법{Dimethyl 2-methylenemalonate process}Method for producing dimethyl 2-methylenemalonate {Dimethyl 2-methylenemalonate process}

본 발명은 디메틸 2-메틸렌말로네이트의 제조방법에 관한 것으로, 보다 상세하게는 용해성 및 열안정성이 우수하고, 소정의 경도 및 적절한 유연성을 갖으며, 가수분해에 의한 포름알데히드 방출량이 적어 안전성이 높은 디메틸 2-메틸렌말로네이트의 제조방법에 관한 것이다.The present invention relates to a method for preparing dimethyl 2-methylenemalonate, and more particularly, has excellent solubility and thermal stability, has a predetermined hardness and appropriate flexibility, and has a high safety due to a small amount of formaldehyde emission due to hydrolysis. It relates to a process for preparing dimethyl 2-methylenemalonate.

순간접착제는 빠른 접착속도 및 우수한 결합강도. 사용 용이성 등의 특성으로, 본딩 플라스틱, 고무, 유리, 금속, 목재와 같은 산업용, 가정용 용도나 생물학적 조직, 의료용 조직, 또는 생체 조직 등의 의료/ 외과적 용도로 사용되고 있다. 이러한 순간접착제 중 시아노아크릴레이트계 순간접착제는 주성분으로써 시아노아크릴레이트가 사용되는 것으로, 이는 강한 전자 흡인성을 갖는 친전자성 단량체이다. Instant adhesive has fast adhesion speed and good bonding strength. Due to its properties such as ease of use, it is used in industrial and household applications such as bonding plastics, rubber, glass, metal, wood, and medical / surgical applications such as biological tissues, medical tissues, or living tissues. Among these instantaneous adhesives, cyanoacrylate-based instant adhesives are cyanoacrylates used as main components, which are electrophilic monomers having strong electron attraction.

이러한 시아노아크릴레이트는 공기중의 수분이나 재료표면에 부착되어 있는 미량의 수분으로도 중합되어 경화되며, 그 경화시간이 10초 이내로 알려져 있는 것으로, 접착제의 성능을 증대시키기 위하여 증점제, 가소제, 착색제, 보존제, 열소산제, 안정제 등과 적절히 혼합되어 사용된다.Such cyanoacrylates are polymerized and cured even with moisture in the air or a small amount of moisture adhering to the surface of the material, and the curing time is known to be within 10 seconds. Thickeners, plasticizers, and colorants are used to increase the performance of the adhesive. It is suitably mixed and used with a preservative, a heat dissipating agent, and a stabilizer.

이러한 시아노아크릴레이트는 일반적으로 염기성 촉매를 사용한 파라포름알데히드와 같은 포름 알데히드 전구체와 알킬 시아노아세테이트 사이의 노베나겔(Knoevenagel) 축합반응에 의해 중합체를 얻고, 고온 감압 하에 해중합(depolymerization)함으로써 제조되며, 알킬기의 종류에 따라 접착성능과 경화특성이 달라진다. 따라서 메틸은 주로 금속용, 에틸은 고무, 플라스틱, 목재용, 이소부틸은 의료용, 올리고머 형태는 다공질 용에 보다 적합하다고 보고되어 있다. Such cyanoacrylates are generally prepared by obtaining polymers by Knoevenagel condensation reactions between formaldehyde precursors such as paraformaldehyde and alkyl cyanoacetates using basic catalysts, and depolymerization under high temperature and reduced pressure. Adhesion performance and curing properties vary depending on the type of alkyl group. It is therefore reported that methyl is mainly suitable for metals, ethyl for rubber, plastics, wood, isobutyl for medical use, and oligomeric forms for porous use.

다만, 이러한 방법으로 제조되는 시아노아크릴레이트는 일반적으로 순도가 낮고, 접착성능, 안정성 등이 떨어지는 문제를 갖고 있었기 때문에 이를 다시 증류함으로써 정제 시아노아크릴레이트로 제조하여 사용되고 있다. However, cyanoacrylates prepared by this method generally have low purity, poor adhesion performance, stability, and the like, and thus have been distilled back into purified cyanoacrylates.

시아노아크릴레이트의 증류 및 정제에 관해서는 2-시아노아크릴레이트의 중합을 방지하기 위해 오산화이인(P2O5), 인산, 파라톨루엔술폰산 등의 음이온 중합억제제와, 하이드로퀴논, 카테콜, 피로갈롤 등의 라디칼 중합억제제를 조제 2-시아노아크릴레이트에 첨가하여 감압하고 가열 증류하는 방법이 알려져 있다.Regarding distillation and purification of cyanoacrylate, in order to prevent polymerization of 2-cyanoacrylate, anionic polymerization inhibitors such as diphosphorous pentoxide (P 2 O 5 ), phosphoric acid, paratoluenesulfonic acid, hydroquinone, catechol, There is known a method of adding a radical polymerization inhibitor such as pyrogallol to the prepared 2-cyanoacrylate, and distilling under reduced pressure.

이때 시아노아크릴레이트는 상기와 같이 제조하는 과정에서 생성되는 물을 제거하는 것이 중요한데, 수분이 많으면 경화물을 가수분해하기 때문에 접착강도가 급격히 떨어지고, 가수분해로 포름알데히드가 방출되어 유해하다는 문제점이 있었다.At this time, it is important to remove the water produced in the manufacturing process as described above, but if there is a lot of moisture hydrolyzes the cured product, the adhesive strength drops sharply, and formaldehyde is released by hydrolysis, which is harmful. there was.

따라서 물의 제거를 위하여 통상적으로 톨루엔, 자일렌, 이소프로필알콜, 메틸에틸케톤(MEK), 파라핀, 아세톤 등과 같은 휘발성유기화합물(VOCs)을 용제가 사용된다. 그러나 이와 같은 용제는 발암성 유해물질로 인체에 유해하며, 대기오염의 주범이라는 문제점이 있었다. Therefore, volatile organic compounds (VOCs) such as toluene, xylene, isopropyl alcohol, methyl ethyl ketone (MEK), paraffin, acetone, etc. are commonly used for the removal of water. However, these solvents are harmful to the human body as a carcinogenic harmful substance, there was a problem that the main culprit of air pollution.

한편, 상기와 같은 순간접착제의 주성분으로 이용되는 기타 유형의 단량체로메틸렌말로네이트가 있다. 이러한 메틸렌말로네이트 역시 시아노아크릴레이트의 제조와 유사한 방법으로 제조되는 것으로, 일예로 미국 특허 제3197318호에서는 dimethyl 2-methylenmalonate의 제조방법이 제안되어 있고, 미국특허 제3523097호에서는 diethyl 2-methylenmalonate의 제조방법이 제안되어 있으며, 미국특허 3221745호에서는 diethyl ethoxy-methylenmalonate의 제조방법이 제안되어 있다. On the other hand, methylenemalonate is another type of monomer used as a main component of the instant adhesive. The methylenemalonate is also prepared by a method similar to the preparation of cyanoacrylate. For example, US Patent No. 3197318 proposes a method for preparing dimethyl 2-methylenmalonate, and US Patent No. 3523097 discloses diethyl 2-methylenmalonate. A manufacturing method has been proposed, and a method of preparing diethyl ethoxy-methylenmalonate has been proposed in US Patent 3221745.

다만, 상기와 같은 미국특허에 제시된 제조방법으로 제조된 순간접착제의 주성분들도 물의 생성 및 제거를 위하여 인체에 유해한 용제를 사용하였으며, 잔류된 포름알데히드의 양이 과다하여 사용시 인체에 해롭다는 문제점이 있었다.However, the main components of the instant adhesive prepared by the method described in the US patent also used a solvent harmful to the human body for the generation and removal of water, and the problem that the amount of formaldehyde remaining is harmful to the human body when used in excess. there was.

본 발명은 상기와 같은 문제점을 해결하기 위한 것으로,The present invention is to solve the above problems,

발암성 유해물질을 사용 및 발생을 방지하여 인체에 무해하고, 용해성 및 열안정성이 우수하며, 접착성이 좋고 물의 제거가 용이하여 순간접착제의 주성분으로 사용되는 디메틸 2-메틸렌말로네이트의 제조방법을 제공하는 것을 목적으로 한다.It is a method of preparing dimethyl 2-methylenemalonate which is used as a main component of instant adhesive because it is harmless to human body by preventing the use and occurrence of carcinogenic harmful substances, has excellent solubility and thermal stability, and has good adhesiveness and easy removal of water. It aims to provide.

본원발명은 상기와 같은 목적을 달성하기 위하여,The present invention to achieve the above object,

포름알데히드와 말로네이트의 축합반응으로 중합체를 합성한 후, 진공하에서 가열 해중합하는 디메틸 2-메틸렌말로네이트의 제조방법에 있어서,In the manufacturing method of dimethyl 2-methylenemalonate which synthesize | combines a polymer by the condensation reaction of formaldehyde and malonate, and heat-depolymerizes under vacuum,

중합체 합성시 물보다 밀도가 낮고 끓는점이 74~177℃인 용제를 사용하는 것을 특징으로 하는 디메틸 2-메틸렌말로네이트의 제조방법을 제공한다.It provides a method for producing dimethyl 2-methylenemalonate, characterized in that a solvent having a lower density than the water and a boiling point of 74 ~ 177 ℃ when synthesizing the polymer.

또한, 상기 용제는 메틸이소부틸케톤, 아세트산, 에틸아세테이트 중에서 선택되는 어느 하나인 것을 특징으로 한다.In addition, the solvent is characterized in that any one selected from methyl isobutyl ketone, acetic acid, ethyl acetate.

또한, 상기 중합체 합성은 염기성 촉매 하에서 용제, 포름알데히드를 혼합하여 70~80℃를 유지하여 150분간 교반한 다음, 말로네이트를 적하하거나 모두 투입하고 100~110℃를 유지하며 240분간 반응시킨 뒤, 증류하여 용제 및 물을 제거하고, 진공여과하여 디메틸 2-메틸렌말로네이트 액상 폴리머를 얻고, 이를 진공증류하여 디메틸 2- 메틸렌말로네이트 중합체를 얻는 것을 특징으로 한다.In addition, the synthesis of the polymer is mixed with a solvent, formaldehyde under a basic catalyst and maintained at 70 ~ 80 ℃ and stirred for 150 minutes, then dropwise or added all the malonate and reacted for 240 minutes while maintaining 100 ~ 110 ℃, Distillation to remove the solvent and water, and vacuum filtration to obtain a dimethyl 2-methylenemalonate liquid polymer, vacuum distillation to obtain a dimethyl 2- methylenemalonate polymer.

또한, 상기 용제는 포름알데히드 및 말로네이트의 사용량 100중량부에 대하여 200~300중량부가 사용되는 것을 특징으로 한다.The solvent may be used in an amount of 200 to 300 parts by weight based on 100 parts by weight of formaldehyde and malonate.

또한, 포름알데히드의 사용량은 말로네이트 0.5mole 대비 0.25~0.6mole인 것을 특징으로 한다. In addition, the amount of formaldehyde is characterized in that 0.25 ~ 0.6mole compared to malonate 0.5mole.

상술한 바와 같이 본 발명에 따른 디메틸 2-메틸렌말로네이트의 제조방법으로 제조된 디메틸 2-메틸렌말로네이트는 VOCs가 아닌 안전한 용제를 사용하고 포름알데히드와 같은 유해물질의 방출량이 적도록 제어할 수 있음에 따라 인체에 무해하며, 용제를 통한 물의 제거효과가 우수하고, 저장안정성과 열안정성이 부여되며, 우수한 접착력을 갖는 접착제로 사용가능하다는 효과를 갖는다.As described above, the dimethyl 2-methylenemalonate prepared by the method for preparing dimethyl 2-methylenemalonate according to the present invention can be controlled to use a safe solvent other than VOCs and to reduce the amount of harmful substances such as formaldehyde. It is harmless to the human body, it is excellent in the water removal effect through the solvent, storage stability and thermal stability is given, and has the effect that it can be used as an adhesive having excellent adhesion.

도 1은 본 발명의 일 실시예에 따른 디메틸 2-메틸렌말로네이트의 제조방법을 나타낸 공정도.
도 2는 본 발명의 다른 실시예에 따른 디메틸 2-메틸렌말로네이트의 제조방법을 나타낸 공정도.
도 3은 실시예 1에서 제조된 디메틸 2-메틸렌말로네이트의 FT-IR분석결과.
1 is a process chart showing a method for preparing dimethyl 2-methylenemalonate according to an embodiment of the present invention.
2 is a process chart showing a method for preparing dimethyl 2-methylenemalonate according to another embodiment of the present invention.
Figure 3 is the FT-IR analysis of the dimethyl 2-methylenemalonate prepared in Example 1.

이하에서는 도면을 참고로 하여 본 발명에 따른 디메틸 2-메틸렌말로네이트의 제조방법에 대하여 보다 상세하게 설명하기로 하나, 이는 본 발명의 이해를 돕기 위하여 제시된 것으로서, 본 발명이 이에 한정되는 것은 아니다.Hereinafter, a method for preparing dimethyl 2-methylenemalonate according to the present invention will be described in more detail with reference to the drawings, which are presented to assist in understanding the present invention, but the present invention is not limited thereto.

도 1은 본 발명의 일 실시예에 따른 디메틸 2-메틸렌말로네이트의 제조방법을 나타낸 공정도이고, 도 2는 본 발명의 다른 실시예에 따른 디메틸 2-메틸렌말로네이트의 제조방법을 나타낸 공정도이다.1 is a process chart showing a manufacturing method of dimethyl 2-methylenemalonate according to an embodiment of the present invention, Figure 2 is a process chart showing a manufacturing method of dimethyl 2-methylenemalonate according to another embodiment of the present invention.

본 발명은 순간 접착제의 주원료로 사용될 수 있는 순수 디메틸 2-메틸렌말로네이트의 제조방법에 관한 것으로, 본 발명의 제조방법으로 제조된 디메틸 2-메틸렌말로네이트(Dimethyl 2-methylenemalonate)는 독성물질의 방출량이 적은 특성을 갖으며, 접착제로 제조시 접착성, 용해성 및 열안정성이 우수하며 소정의 경도와 유연성을 갖는 접착제로 제조될 수 있다.The present invention relates to a method for preparing pure dimethyl 2-methylenemalonate which can be used as a main raw material of an instant adhesive. The dimethyl 2-methylenemalonate prepared by the method of the present invention is a release amount of toxic substances. It has less properties, has excellent adhesiveness, solubility and thermal stability when manufactured with an adhesive, and can be produced with an adhesive having a predetermined hardness and flexibility.

이러한 디메틸 2-메틸렌말로네이트는 포름알데히드와 말로네이트의 축합반응으로 중합체를 합성한 후, 진공하에서 가열 해중합하는 디메틸 2-메틸렌말로네이트의 제조방법에 있어서, 중합체 합성시 물보다 밀도가 낮고 끓는점이 74~177℃인 용제를 사용함으로써 가능하다.The dimethyl 2-methylenemalonate is a method of producing dimethyl 2-methylenemalonate which is synthesized by condensation reaction of formaldehyde and malonate, and then depolymerized by heating under vacuum. It is possible by using the solvent which is 74-177 degreeC.

상기 용제는 중합체 합성 중 발생되는 물을 효과적으로 제거하여 부반응 발생을 막고, 말로네이트와 포름알데히드가 미반응 없이 반응이 원활하게 이루어져 제조된 디메틸 2-메틸렌말로네이트 내에 포함된 포름알데히드의 함량을 감소시키는 역할을 하여 부반응으로 인한 유해물질의 발생을 최소화하는 중요한 역할을 한다.The solvent effectively removes water generated during the synthesis of the polymer to prevent side reactions, and the reaction of the malonate and formaldehyde without reaction is performed smoothly to reduce the content of formaldehyde contained in the prepared dimethyl 2-methylenemalonate. It plays an important role in minimizing the generation of harmful substances due to side reactions.

이때 용제와 더불어 말로네이트와 포름알데히드의 비율을 조절하고, 증류시 온도조절을 함으로써 물을 더욱 효과적으로 제거하여 부반응으로 인한 유해물질의 발생을 최소화할 수 있다.In this case, by controlling the ratio of malonate and formaldehyde together with the solvent, and by controlling the temperature during distillation, water can be more effectively removed to minimize the generation of harmful substances due to side reactions.

또한 상기 밀도는 물보다 낮을 때 분리여부를 용이하게 파악할 수 있기 때문으로, 만약 물보다 밀도가 높은 경우 수분 정량시 물의 제거가 용이하지 않을 수 있다. 그러므로 물의 밀도 1보다 낮은 밀도를 갖는 용제를 사용하는 것이 바람직하며, 보다 구체적으로는 밀도가 0.75~0.95인 것이 더욱 바람직하게 사용될 수 있다.In addition, since the density can be easily determined whether the separation is lower than water, if the density is higher than water, it may not be easy to remove the water when quantitating moisture. Therefore, it is preferable to use a solvent having a density lower than the density 1 of water, and more specifically, one having a density of 0.75-0.95 can be more preferably used.

또한, 상기 끓는점이 74℃미만이면 온도가 너무 낮아 물 제거에 부적합하고, 반대로 말로네이트의 끓는점인 177℃를 초과하는 경우 합성이 완료되기 전 디메틸 2-메틸렌말로네이트가 증류되는 문제점이 있어 부적합하다.
In addition, if the boiling point is less than 74 ℃ temperature is too low unsuitable for water removal, on the contrary, if the boiling point of the malonate exceeds 177 ℃ there is a problem that dimethyl 2-methylenemalonate is distilled before the synthesis is completed is unsuitable. .

본 발명에서는 상기와 같은 조건을 만족하면서 인체에 무해한 용제로써 메틸이소부틸케톤, 아세트산, 에틸아세테이트 중에서 선택되는 어느 하나를 사용하는 것이 바람직하며, 특히 메틸이소부틸케톤을 사용하는 것이 최종 제품의 종합적인 물성이 우수하게 나타나므로 더욱 바람직하다.In the present invention, it is preferable to use any one selected from methyl isobutyl ketone, acetic acid and ethyl acetate as a solvent harmless to the human body while satisfying the above conditions, and in particular, it is preferable to use methyl isobutyl ketone. It is more preferable because it shows excellent physical properties.

보다 구체적으로 본 발명에 따른 디메틸 2-메틸렌말로네이트의 제조방법을 순차적으로 살펴보면, 먼저 상기 중합체를 합성하기 위하여 염기성 촉매 하에서 용제와 포름알데히드를 혼합하여 70~80℃를 유지하여 150분간 교반한 다음, 말로네이트를 도 1에 제시된 것과 같이 적하하거나 도 2에 제시된 것과 같이 모두 투입한다. 이때 발열반응이 발생되며 100~110℃를 유지하며 240분간 반응시킨다. 그 뒤, 증류하여 용제 및 물을 제거하고, 진공여과하여 디메틸 2-메틸렌말로네이트 액상 폴리머를 얻고, 이를 다시 진공증류하여 디메틸 2- 메틸렌말로네이트 중합체를 얻을 수 있다.In more detail, the dimethyl 2-methylenemalonate manufacturing method according to the present invention will be described sequentially. First, in order to synthesize the polymer, a solvent and formaldehyde are mixed under a basic catalyst, and then stirred at 150 ° C. for 70 minutes to 80 ° C. , Malonate is added dropwise as shown in FIG. 1 or all added as shown in FIG. 2. At this time, an exothermic reaction occurs and the reaction is carried out for 240 minutes while maintaining 100 to 110 ° C. Thereafter, the solvent and water are distilled off to remove the solvent, followed by vacuum filtration to obtain a dimethyl 2-methylenemalonate liquid polymer, which is then vacuum distilled to obtain a dimethyl 2-methylenemalonate polymer.

이러한 포름알데히드와 말로네이트를 통한 디메틸 2-메틸린말로네이트 중합체의 합성은 하기 반응식 1과 같은 복합적인 반응을 거쳐 생성될 수 있으며, 이와 같이 합성된 중합체를 진공상태에서 150~260℃로 해중합하여 접착제의 주성분으로 사용되는 디메틸 2-메틸렌말로네이트(반응식 1의 화학식 Ⅴ)를 제조할 수 있는 것이다.
Synthesis of the dimethyl 2-methyllinmalonate polymer through the formaldehyde and malonate can be produced through a complex reaction as shown in Scheme 1, by depolymerizing the polymer thus synthesized in a vacuum at 150 ~ 260 ℃ Dimethyl 2-methylenemalonate (Formula V of Scheme 1) used as the main component of the adhesive can be prepared.

[반응식 1][Reaction Scheme 1]

Figure pat00001
Figure pat00001

이때 상기 염기성 촉매로는 피페리딘, 디에틸아민, 디부틸아민, 모르폴린, 수산화칼륨, 수산화나트륨, 나트륨알콕시드 등이 선택적으로 사용될 수 있는 것으로, 이러한 염기성 촉매는 말로네이트 100중량부에 대하여 15~25중량부가 사용되는 것이 바람직하다.In this case, piperidine, diethylamine, dibutylamine, morpholine, potassium hydroxide, sodium hydroxide, sodium alkoxide, etc. may be selectively used as the basic catalyst, and the basic catalyst is based on 100 parts by weight of malonate. It is preferable that 15-25 weight part is used.

만약 염기성촉매의 사용량이 상기 범위를 벗어나면, 말로네이트와 포름알데히드의 반응시 발생하는 물의 생성이나 제거가 용이하게 이루어지지 않아 디메틸 2-메틸렌말로네이트를 생성률이 저하될 수 있다.If the amount of the basic catalyst is out of the above range, the generation or removal of water generated during the reaction of malonate and formaldehyde may not be easily performed, and thus the production rate of dimethyl 2-methylenemalonate may be reduced.

그리고 상기 용제는 포름알데히드 및 말로네이트의 사용량 100중량부에 대하여 200~300중량부가 사용되는 것이 바람직한데, 만약 상기 용제의 사용량이 200중량부 미만으로 사용되면 말로네이트와 포름알데히드의 용해가 충분히 이루어지지 않아 다른 부반응이 발생될 수 있다. 또한 상기 용제의 사용량이 300중량부를 초과하여 사용되면 추후 용제 제거시 잔량이 많아 증류가 효과적으로 이루어지지 않을 수 있다.
The solvent is preferably used in an amount of 200 to 300 parts by weight based on 100 parts by weight of formaldehyde and malonate. If the amount of the solvent is used in an amount less than 200 parts by weight, the dissolution of malonate and formaldehyde is sufficient. Other side reactions may occur. In addition, when the amount of the solvent used exceeds 300 parts by weight, the remaining amount may be largely removed when the solvent is removed later.

한편, 포름알데히드의 사용량은 말로네이트 0.5mole 대비 0.25~0.6mole인 것이 바람직한데, 만약 포름알데히드의 양이 말로네이트 0.5몰(mole) 대비 0.25몰보다 적게 사용되면, 반응이 충분히 이루어지지 않아 디메틸-2-메틸렌말로네이트의 수득량이 떨어지고, 0.6몰보다 많게 사용되면 반응은 충분히 이루어지나, 잔류되는 포름알데히드량이 증가되고, 물의 제거가 효과적으로 이루어지지 않아 부반응으로 인한 유해물질이 발생될 수 있다. 이때 상기 포름알데히드와 말로네이트가 1:1의 몰비로 사용되는 것이 잔류되는 성분없이 완전히 반응될 수 있어 더욱 바람직하다.
On the other hand, the amount of formaldehyde is preferably 0.25 ~ 0.6mole compared to 0.5 mole of malonate, if the amount of formaldehyde is used less than 0.25 mole compared to 0.5 mole (mole) of malonate, the reaction is not sufficiently made dimethyl- When the yield of 2-methylenemalonate is lowered and used more than 0.6 moles, the reaction is sufficiently performed, but the amount of formaldehyde remaining is increased, and the removal of water is not effective, and harmful substances may be generated due to side reactions. At this time, the use of the formaldehyde and malonate in a molar ratio of 1: 1 is more preferable because it can be completely reacted without remaining components.

하기 실시예를 통하여 본 발명을 보다 구체적으로 설명한다. 단, 하기 실시예는 본 발명의 이해를 돕기 위해서 제시되는 것일 뿐, 본 발명의 특허 청구 범위가 이에 따라 한정되는 것은 아니다.
The present invention will be described in more detail with reference to the following examples. However, the following examples are only presented to aid the understanding of the present invention, and the claims of the present invention are not limited thereto.

<실시예 1> &Lt; Example 1 >

피페리딘(piperidine) 10g, 파라포름알데히드(paraformadehyde) 15g과, 용제로써 메틸이소부틸케톤(Methyl isobutyl ketone(d=0.800) 250g을 혼합하여 70~80℃를 유지하여 150분간 교반한 다음, 디메틸말로네이트(dimethyl malonate) 66g을 20분간 적하하여 수분정량장치와 환류냉각기를 장착시킨 상태에서 100~110℃를 유지하며 240분간 반응시킨 다음 증류하여 용제 및 물을 제거하고, 진공여과하여 디메틸 2-메틸렌말로네이트 액상 폴리머를 얻고, 이를 다시 진공증류하여 1차로 액상폴리머 내에 잔류하고 있는 메틸이소부틸케톤을 증류하고 2차로 디메틸 2-메틸렌말로네이트 중합체를 얻었다. 그런 다음진공상태에서 150~260℃로 해중합하여 접착제의 주성분으로 사용되는 디메틸 2-메틸렌말로네이트를 제조하였다.10 g of piperidine, 15 g of paraformadehyde, and 250 g of methyl isobutyl ketone (d = 0.800) as a solvent were mixed and the mixture was stirred at 70 to 80 ° C. for 150 minutes, followed by dimethyl 66 g of malonate was added dropwise for 20 minutes, and the reaction mixture was maintained at 100 to 110 ° C. for 240 minutes while the water determination device and the reflux cooler were installed, followed by distillation to remove the solvent and water, followed by vacuum filtration. Methylenemalonate liquid polymer was obtained, and vacuum distillation was carried out to distill the methyl isobutyl ketone remaining in the liquid polymer in the first step, and to obtain the dimethyl 2-methylenemalonate polymer in the second step. Depolymerization was carried out to prepare dimethyl 2-methylenemalonate used as the main component of the adhesive.

<실시예 2><Example 2>

용제로 에틸아세테이트(Ethyl acetate(d=0.897))을 사용한 것을 제외하고는 실시예 1과 동일한 방법으로 디메틸 2-메틸렌말로네이트를 제조하였다.Dimethyl 2-methylenemalonate was prepared in the same manner as in Example 1 except that ethyl acetate (Ethyl acetate (d = 0.897)) was used as a solvent.

<비교예 1>&Lt; Comparative Example 1 &

용제로 톨루엔(Toluene(d=0.867))을 사용한 것을 제외하고는 실시예 1과 동일한 방법으로 디메틸 2-메틸렌말로네이트를 제조하였다. Dimethyl 2-methylenemalonate was prepared in the same manner as Example 1 except for using toluene (Toluene (d = 0.867)) as a solvent.

<비교예 2>Comparative Example 2

용제로 트리클로로에틸렌(Trichlorethylene(d=1.460))을 사용한 것을 제외하고는 실시예 1과 동일한 방법으로 디메틸 2-메틸렌말로네이트를 제조하였다.
Dimethyl 2-methylenemalonate was prepared in the same manner as in Example 1, except that trichloroethylene (Trichlorethylene (d = 1.460)) was used as a solvent.

<실험예 1><Experimental Example 1>

실시예 1, 실시예 2 및 비교예 1 내지 비교예 2에서 제조된 디메틸 2-메틸렌말로네이트의 제조상태를 확인한 결과, 실시예 1 및 비교예 1의 경우 물의 제거가 효과적으로 이루어져 순수 디메틸 2-메틸렌말로네이트를 얻을 수 있었다. 실시예 2는 용제의 밀도가 물에 비하여 충분히 낮기는 하나, 끓는점이 너무 낮아 실시예 1에 비하여 물 제거효과가 다소 떨어졌다. 그리고 비교예 2의 경우 물보다 밀도가 높아 수분 정량시 물의 제거가 용이하지 않아 순수 디메틸 2-메틸렌말로네이트를 얻기 어려웠다. As a result of confirming the production state of the dimethyl 2-methylenemalonate prepared in Example 1, Example 2 and Comparative Examples 1 to 2, in the case of Example 1 and Comparative Example 1 was effectively removed water pure dimethyl 2-methylene Malonate could be obtained. In Example 2, although the density of the solvent was sufficiently low compared to water, the boiling point was too low, and the water removal effect was slightly inferior to that of Example 1. In the case of Comparative Example 2, since the density is higher than that of water, water is not easily removed during water quantification, and thus it is difficult to obtain pure dimethyl 2-methylenemalonate.

아울러 실시예 1에서 제조된 디메틸 2-메틸렌말로네이트의 합성이 제대로 이루어 졌는지 확인하기 위하여 FT-IR분석을 하였고, 그 결과를 도 3에 나타내었다. In addition, FT-IR analysis was performed to confirm whether synthesis of dimethyl 2-methylenemalonate prepared in Example 1 was properly performed, and the results are shown in FIG. 3.

도 3에 나타난 바와 같이 실시예 1에서 제조된 디메틸 2-메틸렌말로네이트는 C=CH2 이중결합을 통해 합성이 잘 이루어졌음을 확인할 수 있었다.
As shown in FIG. 3, the dimethyl 2-methylenemalonate prepared in Example 1 was confirmed to be well synthesized through a C = CH 2 double bond.

<실시예 3><Example 3>

디메틸말로네이트를 한번에 모두 투입한 것을 제외하고는 실시예 1과 동일한 방법으로 디메틸 2-메틸렌말로네이트를 제조하였다.Dimethyl 2-methylenemalonate was prepared in the same manner as in Example 1 except that all of the dimethylmalonate was added.

<실험예 2><Experimental Example 2>

수분정량장치 및 환류냉각기를 통하여 실시예 1, 실시예 3 및 비교예 1에서 제조된 디메틸 2-메틸렌말로네이트의 제조시 생성되는 물의 양을 확인하고, 포름알데히드의 잔류량 및 VOCs 검출량을 측정하였으며, 그 결과를 하기 표 2에 나타내었다. 이때 포름알데히드의 잔류량 및 VOCs 검출에 사용된 시험방법 및 기준규격은 하기 표 1의 방법을 사용하였다.The amount of water generated during the preparation of the dimethyl 2-methylenemalonate prepared in Examples 1, 3 and Comparative Example 1 was checked through a water determination device and a reflux cooler, and the residual amount of formaldehyde and the amount of VOCs were measured. The results are shown in Table 2 below. At this time, the test method and the standard used for the residual amount of formaldehyde and VOCs detection were used in the method of Table 1 below.

시험항목Test Items 시험방법Test Methods 비고Remarks 기준치Reference value 기준규격Standard 적용제품Products 포름알데히드Formaldehyde US EPA 8315 A : 1996US EPA 8315 A: 1996 HPLCHPLC 20 mg/kg이하20 mg / kg or less 안전인증 안전기준 부속서 01 (가속눈썹)Safety Certification Safety Standard Annex 01 (Acceleration Eyelashes) 가속눈썹접착제Accelerated eyebrow glue VOCs(Benzene,Toluene,Xylene)VOCs (Benzene, Toluene, Xylene) US EPA 5021 : 1996US EPA 5021: 1996 Headspace-GC/MSHeadspace-GC / MS 20 mg/kg이하20 mg / kg or less KS M 0031: 2002KS M 0031: 2002 GC/FIDGC / FID


시험결과(mg/kg)Test result (mg / kg)
ACN추출ACN extraction DW추출DW extraction BenzeneBenzene TolueneToluene XyleneXylene 실시예 1Example 1 2626 88 NDND 44 NDND 실시예 3Example 3 NDND NDND NDND NDND NDND 비교예 1Comparative Example 1 174174 249249 NDND 7.27.2 13201320

- ND: 검출되지 않음ND: not detected

표 2에 도시된 바와 같이 실시예 1과 실시예 3의 경우 용제를 첨가하는 방식에 관계없이 포름알데히드나 VOCs의 잔류량이 검출되지 않거나 매우 낮아 인체에 영향을 미치지 않는 수준임을 확인할 수 있었다.As shown in Table 2, in the case of Example 1 and Example 3, it was confirmed that the residual amount of formaldehyde or VOCs was not detected or very low regardless of the method of adding the solvent, and thus the level did not affect the human body.

반면, 용제로 톨루엔을 사용한 비교예 1의 경우 제조된 디메틸 2-메틸렌말로네이트 내에 포름알데히드의 잔류량이 높아 인체에 유해함을 알 수 있었다.
On the other hand, in the case of Comparative Example 1 using toluene as a solvent, the residual amount of formaldehyde in the prepared dimethyl 2-methylenemalonate was found to be harmful to the human body.

<실시예 4 내지 실시예 6> <Examples 4 to 6>

파라포름알데히드의 양을 말로네이트 0.5mole 대비 0.25(실시예 4), 0.3(실시예 5), 0.45(실시예 6)mole로 변화시키면서 제조한 것을 제외하고는, 실시예 3과 동일한 방법으로 디메틸 2-메틸렌말로네이트를 제조하였다.
Dimethyl was prepared in the same manner as in Example 3, except that the amount of paraformaldehyde was prepared while changing from 0.5 mole of malonate to 0.25 (Example 4), 0.3 (Example 5), 0.45 (Example 6) mole. 2-methylenemalonate was prepared.

<실험예 3><Experimental Example 3>

실시예 3 내지 실시예 6에서 제조된 디메틸 2-메틸렌말로네이트의 제조시 생성되는 물의 양을 확인하고, 포름알데히드의 잔류량 및 VOCs 검출량을 측정하였으며, 그 결과를 하기 표 3에 나타내었다. 이때 포름알데히드의 잔류량 및 VOCs 검출에 사용된 시험방법 및 기준규격은 상기 표 1의 방법과 동일하다.The amount of water produced during the preparation of dimethyl 2-methylenemalonate prepared in Examples 3 to 6 was confirmed, and the residual amount of formaldehyde and the amount of VOCs detected were measured, and the results are shown in Table 3 below. At this time, the test method and standard used for the residual amount of formaldehyde and VOCs detection are the same as the method of Table 1.


시험결과(mg/kg)Test result (mg / kg)
ACN추출ACN extraction DW추출DW extraction BenzeneBenzene TolueneToluene XyleneXylene 실시예 3Example 3 NDND NDND NDND NDND NDND 실시예 4Example 4 NDND NDND NDND NDND NDND 실시예 5Example 5 NDND NDND NDND 3939 NDND 실시예 6Example 6 1111 NDND NDND 66 NDND

- ND: 검출되지 않음ND: not detected

상기 표 3에 나타난 바와 같이 본 발명에서 제시한 포름알데히드와 말로네이트의 사용량으로 제조된 디메틸 2-메틸렌말로네이트는 모두 유해물질이 거의 검출되지 않거나 낮음을 확인할 수 있었다. As shown in Table 3, all of the dimethyl 2-methylenemalonate prepared by the use amount of formaldehyde and malonate presented in the present invention was confirmed that little or no harmful substances were detected.

즉, 본 발명에 따른 제조방법으로 제조된 디메틸 2-메틸렌말로네이트는 성분 내에 포름알데히드나 휘발성 유기화합물(VOCs)의 잔류량이 검출되지 않거나 거의 남아있지 않아 인체에 무해한 순간 접착제의 주성분으로써 사용될 수 있음을 알 수 있었다.That is, the dimethyl 2-methylenemalonate prepared by the production method according to the present invention can be used as the main component of the instant adhesive which is harmless to the human body since no residual amount of formaldehyde or volatile organic compounds (VOCs) is detected or hardly remained in the component. And it was found.

Claims (5)

포름알데히드와 말로네이트의 축합반응으로 중합체를 합성한 후, 진공하에서 가열 해중합하는 디메틸 2-메틸렌말로네이트의 제조방법에 있어서,
중합체 합성시 물보다 밀도가 낮고 끓는점이 74~177℃인 용제를 사용하는 것을 특징으로 하는 디메틸 2-메틸렌말로네이트의 제조방법.
In the manufacturing method of dimethyl 2-methylenemalonate which synthesize | combines a polymer by the condensation reaction of formaldehyde and malonate, and heat-depolymerizes under vacuum,
A method for producing dimethyl 2-methylenemalonate, characterized in that a solvent having a lower boiling point than water and having a boiling point of 74 to 177 ° C when synthesizing a polymer.
청구항 1에 있어서,
상기 용제는 메틸이소부틸케톤, 아세트산, 에틸아세테이트 중에서 선택되는 어느 하나인 것을 특징으로 하는 디메틸 2-메틸렌말로네이트의 제조방법.
The method according to claim 1,
The solvent is a method for producing dimethyl 2-methylenemalonate, characterized in that any one selected from methyl isobutyl ketone, acetic acid, ethyl acetate.
청구항 2에 있어서,
상기 중합체 합성은 염기성 촉매 하에서 용제, 포름알데히드를 혼합하여 70~80℃를 유지하여 150분간 교반한 다음, 말로네이트를 적하하거나 모두 투입하고 100~110℃를 유지하며 240분간 반응시킨 뒤, 증류하여 용제 및 물을 제거하고, 진공여과하여 디메틸 2-메틸렌말로네이트 액상 폴리머를 얻고, 이를 진공증류하여 디메틸 2- 메틸렌말로네이트 중합체를 얻는 것을 특징으로 하는 디메틸 2-메틸렌말로네이트의 제조방법.
The method according to claim 2,
In the polymer synthesis, a solvent and formaldehyde were mixed under a basic catalyst and maintained at 70 ° C. to 80 ° C., followed by stirring for 150 minutes. Then, malonate was added dropwise or added thereto. A solvent and water are removed, and vacuum filtration to obtain a dimethyl 2-methylenemalonate liquid polymer, which is vacuum distilled to obtain a dimethyl 2-methylenemalonate polymer.
청구항 3에 있어서,
상기 용제는 포름알데히드 및 말로네이트의 사용량 100중량부에 대하여 200~300중량부가 사용되는 것을 특징으로 하는 디메틸 2-메틸렌말로네이트의 제조방법.
The method according to claim 3,
The solvent is a method for producing dimethyl 2-methylenemalonate, characterized in that 200 to 300 parts by weight based on 100 parts by weight of formaldehyde and malonate used.
청구항 3에 있어서,
포름알데히드의 사용량은 말로네이트 0.5mole 대비 0.25~0.6mole인 것을 특징으로 하는 디메틸 2-메틸렌말로네이트의 제조방법.
The method according to claim 3,
Formaldehyde is used in the production method of dimethyl 2-methylenemalonate, characterized in that 0.25 ~ 0.6mole compared to malonate 0.5mole.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2995664A1 (en) 2014-09-12 2016-03-16 Afinitica Technologies, S. L. Fast and universal adhesive
EP2995663A1 (en) 2014-09-12 2016-03-16 Afinitica Technologies, S. L. Fast and elastic adhesive
EP3124509A1 (en) 2015-07-31 2017-02-01 Afinitica Technologies, S. L. Fast light curing cyanoacrylate compositions
CN110204441A (en) * 2013-01-11 2019-09-06 瑟拉斯公司 The method for obtaining methylene malonate by the approach of bis- (methylol) malonates

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Publication number Priority date Publication date Assignee Title
US3197318A (en) * 1960-11-07 1965-07-27 Borden Co 2-methylenemalonic acid ester contact adhesive compositions

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Publication number Priority date Publication date Assignee Title
CN110204441A (en) * 2013-01-11 2019-09-06 瑟拉斯公司 The method for obtaining methylene malonate by the approach of bis- (methylol) malonates
EP2995664A1 (en) 2014-09-12 2016-03-16 Afinitica Technologies, S. L. Fast and universal adhesive
EP2995663A1 (en) 2014-09-12 2016-03-16 Afinitica Technologies, S. L. Fast and elastic adhesive
WO2016038514A1 (en) 2014-09-12 2016-03-17 Afinitica Technologies, S. L. Fast and elastic adhesive
US10626299B2 (en) 2014-09-12 2020-04-21 Afinitica Technologies, S.L. Fast and elastic adhesive
EP3124509A1 (en) 2015-07-31 2017-02-01 Afinitica Technologies, S. L. Fast light curing cyanoacrylate compositions
WO2017021785A1 (en) 2015-07-31 2017-02-09 Afinitica Technologies, S.L. Fast light curing cyanoacrylate compositions
US10626310B2 (en) 2015-07-31 2020-04-21 Afinitica Technologies, S.L. Fast light curing cyanoacrylate compositions

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