KR880001842B1 - Process for the preparation of ethyl-4,6,6,6-tetrachloro-3,3,-dimethyl hexenoate - Google Patents
Process for the preparation of ethyl-4,6,6,6-tetrachloro-3,3,-dimethyl hexenoate Download PDFInfo
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- KR880001842B1 KR880001842B1 KR1019850001391A KR850001391A KR880001842B1 KR 880001842 B1 KR880001842 B1 KR 880001842B1 KR 1019850001391 A KR1019850001391 A KR 1019850001391A KR 850001391 A KR850001391 A KR 850001391A KR 880001842 B1 KR880001842 B1 KR 880001842B1
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Abstract
Description
본 발명은 피페트로이드계 살충제 중에서 퍼메트린, 사이퍼메트린 등의 산 성분인 퍼메트린 산을 합성하는데 필요한 에틸-4,6,6,6-테트라클로로-3,3-디메틸헥산노이에트(이하 ETDH라 함)의 제조방법에 관한 것이다.In the present invention, ethyl-4,6,6,6-tetrachloro-3,3-dimethylhexanenoate (hereinafter referred to as ETDH) required for synthesizing permethrinic acid, which is an acid component such as permethrin and cypermethrin, is used in a pipetroid insecticide. It relates to a manufacturing method of.
종래에는 에틸 3,3-디메틸-4-펜텐노에이트(이하 EDP라 함)에 CCl4를 첨가하는 방법으로 ETDH를 제조하였다. 그리고 출발물질 EDP는 트리에틸오르토 아세테이트(TOA)와 프레놀을 산 촉매하에서 크라이젠 전위반응(Claisen rearrangement reaction)에 의해 합성하는데, 이 반응에서는 EDP와 부산물인 프레닐 3,3-디메틸-4-펜텐노에이트(MBDP)가 생성되기 때문에 진공증류시켜 EDP를 수득하고 이어서 부산물인 MBDP는 과량의 에탄올에 산촉매로 트랜스-에스테르화 시킨후 진공증류로 다시 EDP로 전환시킨다.Conventionally, ETDH was prepared by adding CCl 4 to ethyl 3,3-dimethyl- 4- pentenenoate (hereinafter referred to as EDP). The starting material EDP synthesizes triethylortho acetate (TOA) and prenol by a Claisen rearrangement reaction under an acid catalyst, in which prenyl 3,3-dimethyl-4-phene is a byproduct of EDP. Since tennoate (MBDP) is produced, vacuum distillation yields EDP, and the by-product MBDP is trans-esterified with an acid catalyst in excess ethanol and then converted back to EDP by vacuum distillation.
이를 반응식으로 표시하면 다음과 같다.This is expressed as a reaction scheme as follows.
그러나 상기와 같은 방법으로 ETDH를 얻는 경우는 첫째, 출발물질인 EDP를 증류시켜 부산물인 MBDP와 분리시켜야 하므로 증류에 의한 비용이 많이 소요될 뿐 아니라 수율을 높이기 위하여 분리된 MBDP를 트랜스-에스테르화시켜 다시 EDP로 전환시키는 과정이 필요한 2단계 조작으로 수행하므로 조작이 복잡하다.However, in the case of obtaining ETDH as described above, first, since the starting material EDP must be distilled and separated from the by-product MBDP, it is not only costly by distillation but also trans-esterified the separated MBDP to increase the yield. The operation is complicated because the conversion to EDP is performed in two stages of operation.
둘째, 생성된 ETDH의 수율이 낮을 뿐 아니라 순도가 낮아 고진공 증류에 의해 정제시켜야 한다.Second, the yield of the produced ETDH is not only low but also low in purity and should be purified by high vacuum distillation.
세째, EDP의 수율을 높이기 위하여 고가의 TOA를 과량(페놀당 1.3-3.0 당량)사용하므로 비경제적이다.Third, it is uneconomical to use excessive TOA (1.3-3.0 equivalents per phenol) to increase the yield of EDP.
본 발명자들은 상기와 같은 문제점을 해결하기 위하여 예의 연구한 결과 3,3-디메틸-4-펜텐산(이하 DPA라 함)을 출발물질로 하여 CCl4와 FeCl2·4H2O를 에탄올 중에서 반응시키면 에스테르 반응과 CCl4첨가 반응이 동시에 일어나서 최종 생성물인 ETDH를 합성 할 수 있다는데 착안하여 본 발명을 완성하게 된 것이다.The present inventors earnestly researched to solve the above problems, and when 3,3-dimethyl-4-pentenoic acid (hereinafter referred to as DPA) is used as a starting material, CCl 4 and FeCl 2 · 4H 2 O are reacted in ethanol. The present invention was completed in view of the fact that the ester reaction and the CCl 4 addition reaction occur simultaneously to synthesize the final product ETDH.
본 발명의 DPA는 TOA와 프레놀을 크라이젠 전위 반응시켜 EDP와 MBDP의 반응 물을 얻은 후 수산화나트륨 또는 수산화칼륨으로 가수분해하여 수득한다. 이와같이 얻은 DPA는 순도가 높아(순도 98% 이상) 정제과정 없이 ETDH 반응에 사용된다.DPA of the present invention is obtained by reacting TOA and prenol with a Kreisen potential to obtain a reaction product of EDP and MBDP, and then hydrolyzing with sodium or potassium hydroxide. The DPA thus obtained is of high purity (more than 98% purity) and is used for ETDH reactions without purification.
본 발명의 방법을 상세히 설명하면 하기와 같다. 프레놀과 TOA를 반응시켜 EDP와 MBDP의 반응물을 만들어 ETDH를 제조함에 있어서, 상기 EDP와 MBDP의 조성비가 4 : 1인 반응물 1몰을 수산화나트륨 1.0-1.5 당량 또는 수산화칼륨 1.0-1.5 당량으로 가수분해시켜 DPA를 합성하고 이 DPA를 에탄올 5-7 당량 중에서 CCl4-2-4 당량과 제 1 염화철, 수화물 0.15-0.25 당량과를 반응시켜 에스테르화 반응과 CCl4첨가가 동시에 일어나게 함을 특징으로 하는 ETDH 합성방법이다. 이를 반응식으로 표시하면 다음과 같다.The method of the present invention is described in detail as follows. In preparing ETDH by reacting prenol and TOA to make a reactant of EDP and MBDP, 1 mole of a reactant having a composition ratio of EDP and MBDP of 4: 1 is added at 1.0-1.5 equivalents of sodium hydroxide or 1.0-1.5 equivalents of potassium hydroxide. Decomposition is performed to synthesize DPA, and this DPA is reacted with CCl 4 -2-4 equivalents and ferrous chloride and hydrates 0.15-0.25 equivalents in 5-7 equivalents of ethanol to cause simultaneous esterification and addition of CCl 4 . ETDH synthesis method. This is expressed as a reaction scheme as follows.
상기와 같은 본 발명의 방법으로 얻은 ETDH는 종래 방법보다 다음과 같은 장점이 있다.The ETDH obtained by the method of the present invention as described above has the following advantages over the conventional method.
첫째, EDP 합성시 출발물질인 프레놀은 촉매인 산에 의하여 약 10%정도 분해되는데 반해 본 발명에서는 용매인 크실렌을 사용함으로 1% 이하로 분해되게 하여 프레놀의 량을 절감시킨다.First, in the synthesis of EDP, the starting material of prenol is decomposed about 10% by acid as a catalyst, while in the present invention, the amount of prenol is reduced by using 1% or less of xylene as a solvent.
둘째, 출발물질인 DPA는 EDP와 MBDP를 가수분해 하여 얻을 수 있으므로 2단계로 EDP를 얻는 종래의 방법에 비해 단일공정으로 쉽게 얻을 수 있고 순도가 높아 진공증류등의 정제과정이 필요없다.Second, since the starting material DPA can be obtained by hydrolyzing EDP and MBDP, it can be easily obtained in a single process compared to the conventional method of obtaining EDP in two stages, and the purification is not necessary because of high purity.
셋째, 종래 방법인 EDP를 효과적으로 얻기 위해서는 프레놀에 대한 TOA 당량비가 1.3-3.0당량으로 사용되는데 반해 본 발명의 DPA를 얻기 위해서는 TOA가 0.6-0.8당량으로 소량 사용되므로 경제적이다.Third, in order to effectively obtain the conventional EDP, the TOA equivalent ratio to prenol is used in 1.3-3.0 equivalents, while the TOA is used in small amounts in 0.6-0.8 equivalents to obtain the DPA of the present invention.
넷째, EDP에서 출발하여 얻은 ETDH는 진공증류를 거쳐야만 순도가 높은 ETDH를 얻을 수 있었으나, DPA를 출발물질로 하여 얻은 ETDH는 순도가 높아(순도 97%이상) 퍼메트린 산합성에 정제과정 없이 사용될 수 있다.Fourth, ETDH obtained from EDP can be obtained only by vacuum distillation to obtain high purity ETDH.However, ETDH obtained from DPA as a starting material has high purity (more than 97% purity) and can be used without purification for permethrin synthesis. .
이하 본 발명의 방법을 실시예에 의해 상세히 설명하기로 한다.Hereinafter, the method of the present invention will be described in detail by way of examples.
[실시예 1]Example 1
프레놀 95.6g(1.15몰), TOA 162.23g(1.00몰) 및 크실렌 50g에 87% 인산 0.98g(0.01몰)을 넣고 반응온도는 140℃에서 5시간 동안 환류시켜 에탄올이 완전히 증류되도록 한다. 이어서 반응물을 실온까지 냉각한 후 40% 수산화나트륨 수용액 100.03g(1.00몰)을 첨가하여 30분간 환류시키면서 가수분해시킨 다음, 물 120g을 첨가하고, 크실렌과 프레놀을 스팀증류시켜 제거한다. 물층의 생성물에 50% 황산 98g을 가하여 PH를 4로 조절한 후 CCl4340g 및 CCl4171g으로 각각 2번 추출한다. 여기서 추출한 4염화탄소층을 황산 마그네슘으로 탈수하여 여과한 액에 에탄올 230g(5.00몰)과 제 1 염화철,4수화물 39.80g(0.20몰)을 넣고 6시간 환류하여 실온까지 냉각한 후 물 500g과 5%수산화나트륨 수용액 300g으로 세척하고 황산마그네슘으로 건조한 다음 4염화탄소를 완전히 제거하여 ETDH 267.3g을 수득하였다. 이때 TOA에 대한 ETDH의 수율은 85%이다. (순도 97%이상)0.95.6 g (0.01 mol) of 87% phosphoric acid is added to 95.6 g (1.15 mol) of prenol, 162.23 g (1.00 mol) of TOA and 50 g of xylene, and the reaction temperature is refluxed at 140 ° C. for 5 hours to allow the ethanol to be distilled completely. The reaction was then cooled to room temperature and hydrolyzed with reflux for 30 minutes with the addition of 100.03 g (1.00 mol) of 40% aqueous sodium hydroxide solution, then 120 g of water were added and xylene and prenol were removed by steam distillation. 98g of 50% sulfuric acid was added to the product of the water layer to adjust the pH to 4, and then extracted twice with CCl 4 340g and CCl 4 171g, respectively. The carbon tetrachloride extracted here was dehydrated with magnesium sulfate, and 230 g (5.00 mol) of ethanol, 39.80 g (0.20 mol) of ferrous chloride and tetrahydrate were added to the filtrate, and the mixture was refluxed for 6 hours, cooled to room temperature, and then cooled to 500 g and 5 Washed with 300 g of aqueous sodium hydroxide solution, dried over magnesium sulfate, and completely removed carbon tetrachloride to obtain 267.3 g of ETDH. The yield of ETDH against TOA is 85%. (More than 97% of purity)
[실시예 2]Example 2
DPA 128.22g(1.00몰), 4염화탄소 461.52g(3.00몰), 에탄올 276.00g(6.0몰) 및 제 1 염화철, 4수화물 39.73g(0.20몰)의 혼합액을 6시간 동안 환류시킨 다음 물 500.00g, 50% 수산화나트륨 수용액 300.00g으로 세척한다. 이어서 황산마그네슘으로 탈수한 후 4염화탄소를 완전히 제거하여 EDTH 303.69g을 수득하였다. 수율은 97.7%이다.(순도 97.7%)A mixture of 128.22 g (1.00 mole) of DPA, 461.52 g (3.00 mole) of carbon tetrachloride, 276.00 g (6.0 mole) of ethanol, and ferric chloride, 39.73 g (0.20 mole) of tetrahydrate was refluxed for 6 hours, followed by 500.00 g of water. Wash with 300.00 g of 50% aqueous sodium hydroxide solution. After dehydration with magnesium sulfate, carbon tetrachloride was completely removed to give 303.69 g of EDTH. The yield is 97.7% (purity 97.7%).
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KR1019850001391A KR880001842B1 (en) | 1985-03-05 | 1985-03-05 | Process for the preparation of ethyl-4,6,6,6-tetrachloro-3,3,-dimethyl hexenoate |
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KR1019850001391A KR880001842B1 (en) | 1985-03-05 | 1985-03-05 | Process for the preparation of ethyl-4,6,6,6-tetrachloro-3,3,-dimethyl hexenoate |
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