KR19980067531A - Method for preparing N-alkyl-β-hydroxy ethyl sulfon aniline derivative - Google Patents
Method for preparing N-alkyl-β-hydroxy ethyl sulfon aniline derivative Download PDFInfo
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- KR19980067531A KR19980067531A KR1019970003601A KR19970003601A KR19980067531A KR 19980067531 A KR19980067531 A KR 19980067531A KR 1019970003601 A KR1019970003601 A KR 1019970003601A KR 19970003601 A KR19970003601 A KR 19970003601A KR 19980067531 A KR19980067531 A KR 19980067531A
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C317/00—Sulfones; Sulfoxides
- C07C317/26—Sulfones; Sulfoxides having sulfone or sulfoxide groups and nitrogen atoms, not being part of nitro or nitroso groups, bound to the same carbon skeleton
- C07C317/32—Sulfones; Sulfoxides having sulfone or sulfoxide groups and nitrogen atoms, not being part of nitro or nitroso groups, bound to the same carbon skeleton with sulfone or sulfoxide groups bound to carbon atoms of six-membered aromatic rings of the carbon skeleton
- C07C317/34—Sulfones; Sulfoxides having sulfone or sulfoxide groups and nitrogen atoms, not being part of nitro or nitroso groups, bound to the same carbon skeleton with sulfone or sulfoxide groups bound to carbon atoms of six-membered aromatic rings of the carbon skeleton having sulfone or sulfoxide groups and amino groups bound to carbon atoms of six-membered aromatic rings being part of the same non-condensed ring or of a condensed ring system containing that ring
- C07C317/36—Sulfones; Sulfoxides having sulfone or sulfoxide groups and nitrogen atoms, not being part of nitro or nitroso groups, bound to the same carbon skeleton with sulfone or sulfoxide groups bound to carbon atoms of six-membered aromatic rings of the carbon skeleton having sulfone or sulfoxide groups and amino groups bound to carbon atoms of six-membered aromatic rings being part of the same non-condensed ring or of a condensed ring system containing that ring with the nitrogen atoms of the amino groups bound to hydrogen atoms or to carbon atoms
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C315/00—Preparation of sulfones; Preparation of sulfoxides
- C07C315/04—Preparation of sulfones; Preparation of sulfoxides by reactions not involving the formation of sulfone or sulfoxide groups
Abstract
본 발명은 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 제조 방법에 관한 것이다.The present invention relates to a process for the preparation of N-alkyl-β-hydroxy ethyl sulfone aniline derivatives.
본 발명은 알데히드 또는 케톤류와 β-(히드록시 에틸 설폰)니트로 벤젠 또는 β-(히드록시 에틸 설폰)아닐린을 알콜 또는 케톤 용매하에서 주기율표의 귀금속 VIII족에 속하는 촉매와 더불어 조촉매를 사용하여 일정 온도 및 일정 압력하에서 반응시킴으로써 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 제조시, 촉매의 선택도와 활성을 극대화시켜 반응시간을 단축시키고, 제조된 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 순도를 향상시키는 효과가 있다.The present invention relates to the use of aldehydes or ketones and β- (hydroxyethyl sulfone) nitrobenzene or β- (hydroxyethyl sulfone) aniline in co-catalysts in combination with a catalyst belonging to the Group VIII precious metals of the periodic table in an alcohol or ketone solvent. And N-alkyl-β-hydroxy ethyl sulfone aniline derivatives in the preparation of N-alkyl-β-hydroxy ethyl sulfone aniline derivatives by maximizing the selectivity and activity of the catalyst to shorten the reaction time. It has the effect of improving the purity.
Description
본 발명은 반응성 제조 염료의 원료로 사용되는 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 제조 방법에 관한 것이다.The present invention relates to a process for the preparation of N-alkyl-β-hydroxy ethyl sulfone aniline derivatives used as raw materials for reactive preparation dyes.
종래의 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 제조 방법으로는, 알데히드 또는 케톤류와 β-(히드록시 에틸 설폰)니트로 벤젠 또는 β-(히드록시 에틸 설폰)아닐린을 알콜용매하에서 주기율표의 귀금속 VIII족에 속하는 촉매를 사용하여 수소 첨가 알킬화 반응을 시켜 제조하는 방법이 가장 일반적인 방법이나, 이러한 방법에 따라 반응시킬 경우 반응이 완료되기 까지는 3내지 10시간 정도의 긴 반응시간이 소요되고 생성물의 순도가 낮은 문제점이 있었다.Conventional methods for producing N-alkyl-β-hydroxy ethyl sulfone aniline derivatives include aldehydes or ketones and β- (hydroxy ethyl sulfone) nitrobenzene or β- (hydroxy ethyl sulfone) aniline in an alcohol solvent. Hydrogenated alkylation using a catalyst belonging to group VIII of the noble metal is the most common method, but when reacting according to this method, it takes about 3 to 10 hours to complete the reaction. There was a problem of low purity.
본 발명은 이와 같이 종래의 문제점을 해결하기 위해 창안된 것으로서, 촉매의 선택도와 활성을 극대화시켜 반응시간을 단축시키고, 제조된 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 순도를 향상시킨 개선된 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 제조 방법을 제공하는데 목적이 있다.The present invention has been devised to solve the above-mentioned conventional problems, and maximizes the selectivity and activity of the catalyst to shorten the reaction time and improve the purity of the prepared N-alkyl-β-hydroxy ethyl sulfone aniline derivatives. It is an object to provide a process for the preparation of N-alkyl-β-hydroxy ethyl sulfone aniline derivatives.
이러한 목적을 달성하기 위한 본 발명의 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 제조 방법은, 알데히드 또는 케톤류와 β-(히드록시 에틸 설폰)니트로 벤젠 또는 β-(히드록시 에틸 설폰)아닐린을 알콜 또는 케톤 용매하에서 주기율표의 귀금속 VIII족에 속하는 촉매와 더불어 조촉매를 사용하여 일정 온도 및 일정 압력하에서 반응시킴을 특징으로 한다.The method for producing an N-alkyl-β-hydroxy ethyl sulfone aniline derivative of the present invention for achieving this object is aldehyde or ketones and β- (hydroxy ethyl sulfone) nitrobenzene or β- (hydroxy ethyl sulfone) aniline Is reacted under constant temperature and pressure using a cocatalyst with a catalyst belonging to the noble metal group VIII of the periodic table in an alcohol or ketone solvent.
본 발명은 알데히드 또는 케톤류와 β-(히드록시 에틸 설폰)니트로 벤젠 또는 β-(히드록시 에틸 설폰)아닐린을 알콜 또는 케톤 용매하에서 주기율표의 귀금속 VIII족에 속하는 촉매와 더불어 조촉매를 사용하여 일정 온도 및 일정 압력하에서 반응시킴으로서 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 제조하는 것이다.The present invention relates to the use of aldehydes or ketones and β- (hydroxyethyl sulfone) nitrobenzene or β- (hydroxyethyl sulfone) aniline in co-catalysts in combination with a catalyst belonging to the Group VIII precious metals of the periodic table in an alcohol or ketone solvent. And reaction under constant pressure to prepare N-alkyl-β-hydroxy ethyl sulfone aniline derivatives.
본 발명에서 이용되는 β-(히드록시 에틸 설폰)니트로 벤젠은 하기의 구조식을 가진 화합물이며,Β- (hydroxyethyl sulfone) nitro benzene used in the present invention is a compound having the following structural formula,
β-(히드록시 에틸 설폰)아닐린은 하기의 구조식을 가진 화합물이다.β- (hydroxy ethyl sulfone) aniline is a compound having the structure
또한, 알데히드와 케톤은 하기의 구조식을 가지는 화합물을 말한다.In addition, aldehyde and ketone refer to a compound having the following structural formula.
(식 중, R1, R2는 H 또는 CnH2n+1의 화학식을 갖는 알킬기임)(Wherein R 1 , R 2 is an alkyl group having the formula of H or C n H 2n + 1 )
β-(히드록시 에틸 설폰)니트로 벤젠 또는 β-(히드록시 에틸 설폰)아닐린과 알데히드 또는 케톤류의 반응물로서의 반응비는 몰수비로 1:1~1.5가 바람직하다.As for the reaction ratio of (beta)-(hydroxy ethyl sulfone) nitrobenzene or (beta)-(hydroxy ethyl sulfone) aniline, and an aldehyde or a ketone, as a reaction ratio, 1: 1-1.5 are preferable in molar ratio.
예를 들어, 니켈, 팔라듐, 플레티늄 등 주기율표의 귀금속 VIII족에 속하는 원소가 촉매로 사용될 수 있으며, 담체위에 침적시킨 팔라듐, 담체위에 침적시킨 백금, 활성화시킨 니켈 등이 바람직하다. 촉매로 사용되는 귀금속 VIII족에 속하는 원소는 β-(히드록시 에틸 설폰)니트로 벤젠 또는 β-(히드록시 에틸 설폰)아닐린 중량의 1.5~3%를 사용하는 것이 바람직하다.For example, an element belonging to the Group VIII of the periodic table such as nickel, palladium, platinum and the like can be used as a catalyst, and palladium deposited on a carrier, platinum deposited on a carrier, activated nickel, and the like are preferable. The element belonging to the noble metal group VIII used as a catalyst is preferably 1.5 to 3% by weight of β- (hydroxy ethyl sulfone) nitrobenzene or β- (hydroxy ethyl sulfone) aniline.
활성탄 또는 인산등이 조촉매로 사용되며 β-(히드록시 에틸 설폰)니트로 벤젠 또는 β-(히드록시 에틸 설폰)아닐린 중량의 0.001~3%를 사용하는 것이 바람직하다.Activated carbon or phosphoric acid is used as a promoter and it is preferable to use 0.001 to 3% of the weight of β- (hydroxy ethyl sulfone) nitrobenzene or β- (hydroxy ethyl sulfone) aniline.
또한, 일정 온도 및 일정 압력이란 50~160℃의 온도범위와 수소압력 5~50 kg/cm2의 압력범위가 바람직하다.The constant temperature and the constant pressure are preferably in the temperature range of 50 to 160 ° C. and the pressure range of 5 to 50 kg / cm 2 of hydrogen pressure.
본 발명에서 케톤류와 β-(히드록시 에틸 설폰)니트로 벤젠 또는 β-(히드록시 에틸 설폰)아닐린을 알콜 용매를 사용하지 않고 반응물인 케톤을 용매로 사용하여 니켈, 팔라듐, 플레티늄 등 주기율표의 귀금속 VIII족에 속하는 촉매와 활성탄 또는 인산등 조촉매를 함께 사용하여 일정 온도 및 일정 압력하에서 반응시킴으로써 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체의 제조하는 경우에는 반응속도 및 생성물의 순도를 더욱 향상시킬 수 있다.In the present invention, ketones and β- (hydroxy ethyl sulfone) nitrobenzene or β- (hydroxy ethyl sulfone) aniline are used as a solvent without using an alcohol solvent as reactants, and precious metals of the periodic table such as nickel, palladium, and platinum are used. When the N-alkyl-β-hydroxyethyl sulfone aniline derivative is prepared by reacting a catalyst belonging to the group with a cocatalyst such as activated carbon or phosphoric acid at a constant temperature and a constant pressure, the reaction rate and the purity of the product may be further improved. Can be.
이하 본 발명을 하기의 실시예를 통해 구체적으로 설명하고자 하나, 이는 본 발명의 실시예에 불과할 뿐 본 발명이 이에 한정되는 것은 아니다.Hereinafter, the present invention will be described in detail with reference to the following examples, which are only examples of the present invention, but the present invention is not limited thereto.
[실시예 1]Example 1
3-β-(히드록시 에틸 설폰)아닐린 70g, 메탄올 200g, 5%의 Pd/C(탄소상의 팔라듐 촉매) 1.56g, 조촉매로서 인산 0.03~0.05g, 아세트 알데히드 17.6g을 반응기내에 넣은 후 반응기를 밀폐하고 공기를 질소로 치환하였다.70 g of 3-β- (hydroxy ethyl sulfone) aniline, 200 g of methanol, 1.56 g of 5% Pd / C (palladium catalyst on carbon), 0.03 to 0.05 g of phosphoric acid as a promoter, and 17.6 g of acetaldehyde were added to the reactor Was sealed and air was replaced with nitrogen.
80~95℃의 온도, 30~40 kg/cm2의 압력으로 40분동안 환원 알킬화 반응을 진행시켰다. 촉매 여과후 용매를 감압 증류하여 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린을 수득하였으며 전환율은 100%였다.The reduction alkylation reaction was performed for 40 minutes at the temperature of 80-95 degreeC, and the pressure of 30-40 kg / cm <2> . After filtration of the catalyst, the solvent was distilled off under reduced pressure to obtain 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline and the conversion was 100%.
HPLC(고압 액체 크로마토그래피)분석 결과, 수득한 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린의 순도는 91%이상이었다.HPLC (high pressure liquid chromatography) analysis showed that the obtained 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline had a purity of 91% or more.
[실시예 2]Example 2
3-β-(히드록시 에틸 설폰)니트로벤젠 70g, 메탄올 200g, 5%의 Pd/C(탄소상의 팔라듐 촉매) 1.56g, 조촉매로서 활성탄 1.56g, 아세트 알데히드 17.4g을 반응기내에 넣은 후 반응기를 밀폐하고 공기를 질소로 치환하였다.70 g of 3-β- (hydroxy ethyl sulfone) nitrobenzene, 200 g of methanol, 1.56 g of 5% Pd / C (palladium catalyst on carbon), 1.56 g of activated carbon as a promoter, and 17.4 g of acetaldehyde were added to the reactor, and then the reactor was It was sealed and air was replaced with nitrogen.
초기 수소압력은 5~15 kg/cm2, 온도는 80℃ 이하로 반응을 30분간 진행시킨 후 압력을 30~40 kg/cm2, 온도는 80~95℃로 올려 40분동안 환원 알킬화 반응을 진행시켰다. 촉매 여과후 용매를 감압 증류하여 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린을 수득하였으며, 총 반응시간은 70분이 소요되었고, 전환율은 100%였다.The initial hydrogen pressure is 5 ~ 15 kg / cm 2 , the temperature is 80 ℃ or less, the reaction proceeds for 30 minutes, and the pressure is raised to 30 ~ 40 kg / cm 2 and the temperature is 80 ~ 95 ℃ for 40 minutes. Proceeded. After filtration of the catalyst, the solvent was distilled off under reduced pressure to obtain 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline. The total reaction time was 70 minutes and the conversion was 100%.
HPLC(고압 액체 크로마토그래피)분석 결과, 수득한 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린의 순도는 91%이상이었다.HPLC (high pressure liquid chromatography) analysis showed that the obtained 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline had a purity of 91% or more.
[실시예 3]Example 3
3-β-(히드록시 에틸 설폰)니트로벤젠 70g, 메탄올 200g, 5%의 Pd/C(탄소상의 팔라듐 촉매) 1.56g, 조촉매로서 인산 0.03~0.05g, 아세트 알데히드 17.4g을 반응기내에 넣은 후 반응기를 밀폐하고 공기를 질소로 치환하였다.70 g of 3-β- (hydroxy ethyl sulfone) nitrobenzene, 200 g of methanol, 1.56 g of 5% Pd / C (palladium catalyst on carbon), 0.03 to 0.05 g of phosphoric acid as a promoter, and 17.4 g of acetaldehyde were added to the reactor. The reactor was sealed and air was replaced with nitrogen.
초기 수소압력은 5~15 kg/cm2, 온도는 80℃ 이하로 반응을 20분간 진행시킨 후 압력을 30~40 kg/cm2, 온도는 80~95℃로 올려 50분동안 환원 알킬화 반응을 진행시켰다. 촉매 여과후 용매를 감압 증류하여 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린을 수득하였으며 전환율은 100%였다.The initial hydrogen pressure is 5 ~ 15 kg / cm 2 , the temperature is 80 ℃ or less, the reaction proceeds for 20 minutes, and the pressure is raised to 30 ~ 40 kg / cm 2 and the temperature is 80 ~ 95 ℃ for 50 minutes. Proceeded. After filtration of the catalyst, the solvent was distilled off under reduced pressure to obtain 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline and the conversion was 100%.
HPLC(고압 액체 크로마토그래피)분석 결과, 수득한 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린의 순도는 90%이상이었다.As a result of HPLC (high pressure liquid chromatography) analysis, the obtained 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline had a purity of 90% or more.
[실시예 4]Example 4
3-β-(히드록시 에틸 설폰)아닐린 70g, 메탄올 200g, 5%의 Pd/C(탄소상의 팔라듐 촉매) 1.56g, 조촉매로서 활성탄 1.56g, 아세트 알데히드 17.4g을 반응기내에 넣은 후 반응기를 밀폐하고 공기를 질소로 치환하였다.70 g of 3-β- (hydroxy ethyl sulfone) aniline, 200 g of methanol, 1.56 g of 5% Pd / C (palladium catalyst on carbon), 1.56 g of activated carbon as a promoter, and 17.4 g of acetaldehyde were placed in the reactor, and the reactor was sealed. And air was replaced with nitrogen.
80~95℃의 온도, 30~40 kg/cm2의 압력으로 40분동안 환원 알킬화 반응을 진행시켰다. 촉매 여과후 용매를 감압 증류하여 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린을 수득하였으며 전환율은 100%였다.The reduction alkylation reaction was performed for 40 minutes at the temperature of 80-95 degreeC, and the pressure of 30-40 kg / cm <2> . After filtration of the catalyst, the solvent was distilled off under reduced pressure to obtain 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline and the conversion was 100%.
HPLC(고압 액체 크로마토그래피)분석 결과, 수득한 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린의 순도는 91%이상이었다.HPLC (high pressure liquid chromatography) analysis showed that the obtained 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline had a purity of 91% or more.
[실시예 5]Example 5
3-β-(히드록시 에틸 설폰)니트로벤젠 70g, 아세톤 200g, 3%의 Pt/C(탄소상의 플래티늄 촉매) 1.56g, 조촉매로서 인산 0.03~0.05g을 반응기내에 넣은 후 반응기를 밀폐하고 공기를 질소로 치환하였다.70 g of 3-β- (hydroxy ethyl sulfone) nitrobenzene, 200 g of acetone, 1.56 g of 3% Pt / C (platinum catalyst on carbon), 0.03 to 0.05 g of phosphoric acid as a promoter, the reactor was sealed and air Was replaced with nitrogen.
초기 수소압력은 5~15 kg/cm2, 온도는 80℃ 이하로 반응을 30분간 진행시킨 후 압력을 30~40 kg/cm2, 온도는 150℃로 올려 60분동안 환원 알킬화 반응을 진행시켰다. 촉매 여과후 용매를 감압 증류하여 3-β-(히드록시 에틸 설폰)-N-이소프로필 벤젠을 수득하였으며, 총반응시간은 90분이 소요되었고, 전환율은 100%였다.The initial hydrogen pressure was 5 ~ 15 kg / cm 2 , the temperature was lowered to 80 ° C. for 30 minutes, the pressure was raised to 30-40 kg / cm 2 , and the temperature was raised to 150 ° C. for 60 minutes. . After filtration of the catalyst, the solvent was distilled off under reduced pressure to obtain 3-β- (hydroxy ethyl sulfone) -N-isopropyl benzene. The total reaction time was 90 minutes and the conversion was 100%.
HPLC(고압 액체 크로마토그래피)분석 결과, 수득한 3-β-(히드록시 에틸 설폰)-N-이소프로필 벤젠의 순도는 95%이상이었다.HPLC (high pressure liquid chromatography) analysis showed that the obtained 3-β- (hydroxy ethyl sulfone) -N-isopropyl benzene had a purity of 95% or more.
[실시예 6]Example 6
3-β-(히드록시 에틸 설폰)니트로벤젠 70g, 아세톤 200g, 3%의 Pt/C(탄소상의 플래티늄 촉매) 1.56g, 조촉매로서 활성탄 1.56g을 반응기내에 넣은 후 반응기를 밀폐하고 공기를 질소로 치환하였다.70 g of 3-β- (hydroxy ethyl sulfone) nitrobenzene, 200 g of acetone, 1.56 g of 3% Pt / C (platinum catalyst on carbon), 1.56 g of activated carbon as a promoter were placed in the reactor, and the reactor was sealed and air was Substituted by
초기 수소압력은 5~15 kg/cm2, 온도는 80℃ 이하로 반응을 30분간 진행시킨 후 압력을 30~40 kg/cm2, 온도는 150℃로 올려 40분동안 환원 알킬화 반응을 진행시켰다. 촉매 여과후 용매를 감압 증류하여 3-β-(히드록시 에틸 설폰)-N-이소프로필 벤젠을 수득하였으며, 총반응시간은 80분이 소요되었고, 전환율은 100%였다.The initial hydrogen pressure was 5 ~ 15 kg / cm 2 , the temperature was lowered to 80 ° C. for 30 minutes, and the pressure was raised to 30-40 kg / cm 2 and the temperature was raised to 150 ° C. for 40 minutes. . After filtration of the catalyst, the solvent was distilled off under reduced pressure to obtain 3-β- (hydroxy ethyl sulfone) -N-isopropyl benzene. The total reaction time was 80 minutes and the conversion was 100%.
HPLC(고압 액체 크로마토그래피)분석 결과, 수득한 3-β-(히드록시 에틸 설폰)-N-이소프로필 벤젠의 순도는 95%이상이었다.HPLC (high pressure liquid chromatography) analysis showed that the obtained 3-β- (hydroxy ethyl sulfone) -N-isopropyl benzene had a purity of 95% or more.
N-알킬-β-히드록시 에틸 설폰 아닐린 유도체 제조시 조촉매를 사용하지 않는 종래의 방법과 조촉매를 사용하는 본원 발명의 제조방법의 소요시간 및 수율 등을 비교하기 위하여 하기의 비교 실험을 실시하였다.The following comparative experiments were carried out to compare the time required and the yield of the conventional method using no cocatalyst in the preparation of N-alkyl-β-hydroxyethyl sulfone aniline derivatives and the preparation method of the present invention using the cocatalyst. It was.
[비교예 1]Comparative Example 1
3-β-(히드록시 에틸 설폰)니트로 벤젠 70g, 메탄올 200g, 5%의 Pd/C(탄소상의 팔라듐 촉매) 1.56g, 아세트 알데히드 17.4g을 반응기내에 넣은 후 반응기를 밀폐하고 공기를 질소로 치환하였다.70 g of 3-β- (hydroxy ethyl sulfone) nitrobenzene, 200 g of methanol, 1.56 g of 5% Pd / C (carbon-based palladium catalyst) and 17.4 g of acetaldehyde were placed in the reactor, and the reactor was sealed and air was replaced with nitrogen. It was.
초기 수소압력은 5~15 kg/cm2, 온도는 80℃ 이하로 반응을 30분간 진행시킨 후 수소압력을 30~40 kg/cm2, 온도는 85-95℃로 올려 2시간 30분동안 환원 알킬화 반응을 진행시켰다. 촉매 여과후 용매를 감압 증류하여 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린을 수득하였으며, 총반응시간은 3시간이 소요되었고, 전환율은 100%였다. 80~95℃의 온도, 30~40 kg/cm2의 압력으로 40분동안 환원 알킬화 반응을 진행시켰다. 촉매 여과후 용매를 감압 증류하여 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린을 수득하였으며 전환율은 100%였다.The initial hydrogen pressure is 5 ~ 15 kg / cm 2 , the temperature is 80 ℃ or less, and the reaction proceeds for 30 minutes, and then the hydrogen pressure is raised to 30 ~ 40 kg / cm 2 and the temperature is 85-95 ℃ and reduced for 2 hours 30 minutes. The alkylation reaction proceeded. After filtration of the catalyst, the solvent was distilled under reduced pressure to obtain 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline, and the total reaction time was 3 hours and the conversion was 100%. The reduction alkylation reaction was performed for 40 minutes at the temperature of 80-95 degreeC, and the pressure of 30-40 kg / cm <2> . After filtration of the catalyst, the solvent was distilled off under reduced pressure to obtain 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline and the conversion was 100%.
HPLC(고압 액체 크로마토그래피)분석 결과, 수득한 3-β-(히드록시 에틸 설폰)-N-에틸 아닐린의 순도는 87%이상이었다.HPLC (high pressure liquid chromatography) analysis showed that the obtained 3-β- (hydroxy ethyl sulfone) -N-ethyl aniline had a purity of 87% or more.
[비교예 2]Comparative Example 2
3-β-(히드록시 에틸 설폰)니트로 벤젠 70g, 메탄올 200g, 3%의 Pt/C(탄소상의 플래티늄 촉매) 1.56g, 아세톤 26.7g을 반응기내에 넣은 후 반응기를 밀폐하고 공기를 질소로 치환하였다.70 g of 3-β- (hydroxy ethyl sulfone) nitrobenzene, 200 g of methanol, 1.56 g of 3% Pt / C (platinum catalyst on carbon) and 26.7 g of acetone were placed in the reactor, and the reactor was sealed and air was replaced with nitrogen. .
초기 수소압력은 5~15 kg/cm2, 온도는 80℃ 이하로 반응을 30분간 진행시킨 후 수소압력을 30~40 kg/cm2, 온도는 150℃로 올려 4시간 30분동안 환원 알킬화 반응을 진행시켰다. 촉매 여과후 용매를 감압 증류하여 3-β-(히드록시 에틸 설폰)-N-이소프로필 아닐린을 수득하였으며, 총반응시간은 5시간이 소요되었고, 전환율은 98%였다.The initial hydrogen pressure is 5 ~ 15 kg / cm 2 , the temperature is 80 ℃ or less, and the reaction proceeds for 30 minutes, and then the hydrogen pressure is raised to 30 ~ 40 kg / cm 2 and the temperature is 150 ℃ for 4 hours 30 minutes Proceeded. After filtration of the catalyst, the solvent was distilled off under reduced pressure to obtain 3-β- (hydroxy ethyl sulfone) -N-isopropyl aniline. The total reaction time was 5 hours and the conversion was 98%.
HPLC(고압 액체 크로마토그래피)분석 결과, 수득한 3-β-(히드록시 에틸 설폰)-N-이소프로필 아닐린의 순도는 90-93%였다.As a result of HPLC (high pressure liquid chromatography) analysis, the purity of the obtained 3-β- (hydroxy ethyl sulfone) -N-isopropyl aniline was 90-93%.
이상에서 상세히 설명한 바와 같은 본 발명은 알데히드 또는 케톤류와 β-(히드록시 에틸 설폰)니트로 벤젠 또는 β-(히드록시 에틸 설폰)아닐린을 알콜 또는 케톤 용매하에서 주기율표의 귀금속 VIII족에 속하는 촉매와 더불어 조촉매를 사용하여 일정 온도 및 일정 압력하에서 반응시킴으로써 N-알킬-β-히드록시 에틸 설폰 아닐린 유도체 제조시, 반응시간을 현저하게 단축시키고 생성물의 순도 및 수율을 향상시킬 수 있는 효과가 있다.As described in detail above, the present invention provides crude aldehyde or ketones and β- (hydroxy ethyl sulfone) nitrobenzene or β- (hydroxy ethyl sulfone) aniline together with a catalyst belonging to the Group VIII of the precious metal of the periodic table in an alcohol or ketone solvent. In the preparation of N-alkyl-β-hydroxy ethyl sulfon aniline derivatives by reacting at a constant temperature and a constant pressure using a catalyst, the reaction time can be significantly shortened and the purity and yield of the product can be improved.
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