KR950015131B1 - Process for producing polyalkylen oxide-diamine - Google Patents
Process for producing polyalkylen oxide-diamine Download PDFInfo
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- KR950015131B1 KR950015131B1 KR1019920003426A KR920003426A KR950015131B1 KR 950015131 B1 KR950015131 B1 KR 950015131B1 KR 1019920003426 A KR1019920003426 A KR 1019920003426A KR 920003426 A KR920003426 A KR 920003426A KR 950015131 B1 KR950015131 B1 KR 950015131B1
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Abstract
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본 발명은 다음 일반식(Ⅰ)으로 표시되는 폴리알킬렌옥사이드 디아민의 신규 제조방법에 관한 것이다.The present invention relates to a novel method for producing a polyalkylene oxide diamine represented by the following general formula (I).
상기식에서, n은 60-110의 정수이고, R은 에틸렌기 또는 프로필렌기이다.Wherein n is an integer of 60-110 and R is an ethylene group or a propylene group.
상기 일반식(Ⅰ)은 폴리알킬렌옥사이드 디아민은 특수한 용도의 에폭시 수지, 우레탄 등의 경화제 및 폴리아미드 개질제로 쓰이는 공지화합물이다. 일반적인 저분자량의 화합물과는 달리 고분자 화합물에 있어서는 말단기나, 특별한 작용기를 다른 기로 치환하는 기술은 매우 어려운 기술로 알려져 있다.The general formula (I) is a polyalkylene oxide diamine is a known compound used as a curing agent and polyamide modifier of epoxy resin, urethane, etc. for a special use. Unlike general low-molecular weight compounds, the technique of substituting a terminal group or a special functional group with another group in a high molecular compound is known as a very difficult technique.
종래의 기술로서 일본 특허공고 소59-12660에는 폴리에틸렌올사이드로부터 시아노에틸화반응, 고압수소한원반응을 이용하여 폴리에틸렌옥사이드 디아민을 제조하는 방법이 소개되어 있다. 그러나 이 방법은 고압 수소환원반응을 위한 100-150㎏/㎠의 고압설비가 요구되며, 고압수소환원반응 및 시아노에틸화반응의 두단계의 반응으로 반응시간이 길어져 비경제적이며, 또한 제품의 변색이 쉽다.As a conventional technique, Japanese Patent Publication No. 59-12660 discloses a method for producing polyethylene oxide diamine from polyethyleneolside using cyanoethylation reaction and high pressure hydrogen reaction. However, this method requires high pressure equipment of 100-150㎏ / ㎠ for high pressure hydrogen reduction reaction, and it is uneconomical because the reaction time is long due to two-stage reaction of high pressure hydrogen reduction reaction and cyanoethylation reaction. Discoloration is easy
이에 비하여 본 발명에 의한 제조방법은, 염소기의 치환에서 아민기로의 치환이 바로 이어져서 반응시간을 단축할 수 있고, 비교적 저압반응(5-10㎏/㎠)으로 목적물질을 얻을 수 있는 경제적인 방법이며, 제품의 색상면에서도 우수하다.On the other hand, the production method according to the present invention can shorten the reaction time by immediately replacing the chlorine group with the substitution of the amine group, and can economically obtain the target substance by relatively low pressure reaction (5-10 kg / cm 2). It is a method and is excellent also in the color of the product.
본 발명의 제조방법의 구성은 다음과 같다. 다음 일반식(Ⅱ)로 표시되는 폴리알킬렌옥사이드를 극성용매하에서 염화티오닐과 반응시켜 일차로 염소기로 치환시킨다. 이때 사용되는 극성용매로는 톨루엔, 메틸에틸케톤, 크실렌 등이 가능하며 가장 바람직하게는 톨루엔이며, 반응온도 50-60℃에 1시간 반응시켜 양말단이 염소기로 치환된 폴리알킬렌옥사이드 화합물을 제조한다. 이어서 다음 일반식(Ⅲ)의 아민화합물을 투입하고 암모니아 가스를 5-10㎏/㎠로 가압하여, 1-3시간 반응시켜, 다음 일반식(Ⅰ)의 폴리알킬렌옥사이드 디아민을 제조한다.The structure of the manufacturing method of this invention is as follows. The polyalkylene oxide represented by the following general formula (II) is first reacted with thionyl chloride in a polar solvent to be firstly substituted with a chlorine group. At this time, the polar solvent used may be toluene, methyl ethyl ketone, xylene and the like, most preferably toluene, and reacted at 50-60 ° C. for 1 hour to prepare a polyalkylene oxide compound in which the sock end is substituted with a chlorine group. do. Subsequently, the amine compound of the following general formula (III) was added, ammonia gas was pressurized at 5-10 kg / cm 2, and reacted for 1-3 hours to prepare a polyalkylene oxide diamine of the following general formula (I).
상기식에서, n은 60-110의 정수이고, R은 에틸렌기 또는 프로필렌기이며, R'은 탄소수 1-3의 알킬기이다.Wherein n is an integer of 60-110, R is an ethylene group or a propylene group, and R 'is an alkyl group having 1-3 carbon atoms.
이때 상기식(Ⅱ)의 폴리알킬렌옥사이드에서 n이 60 이하이면 본 발명의 조건에서 부반응이 심해져 색상의 질이 저하되며, n이 110 이상이며 반응성이 떨어져 아민기가 저하된다. 또한 암모니아 가스의 압력이 5㎏/㎠이하, 또는 반응온도가 50℃ 이하이면 치환율이 떨어져 전아민가(Total Amine Value)가 저하되고, 100℃ 이상이면 부반응이 진행되어 고분자량의 제품을 얻을 수 없다.In this case, when n is 60 or less in the polyalkylene oxide of Formula (II), the side reaction becomes severe under the conditions of the present invention, and the color quality is lowered. If the pressure of the ammonia gas is 5 kg / cm 2 or less, or the reaction temperature is 50 ° C. or less, the substitution rate decreases, and the total amine value decreases. If the temperature of the ammonia gas is 100 ° C. or more, the side reaction proceeds to obtain a high molecular weight product. .
본 발명의 반응기구는 다음과 같다.The reactor tool of the present invention is as follows.
상기식에서, n은 60-110의 정수이고, R은 에틸렌기 또는 프로필렌기이며, R'은 탄소수 1-3의 알킬기이다.Wherein n is an integer of 60-110, R is an ethylene group or a propylene group, and R 'is an alkyl group having 1-3 carbon atoms.
상기 반응은 핵치환반응(Nucleophilic Substitution)이며, 2단계 반응이나 제자리(in-situ)에서 진행되므로 용이한 반응이다. 상기 ⅱ)의 반응기작에서 (R')3N은 산포획체(Acid Capture)로 작용한다.The reaction is a Nucleophilic Substitution, and is an easy reaction because it proceeds in a two-step reaction or in-situ. In the reactor operation of ii), (R ′) 3 N acts as an Acid Capture.
다음의 실시예 및 비교예로써 본 발명은 구체화한다.The present invention is embodied by the following examples and comparative examples.
[실시예 1]Example 1
폴리에틸렌옥사이드 4000(n=90) 100중량부, 염화티오닐 3중량부, 톨루엔 250중량부를 반응기에 넣고 55℃에서 1시간 반응시킨 후, 트리에틸아민 2.7중량부를 넣고 80℃에서 암모니아를 7㎏/㎠의 압력으로 1.5시간 반응시킨 후, 용매를 회수하려 융점 61℃의 백색 밀랍(wax)상의 고체를 얻었다.100 parts by weight of polyethylene oxide 4000 (n = 90), 3 parts by weight of thionyl chloride, and 250 parts by weight of toluene were added to a reactor and reacted at 55 ° C for 1 hour. Then, 2.7 parts by weight of triethylamine was added and 7 kg / of ammonia at 80 ° C. After reacting at a pressure of cm 2 for 1.5 hours, a white wax (wax) solid having a melting point of 61 ° C. was obtained to recover the solvent.
[실시예 2]Example 2
폴리에틸렌옥사이드 3000(n=60)을 사용한 것 외에는 실시예 1과 동일한 방법으로 진행하였다.It proceeded in the same manner as in Example 1 except that polyethylene oxide 3000 (n = 60) was used.
[실시예 3]Example 3
폴리에티렌옥사이드 5000(n=110)을 사용한 것 외에는 실시예 1과 동일한 방법으로 진행하였다.The same procedure as in Example 1 was carried out except that polystyrene oxide 5000 (n = 110) was used.
[비교예][Comparative Example]
일본 특허공고 소59-12660의 방법.Japanese Patent Publication No. 59-12660.
분자량 4000의 폴리에틸렌옥사이드의 디시아노에틸화물 100중량부, 에틸렌글리콜 70중량부 및 라니코발트 25중량부를 압열기(Autoclave)에 넣고 120℃, 수소압 150㎏/㎠에서 30분 반응시킨 후, 용매 및 촉매를 제거하여 담황색 밀랍상의 고체를 얻었다.100 parts by weight of dicyanoethylate of polyethylene oxide having a molecular weight of 4000, 70 parts by weight of ethylene glycol and 25 parts by weight of lanicobalt were added to an autoclave and reacted at 120 ° C. and hydrogen pressure of 150 kg / cm 2 for 30 minutes. The catalyst was removed to give a pale yellow waxy solid.
상기 실시예 및 비교예의 각 특성 측정방법은 다음과 같다.Each characteristic measurement method of the said Example and a comparative example is as follows.
* 융점 ; DSC(시차주사열량분석기)로 10℃/분의 속도로 0-100℃ 사이를 주사하여 융점을 조사하였다. 단위 : ℃.Melting point; Melting points were investigated by scanning between 0-100 ° C. at a rate of 10 ° C./min with DSC (differential scanning calorimetry). Unit: ℃.
* 색상 ; 시료를 비색관에 넣고 가열하여 투명하게 만든 다음 표준 비색관을 좌우로 위치하여 비교하였다(하젠법).* color ; The sample was placed in a colorimetric tube, heated to make it transparent, and then the standard colorimetric tube was placed from side to side and compared (Hagen method).
* 전아민가 ; 시료를 취하여 메탄올에 용해한 후, 브로모크레졸레드를 지시약으로 염산 표준용액으로 적정하여 계산하였다. 단위 ; 당량/g.* Total amine number; After taking a sample and dissolving in methanol, it was calculated by titrating bromocresol red with hydrochloric acid standard solution as an indicator. unit ; Equivalent / g.
다음 표 1에 그 결과를 나타냈다.The results are shown in Table 1 below.
[표 1]TABLE 1
상기 결과로써, 본 발명의 제조방법에 의한 폴리알킬렌옥사이드 디아민은 전아민기가 비슷한 수준(실시예 1, 실시예 4, 비교예)에서, 보다 색상이 우수하고, 반응시간의 단축 및 비교적 저압반응으로 생산설비가 용이하여 경제적으로 제조할 수 있음이 밝혀졌다.As a result, the polyalkylene oxide diamine according to the production method of the present invention is more excellent in color at a similar level (Example 1, Example 4, Comparative Example), shorter reaction time and relatively low pressure reaction As a result, it was found that the production equipment can be easily manufactured economically.
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