• Applied Biological Chemistry
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• 제40권1호
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• pp.53-57
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• 1997

중성과 알카리성의 $45^{\circ}C$, 15%(v/v) dioxane 수용액중에서 살충성 imidacloprid (lUPAC:1-(6-chloro-3-pyridylmethyl)-3-N-nitro-iminoimidazolidine-2-ylideneamine)의 가수분해 반응속도 상수를 측정하고 pH-효과, 용매효과(m=0.04, n=0.30 및 m${\ll}$l), 열역학적 활성화 파라미터(${\Delta}S^{\neq}$=-0.03e.u. 및 ${\Delta}S^{\neq}=16.14\;kcal{\cdot}mol^-$), 반응 생성물 분석등의 결과로부터 반응 속도식($K_{obs}=4.56{\times}10^{-3}[OH^-]$)을 유도하여 특정 염기촉매 반응($K_{OH^-}$)으로 사면체($sp^3$) 중간체인 1-(6-chloro-3-pyridylmethyl)-2-hydroxy-2-imidazolidinylisonitraminate(I)을 거쳐 imidazolidine 고리 열림반응으로 $\beta$-3-(6-chloro-3-pyridylmethyl)aminoethyl-1-nitrourea(III)를 경유한 다음에 1-(6-chloro-3-pyridylmethyl)aminoethyl-1-nitrourea(III)으로 분해되는 일련의 친핵성 첨가-제거($Ad_N-E$) 반응메카니즘을 제안하였다. 그리고 $45^{\circ}C$의 중성(pH 8.0)에서 반감기(t1/2)는 약 4.5개월로 잔류성이 큰 화합물임을 알았다.

• 멤브레인
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• 제21권2호
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• pp.118-126
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• 2011

본 연구에서는 소수성 표면의 막을 친수화시키는 방법으로 기존의 방법(브렌딩, 화학적처리 및 post-irradiation에 의한 광조사법)의 단점을 극복하기 위해 주고분자에 전자빔을 전조사하는 방법을 제안하였다. 본 연구 제조공정은 4부분으로 구성되며 첫째로 주고분자를 전자빔을 이용하여 수증기 및 공기조건하에서 전조사함으로써 친수기를 도입하는 전구체의 제조공정, 이를 이용하여 도프을 제조하는 도프용액 제조공정, 도프용액을 부직포 위에 캐스팅 하는 캐스팅 공정, 마지막으로 비용매에 침적하여 응고시켜 분리막을 형성시키는 분리막 제조공정으로 이루어진다. 이렇게 제조된 분리막은 기존의 친수화 방법을 통하여 얻어진 다공 분리막에 비하여 보다 균일한 형태의 친수화가 가능하며, 제조공정의 단순화를 꾀할 수 있다는 장점을 가지고 있다. 이를 수행하기 위해 소수성 고분자인 polyvinylidene f1uoride (PVDF)를 75~125 K Gray 범위 선량의 전자빔 (electron beam, EB) 조사하여 전구체를 제조하였다. 제조된 전구체는 FTIR, EDS, DSC 등에 의해 친수기의 도입 및 도입경로를 확인한 결과, 하이드록실기가 친수성기로 도입되었고, 도입경로로는 주쇄의 탈수소화 반응경로에 의해 이루어진 것으로 추론 할 수 있었다. 제조막의 친수화는 접촉각 측정을 통하여 평가하였다.(pristine PVDF로 제조된 막의 접촉각은 약 $62^{\circ}$ 125 K Gray-PVDF로 제조된 막의 접촉각은 $13^{\circ}$). 또한 제조된 PVDF 다공막의 다공성도를 수은압입측정을 통하여 평가하였으며 SEM 이미지를 통하여 몰폴로지 및 표변 공경싸이즈를 관찰하였다. 그들의 결과는 전자빔의 선량이 높게 조사된 PVDF전구체를 사용한 막일수록 공경의 크기 및 다공도(pristine PVDF : 82%, 125 K Gray-PVDF : 63%)가 감소되고 있음을 나타내었다. 순수 투과실험에서도 동일한 경향을 나타내어 pristine PVDF의 경우는 892 LMH, 125 K Gray-PVDF의 경우는 355 LMH의 결과를 얻었다.

• 한국막학회:학술대회논문집
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• 한국막학회 1999년도 The 7th Summer Workshop of the Membrane Society of Korea
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• pp.39-42
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• 1999

Perfluoropolymers represent the ultimate resistance to hostile chemical environments and high service temperature, attributed to the presence of fluorine in the polymer backbone, i.e. to the high bond energy of C-F and C-C bonds of fluorocarbons. Copolymers of Tetrafluoroethylene (TEE) and 2, 2, 4Trifluoro-5Trifluorometoxy- 1, 3Dioxole (TTD), commercially known as HYFLON AD, are amorphous perfluoropolymers with glass transition temperature (Tg)higher than room temperature, showing a thermal decomposition temperature exceeding 40$0^{\circ}C$. These polymer systems are highly soluble in fluorinated solvents, with low solution viscosities. This property allows the preparation of self-supported and composite membranes with desired membrane thickness. Symmetric and asymmetric perfluoropolymer membranes, made with HYFLON AD, have been prepared and evaluated. Porous and not porous symmetric membranes have been obtained by solvent evaporation with various processing conditions. Asymmetric membranes have been prepared by th wet phase inversion method. Measure of contact angle to distilled water have been carried out. Figure 1 compares experimental results with those of other commercial membranes. Contact angles of about 120$^{\circ}$for our amorphous perfluoropolymer membranes demonstrate that they posses a high hydrophobic character. Measure of contact angles to hexandecane have been also carried out to evaluate the organophobic character. Rsults are reported in Figure 2. The observed strong organophobicity leads to excellent fouling resistance and inertness. Porous membranes with pore size between 30 and 80 nanometers have shown no permeation to water at pressures as high as 10 bars. However high permeation to gases, such as O2, N2 and CO2, and no selectivities were observed. Considering the porous structure of the membrane, this behavior was expected. In consideration of the above properties, possible useful uses in th field of gas- liquid separations are envisaged for these membranes. A particularly promising application is in the field of membrane contactors, equipments in which membranes are used to improve mass transfer coefficients in respect to traditional extraction and absorption processes. Gas permeation properties have been evaluated for asymmetric membranes and composite symmetric ones. Experimental permselectivity values, obtained at different pressure differences, to various single gases are reported in Tab. 1, 2 and 3. Experimental data have been compared with literature data obtained with membranes made with different amorphous perfluoropolymer systems, such as copolymers of Perfluoro2, 2dimethyl dioxole (PDD) and Tetrafluorethylene, commercialized by the Du Pont Company with the trade name of Teflon AF. An interesting linear relationship between permeability and the glass transition temperature of the polymer constituting the membrane has been observed. Results are descussed in terms of polymer chain structure, which affects the presence of voids at molecular scale and their size distribution. Molecular Dyanmics studies are in progress in order to support the understanding of these results. A modified Theodoru- Suter method provided by the Amorphous Cell module of InsightII/Discover was used to determine the chain packing. A completely amorphous polymer box of about 3.5 nm was considered. Last but not least the use of amorphous perfluoropolymer membranes appears to be ideal when separation processes have to be performed in hostile environments, i.e. high temperatures and aggressive non-aqueous media, such as chemicals and solvents. In these cases Hyflon AD membranes can exploit the outstanding resistance of perfluoropolymers.