• 대한화학회지
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• 제13권4호
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• pp.373-377
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• 1969

In order to determine the monomer reactivity ratio in copolymerization of acrolein, the copolymerization of acrolein with styrene, methyl methacrylate and vinyl acetate respectively was studied. The Q and e value of acrolein in each copolymerization were also calculated from those of monomer reactivity ratios, but the calculated values were slightly different from each other. The Q and e of acrolein for the system of acrolein-styrene copolymerization were Q = O.64 and e = O.62 respectively. Relations among the Q and e value, the composition and structure of copolymers and the mean sequence length in copolymerization were also discussed for acrolein copolymers.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1996년도 한국자동제어학술회의논문집(국내학술편); 포항공과대학교, 포항; 24-26 Oct. 1996
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• pp.788-791
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• 1996

A mathematical model is developed for thermal solution copolymerization of styrene and acrylonitrile in a continuous stirred tank reactor(CSTR). Computational studies are carried out with the continuous copolymerization system model developed in this work to give the monomer conversion, copolymer composition and the average molecular weights of the copolymer. By performing the dynamic analysis of the reaction system, the polymer properties against the changes in the operating conditions are determined quantitatively. The cascade PID and fuzzy controller show satisfactory performances for both set point tracking and disturbance rejection. Especially, the fuzzy controller is superior to the PID controller.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1994년도 Proceedings of the Korea Automatic Control Conference, 9th (KACC) ; Taejeon, Korea; 17-20 Oct. 1994
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• pp.207-212
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• 1994

A mathematical model is developed for a batch reactor in which the free radical bulk copolymerization of styrene and acrylonitrile takes place. In this model, we introduce the free volume theory to quantify the diffusion controlled termination and propagation reactions, and develop a model for the chain length dependent termination reaction in the context of the pseudo kinetic rate constant method(PKRCM). The simulation results from this model are found to be in good agreement with experimental data under different copolymerization conditions. The present model can predict both the copolymer composition and the number and weight average molecular weights. These kinetic approaches provide greater insight into the performance of the batch reactor used for the free radical bulk copolymerization of styrene and acrylonitirle.

• 폴리머
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• 제24권1호
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• pp.16-22
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• 2000

폴리부틸렌테레프탈레이트 (poly(butylene terephthalate), PBT)와 파라아세톡시벤조산 (p-acetoxybenzoic acid, ABA)을 용융 에스테르 교환반응시킴으로써 주쇄 고분자에 강직한 벤젠고리가 도입된 poly(butylene terephthalate-co-oxybenzoate) (PBOT)를 합성하였다. PBT와 ABA를 다양한 조성비에서 중합하는 과정의 속도론적 고찰을 통해 ABA의 단독중합 속도상수와 PBT에의 공중합 속도상수 및 그 비를 구하였으며 각각의 활성화에너지를 구하였다. PBT와 ABA의 조성비를 4/6, 5/5, 6/4로 하고 온도를 각각 250, 260, 27$0^{\circ}C$로 하여 실험한 결과 공중합반응은 ABA함량이 낮고 또 그 전환율이 크지 않을 경우 의사 2차반응으로 볼 수 있었다. 이때의 공중합 속도에 대한 단독중합 속도의 비는 1.08에서 3.17사이의 값을 가졌으며, ABA함량과 온도가 높을수록 큰 값을 가졌다. 이로써 PBT/ABA계의 공중합은 반응온도가 높고 ABA의 조성비가 클수록 ABA의 블록성이 강해지는 경향을 나타내었다.

• 대한화학회지
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• 제26권3호
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• pp.179-187
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• 1982

N-acryloylpyrrolidone과 acrylonitrile을 혼성중합시켜 각 단위체의 반응성비를 구한 결과 생성되는 혼성중합체는 pyrrolidone이 음이온 중합에 매우 좋은 개시제임을 알 수 가 있었다. ($r_1$ = 0.43과 $r_2$ = 1.56) 그리고 그 혼성중합체를 개시제로 하여 그라프트된 nylon-4를 합성하여 중합속도 상수를 구했으며, 그에 따르는 여러 인자들의 효과를 관찰하였다. 그 결과 중합속도 상수로 40$^{\circ}$C에서 2.82${\times}10^3$(l/mole, min)와 50$^{\circ}$C에서 2.93${\times}10^3$(l/mole, min)을 얻었다.

• 공업화학
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• 제7권4호
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• pp.623-632
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• 1996

코모노머와 코모노머의 조성을 변화시켜 프로필렌/부텐-1 및 트로필렌/헥센-1의 공중합을 실시하여 반응성비, 용융점 및 폴리머 형상등을 관찰하였다. 공중합에 사용한 촉매는 담체로서 실리카(촉매 I)와 마그네슘(촉매 II)을 사용한 고활성촉매이다. 코모노머의 조성이 증가함에 따라 폴리머의 용융점이 낮아지며, 또한 코모노머의 조성이 프로필렌/부텐-1 공중합의 경우에는 40% 이상, 프로필렌/헥센-1 공중합의 경우에는 80% 이상이면 폴리머의 형상이 무정형화 되어진다. 반응성비는 Fineman-Ross법과 Kelen-$T{\ddot{u}}d{\tilde{o}}s$법으로 구하였다.

• 대한화학회지
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• 제20권4호
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• pp.316-320
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• 1976

단백질에 대한 비닐 단위체의 그라프트 공중합 실험결과를 기초로하여 유기물과 Ce(IV)이온의 산화환원계에 의하여 개시되는 중합반응에 대하여 중합반응 메카니즘을 추구하였다. Ce(IV) 이온에 의한 산화성 종결반응을 고려하여 반응속도식을 유도 하였으며 Ce(IV) 이온 농도가 클때와 작을 때를 별개로 취급하여 Ce(IV) 이온 농도의 변화에 따라 그라프트 수득률의 최대점이 나타나는 현상을 설명하였다.

• 대한화학회지
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• 제62권3호
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• pp.191-202
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• 2018

The aim of this work is to study Monte Carlo simulation of ethylene (co)polymerization over Ziegler-Natta catalyst as investigated by Chen et al. The results revealed that the Monte Carlo simulation was similar to sum square error (SSE) model to prediction of stage II and III of polymerization. In the case of activation stage (stage I) both model had slightly deviation from experimental results. The modeling results demonstrated that in homopolymerization, SSE was superior to predict polymerization rate in current stage while for copolymerization, Monte Carlo had preferable prediction. The Monte Carlo simulation approved the SSE results to determine role of each site in total polymerization rate and revealed that homopolymerization rate changed from site to site and order of center was different compared to copolymerization. The polymer yield was reduced by addition of hydrogen amount however there was no specific effect on uptake curve which was predicted by Monte Carlo simulation with good accuracy. In the case of copolymerization it was evolved that monomer chain length and monomer concentration influenced the rate of polymerization as rate of polymerization reduced from 1-hexene to 1-octene and increased when monomer concentration proliferate.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
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• pp.48-51
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• 2000

The poly(3-hydroxybutyrate) (PHB) synthase of Ralstonia. eutropha, which was produced by a recombinant strain E. coli and purified in one-step with a methyl-HIC column to a purity of more than 90%, was used to polymerize 3-hydroxypropionyl-CoA (3HPCoA) and to copolymerize 3HPCoA with 3-hydroxybutyryl-CoA (3HBCoA) in vitro. A $K_m$ of $189\;{\mu}M$ and a $k_{cat}$ of $10\;sec^{-1}$ were determined for the activity of the enzyme in the polymerization reaction of 3HPCoA based on the assumption that the dimer form of PHB synthase was the active form. Free coenzyme A was found to be a very effective competitive inhibitor for the polymerization of 3HPCoA with a $K_i$ of $85\;{\mu}M$. The maximum degree of conversion of 3HPCoA to polymer was less than 40 %. In the simultaneous copolymerization reactions of these two monomers, both the turnover number for the copolymerization reaction and the maximum degree of conversion of 3HPCoA and 3HBCoA to copolymers increased with an increase in the amount of 3HBCoA in the monomer mixture. However, the maximum conversion of 3HPCoA to a copolymer was less than 35 % regardless of the ratio of 3HPCoA to 3HBCoA. Block copolymers were obtained by the sequential copolymerization of the two monomers and these copolymers had a much narrower molecular weight distribution than those obtained by the simultaneous copolymerization of the same molar ratio of 3HPCoA and 3HBCoA.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1997년도 한국자동제어학술회의논문집; 한국전력공사 서울연수원; 17-18 Oct. 1997
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• pp.309-312
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• 1997

The dynamic characteristics of a continuous MMA/MA free-radical solution copolymerization reactor were studied. A mathematical model was developed and kinetic parameters which had been estimated in the previous work were used. With this model, bifurcation diagrams were constructed with various parameters as the bifurcation parameter to predict the region of stable operating conditions and to enhance the controller performance. It was shown that the steady-state multiplicity existed over wide ranges of residence time and jacket inlet temperature. Periodic solution branches were found to emanated from Hopf bifurcation points. Under certain conditions isola was also observed, which would result in poor performance of feedback controllers.