• Title/Summary/Keyword: 중합속도

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Study on Model of Emulsion Polymeration 2. Kinetics of Termonomer Emulsion Polymerization (유화중합의 모델연구 2. 삼모노머유화중합의 동력학)

  • Park, S.B.;SE, C.S.
    • Applied Chemistry for Engineering
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    • v.9 no.2
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    • pp.300-305
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    • 1998
  • Kinetics of termonomer emulsion polymerization during interval II (i.e, after completion of latex particle formation) were studied through pseudo-homopolymerization (PHP) method. Extended Smith-Ewart equation and equation of instantaneous polymer composition are respectively reduced to the corresponding equation for homopolymerization by defining average rate constants. Average number of radicals per particle and instantaneous polymer compositions were respectively predicted by varying termonomer composition within latex particles for systems containing no more than one growing radical per particle. Styrene-Methyl methacrylate-Acrylonitrile (SMA) system was used for model calculation.

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Change of Surface Morphology with the Spreading Rate of Organic Solution During Interfacial Polymerization for Polyamide-based Thin Film Composite Membrane Manufacturing Process (폴리아마이드계 박막복합막 제조 공정에서 계면중합의 유기용액 퍼짐 속도에 따른 표면 모폴로지의 변화)

  • Park, Chul Ho
    • Membrane Journal
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    • v.27 no.6
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    • pp.506-510
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    • 2017
  • The interfacial polymerization method has been applied to various fields as a reaction in which reactive monomers dissolved in two immiscible solutions cause polymerization at the interface. In the case of water treatment membranes, m-phenylene diamine and trimesoyl chloride are used as reactants. The performance of the membrane is affected by various polymerization factors. In this study, we investigated how the spreading rate of the organic solution influences the surface and structure of the membrane. Spreading rate of organic solutions was adjusted to 7.6 and 25 mm/sec. The solution volume of the organic phase was adjusted to 1~3 drops. The observed results showed that cracks were not found in the polyamide membrane when dropping at a drop of 7.6 mm/sec and dropping two drops at 25 mm/sec. On the other hand, cracks occurred in all cases. Therefore, the spreading rate of the initial organic solvent is expected to greatly affect the performance of the polyamide membrane.

Studies on Synthesis of Acrylic Water Borne Polymer;Synthesis of Poly(vinyl acetate) and Poly(vinyl acetate-co-2-ethylhexyl acrylate) (Aerylic Water Borne Polymer의 합성 연구;Poly(vinyl acetate)와 poly(vinyl acetate-co-2-ethylhexyl acrylate)의 합성 연구)

  • Kim, Sang-Hern
    • Journal of the Korean Applied Science and Technology
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    • v.13 no.2
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    • pp.77-84
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    • 1996
  • Poly(vinyl acetate)와 poly(vinyl acetate-co-2-ethylhexyl acrylate)를 여러 조건에서 semicontinuous emulsion 중합으로 합성하였다. Overall conversion, emulsion 입자크기, pH, 점도 등을 합성한 두 emulsion polymer에 대해 측정하였다. Vinyl acetate monomer에 2-ethylhexyl acrylate를 도입함으로서 emulsion 입도, 점도, 중합 속도, 유리 전이 속도가 감소함을 확인하였다.

Interfacial Polymerization Formation and Thickness of Thin Film (계면중합 반응과정 고찰 및 박막의 두께 측정)

  • 박종원;민병렬
    • Proceedings of the Membrane Society of Korea Conference
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    • 1997.10a
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    • pp.87-89
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    • 1997
  • 1. 서론 : 막을 이용한 분리기술의 실용화의 최대 과제는 선택성이 높고 용매의 투과용매의 투과속도가 높은 막재질 및 처리 면적이 큰 막의 개발이 필요하게 되었다. 이러한 성능 개발은 1960년대 cellulose acetate 계통의 막개발 이후 1980년대 지지층 고분자위에 다른 고분자 물질을 도포한 복합막(thin film composite layer)이 개발되어 막의 성능을 급격히 발전시켰다. 그 중에서 초박막화(ultrathin membrane)는 분리막에 의한 분리공정의 최대 결점인 낮은 투과량의 개선을 꾀할 수 있다는 장점 때문에 다양한 시도가 이루어지고 있다. 이러한 박막 제조 방법에는 박층분산법, 침지코팅법, 기상증착법, 계면중합법이 있으나, 섞이지 않는 두 계면 사이에서 고분자를 형성시키는 계면중합법은 수용상에 함침된 지지막위에 유기상을 계변에서 중합시켜 박막을 얻는 기술이다. 중합과정에서 일어나는 계면의 형성과정에 대한 연구는 미흡하기에 이에 본 연구는 시간에 따른 계면중합 반응 형성과정을 고찰하는 방법을 소개하고, 형성된 박막의 아론적, 실험적 두께 측정을 비교하였다.

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Kinetics of Pholopolymerization of Acrylonitrile Using Sensitizer (광증감제에 의한 Acrylonitrile의 광중합 속도 (I))

  • Seul, Soo-Duk
    • Elastomers and Composites
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    • v.34 no.1
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    • pp.3-10
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    • 1999
  • Kinetics of solution photopolymerization of acrylonitrile(AN) with sensitizer, such as $NaSCN,\;KSCN,\;Ba(SCN)_2,\;NH_4SCN,\;ZnCl_2$ and $Na_2SeO_3$, were studied using UV crosslinker at various monomer concentrations($1.8{\sim}7.58mo1/1$), sensitizer concentrations($10{\sim}60%$), reaction temperature($10{\sim}70^{\circ}C$), energy intensities($1,000{\sim}9,900{\mu}J/cm^2$) at isothermal condition under nitrogen atmosphere. Under the irradiation of high pressure mercury lamp(${\lambda}=365nm$). High conversion and uniform molecular weight were obtained compare to thermal polymerization at reaction temperature of $50^{\circ}C$, reaction time of 3hr and 50% NaSCN without any initiator. Their kinetic model was as follows : $R_p=0.0142[M]^{0.82}[I]^{0.49}[S]^{0.52}$ exp(-1.33/RT).

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Anionic Polymerization of 2-Pyrrolidone by Toluene Diisocyanate / KOH Catalysis (Toluene Diisocyanate/KOH 촉매작용에 의한 2-Pyrrolidone의 음이온 중합)

  • Bal Jung;Ki Sung Kwon;Sam Kwon Choi;Mun Sam Ryoo
    • Journal of the Korean Chemical Society
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    • v.27 no.1
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    • pp.66-72
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    • 1983
  • Anionic polymerization of 2-pyrrolidone was carried out by TDI (Toluene Diisocyanate)/KOH catalysis. The effects of TDI / KOH mole ratio, KOH concentration, temperature and time on polymerization were investigated. It was observed that the highest rate of polymerization and maximum conversion were obtained when TDI / KOH mole ratio was about 0.25. The maximum conversion and the highest viscosity were obtained when the concentration of KOH was 5 mole percent. It was also found that the rate of polymerization and inherent viscosity at $30^{\circ}C$ were higher than those at $50^{\circ}C$. The rate constant ($k_p$) of polymerization was determined by least square method; the values of kp obtained were $57.53{\ell}/mole{\cdot}min\;at\;30^{\circ}C$ and $52.36{\ell}/mole{\cdot}min\;at\;50^{\circ}C$, respectively.

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The Kinetics of Radical Polymerization of Styrene with Tricaprylymethylammonium Chloride as a Phase-Transfer Catalyst (상이동촉매인 트리카프릴메틸암모니움 클로라이드를 사용한 스티렌 라디칼중합의 동력학적 연구)

  • Park, Sang-Wook;Sohn, In-Joe;Park, Sang-Bo
    • Journal of Adhesion and Interface
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    • v.2 no.2
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    • pp.11-19
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    • 2001
  • The phase-transfer catalyzed radical polymerization of styrene was carried out using tricaprylylmethylammonium chloride as a phase-transfer catalyst in a two-phase system of an aqueous $Na_2S_2O_8$ solution and toluene at $60^{\circ}C$ under nitrogen atmosphere. The initial rate of radical polymerization was expressed as the combined terms of concentrations of quaternary onium cation and peroxydisulfate anion in the aqueous phase rather than the fed concentrations of catalyst and $Na_2S_2O_8$. The observed initial rate of radical polymerization was used to analyze the radical polymerization mechanism with a cycle phase-transfer initiation step in the heterogeneous liquid-liquid system. The viscosity average molecular weight of polystyrene was inversely proportional to concentration of $Na_2S_2O_8$ expressed as $[Q^+]([S_2O{_8}^{2-}]{\alpha}_2)^{1/2}$ derived by the radical polymerization mechanism.

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Iterative Least-Squares Method for Velocity Stack Inversion - Part B: CGG Method (속도중합역산을 위한 반복적 최소자승법 - Part B: CGG 방법)

  • Ji Jun
    • Geophysics and Geophysical Exploration
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    • v.8 no.2
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    • pp.170-176
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    • 2005
  • Recently the velocity stack inversion is having many attentions as an useful way to perform various seismic data processing. In order to be used in various seismic data processing, the inversion method used should have properties such as robustness to noise and parsimony of the velocity stack result. The IRLS (Iteratively Reweighted Least-Squares) method that minimizes ${L_1}-norm$ is the one used mostly. This paper introduce another method, CGG (Conjugate Guided Gradient) method, which can be used to achieve the same goal as the IRLS method does. The CGG method is a modified CG (Conjugate Gradient) method that minimizes ${L_1}-norm$. This paper explains the CGG method and compares the result of it with the one of IRSL methods. Testing on synthetic and real data demonstrates that CGG method can be used as an inversion method f3r minimizing various residual/model norms like IRLS methods.

Core 원료들의 관능기 변화에 따른 Core-Shell latex의 열적 특성 고찰

  • 권재범;김남석;이내우;설수덕
    • Proceedings of the Korean Institute of Industrial Safety Conference
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    • 2003.10a
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    • pp.148-153
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    • 2003
  • 고분자 물질은 유기용제를 사용하여 제조되는 경우가 일반적이다. 이들 중에서 용제형 아크릴계 고분자는 점착강도, 내습성, 내수성 그리고 내열성 등이 우수하여 페인트, 접ㆍ점착제, 섬유 등의 산업전반에 이용되고 있으나 용제사용에 따른 화재의 위험성과 환경적인 문제점 때문에 규제의 대상이 되고 있다. 이러한 위험성과 환경문제점은 유화중합법에 의해 고분자물질을 제조함으로써 해결되며, 그 중에서 단계 유화중합법은 다른 중합법에 비해 온도조절이 용이하며, 반응속도와 분자량을 조절할 수 있다는 장점 때문에 latex 공업이나 고분자 blending 기술면에서 많이 이용되고 있는 실정이다.(중략)

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Prestack Depth Migration for Gas Hydrate Seismic Data of the East Sea (동해 가스 하이드레이트 탄성파자료의 중합전 심도 구조보정)

  • Jang, Seong-Hyung;Suh, Sang-Yong;Go, Gin-Seok
    • Economic and Environmental Geology
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    • v.39 no.6 s.181
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    • pp.711-717
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    • 2006
  • In order to study gas hydrate, potential future energy resources, Korea Institute of Geoscience and Mineral Resources has conducted seismic reflection survey in the East Sea since 1997. one of evidence for presence of gas hydrate in seismic reflection data is a bottom simulating reflector (BSR). The BSR occurs at the interface between overlaying higher velocity, hydrate-bearing sediment and underlying lower velocity, free gas-bearing sediment. That is often characterized by large reflection coefficient and reflection polarity reverse to that of seafloor reflection. In order to apply depth migration to seismic reflection data. we need high performance computers and a parallelizing technique because of huge data volume and computation. Phase shift plus interpolation (PSPI) is a useful method for migration due to less computing time and computational efficiency. PSPI is intrinsically parallelizing characteristic in the frequency domain. We conducted conventional data processing for the gas hydrate data of the Ease Sea and then applied prestack depth migration using message-passing-interface PSPI (MPI_PSPI) that was parallelized by MPI local-area-multi-computer (MPI_LAM). Velocity model was made using the stack velocities after we had picked horizons on the stack image with in-house processing tool, Geobit. We could find the BSRs on the migrated stack section were about at SP 3555-4162 and two way travel time around 2,950 ms in time domain. In depth domain such BSRs appear at 6-17 km distance and 2.1 km depth from the seafloor. Since energy concentrated subsurface was well imaged we have to choose acquisition parameters suited for transmitting seismic energy to target area.