• Title/Summary/Keyword: 화학 결합

Search Result 2,292, Processing Time 0.022 seconds

Effect of Fluorination and Ultrasonic Washing Treatment on Surface Characteristic of Poly(ethylene terephthalate) (불소화 및 초음파 수세가 폴리(에틸렌 테레프탈레이트) 필름의 표면 특성에 미치는 영향)

  • Kim, Do Young;In, Se Jin;Lee, Young-Seak
    • Polymer(Korea)
    • /
    • v.37 no.3
    • /
    • pp.316-322
    • /
    • 2013
  • In this study, poly(ethylene terephthalate) (PET) was treated with fluorination and ultrasonic washing treatment for hydrophilic modification of PET film. We measured the change of surface modified PET film surface characteristics using contact angle, surface free energy, FE-SEM, AFM and XPS. After direct fluorination and ultrasonic washing treatment, the water contact angle was measured to be $10.81^{\circ}$, 85% reduction compared to the untreated PET film. Total surface free energy has been measured to be $42.25mNm^{-1}$, 650% increase compared to the untreated PET film. Also RMS roughness has been measured to be 1.965 nm, 348% increase compared to the untreated PET film. Hydrophilic functional group C-OH bond concentration has increased approximately 3 times. These results are attributed to the hydrophilic functional group and cavitation due to chemical etching. From this result, it was suggested that the fluorination-ultrasonic washing treatment method could be useful to make PET film surface hydrophilic.

Microstructure and plasma resistance of Y2O3 ceramics (Y2O3 세라믹스의 미세구조 및 플라즈마 저항성)

  • Lee, Hyun-Kyu;Lee, Seokshin;Kim, Bi-Ryong;Park, Tae-Eon;Yun, Young-Hoon
    • Journal of the Korean Crystal Growth and Crystal Technology
    • /
    • v.24 no.6
    • /
    • pp.268-273
    • /
    • 2014
  • $Y_2O_3$ ceramic specimens were fabricated from the granular powder, obtained by spray drying process from the slurry. The slurry was prepared by mixing PVA binder, NaOH for Ph control, PEG and $Y_2O_3$ powder. The $Y_2O_3$ specimen was shaped in size of ${\phi}14mm$ and then sintered at $1650^{\circ}C$. The characteristics, microstructure, densities and plasma resistance of the $Y_2O_3$ specimens were investigated with the function of forming pressure and sintering time. $Y_2O_3$ specimens were exposed under the $CHF_3/O_2/Ar$ plasma, the dry etching treatment of specimens was carried out by the physical reaction etching of $Ar^+$ ion beam and the chemical reaction etching of $F^-$ ion decomposed from $CHF_3$. With increasing sintering time, $Y_2O_3$ specimens showed relatively high density and strong resistance in plasma etching test.

Prognostic Significance of Fascin Expression in Stage I Non-small Cell Lung Cancer (수술 절제를 시행받은 제1기 비소세포폐암 환자에서의 Fascin 발현과 예후)

  • Roh, Mee-Sook;Um, Su-Jung;Choi, Youngmin;Kim, Ki-Nam;Choi, Pil Jo;Lee, Soo-Keol;Son, Choonhee;Yang, Dookyung
    • Tuberculosis and Respiratory Diseases
    • /
    • v.65 no.2
    • /
    • pp.105-109
    • /
    • 2008
  • Background: Fascin is an actin-bundling protein that plays an important role in cellular motility. Fascin is normally expressed in the neuronal and mesenchymal cells and its expression is low or absent in the epithelia. However, an overexpression of fascin has been linked to the invasive behavior of some neoplasms such as breast, stomach and ovarian tumors. In this study, we evaluated the expression of fascin and its prognostic significance in stage I non-small cell lung cancer (NSCLC). Methods: Immunohistochemical staining for fascin was performed on the paraffin-embeded tissue sections of 81 cases of resected NSCLC. Staining of more than 5% of the tumor cells was recorded as positive immunoreactivity. Results: Fascin expression was seen in 73% (59/81) of the cases and this was more frequently seen in squamous cell carcinoma than in adenocarcinoma (93% vs 42%). There were no significant correlations of fascin immunoreactivity with tumor recurrence and overall survival. Conclusion: The expression rate of fascin was relatively high in NSCLC, but this was without prognostic significance. The exact clinical role of fascin should be defined through further investigations.

Utilization of Corynebacterium glutamicum Biomass as a Regenerable Biosorbent for Removal of Reactive Dyes from Aqueous Solution (반응성 염료 제거를 위한 재생 가능한 흡착제로서 Corynebacterium glutamicum 바이오매스의 이용)

  • Won, Sung -Wook;Choi, Sun Beom;Han, Min Hee;Yun, Yeoung-Sang
    • Korean Chemical Engineering Research
    • /
    • v.43 no.4
    • /
    • pp.542-547
    • /
    • 2005
  • Biosorption is considered to be a promising alternative to replace or supplement the present methods for the treatment of dye-containing wastewater. In this study, the protonated biomass of Corynebacterium glutamicum was evaluated for its potential to remove two types of reactive dyes (Reactive Red 4, Reactive Blue 4) from aqueous solution. The uptakes of dyes were enhanced with decrease in the solution pH, which was likely because the biomass functional groups increased at acidic pH and the positively charged sites could bind the negatively charged sulfonate group ($dye-SO_3^-$) of dye molecules. An equilibrium state was practically achieved in 10 hr. The Langmuir sorption model was used for the mathematical description of the sorption equilibrium. The maximum sorption capacities of C. glutamicum biomass for Reactive Red 4 and Reactive Blue 4 were estimated to 112.36 mg/g and 263.16 mg/g at pH 1, and 71.94 mg/g and 155.88 mg/g at pH 3.

Excess Molar Enthalpies and Excess Molar Volumes for the Binary Mixtures {1,2-dichloropropane+2-(2-methoxyethoxy)ethanol, and +2-(2-ethoxyethoxy)ethanol} at 298.15 K (2성분계 {1,2-dichloropropane+2-(2-methoxyethoxy)ethanol 및 + 2-(2-ethoxyethoxy)ethanol}에 대한 298.15 K에서의 과잉몰엔탈피 및 과잉몰부피)

  • Kim, Jaewon;Kim, Moongab
    • Korean Chemical Engineering Research
    • /
    • v.44 no.5
    • /
    • pp.444-452
    • /
    • 2006
  • This paper reports experimental excess molar volumes $V^E_m$ using a digital vibrating-tube densimeter and excess molar enthalpies $H^E_m$ by means of an isothermal microcalorimeter with a flow mixing cell for the binary mixtures{1,2-dichloropropane + 2-(2-methoxyethoxy)ethanol} and {1,2-dichloropropane + 2-(2-ethoxyethoxy)ethanol} at 298.15 K under atmospheric pressure. All the $V^E_m$ and $H^E_m$ of the two binary mixtures showed S-shaped forms, being negative for poor and positive for rich 1,2-dichloropropane mole fractions. These show that the excess properties were shown to be negative deviation from ideality due to the strong self-association effect among 2-(2-alkoxyethoxy)ethanol molecules at an early stage of mixing, a relatively high energy then is needed to break hydrogen bonds of 2-(2-alkoxyethoxy)ethanol with an increase ofhalogenated hydrocarbon molecular at high mole fraction of 1,2-dichloropropane. The values of excess molar properties($V^E_m$ and $H^E_m$) were fitted by the Redlich-Kister equation using Nelder-Mead's simplex pattern search method. The Wilson, NRTL, and UNIQUAC models were used to correlate the $H^E_m$ values.

Etch Characteristics of CoTb and CoZrNb Thin Films by High Density Plasma Etching (고밀도 플라즈마 식각에 의한 CoTb과 CoZrNb 박막의 식각 특성)

  • Shin, Byul;Park, Ik Hyun;Chung, Chee Won
    • Korean Chemical Engineering Research
    • /
    • v.43 no.4
    • /
    • pp.531-536
    • /
    • 2005
  • Inductively coupled plasma reactive ion etching of CoTb and CoZrNb magnetic materials with the photoresist mask was performed using $Cl_2/Ar$ and $C_2F_6/Ar$ gas mixtures and characterized in terms of etch rate and etch profile. As the concentrations of $Cl_2$ and $C_2F_6$ gases increased, the etch rates of magnetic films decreased and the etch slopes became slanted. The $Cl_2/Ar$ gas was more effective in obtaining fast etch rate and steep sidewall slope than the $C_2F_6/Ar$ gas. As the coil rf power and dc bias increased, fast etch rate and steep etch slope were obtained but the redeposition on the sidewall was observed. This is due to the increase of ion and radical densities in plasma with increasing the coil rf power and the increase of incident ion energy to the substrate with increasing the dc bias voltage. By applying high density reactive ion etching to magnetic tunnel junction stack containing various magnetic films and metal oxide, steep etch slope and clean etch profile without redeposition were obtained.

Effect of Cosurfactant on Preparation of Silica Nanoparticles using Water in Oil Microemulsion of Nonionic Surfactant (보조계면활성제가 비이온 계면활성제의 Water in Oil 마이크로에멀젼을 이용한 실리카 나노입자 제조에 미치는 영향)

  • Kim, TaeHoon;Lim, JongChoo
    • Korean Chemical Engineering Research
    • /
    • v.46 no.2
    • /
    • pp.356-368
    • /
    • 2008
  • The effects of cosurfactant on silica nanoparticles were investigated in systems containing surfactant, oil and aqueous ammonia solution where nanoparticles were prepared using a single phase water-in-oil (W/O) microemulsion. For the same oil phase, a single phase region was dependent on the interaction between surfactant and oil. For the cyclohexane system, NP-5 surfactant showed a wider single phase region than NP-4. The addition of n-propanol as a cosurfactant resulted in an increase or a decrease of a single phase W/O microemulsion region depending on the continuous oil phase. For both cyclohexane and isooctane systems, the addition of n-propanol resulted in a decrease in the single phase region. On the other hand, for n-heptane system, the addition of n-propanol expanded a single phase W/O microemulsion region. Silica nanoparticles prepared within a single phase region showed that relatively large number of particles of irregular shape were obtained with the addition of n-propanol to NP surfactant system. The addition of n-propanol to LA-5 surfactant and n-heptane system produced a decrease in average particle size and an increase in the number of particles formed due to a decrease in the intermicellar exchange rate among microemulsion droplets.

Treatment of an Authentic Textile-dyeing Wastewater Utilizing a Fluidized Biofilter and Hybrid Recirculating System Composed of the Fluidized Biofilter and a UV/photocatalytic Reactor (실제 혼합염색폐수의 유동상 시스템을 활용한 미생물처리와 하이브리드 재순환시스템처리)

  • Lee, Eun Ju;Lim, Kwang-Hee
    • Korean Chemical Engineering Research
    • /
    • v.53 no.1
    • /
    • pp.71-77
    • /
    • 2015
  • A fluidized biofilter was filled with Pseudomonas sp. and Bacillus cereus/thuringiensis-fixed waste-tire crumb media and was run to treat authentic textile-dyeing wastewater mixed with alkaline polyester-weight-reducing wastewater. As a result, its removal efficiency of $COD_{Cr}$ and color were 75~80% and 67%, respectively. In addition, upon constructing hybrid-recirculating system composed of the fluidized biofilter and a 450 W-UV/photocatalytic reactor, only fluidized biofilter was run bypassing UV/photocatalytic reactor at stage I. Subsequently, the hybrid system was continuously run at stage II-i, ii and iii. At stage II-i, the total removal efficiency of $COD_{Cr}$ was enhanced to be 80~85%, compared to 75% at stage I, owing to 20~30% removal efficiency of the UV/photocatalytic reactor. However, at stage II-i, the total removal efficiency of color was enhanced to be 65~70%, compared to 45~65% at stage I, even though the removal efficiency of the UV/photocatalytic reactor was tantamount to merely 0~5%. As far as the removal efficiency of fluidized biofilter of the hybrid-recirculating system is concerned, its removal efficiency of color was enhanced by the synergy effect of the hybrid-recirculating system unlike $COD_{Cr}$. Besides, despite of the increase of hybrid-recirculating system-recycle ratio, the deactivation of photo-catalytic activity was scarcely observed to eliminate the color while its irreversible deactivation was observed to eliminate $COD_{Cr}$.

Catalytic Cracking of n-Octane over H-ZSM-5 Catalysts: Effect of Calcination and Steam Treatment (H-ZSM-5 촉매에서 n-옥탄의 촉매분해반응: 소성 및 스팀 처리 효과)

  • Lee, Hyun-Ju;Shin, Chae-Ho;Choi, Won Choon;Lee, Chul Wee;Park, Yong Ki
    • Korean Chemical Engineering Research
    • /
    • v.46 no.2
    • /
    • pp.291-300
    • /
    • 2008
  • Catalytic cracking of n-octane was carried out over H-ZSM-5 zeolite catalysts after calcination with air and steaming with 100% steam in the temperature range of $550-750^{\circ}C$ for 24 h and compared with the results of thermal cracking. The increase of calcination and steaming temperature resulted in the decrease of surface area, pore volume, and strong acid sites, which was mainly caused by the dealumination of H-ZSM-5 framework. It was found by $^{27}Al$ and $^{29}Si$ MAS NMR that the dealumination was proceeded through the transformation process of tetrahedral framework Al${\rightarrow}$penta-cordinated Al ${\rightarrow}$ octahedral framework Al and the phenomena was much more severe in steaming conditions than that of calcination. In the catalytic cracking of n-octane, as the temperatures of calcination and steaming were increased, the conversion of n-octane, the selectivity of light olefins and ethylene to propylene ratio were decreased due to the dealumination of framework aluminum resulting the loss of acidic strengths. The conversion, selectivity of light olefins and ethylene to propylene ratio reached almost to the level of thermal cracking after steaming at $750^{\circ}C$ for 24 h.

Removal of Aqueous Iron Ion by Micellar Enhanced Ceramic Microfiltration Adding Surfactant (계면활성제를 첨가한 미셀 형성 세라믹 정밀여과에 의한 용존 철 이온 제거)

  • Park, Jin Yong;Yu, Byeong Gwon
    • Korean Chemical Engineering Research
    • /
    • v.47 no.2
    • /
    • pp.190-194
    • /
    • 2009
  • In this study sodium dodecyl sulfate (SDS), which was anionic surfactant, was added for forming micelles to remove iron ion that could be contained with small amount in industrial water. Then aggregates binding between iron ions and micelles were rejected by a ceramic microfiltration membrane. As result of SDS concentration effect on removal rates of iron and SDS in modified iron solution, the removal rate of iron was the highest value of 92.26% and the removal rate of SDS was 61.10% a little higher than the result of calcium ion at 8 mM which was CMC (Critical micelle concentration) of SDS. As final resistance of membrane fouling $R_f$ increased the more at the higher SDS concentration, it showed the highest value at 4 mM and the lowest at 10 mM of SDS. The final permeate flux $J_{180}$ had the highest value and the largest total permeate volume could be finally acquired at SDS 10 mM. In case of CMC 8 mM, low $R_f$ was shown as same as that of 10 mM until 80 minutes of operation, and tended to increase dramatically to 120 minutes and increase slowly again until 180 minutes.