• Applied Chemistry for Engineering
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• v.9 no.5
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• pp.689-697
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• 1998

In this work, we studied the equilibrium, rate and rate determining step of uranium adsorption on RGP resins of MR type prepared by varying the degree of crosslinking and the amount of diluent. The equilibrium of uranium adsorption on RGP resins were well explained by Frendrich isotherm as well as Langmuir isotherm model. The amount of adsorption and adsorption rate increase with the adsorption temperature. The heat of the adsorption was 11 kcal/mol. The adsorption rates of uranium on RGP resins were decreased in the order of RGP-10(50)>RGP-1(50)>RGP-2(50)>RGP-5(50)>RGP-0(50) and RGP-2(75)>RGP-2(100)>RGP-2(50)>RGP-2(30)>RGP-2(0). The diffusion resistance of uranium into RGP resin increased as follows; molecular diffusion < pore diffusion < surface diffusion. On the other hand, the surface diffusion was more dominative than the pore diffusion in intraparticle region. Thus, this result indicates that the adsorption mechanism of uranium on RGP resins is intraparticle diffusion controlled.

• Proceedings of the Korean Vacuum Society Conference
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• 2015.08a
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• pp.56.1-56.1
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• 2015

RF 마그네트론 스퍼터링법을 이용하여 유리 기판위에 ZnO:Al 박막을 증착하고 열공정에 따른 박막의 구조적, 광학적, 전기적 특성을 연구하였다. 열공정 파라미터로는 공정 온도와 어닐링 온도를 이용하였다. 각각의 열공정 파라미터 변화에 따라 ZnO:Al 박막의 특성이 영향 받음을 확인하였다. 모든 샘플에서(002) 우선 배향성을 보였으며 80% 이상의 투과도 특성을 보였다. 하지만, 열공정에 따라 결정성이 나빠지기도 좋아지기도 하였다. 표면 거칠기는 열공정 종류에 상관없이 온도 증가에 따라 증가하였다. 또한, 투과도도 열공정 종류에 상관없이 온도 증가에 따라 감소함을 보인 반면 광학적 밴드갭은 적색이동 현상을 나타내었다. 적색이동 현상은 Burstein-Moss effect와 관련이 있으며 온도증가에 따라 캐리어 이동도가 감소하여 나타난 현상이다. 열공정에서 따라 비저항이 민감하게 변화하였다. 각각의 열공정에서 온도가 증가함에 따라 비저항이 증가하였고 캐리어 농도와 이동도는 감소함을 보이고 있다. ZnO:Al 박막의 화학적인 상태를 분석한 결과, 열공정 온도에 따라 Al 농도 변화와 불순물 표면 흡착 변화가 발생하였으며 이에 따라캐리어 농도와 이동도의 감소가 나타난 것으로 판단된다.

• Korean Journal of Soil Science and Fertilizer
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• v.21 no.4
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• pp.380-385
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• 1988

The urease adsorption on zeolite and the various properties of adsorbed urease were investigated to find out the influence of zeolite on activity and properies of urease. Free urease in solution was adsorbed on zeolite untill the max. adsorption, and the amount of max. adsorption was 11.3mg urease/100mg zeolite at pH 7.0. It is apparent that free urease was adsorbed on the outer surface of zeolite by cation exchange reaction, and more than 70% of urease adsorption was adsorbed within 30 min. The activity of adsorbed urease was decreased by 89.6%, whereas Km value was increased to 34.4mM, which is higher than that of free urease. The optimum pH of adsorbed urease was widened 6.5 to 7.0, compared to that of free urease 7.0. The resistance of urease to protease became weaker by adsorption, however substrate specificity and thermal stability were not affected.

• Proceedings of the Korean Institute of Building Construction Conference
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• 2017.11a
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• pp.151-152
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• 2017

This tests examined the effectiveness of bacteria slime on the chloride ion penetration resistance of cement mortar. Test results exhibited that the chloride ion penetration depth of mortars including 5% expanded vermiculite immobilizing bacteria was 17% smaller than that of the control mortar without expanded vermiculite.

• Journal of the Korean Electrochemical Society
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• v.3 no.2
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• pp.109-114
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• 2000

The relation between the phase-shift profile fur the intermediate frequencies and the Langmuir adsorption isotherm at the poly-Ir/0.1 M $H_2SO_4$ aqueous electrolyte interface has been studied using ac impedance measurements, i.e., the phase-shift methods. The simplified interfacial equivalent circuit consists of the serial connection of the electrolyte resistance $(R_s)$, the faradaic resistance $(R_F)$, and the equivalent circuit element $(C_P)$ of the adsorption pseudoca-pacitance $(C_\phi)$. The comparison of the change rates of the $\Delta(-\phi)/{\Delta}E\;and\;\Delta{\theta}/{\Delta}E$ are represented. The delayed phase shift $(\phi)$ depends on both the cathode potential (E) and frequency (f), and is given by $\phi=tan^{-1}[1/2{\pi}f(R_s+R_F)C_P]$. The phase-shift profile $(-\phi\;vs.\;E)$ for the intermediate frequency (ca. 1 Hz) can be used as an experimental method to determine the Langmuir adsorption isotherm $(\theta\;vs.\;E)$. The equilibrium constant (K) for H adsorption and the standard free energy $({\Delta}G_{ads})$ of H adsorption at the poly-Ir/0.1 M $H_2SO_4$ electrolyte interface are $2.0\times10^{-4}$ and 21.1kJ/mol, respectively. The H adsorption is attributed to the over-potentially deposited hydrogen (OPD H).

• Journal of the Korean Electrochemical Society
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• v.3 no.1
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• pp.25-30
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• 2000

The relation between the phase-shift profile for the intermediate frequencies and the Langmuir adsorption isotherm at the poly-$Pt/0.1\;M\;H_2SO_4$ aqueous electrolyte interface has been studied using ac impedance measurements, i.e., the phase-shift methods. The suggested interfacial equivalent circuit consists of the serial connection of the electrolyte resistance ($R_S$), the faradaic resistance $(R_F)$ and the equivalent circuit element $(C_P)$ of the adsorption pseudocapacitance $(C_\varphi)$. The delayed phase shift $(\varphi)$ depends on both the cathode potential (E) and frequency (f), and is given by $\varphi=-tan^{-1}[1/2{\pi}f(R_s+R_F)C_p]$. The phase-shift profile $(\varphi\;vs.\;E)$ for the intermediate frequency (ca. 6Hz) can be used as an experimental method to determine the Langmuir adsorption isotherm (9 vs. E). The equilibrium constant (K) for H adsorption and the standard free energy $({\Delta}G_{ads})$ of H adsorption at the poly-$Pt/0.1\;M\;H_2SO_4$ electrolyte interface are $1.8\times10^{-4}\;and\;21.4kJ/mol$, respectively. The H adsorption is attributed to the over-potentially deposited hydrogen (OPD H).

• Proceedings of the KIEE Conference
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• 2008.07a
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• pp.2027-2029
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• 2008

옥외용 고전압 절연물의 절연성능은 표면저항과 밀접한 관계를 가지며, 이는 절연물 표면에 존재하는 수분의 거동에 의해 민감하게 반응하게 된다. 또한 절연물 표면에 흡착된 수분의 존재로 인해 절연물과 수분, 공기층의 유전율 차이로 인해 경계면에서의 전기력선속과 공간전하밀도의 변화가 급격해지므로 불평등전계를 형성할 우려가 있다. 따라서 본 논문에서는 옥외용 고전압 절연물의 표면에 작은 물방울 형태로 존재하게 되는 흡착수분에 의한 전계분포를 확인하기 위해 FEM을 이용하여 전산해석을 수행하였다.

• Korean Chemical Engineering Research
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• v.45 no.2
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• pp.166-171
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• 2007

The adsorption behavior of $Pb^{2+}$ was compared between calcium alginate beads and capsules, which have different structures of alginate-gel core beads and liquid core alginate-membrane capsules, respectively. In terms of adsorption kinetics and isotherms, adsorption characteristics depending on pH and hardening time were compared for both adsorbents and also released calcium ion during the adsorption process was monitored. The adsorption of $Pb^{2+}$ on both adsorbents was caused by surface complexation and ion exchange mechanisms, both of which have similar effects on adsorption process regardless of the amount of adsorbed $Pb^{2+}$. The dependence of $Pb^{2+}$ adsorption upon pH was also similar for both adsorbents indicating the existence of similar functional groups on the surface of adsorbents. However, a different $Pb^{2+}$ adsorption behavior was observed considering the adsorption kinetics. The adsorption kinetic of $Pb^{2+}$ on alginate beads was slower than on alginate capsules and the maximum adsorption loading ($Q_{max}$) onto alginate beads was also less than onto alginate capsules by 49%. This drawback of alginate beads compared to capsules were ascribed to a diffusion limitation due to solid gel-core structure of alginate beads.

• 한국신재생에너지학회:학술대회논문집
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• 2009.06a
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• pp.777-780
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• 2009

본 연구에서는 연료전지에의 응용을 위한 저가격의 무산소, 상온동작 가능한 센서구조를 설계, 제작하고 특성을 평가하였다. 연료전지의 수소 농도를 측정하기 위해서는 50ppm에서 5% 이상까지 넓은 범위를 감지할 수 있는 수소센서의 성능이 매우 중요하다. 이러한 특성과 상용화를 위해 가격 경쟁력을 갖는 수소센서로서, 수소흡착에 따른 Pd의 저항변화 특성을 이용한 센서 구조에 대하여 연구하였다. 높은 저항치를 갖는 Pd 후막 구조설계를 통하여 저항 감소형의 센서를 제작하여 특성평가를 하였다. 저가형으로 설계 제작된 Pd 수소센서는 50~20000ppm 범위에서 감지특성을 나타내었으며, 약 40sec의 응답속도를 보였다.

• Membrane Journal
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• v.6 no.2
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• pp.109-116
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• 1996

This work is a fundamental study for applying hybrid process coupling adsorption with microfiltration to waste-water treatment. Phenol was separated by adsorption on powdered activated carbon, adsorbed phenol with activated carbon was separated by microfiltration. As the particle size in suspension increased, filtration resistance decreased, and effect of particle concentration on resistance was less pronounced. The rate of uptake was greatly dependent on the degree of phenol loading. For a smaller amounts of activated carbon, the change of permeate concentration before break point and phenol loading with time were steeper than in the case of large amounts. Permeate concentration before break point decreased with decreasing particle size, this could be due to the increase of outer surface of particle and film mass transfer coefficient.