• 대한환경공학회지
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• 제22권2호
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• pp.279-289
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• 2000

본 연구에서는 정수공정에서 응집제 종류와 고액분리방법이 조류제거에 미치는 영향을 조사하였다. 따라서, 원수의 특성을 탁도, $KMnO_4$ 소비량, UV-254, chlorophyll-a 등으로 파악하고 이들 수질인자간의 상관관계를 분석하였다. 또한 시판중인 Alum계열 응집제(Alum, PAC, PACS)가 조류제거에 미치는 영향을 실험실 쟈테스트를 이용하여 탁도 및 유기물제거, pH 저하특성 및 알카리도 소모특성 및 개체수 제거율 등으로 연구하였다. 상관관계 분석에 의하면 유기물항목인 UV-254, $KMnO_4$ 소비량, chlorophyll-a와 탁도의 상관계수는 각각 0.775, 0.674 및 0.623으로 상관성이 매우 높은 것으로 나타났다. 조류발생시 응집제 종류별 응집침전에서 유기물 제거특성은 조류의 농도가 적을 경우에는 유사한 효율을 보였으나 조류농도 증가에 의한 높은 유기물 농도($KMnO_4$ 소비량 20mg/l 이상)와 높은 탁도(100NTU 이상)에서는 PAC, PACS와 같은 무기고분자 응집제가 Alum보다 제거효율이 우수하였다. 조류번성시 응집공정을 거친 후 침전과 부상공정의 비교실험에서 부상분리공정을 사용할 경우 Alum이 모든 분석항목에서 고분자 응집제인 PAC, PACS보다 우수하였으며, 95% 이상의 제거율을 나타내었다. 반면에 PAC와 PACS의 경우는 침전공정이 부상공정보다 효율이 높았으며, $KMnO_4$ 소비량의 경우 부상법 제거율의 2배 이상 효율을 보여주었다. 따라서 조류제거를 향상시키기 위해서는 Alum을 사용할 경우 부상분리, PAC, PACS를 사용할 경우 침전공정이 바람직한 것으로 나타났다. 대상원수에서는 남조식물문의 Microcystic와 녹조식물문의 pediastrum simplex 등 두 가지의 속이 다수 속으로 출현하였으며, Alum, PAC, PACS의 투입후 침전실험에서 27%, 45%, 22%의 조류개체수의 제거율을 보였으나, 용존공기부상법(DAF)을 적용한 경우에는 모든 응집제에서 동, 식물플랑크톤 모두가 100%에 가까운 제거율을 보여주었다.

• 공업화학
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• 제8권5호
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• pp.777-783
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• 1997

n-propanol 용매내에서 titanium n-propoxide($Ti(O^nPr)_4$)의 가수분해반응에 의하여 $TiO_2$ 미분말을 합성하였고, 가수분해속도를 자외선 분광법에 의하여 측정하였다. 분말합성은 water/alkoxide의 농도비가 약 300정도에서 실시하였으며, 물농도, 반응온도, 반응시간 및 반응용액의 산 염기효과에 의한 합성조건을 조사하였다. 반응은 $Ti(O^nPr)_4$의 농도에 비하여 물농도를 과량으로 하여 유사일차반응으로 진행시켰고, 반응속도상수를 Guggenheim method로 계산하였다. 또한 물의 동위원소효과($D_2O$)를 측정하여 반응에 관여하는 물분자의 촉매성을 확인하였다. 실험결과 중성 및 염기성 용액 조건에서 $TiO_2$미분말이 합성되었고, 미세구조 관찰로부터 $TiO_2$입자는 직경 $0.4-0.7{\mu}m$ 정도의 구형입자로 확인되었으며, 물의 농도와 반응온도가 증가할수록, 반응시간이 감소할수록 입자크기는 작아지는 경향을 보였다. 물의 동위원소효과로부터, 물분자는 nucleophilic catalysis로 작용하고 있으며, 반응속도로부터 전이상태에 참여하는 n-value와 열역학적 파라미터를 계산한 결과, $Ti(O^nPr)_4$의 가수분해반응은 이분자 반응인 associative $S_N2$ mechanism으로 진행하는 것으로 추정되었다.

• Korean Chemical Engineering Research
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• 제53권1호
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• pp.78-82
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• 2015

유기주형(organic template) 입자를 이용하여 소디움실리케이트(sodium silicate)로부터 중공형 실리카(hollow silica) 입자를 제조하였다. 유기주형 입자로는 스티렌 단량체(styrene monomer)로부터 분산중합(dispersion polymerization)에 의해 제조된 폴리스티렌 라텍스(polystyrene latex, PSL) 입자를 사용하였다. 유기주형 입자 제조 시 중합개시제인 2,2'-azobisisobutyronitrile(AIBN)의 주입량을 조절하여 $1{\sim}3{\mu}m$의 크기를 가진 입자를 제조하였다. 생성된 유기주형 입자 표면에 졸-겔(sol-gel)법에 의해 소디움실리케이트로부터 생성된 실리카($SiO_2$) 나노 입자를 코팅하여 PSL/$SiO_2$ 코어-쉘 형태의 입자를 제조하였다. 유기용매인 테트라하이드로푸란(tetrahydrofuran, THF)을 이용하여 코어-쉘 입자 내부의 유기주형을 제거 하였다. 코어-쉘 입자 제조 시 용매의 종류 및 pH의 변화에 따라 생성되는 중공형 실리카 입자의 형상을 조사하였다. PSL/$SiO_2$ 코어-쉘 입자 제조 시 용매를 에탄올에서 물로 변경했을 때 중공형 실리카 입자가 성공적으로 제조되었으며 낮은 pH 값을 갖는 용매에서 쉘 두께가 균일한 중공형 실리카 입자가 형성되었다. 중공형 실리카 입자의 반사도를 측정한 결과 상용 제품(Insuladd)보다 높은 반사 특성을 보여주었다.

• 상하수도학회지
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• 제13권1호
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• pp.125-133
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• 1999

The objective of present work is to evaluate the optimum coagulation conditions in order to decrease dissolved organic carbon(DOC) and turbidity at different polyaluminum chloride dosage and pH from Nakdong River water. This studies were carried out to examine distribution on apparent molecular weight(AMW) of DOC in the Nakdong River water and its coagulation-sedimentation water. On the basis of jar tests, at the optimum coagulation pH in order to decrease DOC and turbidity were pH 5.0~6.0 and optimum dosage of polyaluminum chloride were 10~15mg $Al_2O_3/L$. The removal percentage of DOC and UV-254 absorbance were 35~40%, 45~60%, respectively. In pilot plant, at the optimum coagulation pH in order to decrease DOC and turbidity were 5.0-6.5, and the removal percentage of DOC were 30~45%. Distributions of AMW in the Nakdong River, less than 6,800dalton were 60.7% 6,800~11,000dalton were 32.8%, more than 11,000dalton were 6.4%. When the polyaluminum chloride dosage was 12~20mg/L, the removal percentages of each AMW for AMW of Nakdong River water, less than 6,800dalton were 25~28%, 6,800~11,000dalton were 65~68% more than 11,000dalton were 10~60%.

• 한국진공학회:학술대회논문집
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• 한국진공학회 2014년도 제46회 동계 정기학술대회 초록집
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• pp.362-362
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• 2014

Atomic layer deposition (ALD) can be regarded as a special variation of the chemical vapor deposition method for reducing film thickness. ALD is based on sequential self-limiting reactions from the gas phase to produce thin films and over-layers in the nanometer scale with perfect conformality and process controllability. These characteristics make ALD an important film deposition technique for nanoelectronics. Tantalum pentoxide ($Ta_2O_5$) has a number of applications in optics and electronics due to its superior properties, such as thermal and chemical stability, high refractive index (>2.0), low absorption in near-UV to IR regions, and high-k. In particular, the dielectric constant of amorphous $Ta_2O_5$ is typically close to 25. Accordingly, $Ta_2O_5$ has been extensively studied in various electronics such as metal oxide semiconductor field-effect transistors (FET), organic FET, dynamic random access memories (RAM), resistance RAM, etc. In this experiment, the variations of chemical and interfacial state during the growth of $Ta_2O_5$ films on the Si substrate by ALD was investigated using in-situ synchrotron radiation photoemission spectroscopy. A newly synthesized liquid precursor $Ta(N^tBu)(dmamp)_2$ Me was used as the metal precursor, with Ar as a purging gas and $H_2O$ as the oxidant source. The core-level spectra of Si 2p, Ta 4f, and O 1s revealed that Ta suboxide and Si dioxide were formed at the initial stages of $Ta_2O_5$ growth. However, the Ta suboxide states almost disappeared as the ALD cycles progressed. Consequently, the $Ta^{5+}$ state, which corresponds with the stoichiometric $Ta_2O_5$, only appeared after 4.0 cycles. Additionally, tantalum silicide was not detected at the interfacial states between $Ta_2O_5$ and Si. The measured valence band offset value between $Ta_2O_5$ and the Si substrate was 3.08 eV after 2.5 cycles.

• 상하수도학회지
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• 제36권2호
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• pp.59-79
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• 2022

Conventional wastewater treatment plants (WWTPs) do not fully remove micropollutants. Enhanced treatment of sewage effluents is being considered or implemented in some countries to minimize the discharge of problematic micropollutants from WWTPs. Representative enhanced sewage treatment technologies for micropollutant removal were reviewed, including their current status of research and development. Advanced oxidation processes (AOPs) such as ozonation and UV/H₂O₂ and adsorption processes using powdered (PAC) and granular activated carbon (GAC) were mainly discussed with focusing on process principles for the micropollutant removal, effect of process operation and water matrix factors, and technical and economic feasibility. Pilot- and full-scale studies have shown that ozonation, PAC, and GAC can achieve significant elimination of various micropollutants at economically feasible costs(0.16-0.29 €/m³). Considering the current status of domestic WWTPs, ozonation and PAC were found to be the most feasible options for the enhanced sewage effluent treatment. Although ozonation and PAC are all mature technologies, a range of technical aspects should be considered for their successful application, such as energy consumption, CO₂ emission, byproduct or waste generation, and ease of system construction/operation/maintenance. More feasibility studies considering domestic wastewater characteristics and WWTP conditions are required to apply ozonation or PAC/GAC adsorption process to enhance sewage effluent treatment in Korea.

• 상하수도학회지
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• 제28권4호
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• pp.391-396
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• 2014

Ultrapure water (UPW) is water containing nothing but water molecule ($H_2O$). The use of UPW is increasing in many industries such as the thermal and nuclear power plants, petrochemical plants, and semiconductor manufacturers. In order to produce UPW, several unit processes such as ion exchange, reverse osmosis (RO), ultraviolet (UV) oxidation should be efficiently arranged. In particular, RO process should remove not only ions but also low molecular weight (LMW) organic matters in UPW production system. But, the LMW organic matter removal data of RO membranes provided by manufacturers does not seem to be reasonable because they tested the removal in high concentration conditions like 1,000 ppm of isopropyl alcohol (IPA, MW=60.1). In this study, bench-scale experiments were carried out using 4-inches RO modules. IPA was used as a model LMW organic matter with low concentration conditions less than 1 ppm as total organic carbon (TOC). As a result, the IPA removal data by manufacturers turned out to be trustable because the effect of feed concentration on the IPA removal was negligble while the IPA removal efficiency became higher at higher permeate flux.

• 대한환경공학회지
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• 제31권1호
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• pp.9-14
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• 2009

본 연구에서는 폴리에스테르 중합폐수의 배출 원수에 약 600 mg/L의 고농도로 존재하는 1,4-dioxane을 5 mg/L 이하까지 (2011년 규제 시행) 제거할 수 있는 고급산화공정의 현장 적용 기술을 개발하고자 구미지역 폴리에스테르 제조회사 중 K사의 폐수처리 시설을 선정하여 연구를 하였다. 공기의 공급 하에 광펜톤산화반응을 K사에 설치된 pilot에서 운전하였다. 막대형 산기관을 통해 공기를 공급하면서 10개의 UV-C 램프(240 ${\mu}W/cm^2$)의 조사 하에 과산화수소(2,800 ppm)와 철염(1,400 ppm)을 주입하였을 때 1,4-dioxane의 제거 효율이 2시간 만에 90%까지 나타나는 결과를 도출할 수 있었다. 그러나 처리수의 1,4-dioxane 농도는 약 60 mg/L으로 여전히 높았다. 그리하여 후속 처리로 bench-scale의 활성슬러지공정(V=8.9 L)을 이용하여 광펜톤산화 처리수 내의 1,4-dioxane 제거 가능성을 평가하였다. 그 결과로서 활성슬러지공정의 유출수내의 1,4-dioxane의 농도는 약 2~3 mg/L까지 저감되었으며 이를 통해, 광펜톤산화공정과 활성슬러지공정의 연계처리를 통해 1,4-dioxane 배출 허용기준(5 mg/L, 2011년)에 부합될 수 있는 효과적인 처리공정임을 입증하였다.

• 대한화학회지
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• 제61권1호
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• pp.29-33
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• 2017

Formation of Au particles in nonstoichiometric $Cu_{2-x}{^I}Cu{_2}^{II}O_{3-{\delta}}$ ($x{\approx}0.20$; ${\delta}{\approx}0.10$) oxide from aniline + hydrochloric acid mixtures and chloroauric acid in the ratios 30 : 1; 60 : 1; 90 : 1 (S1-S3) by volume and 0.01 mol of copper acetate, $Cu(OCOCH_3)_2.H_2O$, in each case is performed by sol-gel growth. Powder x-ray diffraction (XRD) results show Au particles are dispersed in tetragonal nonstoichiometric dicopper (I) dicopper (II) oxides, $Cu_{2-x}{^I}Cu{_2}^{II}O_{3-{\delta}}$ ($x{\approx}0.20$; ${\delta}{\approx}0.10$). Average crystallite sizes of Au particles determined using Scherrer equation are found to be in the approximate ranges ${\sim}85-140{\AA}$, ${\sim}85-150{\AA}$ and ${\sim}80-150{\AA}$ in S1-S3, respectively which indicate the formation of Au nano-micro size particles in $Cu_{2-x}{^I}Cu{_2}^{II}O_{3-{\delta}}$ ($x{\approx}0.20$; ${\delta}{\approx}0.10$) oxides. Hysteresis behaviour at 300 K having low loop areas and magnetic susceptibility values ${\sim}5.835{\times}10^{-6}-9.889{\times}10^{-6}emu/gG$ in S1-S3 show weakly ferromagnetic nature of the samples. Broad and isotropic electron paramagnetic resonance (EPR) lineshapes of S1-S4 at 300, 77 and 8 K having $g_{iso}$-values ${\sim}2.053{\pm}0.008-2.304{\pm}0.008$ show rapid spin-lattice relaxation process in magnetic $Cu^{2+}$ ($3d^9$) sites as well as delocalized electrons in Au ($6s^1$) nano-micro size particles in the $Cu_{2-x}{^I}Cu{_2}^{II}O_{3-{\delta}}$ ($x{\approx}0.20$; ${\delta}{\approx}0.10$) oxides. Broad and weak UV-Vis diffuse reflectance optical absorption band ~725 nm is assigned to $^2B_{1g}{\rightarrow}^2A_{1g}$ transitions, and the weak band ~470 nm is due to $^2B_{1g}{\rightarrow}^2E_g$ transitions from the ground state $^2B_{1g}$(${\mid}d_{x^2-y^2}$>) of $Cu^{2+}$ ($3d^9$) ions in octahedral coordination having tetragonal distortion.

• 한국물환경학회지
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• 제26권3호
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• pp.460-467
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• 2010

For D-WTP's sedimentation basin and distribution reservoir, and water tap the predictive models proposed tentatively herein included the models for estimating TTHM concentration in precipitated water, for treated water and for tap water, and the estimated correlation formula between treated water's TTHM concentration and tap water. As for TTHM-concentration predictive model in sedimentation water, the coefficient of determination is 0.866 for best-fitted short-term $DOC{\times}UV_{254}$ based Model (TTHM). As for $HAA_5$-concentration predictive model in sedimentation water, the coefficient of determination is 0.947 for the suitable $UV_{254}$-based model ($HAA_5$). In case of the predictive model in treated water, the coefficient of determination is 0.980 for best-fitted $DOC{\times}UV_{254}$ based model (TTHM) using coagulated waters, while the coefficient of determination is 0.983 for best-fitted $DOC{\times}UV_{254}$ based model ($HAA_5$) using coagulated waters, which described the $HAA_5$ concentration well. However, the predictive model for tap water could not be compatible with the one for treated water, only except for possibility inducing correlation formula for prediction, [i.e., the correlation formula between TTHM concentration and tap water was verified as TTHM (tap water) = $1.162{\times}TTHM$ (treated water), while $HAA_5$ (tap water) = $0.965{\times}HAA_5$ (treated water).] The correlation analysis between DOC and $KMnO_4$ consumption by process resulted in higher relationship with filtrated water, showing that its regression is $DOC=0.669{\times}KMnO_4$ consumption - 0.166 with 0.689 of determination coefficient. By substituting it to the existing DOC-based model ($HAA_5$) for treated water, the consequential model formula was made as follows; $HAA_5=8.35(KMnO_4\;consumption{\times}0.669-0.166)^{0.701}(Cl_2)^{0.577}t^{0.150}0.9216^{(pH-7.5)}1.022^{(Temp-20^{\circ}C)}$