• Environmental engineer
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• s.324
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• pp.86-93
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• 2013

본 발명은 녹색 건축물에 적용되는 중수도 설치를 위한 수처리 시스템에 관한 것으로서, 더욱 상세하게는 건축물에서 배출되는 오수의 유입량을 제어하면서, 산기장치를 이용하여 상기 오수에 일정량의 에어를 공급하여 슬러지의 침강과 부패방지를 유도하는 유량조정조와, 상기 유량조정조를 거친 오수를 응집 및 침전처리하고 가압부상에의해 슬러지를 처리하는 가압부상조와, 상기 가압부상조를 거친 오수에 포함되어 있는 질소, 인을 처리하는 무산소조와, 상기 무산소조를 거친 오수에 포함되어 있는 유기물을 수처리용 접촉 메디아(DSBB)에 의해 분해하는 생물막조와, 상기 생물막조를 거친 오수를 침전과정을 통해 침전된 슬러지를 외부로 배출하는 침전조와, 상기 침전조를 거친 오수를 분리막에 통과시켜 오수에 포함되어 있는 미생물, 세균등의 미세입자들을 제거하는 분리막조와, 상기 분리막조를 거친 오수에 포함되어 있는 미처리 미세입자를 여과기에 통과시켜 처리하는 여과조와, 상기 여과조를 거친 오수를 오존($O_3$) 또는 UV 살균 처리하는 소독조와, 상기 소독조를 거쳐 최종적으로 처리된 처리수를 일정시간 동안 체류시켰다가 건축물의 중수로 재이용하기 위해 방출시키는 저수조를 포함하여 이루어지는 녹색 건축물에 적용되는 중수도 설치를 위한 수처리 시스템에 관한 것이다.

• Journal of KIISE:Software and Applications
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• v.28 no.6
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• pp.403-413
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• 2001

시스템이 진화와 노화를 거듭하는 경우 프로그램을 이해하는데 있어서 가장 정확한 문서는 기존의 시스템 자체에서 추출되어진 정보이다. 프로그램의 이해를 돕기 위한 분석기법중의 하나인 프로그램 슬라이싱은 1984년 Weiser에 의해서 소개되어진 이후 다양한 방향으로 연구가 진행되어져 왔다. 특히, 생성되어지는 프로그램 슬라이스가 사이즈가 크고 충분히 집약적이지 못하다는 문제점과 슬라이스의 계산방법이 효율적이지 못하다는 문제점을 극복하기 위하여 여러 가지 방법들을 시도되어 왔다. 본 논문은 고전적인 슬라이싱 기준에 새로운 파라미터를 추가함으로써 제외개념을 이용하여 보다 함수적으로 응집력있고, 사이즈가 작은 슬라이스를 생성하는 선택 슬라이스를 제시하며 이 선택슬라이스를 계산하기 위한 효율적인 방법을 기술한다. 데이터와 제어의 흐름을 이용하여 선택 슬라이싱을 정의하고, 선택 슬라이싱을 위한 종속그래프를 정의하고 이를 사용하여 선형적 시간 내에 선택 슬라이스를 생성하는 알고리즘을 기술한다.

• Journal of the Korean Ceramic Society
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• v.40 no.7
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• pp.677-682
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• 2003

The physical properties of sintered body made from 3 kinds of slip, F (Flocculated), M (Moderate), and D (Dispersed) for coal fly ash 70-clay 30 (wt%) were studied in terms of slip states and pore size distribution of sintered bodies. The floc particle size distribution for slip F was wider than slip D and the slip F contained flocs larger than 11 $\mu\textrm{m}$. The pore size distribution of the green body of all slips ranged over 1∼4 $\mu\textrm{m}$. The pores smaller than 1 $\mu\textrm{m}$ almost disappeared during the sintering process, while the larger pore of 2.5∼3 $\mu\textrm{m}$ growed by 1 $\mu\textrm{m}$. The pore distribution for the green body of slip F became a narrow in width and high in height after sintering and the large pore limit in a slip F sintered body was 5.1 $\mu\textrm{m}$ which is smaller than that of other slip. The slip F rather flocculated was favorable over slip D well dispersed, in offering a higher compressive strength. From these results, the mechanical strength of sintered body is dependent on the pore distribution which could be controlled by dispersion state of the slips.

• Journal of Korean Society of Environmental Engineers
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• v.27 no.10
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• pp.1035-1042
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• 2005

Granular Activated Carbon(GAC) is widely used in drinking water treatment. At S and B Water Treatment Plant, GAC is used in place of granular media in conventional rapid filters(GAC Filter-Adsorber) for removal of Disinfection By-products(DBPs). The primary focus of this study is on the performance of existing filter-adsorber, and their operation. It was found that F/A process removed turbidity as effective as sand system. The ratio of Hydrophobic DOM (HPO) and hydrophilic DOM (HPI) fraction in the raw water at S and B WTP was similar. Filter Adsorber presented earlier DOC breakthrough and steady state condition which was contributed by biodegradation during operation period. The removal efficiency of DBPs were used to evaluate the filter performance. The DBPs concentration of F/A treated water was below treatment goal level (THM < $80\;{\mu}g/L$, HAA < $60{\mu}g/L$). The removal efficiency of THM decreased rapidly during operation period. However, HAA were removed steadily regardless of the influent concentration of HAA. These results indicate that the removal of THM depend upon the adsorption mechanism while the removal of HAA depend upon biodegradation as well as adsorption. The decrease of adsorption capacity and characteristic value of GAC may be attributed to the effect of high organic loading, residual free chlorine, coagulants, manganese oxidants and frequently backwashing. This study has confirmed that Filter adsorber process can be considered as effective alternatives for the removal of DBPs, especially HAA.

• Resources Recycling
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• v.17 no.5
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• pp.52-59
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• 2008

Sol-gel process applied in this study was carried out by chelation of metal ions and citric acid. From the results of thermal gravimetric analysis and XRD analysis of gel powder obtained through sol-gel and heat treatment, gel powders are mostly amorphous, and crystallize completely at $900^{\circ}C$, and the crystalline structure of YAG increases with increasing calcinations temperature. Since YAG prepared by sol-gel & calcinations process was porous, and the sape and size was irregular and nonuniform, the shape and size of YAG powder had to be controlled. Therefore the effects of organic materials such as ethylene glycol and surfactant on the crystalline structure of YAG powder were investigated. Polyesterification of ethylene glycol and citric acid separated reaction area of metal ions in the solution and decreased the size of YAG primary particles. The addition of Igepal 630 as surfactant formed the droplet in the solution, and increased the size of primary particles which forms the aggregate of YAG In order to obtain monodispersed YAG particles of uniform size, gel powder prepared with organic materials had to be milled before calcination. And milling process was very important for obtaining YAG of uniform size.

• Korean Chemical Engineering Research
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• v.55 no.6
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• pp.822-829
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• 2017

As a method to reduce the total phosphorus in sewage treatment plant, we applied the integral type slow mixing/sedimentation fiber filtration system to compare the control methods for the sewage effluent and the reject water. It was analyzed that about 92.4 kg T-P/day should be removed in order to satisfy the final concentration of phosphorus of 0.2 mg T-P/L, which is reinforced effluent standard. Therefore the total phosphorus removal efficiency should be 96% for sewage effluent and 69.2% for reject water (dehydrated filtrate) respectively. The system operation cost to achieve the target of total phosphorus removal efficiency was assessed. It has been found that the treatment cost of the reject water containing high concentration of phosphorus with a low flow rate is reduced to about 1/2.4 of the coagulant cost and about 1/120 of the electricity cost, compared to that of the sewage effluent treatment. Also the economics of the integral type slow mixing/sedimentation fiber filtration system and the general coagulation and sedimentation system were compared. It was evaluated that the development system was more economical because the installation area of the integral type slow mixing/sedimentation fiber filtration system was about 1/7 smaller than that of the general coagulation and sedimentation system, and the annual operation cost including the required amount of coagulant and electricity cost of the development system was lowered about 1/1.7 than that of the general system.

• Journal of IKEEE
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• v.20 no.2
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• pp.177-180
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• 2016

The effect of varying thickness of Ag/Ti metal bilayer and annealing time have investigated for controlling self-organized nanoparticles (NPs) on 4H-SiC substrate. In addition, Glass and Si substrate which have different surface energy from SiC were fabricated for analyzing interaction of agglomeration. The results of FE-SEM indicated the different formation behaviors of NPs in various ranges of fabrication condition. The surface energy was measured by using a Contact Angle Analyzer. The formation of network-like NPs was observed on Glass and 4H-SiC, respectively, whereas it was not the case on Si substrates. It has been found that the size of NPs increases with decreasing surface energy, due to particle size-dependent hydrophilic properties of substrates. The different formation behavior was explained by using Young's equation for the contact angles between the metal and different substrates.

• Korean Journal of Materials Research
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• v.10 no.1
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• pp.69-76
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• 2000

Despite the improved formability and processing advantages, the use of semi-solid metals is greatly limited due to the difficulties in controlling the optimum forming parameters. In the present study, the tensile properties of closed die, pressure formed semi-solid A356 alloy were examined. It was demonstrated that the tensile strength of thixoformed A356 alloy could be greatly reduced when the forming parameters were not rigorously controlled. The reduced strength of unappropriately formed products appeared to be related to the coarsening of the primary phases. The possibility of improving tensile properties of as-formed products by simple post heat treatment was also assessed.

• Proceedings of the Korean Vacuum Society Conference
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• 2012.02a
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• pp.113-113
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• 2012

플라즈마 내에서 발생하는 입자는 플라즈마 내 전기적 및 화학적 특성으로 인해 응집이 적고 균일한 특성을 가진다. 이에 따라 도포성이 좋으며 낮은 응력을 가지는 박막의 형성이 가능하다. 이러한 특성을 가지는 나노입자는 메모리, 고효율 박막형 태양전지 등에 이용될 수 있다. 특히, PECVD (Plasma enhanced chemical vapor deposition) 공정 중 플라즈마가 켜져있는 동안 수소 가스를 펄스형태로 추가 주입하는 방법은 실리콘 이온 사이의 결합을 통한 표면 성장을 일부 방해하여 이를 통해 최종적으로 생성되는 실리콘 입자의 크기제어를 가능하게 한다. 이러한 과정으로 PECVD내에서 생성된 입자의 입경 분포는 기존의 경우 공정 중 포집을 한 후 전자현미경을 이용하였지만 실시간 측정이 불가능한 한계가 있었고, 레이저를 이용한 실시간 측정은 그 측정범위의 한계로 인해 적용에 어려움이 있었다. 이에 따라 본 연구에서는 저압에서 실시간으로 나노입자 크기분포 측정이 가능한 PBMS (particle beam mass spectrometer)를 이용하여 PECVD 내에서 수소가스 펄스를 이용하여 발생되는 실리콘 입자를 공정 변수별로 측정하여 각 변수에 따른 입자 생성 경향을 분석하였다. 실리콘 나노 입자의 측정은 PBMS 장비의 전단 부분을 PECVD 장치 내부에 연결하여 진행하였다. 수소 가스 펄스를 이용한 실리콘 입자 생성의 주요 변수는 RF pulse, $H_2$ pulse, 가스 유량 (Ar, $SiH_4$, $H_2$), Plasma power, 공정 압력 등이 있다. 이와 같이 주어진 변수들의 제어를 통해 생성된 나노입자의 입경분포를 PBMS에서 실시간으로 측정하고, 동일한 조건에서 포집한 입자를 TEM 분석 결과와 비교하였다. 측정 결과 각각의 변수에 대하여 생성되는 입자의 크기분포 경향을 얻을 수 있었으며, 이는 추후 생성 입자의 응용 분야에 적합한 크기 분포 특성을 가지는 실리콘 입자를 제조하기 위한 조건을 정립하는데 중요한 역할을 할 것을 기대할 수 있다.

• Journal of Institute of Control, Robotics and Systems
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• v.3 no.6
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• pp.644-651
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• 1997

In the water purification plant, chemicals are injected for quick purification of raw water. It is clear that the amount of chemicals intrinsically depends on water quality such as turbidity, temperature, pH and alkalinity. However, the process of chemical reaction to improve water quality (e.g., turbidity) by chemicals is not yet fully clarified nor quantified. The feedback signal in the process of coagulant dosage, which should be measured (through the sensor of the plant) to compute the appropriate amount of chemicals, is also not available. Most traditional methods focus on judging the conditions of purifying reaction and determine the amounts of chemicals through manual operation of field experts using Jar-test data. In this paper, a systematic control strategy is proposed to derive the optimum dosage of coagulant, PAC(Polymerized Aluminium Chloride), using Jar-test results. A neural network model is developed for coagulant dosing and purifying process by means of six input variables (turbidity, temperature, pH, alkalinity of raw water, PAC feed rate, turbidity in flocculation) and one output variable, while considering the relationships to the reaction of coagulation and flocculation. The model is utilized to derive the optimum coagulant dosage (in the sense of minimizing turbidity of water in flocculator). The ability of the proposed control scheme validated through the field test has proved to be of considerable practical value.