• Journal of the Korean Society for Precision Engineering
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• v.20 no.3
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• pp.194-201
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• 2003

This study presents the comparative filtration performance evaluation of automotive fuel filters based on the theory of Beta ratio. For the experiments, the fuel component's test stand incorporating the multi-pass filtration test circuit was developed. A mathematical description of filtration process in general was derived. And the theoretical basis of multi-pass test and the test procedure were described in detail. Experimental results revealed that domestic fuel filter tested could not maintain consistent Beta ratio, that is filtration efficiency, although it had the holding capacity of contaminants close to the specification at maximum pressure drop across the filter assembly. The results of experiments and simulations also showed that filtration system model could be refined including desorption ratio to estimate the variable Beta ratio in service life.

• YAKHAK HOEJI
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• v.13 no.1
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• pp.38-42
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• 1969

Chloropentammine chromium(III) chloride를 출발물질로 하여 여러가지의 thiocyanatoammine계 착화합물을 합성하는 실험에 있어서 그 수득량이 예상보다 매우 적고 그 염의 모액이 농적자색이라는 점으로 보아 그 모액중에 어떠한 다른 착화합물이 다량 형성되어 있으리라고 추측하여 그 분리를 시도하였다든바 미려한 적자색의 결정을 얻었다. 그리고 분석에 의하여 이 물질이 potassium hexathiocyanatochromate(III) 임을 증명하였다. Cr$^{+++}$ 의 thiocyanate 착화합물형성에 관하여는 Niel Bjerrm$^{(8)}$에 의한 보고문이 있고 또 이들의 제법으로서는 Roesler$^{(9)}$들에 의하여 Potassium chromium alum에서부터 이 물질을 만드는 방법만이 보고되어 있을뿐이다. 따라서 Chloropentammine chromium(III) chloride에서 부터 이 물질을 만드는 이 새로운 방법이 이러한 화합물들의 제법으로서 앞으로 이용될 수 있는것으로 사료한다. 제조 방법: Chloropentammine chromium(III) chloride 3g을 KSCN 24g, 빙초산 24ml및 물 48ml의 혼합수용액에 현탁시킨 혼합물을 처음에는 잘 교반하면서 가온하고 다음 완전히 용해될때까지 끊인다. 냉각시킨 다음 생성된 증황색의 침반 Thiocyanatopentammine chromium(III) thiocyanate를 여과하고 여액 65ml에 KSCN 50g을 추가하여 완전용해시킨다. 이 용액을 방냉시키면 적자색의 미려한 결정이 석출되므로 이 결정을 여과하여 ethanol로 세척하고 진공 desiccator중에서 건조시켰다. 수득량 1.2~1.3g.

• Proceedings of the Membrane Society of Korea Conference
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• 1997.10a
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• pp.133-134
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• 1997

1. 서론 : 제지산업은 용수 다소비용 산업으로, 생산하는 제품 톤당 약 40톤으로 폐수가 배출되고 있으며 공정내로 재활용하는 폐수량을 고려한다면 그 사용량은 더욱 클 것이다. 이와 같은 다량의 용수 사용으로 인하여 제지 공장의 폐수를 제조공정에서 재활용하는 방법이나 배출량을 감소시키는 방안들이 법률적이나 경제적인 측면에서 연구되고 있는 실정이다. 본 연구에서는 기존의 응집, 침전공정을 대신하고 여재를 이용힌 물리적 여과와 활성높은 미생물이 여재 표면에 부착되어 수중 유기물질을 생물학적으로 분해 제거하는 이중의 효과를 거둘 수 있는 호기성 생물막 공정을 도입하고 그 처리수의 유기물 및 용존 무기물을 Membrane 공정으로 제거함으로써 제지공업폐수를 재활용하여 용수기준까지 처리하 System의 개발을 그 목적으로 하였다.

• Journal of the Korean Society of Industry Convergence
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• v.3 no.3
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• pp.237-243
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• 2000

최근에 경제성장과 생활향상에 따른 물수요량이 급증함과 동시에 소비자의 질적요구가 강화되고 있는 실정이다. 기존 상수원인 하천의 수질오염으로 인하여 소비자의 요구사항을 충족시키기 위해서는 기존 정수처리법의 개선이 요구된다. 따라서 본 연구에서는 기존 급속여과법의 전염소 처리공정 및 응집.침전 공정의 개선을 통하여 음용수 수질을 개선하고자 하였다. 전염소 대신에 적용한 생물막여과 공정(BAF)의 처리효과 및 응집.침전 공정의 경우는 교반강도에 따른 침전효과에 따른 수질특성을 조사하였다. BAF공정은 탁월한 $NH_4$-N의 제거를 통하여 후속공정에 대한 오염부하량을 저감시킬수 있었고, 응집.침전의 경우 본 연구에서 제안한 응집제 주입량에 따른 교반강도의 실험식인에 의하여 구한 최적교반강도용 용집공정에 적용시 응집.침전의 효과를 향상시킨 수 있어 음용수 수질 향상을 기대 할 수 있었다.

• Journal of Korean Society of Environmental Engineers
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• v.36 no.8
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• pp.579-587
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• 2014

Various kinds of micro organic pollutants have frequently been detected from a water system. Therefore, it is considered to be very important part in the drinking water treatment system. And the research about removal process and processing efficiency have been being conducted briskly. In this study, the removal efficiency was evaluated using advanced water treatment process and nanofiltration process. The removal efficiency of nanofiltration process was very different according to physical and chemical characteristics of materials. The molecular weight of cutoff was the most influential factor in the removal efficiency. And when pKa value was higher than pH of raw water or Log Kow value was below 2, the removal efficiency of material was decreased. In case of oxidation reaction, the bigger the molecular weight of material was and the more hydrophobic a material was, the less oxidation reaction occurred. And the removal efficiency was decreased. Most unoxidized materials were removed by absorption. And the more actively oxidation reaction occurred by $H_2O_2$, the more absorption reaction increased.

• Journal of KIISE:Software and Applications
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• v.36 no.4
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• pp.298-305
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• 2009

In contrast to content_based filtering systems, collaborative filtering systems not only don't contain information of items, they can not recommend items when users don't provide the information of their interests. In this paper, we propose the recommender agent using association item tree to solve the shortcomings of collaborative filtering systems. Firstly, the proposed method clusters users into groups using vector space model and K-means algorithm and selects group typical rating values. Secondly, the degree of associations between items is extracted from computing mutual information between items and an associative item tree is generated by group. Finally, the method recommends items to an active user by using a group typical rating value and an association item tree. The recommender agent recommends items by combining user information with item information. In addition, it can accurately recommend items to an active user, whose information is insufficient at first rate, by using an association item tree based on mutual information for the similarity between items. The proposed method is compared with previous methods on the data set of MovieLens recommender system.

• Membrane Journal
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• v.13 no.4
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• pp.211-218
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• 2003

The removal characteristics of cadmium in micellar enhanced ultrafiltration (MEUF) were investigated by using an anionic biosurfactant, deoxycholic acid (DCA). The ultrafiltration experiments were performed in a batch-type stirred cell. The ultrafiltration membranes used were Millipore YM1, YM3, YM10, and YM30 which had a difference in molecular weight cut-off. The presence of cadmium ion in DCA solution tends to reduce the critical micell concentration considerably and increase the micell size. The molecular weight cut-off of ultrafiltration membrane had a minimal effect on cadmium removal whereas DCA/Cd ratio had a substantial influence. When DCA/Cd ratio was 3, the removal efficiency of cadmium was more than 99.6%. A relative flux, which is defined as ratio of the flux for a separation trial to that of deionized water run using the same piece of membrane, decreased in the order of YM3 > YM1 > YM10 > YM30.

• The Journal of Engineering Geology
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• v.14 no.4 s.41
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• pp.391-400
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• 2004

Excess pumping on the river bank filtration well causes the over drawdown in the protected area of bank, which may make many problems such as soil water contents, Pumping head in the irrigated land, and it needs more irrigation and development of the deeper irrigating well. In this study the installation of the artificial recharging well was suggested to reduce the excess draw down in the protected land. Artificial recharging wells were applied at the bank filtration site of Changwon city by using Visual-MODFLDW. The optimized conditions are calculated that the recharging well is located about loom apart from the pumping well, and the recharging rate is $5\%$ of the pumping yield.

• Membrane Journal
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• v.18 no.1
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• pp.1-6
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• 2008

After membrane fouling factors in acrylic wastewater were minimized by pretreatment process accompanied with coagulation-filtration-neutralization, it was utilized in UF/RO process. After composing of ultrafiltration and reverse osmosis module set according to types and kinds of membrane, the separation characteristics were examined with the variation temperature and pressure using pretreated acrylic wastewater by membrane module sets. It was found that permeate flux of UF module in module set 4 was about two${\sim}$three times larger than that of UF module in module set 1. Final quantity of permeate from the module set 2 and module set 3 combined with tubular module was shown very good result. It was shown that the removal efficiency of TDS, T-N and COD was very low and was not dependent on the variation of temperature and pressure in all UF modules. The removal efficiency of TDS, T-N and COD was very excellent in RO module. Final water quality of acrylic wastewater was satisfied with effluent allowances limit and membrane module sets were ascertained to reuse wastewater.

• Membrane Journal
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• v.25 no.3
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• pp.256-267
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• 2015

The goal is to compare two different aeration strategies for a pilot scale operation of submerged microfiltration with respect to the minimization of membrane fouling. A constant aeration (65 L/min) was examined parallel with a step-wise increase in airflow rate (40 to 65 L/min). The airflow rate was stepped to a higher rate every 5 min and the step-aeration cycles were repeated at regular intervals of 15 min. The comparative filtration runs were conducted with synthetic water containing powdered activated carbon (~10 g/L) and/or kaolin (~20 g/L) at a constant flux of 80 LMH. The extent and mechanisms of fouling in the microfiltration were identified by determining hydraulic resistance to filtration and the fouling reversibility after cleaning. Results showed that the step-aeration effectively alleviated fouling in the microfiltration of synthetic water compared to when using constant aeration. A substantial decrease in fouling was achieved by combining with coagulation using aluminum salts regardless of the aeration strategies. The constant aeration resulted in increased pore blocking likely due to increased accumulation of particles on the surface of membrane.