• Proceedings of the Korean Vacuum Society Conference
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• 2012.02a
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• pp.480-481
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• 2012

LED (Light Emitting Diode)는 친환경적이며 고수명 등의 여러 장점을 가지고 있어서 액정디스플레이의 광원으로 널리 사용되고 있다. 그러나 LED 제품을 제조하기 위해서는 칩, 패키지, 모듈, 시스템으로 구성된 4단계의 복잡한 제조공정을 거쳐야 하므로 가격이 높은 단점이 있다. 이를 개선하기 위해서 패키지, 모듈, 시스템의 3단계의 공정을 하나로 통합한 hybrid LED package(HLP) 개념이 제시되었다. HLP는 LED chip을 PCB에 직접 실장한 뒤 초정밀 가공 및 성형 기술을 활용하여 일체형 광학패턴을 인가함으로써 공정을 단순화하면서도 광효율을 향상시킬 수 있다. 이에 본 연구에서는 다구찌 실험계획법을 사용하여 디스플레이에서 중요시되는 휘도를 높일 수 있는 일체형광학패턴 형상 최적화를 실시하였으며, 최적화된 일체형 광학패턴을 제조하기 위한 초정밀 가공 및 성형기술을 개발하였다. 최적화 결과 높이 25um, 꼭지각 90도의 음각형태의 사각피라미드 패턴이 최적형상으로 결정되었으며, 패턴이 없을 때와 비교하여 휘도가 약 32.3% 높아지는 것으로 나타났다. 이러한 일체형 광학패턴을 제품으로 구현하기 위하여 초정밀 절삭기술을 활용하여 마스터 금형을 제작하였다. 최종적으로 사출성형을 통해 일체형 광학패턴을 제작하게 되는데 이때 사출기 내부 공기흐름 및 진공도를 최적화함으로써 패턴 내부에 불필요한 기포가 발생하지 않도록 하는데 성공하였다. 이를 통해 생산성이 높은 사출성형으로 HLP 제품을 양산할 수 있는 가능성을 확인하였고, 추후에는 실제 제품을 제작하는 연구를 수행할 예정이다.

• Journal of the Korea Organic Resources Recycling Association
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• v.21 no.2
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• pp.63-70
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• 2013

Experiments in a pilot-scale hybrid multi-stage unit system (HMUS) combination of ATAD and EGSB followed by SBR process for pig slurry treatment were conducted to demonstrate the feasibility of using autothermal thermophilic aerobic digestion (ATAD) and expended granular sludge bed (EGSB) followed by sequencing batch reactor (SBR) system. Contaminants in pig slurry with high organic matter, nitrogen (N) and phosphorus (P) content were completely removed in the combined process. The highest removal rate for CODcr among contaminants in the feed pig slurry was attained by about 43.3% in ATAD unit process. Also TS removal rate of 96.5% was attained and the highest in the next coagulation unit process. The highest removal rate of CODcr under operating parameter conditions of OLR(organic loading rate), 3-6Kg $COD/m^3{\cdot}day$ and line velocity, 1.5-4m/h was earned at 3days of HRT. The disinfection of pathogens was effective at 50,000mg/L of TS in ATAD unit process. Biogas production per organic removal was $2.3{\sim}8.5m^3/kgTS{\cdot}d$ (average $5.2m^3/kgTS{\cdot}d$) in EGSB unit process. The average removal rates of CODcr 71.7%, TS 64.1%, TN 45.9%, and TP 50.4% were earned in the intermittent aeration SBR unit process.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.3 no.4
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• pp.303-307
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• 2002

A new product development procedure that uses a rapid prototyping and 3D CAD has been suggested. By applying this procedure to the development of an aroma diffuser, considerable amount of development time and cost were reduced. Moreover, by using 3D CAD from the early design stage, the number of trial and error can be reduced.

• Tribology and Lubricants
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• v.2 no.2
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• pp.59-64
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• 1986

쌍용정유는 윤활기유 생산을 위한 최신공정인 Gulf 특허의 수질첨가 개질공정을 채택, 일본, 카나다에 이에 세계에서 3번째로 건설된 공장으로서 국내 수요전량을 수입에만 의존해 오던 재래식 공정인 용제유출 방식의 윤활기유를 대신하여, 최고급 품질의 윤활기유를 국내에 안정적으로 공급할 수 있는 확고한 기반을 마련하고 지난 5년여 동안 국내수요에 적극 공급해오고 있다. 일반적으로 볼때 쌍용정유에서 생산.공급하고 있는 윤활기유는 국내 각 정유사등 윤활유배합(제조)회사에 공급되어 용제에 따라 첨가제를 배합하는등, 소포장 단계를 거쳐 일반수요자에게 판매되는데, 완제품 윤활유의 사용은 대략 65% 정도가 자동차에 쓰여지고 있으며 공장등 산업시설에 23%, 선박, 기타 용도로 12%정도의 사용분포를 보이고 있다. 산화, 열안정성은 기유의 생명 불순물제거 완벽, 색상 뛰어나 수질첨가 개질공정은 재래식 공정인 용제추출 방식과 어떤 차이점을 갖고, 제품의 특성이 어떤 차이를 나타내는가를 알아보기 위해서는 2가지 방식에 의한 제품의 장단점을 비교해보는 것이 바람직하다고 하겠다.

• Proceedings of the KAIS Fall Conference
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• 2002.05a
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• pp.67-69
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• 2002

주얼리 제품에서 마스터패턴 제작비는 최종제품의 20% 정도로 전체 주얼리제품 시장에서 매우 큰 비중을 차지한다. 기존 주얼리 제품을 제작하는 일반 공정인 ‘디자인 시안→상세도면 제작→1왁스형 제작→석고 플라스크 제작→은 마스터패턴의 제작→왁스패턴의 대량생산→정밀주조→최종제품’의 복잡한 단계를 ‘CAD 디자인 시안→쾌속조형기 듀라폼 음각몰드 제작→저융점 합금으로 마스터패턴 제작→정밀주조→최종제품’의 공정으로 단순화하면서도 대폭시간을 단축할 수 있는 신공정을 제안하였다. 주요공정인 selective laster sintering (SLS)형 쾌속조형기(rapid prototype: RP)를 이용해서 분해온도가 190℃인 듀라폼 분말로 미리 3D CAD로 설계한 직경 20mm의 구, 링 요소를 각각 상하형의 합체형 몰드와 일체형 몰드로 제작하였다. 제작된 몰드에 융점이 70℃인 Pb-Sn-Bi-Cd 저융점 합금을 주입하여 마스터패턴을 제조하였다. 완성된 마스터패턴은 목표형상에 비해 치수 변형율이 2% 이내로 우수하고 주입공정 및 후가공공정이 용이하여 주얼리용 마스터패턴으로 응용이 가능하였다.

• 한국생물공학회:학술대회논문집
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• 2005.04a
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• pp.355-359
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• 2005

Fractional precipitation is a simple, efficient method for pre-purifying paclitaxel from plant cell cultures. The storage temperature of factional precipitation was optimized in terms of the yield and purity of paclitaxel with a fixed methanol concentration in water (61.5%, v/v), paclitaxel content in the crude extract (0.5%, w/v), and storage time (3 days). The greatest yield $({\sim}84%)$ was obtained with storage at a constant temperature $(0^{\circ}C)$ for 3 days. Conversely, the highest purity $({\sim}79%)$ was obtained with stepwise reduction in temperature over 3 days. For a constant storage temperature, the maximum purity $({\sim}67%)$ was obtained at $0^{\circ}C$. There was little difference in the yield of paclitaxel between -20 and $12^{\circ}C$. This pre-purification process serves to minimize solvent usage, and the size and complexity of the high-performance liquid chromatography (HPLC) operation required for paclitaxel purification.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.18 no.5
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• pp.29-34
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• 2017

In this paper, we report a method of improving the productivity of lead wire fabricated through the rolling process by increasing its linear velocity. The most important point to consider when raising the linear velocity is that the original specifications must still be adhered to. In other words, the dimensional tolerance must be satisfied when increasing the linear velocity of the wire without causing cracks. However, if the linear velocity of the wire is increased, the degree of reduction must also be increased, which causes more damage to the wire and increases the load on its surface. Therefore, we studied a three step rolling process which can satisfy the specifications of the wire produced through the two step rolling process and improve the productivity. In this study, only the roll gap of the three-stage rolling roller is assumed to be a variable, while the other conditions are the same as the field conditions. In addition, through the PIANO (Process Integration, Design and Optimization) tool, the (optimum?) surface roughness and maximum stress are maintained.

• Journal of the Korean Society of Food Science and Nutrition
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• v.39 no.4
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• pp.637-642
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• 2010

Pre-treatment steps of fresh produce as Saengshik raw materials are followed by initial clean-up, dipping, primary washing, and cutting. Hypochlorous acid solution was applied in the dipping step to reduce natural microflora. Also, procedures were changed by cutting, dipping and then primary washing, and the efficacy of hypochlorus acid was evaluated. Potatoes, carrots, kales, and angelicas were submerged in water or 100 ppm of hypochlorous acid for 5 min. After initial clean-up, the aerobic plate counts of potatoes, carrots, kales and angelicas were 4.7, 5.3, 5.6, and 5.7 log CFU/g, respectively. When samples were submerged into water, it only reduced the population of natural microflora by 0.2 to 1.1 log CFU/g, whereas when treated with hypochlorous acid, it reduced the population by 0.5 to 2.8 log CFU/g. Reductions of natural microflora in green leafy vegetables were more highly achieved than bulbs such as potatoes and carrots. However, the numbers of natural microflora were increased after cutting step. To control the cross contamination at the cutting process, the process was changed as follows: initial clean-up, cutting, dipping in hypochlorous acid, and then primary washing. It showed effective reduction of the population by 2.3 to 3.2 log CFU/g. Hypochlorous acid solution could be useful as a sanitizer for surface washing of fresh vegetables.

• Applied Chemistry for Engineering
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• v.5 no.4
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• pp.681-697
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• 1994

The enzymatic hydrolysate of gelatin extracted from fish skin was fractionated and recycled through the membrane reactor according to the molecular weight for the purpose of using as functional material. In addition, the enzymatic hydrolysis conditions of gelatin, enzyme stability by membrane and mechanical shear, and effect on the long-term operational stability of the recycle membrane reactor were investigated. Using the pH-drop technique, Alcalase, pronase E and collagenase were identified as the most suitable enzymes for the hydrolysis of fish skin gelatin. The optimum hydrolysis conditions in the 1st-step membrane reactor(1st-SMR) by Alcalase were enzyme concentration 0.2mg/ml, substrate-to-enzyme ratio(S/E) 50(w/w), $50^{\circ}C$, pH 8.0, reaction volume 600ml and flow rate 6.14ml/min. In the 2nd-SMR by pronase E were enzyme concentration 0.3mg/ml, S/E 33(w/w), $50^{\circ}C$, pH 8.0, reaction volume 600ml and flow rate 6.14ml/min. In the case of 3rd-SMR, enzyme concentration 0.1mg/ml, S/E 100(w/w), $37^{\circ}C$, pH 7.5, reaction volume 600ml and flow rate 10ml/min. Decreased enzyme activities by mechanical shear and membrane were 30% and 15% in the 1st-SMR, were 14% and 5% in the 2nd-SMR, and 18% and 8% in the 3rd-SMR, respectively. Under the optimum conditions, the degree of hydrolysis in the 1st, 2nd and 3rd-SMR were 3.5%(Kjeldahl method, 87%), 3.1%(77%) and 2.7%(70%), respectively. The productivity of hydrolysate in the continuous three-step membrane reactor was 430mg per enzyme(mg) for 10 times of volume replacements.

• Journal of Korean Society of Industrial and Systems Engineering
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• v.32 no.3
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• pp.188-193
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• 2009

본 논문은 조립과 분리시스템이 혼합된 Fork-and-Join 시스템에서의 일정계획문제를 고려하고 있다. 최초 단계에서는 구성품단위로 분리가 발생하고 두 번째 단계에서는 부품생산단계에서 각 부품 또는 구성품이 서로 다른 설비와 경로를 통해 독립적으로 생산된 후 최종 조립단계로 이동하게 되고, 그곳에서 조립공정을 통해 제품으로 완성된다. 본 논문에서는 이러한 Fork-and-Join 시스템에서 최종완료시간(makespan)을 최소화 할 수 있는 발견적 해법을 제안하고 이 해법의 최악오차한계(worst-case error bound)가 2라는 것을 증명한다. 또한, 제안된 문제의 효과적인 3가지 하한값(lower bound)을 제시하고 다양한 수치실험을 통해 제안된 발견적 해법의 결과와 하한값과의 비교를 통해 제안된 해법이 성능이 우수함을 증명한다.