• 한국생물공학회:학술대회논문집
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• 2000.04a
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• pp.239-242
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• 2000

Experimental studies on the effects of impeller to provide the microbial transglutaminase derived from Streptoverticillium mobaraense have been conducted. The optimal production medium was determined by latin-square design, and the effects of aeration and agitation were observed by using different sizes and shapes of impellers for the poduction of transglutaminase. The effects of pH and temperature were also evaluated for the production of transglutaminase in flasks. As a result, pH is more effective than temperature for both enzyme production and growth of the microorganism. The peak enzyme activity for transglutaminase in fermenter was 0.7 U/mL, but this was still well below the avereage enzyme activity, 1,3 U/mL, obtained in flask runs.

• Proceedings of the Korean Society of Precision Engineering Conference
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• 1997.10a
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• pp.163-166
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• 1997

Aluminium foam material is a highly porous material having complicated cellular structure defined by randomly distributed air pores in metallic matrix. this structure gives the aluminium a set of properties which cannot be achieved by any of conventional treatments. The properties of aluminium foam material significantly depend on its porosity, so that a desired profile of properties can be tailored by changing the foam density. Melting method is the one of foaming processes, which the production has long been considered difficult to realize becaues of such problems as the low foamability of molten metal, the varying size of. cellular structures, solidification shrinkage and so on. These problems, however, have gradually been solved by researchers and some manufacturers are now producing foamed aluminum by their own methods. Most of all, the parameters of solving problem in electric furnace were stirring temperature, stirring velocity, foaming temper:iture, and so on. But it has not considered about those in induction heating, foaming velocity and foaming temperature in semi-solid state yet. Therefore, this paper presents the effects on these parameter to control cell size, quantity and distribution.

• Journal of the Korea Organic Resources Recycling Association
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• v.11 no.1
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• pp.101-101
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• 2003

본 연구는 남은 음식물을 유산균을 이용하여 발효 사료화 하기 위해 실시하였다. 발효를 촉진시키기 위한 균주로는 Lactobacillus acidophilus를 사용하였고 최적의 발효조건을 갖는 공기 주입량을 알아보기 위해 시료의 발효 조건을 각각 달리 하였다. 시료는 교반하지 않고 공기주입 또한 없는 혐기적 조건의 것과 50rpm의 속도로 교반하면서 0.25v.v.m의 공기를 주입한군, 70rpm의 속도로 교반하면서 0.5v.v.m의 공기를 주입한 군으로 나누었다. 시료는 모두 $37^{\circ}C$로 유지하면서 48시간 발효 시키며 12시간 단위로 시료를 채취하였다. p.H와 유기산함량, 환원당함량과 유산균수를 측정하여 남은 음식물을 발효시키기 위한 최적의 공기 주입량을 알아보았다. 실험결과 50rpm 0.25v.v.m에서 가장 낮은 p.H를 보여주었고 유기산 함량과 환원당 함량은 70rpm 0.5v.v.m에서 가장 높은 함량을 보였다. 유산균은 50rpm 0.25v.v.m에서 가장 많은 증식되었음을 보여주어 적절한 공기의 주입이 남은 음식물의 발효를 촉진하는 것으로 보여진다.

• Transactions of the Korean Society of Mechanical Engineers A
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• v.33 no.7
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• pp.693-699
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• 2009

This paper shows mechanical properties and behaviors of macro- and micro-structures on friction stir welded specimen with 6061-T6 aluminum alloy plate. It apparently results in defect-free weld zone jointed at welding conditions like the traverse speed of 267mm/min, tool rotation speed of 2500rpm, pin inserted depth of 4.5mm and tilting angle of $2^{\circ}$ with tool dimensions such as tool pin diameter of 5mm, shoulder diameter of 15mm and pin length of 4.5mm. The tensile stress ${\sigma}_T=228MPa$ and the yield point ${\sigma}Y=141MPa$ are obtained at the condition of traverse speed of 267mm/min and tool rotation speed of 2500rpm. With the constant rotation speed, the higher traverse speed become, the higher tensile stress and yielding point become. Vickers hardness for welding zone profile were also presented.

• Proceedings of the International Microelectronics And Packaging Society Conference
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• 2001.11a
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• pp.185-188
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• 2001

본 연구는 알루미늄 기판 위에 징케이트 처리 시 생성되는 아연 입자들의 성장거동에 관하여 연구하였다. 알루미늄 기판 상에서 아연입자들은 기판 표면의 요철 꼭지점이나 모서리에서 먼저 생성되었고, (0001)면들이 적층되어 성장하였다. 또한 온도를 증가에 따른 성장속도를 증가시켜 징케이트 처리를 실시하였을 때 육방정계을 갖는 아연 입자의 경우 <1100> 결정방향으로 성장이 이루어져 불가사리 형태의 입자형태를 나타내었으며 초음파 교반에 의한 징케이트 처리를 하였을 경우 조밀하고 균일한 아연 막을 형성하였다.

• Proceedings of the Korean Society of Dyers and Finishers Conference
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• 2003.04a
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• pp.93-96
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• 2003

일반적으로 폴리우레탄계 마이크로캡슐은 양말단에 과량의 NCO기를 가지는 폴리우레탄 프리폴리머의 중합에 의한 것으로서, 이어서 수용액상에서 쇄연장제의 첨가에 의해 계면에서 완전한 폴리우레탄막을 중합하는 방법을 취하고 있다. 그러나 이러한 프리폴리머법에 의한 마이크로캡슐의 형성은 여러 가지 제조상의 문제점을 지니고 있다. Vanzo 등이 10$\mu\textrm{m}$이하의 작은 입자를 얻기 위해서는 비교적 고농도의 분산제와 높은 교반속도를 사용할 필요가 있었으며, 또한 그 입자크기분포의 제어가 어려웠다. (중략)

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2005.05a
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• pp.319-321
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• 2005

음이온계와 양이온계의 계면활성제를 사용하여 천연세정성분인 리모넨의 유화특성을 고찰한 결과 두 계열 모두 만족할 만한 결과를 나타내지 못하였고, 교반속도는 1500 rpm이상에서는 영향이 거의 없었으며, 유화온도는 상온에서도 가능할 것으로 판단된다. 유사한 구조와 물성을 가지는 리모넨과 ${\sigma}$-피넨을 비교한 결과 리모넨이 우수한 것으로 나타났으며 무독성인 IPA를 첨가한 경우가 첨가하지 않은 것보다 양호한 결과를 얻었다.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2009.05a
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• pp.123-124
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• 2009

염화물이 전기아연도금에 미치는 영향을 분석해본 결과 염화물의 양이 부족한 경우에는 도금이 원활하지 않았지만 교반속도를 충분히 주면 도금이 가능하였고, 염화칼륨의 양에 따라서 우선성장하는 면이 달랐으며 가격이 비싼 염화칼륨을 염화나트륨으로 대체 가능성이 확인되었다.

• 유체기계공업학회:학술대회논문집
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• 2005.12a
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• pp.425-430
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• 2005

This Study presents to be Agitator maintenance for Water and Wastewater treatment Plant. This procedures offers methods of Design Creteria and performance tests on mixing equipment. These tests may be conducted to determine process performance, mechanical reliability. or suitability of equipment for the intended use. The reasons for conducting performance tests can be varied, but the methods presented should be generally applicable to most situations.

• Microbiology and Biotechnology Letters
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• v.48 no.3
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• pp.344-357
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• 2020

Strain improvement and bioprocess development were undertaken to enhance hyaluronic acid(HA) production by Streptococcus zooepidemicus cells. Using a high-yielding mutant strain, statistical medium optimization was carried out in shake flask cultures, resulting in 52% increase in HA production (5.38 g/l) at the optimal medium composition relative to the parallel control cultures. For sufficient supply of dissolved oxygen (DO), which turned out to be crucial for enhanced production of HA, agitation system and speed were intensively investigated in 5 L bioreactor cultures. Increase in oxygen mass transfer coefficient (k_La) through increment of agitation speed (rpm) and 35% expansion of diameter of the newly-designed impellers showed significantly positive effects on HA production. By installing an expanded Rushton-turbine impeller for efficient break-down of sparged air, and an extended marine impeller above the Rushton-turbine impeller for efficient mixing of the air-born viscous fermentation broth, maximum amount of HA (9.79 g/l) was obtained at 450 rpm, 1.8 times higher level than that of the corresponding flask culture. Subsequently, the possibility of bioprocess scale-up to a 50 L bioreactor was investigated. Despite almost identical maximum HA production (9.11 vs 9.25 g/l), the average HA volumetric productivity (r_p) of the 50 L culture turned out only 74% compared to the corresponding 5 L culture during the exponential phase, possibly caused by shear damages imposed on the producing cells at the high stirring in the 50 L culture. The scale-up process could be successfully achieved if a scale-up criterion of constant oxygen mass transfer coefficient (k_La) is applied to the 50 L pilot-scale bioreactor system.