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35 VEGF 발현 증가에 의한 세포 증식 효과 및 재생 효과 -기전 및 signaling을 중심으로-
이기명 ( K. M. Lee ),박현진 ( H. J. Park ),김인혜 ( I. H. Kim ),오태영 ( T. Y. Oh ),안병옥 ( B. O. An ),김도현 ( D. H. Kim ),이은희 ( E. H. Lee ),황재철 ( J. C. Hwang ),유병무 ( B. M. Yoo ),김진홍 ( J. H. Kim ),조성원 ( S. W. Cho ),함 대한소화기학회 2002 대한소화기학회 추계학술대회 Vol.2002 No.-
허도행,이은희,정한섭,김우철,Hur, D.H.,Lee, E.H.,Chung, H.S.,Kim, U.C. Korean Nuclear Society 1994 Nuclear Engineering and Technology Vol.26 No.1
원전 증기발생기 2차측 제철 화학세정을 기존의 93$^{\circ}C$ 표준공정보다 고온인 1$25^{\circ}C$에서 검증시험을 수행하였다. 원전 증기발생기를 1$25^{\circ}C$에서 화학 세정한다는 가정아래 현장세정 조건을 결정하고 이를 다시 모사하여 3l 용량의 소형 검증시험 조건을 결정하였다. 1 gallon 용량의 316 스텐레스강 압력용기를 반응용기로 사용하는 화학세정 시험장치에서 검증시험을 수행하여 스러지 용해거동, 모재 부식률, 세정제 화학조성 변화거동 등을 측정하였다. 1$25^{\circ}C$ 검증시험 결과에서 93$^{\circ}C$ 표준공정보다 세정시간을 절반이하로 단축시키고도 더 효율적인 세정효과를 얻을 수 있을 뿐만이 아니라 2차측 모재의 부식률도 감소함을 확인할 수 있었다. 그러나 고온 세정공정은 아직 현장적용 경험이 없고, 별도의 외부순환 세정 장치를 이용하는 93$^{\circ}C$ 표준공정과는 달리 주냉각재의 잠열로 2차측을 가열하므로 세정이 완료될 때까지 주냉각 펌프를 계속 가동하여야 하는 단점이 있다. 가동중인 증기발생기에 대한 화학세정을 수행할 때 93$^{\circ}C$ 표준공정과 고온공정의 장 단점을 신중히 검토하여 최적공정을 적용하여야 할 것이다. A qualification test was performed for the iron removal chemical cleaning of the secondary side of nuclear steam generators at the selected temperature, 1$25^{\circ}C$, higher than the standard application temperature, 93$^{\circ}C$. The field cleaning condition for a nuclear unit was tested in a bench scale test loop including a SUS 316 stainless steel autoclave with one gallon capacity as a test vessel. The kinetics of sludge dissolution, corrosion of the secondary side materials and change of solvent chemistry were monitored. Test results indicated that more thorough cleaning was accomplished in less than half of the cleaning time required at 93$^{\circ}C$. And the total corrosions of the secondary side materials were found to be less than the values at 93$^{\circ}C$. While the solvent is recirculated and heated by an external chemical cleaning equipment for the conventional 93$^{\circ}C$ process, the secondary side is heated by the lateral heat of the primary coolant without the recirculation of the cleaning solution, and the solvent is mixed by vigorous boiling induced by periodic ventilation for the high temperature process. The requirement that the reactor coolant pumps should be running during the cleaning operation is the major disadvantage of the high temperature process which also should be considered when chemical cleaning is planned for steam generators under operation.
Conceptual Design of PLS-II Control System for PLS
J.C. Yoon(윤종철),J.W. Lee(이진원),E.H. Lee(이은희),H.G Ha(하기만),J.M. Kim(김재명),S.J. Park(박성주),K.R. Kim(김경렬) 대한전기학회 2009 대한전기학회 학술대회 논문집 Vol.2009 No.7
PLS(Pohang Light Source) will begin the PLS-Ⅱ project that has been funded by the KOREA Government in order to further upgrade the PLS which has operated since 1992. The control system of the PLS-II has distributed control architecture, with two layers of hierarchy; operator interface computer (OIC) layer and machine interface computer (MIC) layer. The OIC layer is based on SUN workstation with UNIX. A number of PC-based consoles allow to remotely operating the machine from the control room. PC-based consoles use the Linux or Windows operation system. Similar consoles in the experimental hall are used to control experiments. The MIC layer is directly interfaced to individual machine devices for low-level data acquisition and control. MIC layer is based on VMEbus standard with vxWorks real-time operating system. Executable application software modules are downloaded from host computers at the system start-up time. The MIC's and host computers are linked through Ethernet network. It should enable the use of hardware and software already developed for specific light source requirements. The core of the EPICS (Experimental Physics and Industrial Control System)[1] has been chosen as the basis for the control system software.
대규모 원단 도매 시장에서의 포름알데히드 노출에 관한 연구
최상준,백남원,김지현,이미선,황정희,정현희,이은희,최연기,양윤정,이태범,이경민,공정옥,이영미 서울대학교 보건대학원 2001 서울大學校 保健環境硏究所論叢 Vol.11 No.1
This study was conducted to assessment airborne formaldehyde concentration at dry-goods stores, 'G' market and additionally at the reconstructed lecture room in the university during November, 2001. 'NIOSH 2016' method, with 2,4-DNPH treated silica gel sampler and HPLC, was used for sampling and analysis of formaldehyde concentration. Because every merchant rejects to participate in study, volunteers, pretend to customer, were involved to monitor personal exposure level. The results are summarized as follows ; 1. The geometric mean(GM) and geometric standard deviation(GSD) of TWA concentrations from 'G' market were 0.037 ppm and 2.17 respectively. 2. The TWA concentrations of the personal samples from 'G' market ranged from 0.009 to 0.065 ppm and those of the area samples from '' market ranged from 0.06 to 0.071 ppm. 3. The TWA concentrations of the area samples from reconstructed lecture room ranged from 0.022 to 0.094 ppm. The TWA concentration from latest reconstructed lecture room was higher than that of older reconstructed lecture room. 4. All of samples except one were exceeding NIOSH TWA criteria, 0.016 ppm.