• Korean Journal of Soil Science and Fertilizer
• /
• v.1 no.1
• /
• pp.125-128
• /
• 1968

The effect of number of leaf after heading time on the growth of residual part and translocation of carbohydrates were investigated with water culture condition. Mutual shading and root rot were prevented. The results may be summerized as follows; 1. The ratio of ripened grain in the plot of no-leaf, flag leaf, two-leaf(flag and 2nd leaf) and three-leaf (flag, 2nd and 3rd leaf) was 38.8, 74.7, 83.9 and 87.0% respectively. The thousand grain weight was 21.3g, as the lowest value in no-leaf plot and was 28.7g in all other plots. 2. The accumulation of carbohydrate translocated in culm was increased by increment of leave-cutting, whereas the weight of culm was decreased. 3. It was suggested that healthy flag and 2nd leaf can keep the ratio of ripened grain around 80 percent.

• Proceedings of the Korean Institute of Surface Engineering Conference
• /
• 2011.05a
• /
• pp.79-79
• /
• 2011

water cavitation peening(WCP)은 water jet 과정으로 인한 cavitation이 발생할 때, 금속표면 cavitation 현상에 의해 재료표면의 잔류응력과 경도 등의 물성을 변화시키게 되며, 그로 인해 생긴 잔류 응력으로 재료의 내구성 및 수명을 향상시키는 기술이다. 최근에는 water jet을 이용한 장치들이 건설 분야, 일반기계분야, 컷팅 공정, 분쇄 등 다양한 분야에서도 사용되고있다. 그러나 water jet을 이용한 peening은 소개 된지 20여년이 경과했음에도 불구하고 연구 및 개발 내용은 shot peening에 비해 아직 초기 단계이다. water cavitation peening은 기존의 피닝 방법의 단점을 보완 할 뿐만 아니라 환경적인 측면에서도 그 가치가 크다. 아직은 다른 peening 기법 보다 잔류압축응력 부가 측면에서 그 효과가 떨어지지만, water cavitation peening은 열에 영향을 받는 영역이 생성되지 않으며, 기계의 표면 가공을 하는 동안 어떤 미세한 먼지도 생성하지 않아 친환경적이다. 또한 복잡한 외형을 가지는 부품 및 내면에 적용성이 뛰어나고, 표면 정밀도 저하가 낮다는 장점이 있다. 본 연구에서는 조류발전용 블레이드의 재료로 사용하려는 동합금에 대하여 증류수 내에서 water cavitation peening 시간, 거리, 파형 등의 변수를 적용하여 최적 조건을 찾고, 다양한 전기화학적 실험을 실시하였으며, water cavitation peening 부의 부식특성을 평가 하였다. ASTM-G32 규정에 의거하여 압전효과를 용한 진동발생 장치(RB 111-CE)를 이용하여 동합금 표면에 water cavitation peening을 실시하고, 실험 후 표면의 손상거동을 관찰하기 위하여 3D현미경 및 전자주사현미경(SEM)을 사용하였다. 물성치 변화를 확인하기 위하여 SHIMADZU사의 HVM-2 Model의 비커스 경도기를 이용하여 표면 경도값을 측정하였다. 전기화학실험은 각 3회 이상 실시하였으며, Tafel 분석결과로 부식전류밀도와 부식전위의 평균, 부식전위를 알 수 있었고, 음분극 실험결과, 용존산소 환원반응에 의한 농도분극에서 수소가스발생에 의한 활성화 분극으로 진행되는 변곡점을 확일 할 수 있었다.

• Journal of Korean Society of Environmental Engineers
• /
• v.37 no.4
• /
• pp.204-209
• /
• 2015

The effluent limit of nickel from electroplating wastewater has been strengthened from 5 mg/L to 3 mg/L from 2014. However, currently applied treatment process for nickel plating wastewater is unable to meet the effluent limit, most of the treatment concept conducted by treatment plant is dilution with other metal bearing wastewater. This can cause very significant impact to the environment of nickel contamination. With this connection, the feasibility test has been conducted with the use of electrolysis by using sacrificial electrodes. Experiments were conducted in synthetic and electroless nickel plating wastewater. Optimal condition of current density, pH were derived from the synthetic wastewater. It was found that the removal efficiency of nickel exceeded 94% at the operation condition of at pH 9 and the current density of $1{\sim}2mA/cm^2$. At this conditions, the iron sludge was generated very low amount. However, it was unsuccessful to meet the effluent limit by applying these treatment conditions to the real electroplating wastewater. This can be explained due to the matrix effect of other metals and anions contained real electroplating wastewater. From the result of further study, the optimal conditions for the real wastewater treatment were found out to be at pH 9, current density $6{\sim}7mA/cm^2$, for 5 minutes of operating time. At these conditions, 88% removal of nickel was achieved, which results the residual nickel concentration was below 3 mg/L.

• Journal of the Korean Electrochemical Society
• /
• v.18 no.1
• /
• pp.7-16
• /
• 2015

Effects of chemical composition ($Cu^{2+}$, $K_4P_2O_7$ and additive concentrations) of baths on properties of Cu thin films electrodeposited from pyrophosphate copper bath were investigated. Current efficiency was increased to be near 100% with increasing $Cu^{2+}$ concentrations from 0.02 to 0.3M. Decrease of current efficiency was observed in the range of 1.5~1.8M $K_4P_2O_7$ concentration, but current efficiency of about 100% was measured in the ranges of both 0.9~1.3M and 2.1~2.4M. The change of additive concentration did not influenced current efficiency. Residual stress of electrodeposited Cu thin films was measured to be about 20 MPa below 0.15 M $Cu^{2+}$ concentration and increased with the increase of it to 0.25 M. Maximum residual stress of 120MPa was observed at 0.25M $Cu^{2+}$ concentration. On the other hand, residual stress decreased from 80 to near 0 MPa as $K_4P_2O_7$ concentration varied from 0.9 to 2.4M and but The change of additive concentration did not affected on residual stress. $Cu^{2+}$ and $K_4P_2O_7$ concentrations significantly affect on surface morphology of electrodeposited Cu thin films, but additive concentration slightly affected. From XRD analysis, the microstructures of electrodeposited Cu thin film was affected from the changes of $Cu^{2+}$ and $K_4P_2O_7$ concentrations, but not from that of additive concentration. Strong preferred orientation of (111) peak was observed with increasing $Cu^{2+}$ and $K_4P_2O_7$ concentrations.

• Clean Technology
• /
• v.28 no.4
• /
• pp.309-315
• /
• 2022

Research was conducted to derive the optimal operation conditions and the optimal cathode for using a DSA electrode as an anode to minimize electrode consumption during the removal of nitrogen from wastewater by the electro-chemical method. Of the various electrodes tested as cathodes, brass was determined to be the optimal electrode. It had the highest NO₃-N removal rate and the lowest concentration of residual NH₃-N, a by-product when Cl is present in the solution. Investigating the effect of current density found that when the initial concentration of NO₃-N was 50 mg L^-1, the optimal current density was 15 mA cm^-2. In addition, current densities above 15 mA cm^-2 did not significantly affect the NO₃-N removal rate. The effect of electrolytes on removing NO₃-N and minimizing NH₃-N was investigated by using Na₂SO₄ and NaCl as electrolytes and varying the reaction times. When Na₂SO₄ and NaCl are mixed at a ratio of 1.0 g L^-1 to 0.5 g L^-1 and reacted for 90 min at a current density of 15 mA cm^-2 and an initial NO₃-N concentration of 50 mg L^-1, the removal rate of NO₃-N was about 48% and there was no residual NH₃-N. On the other hand, when using only 1.5 g L^-1 of NaCl as an electrolyte, the removal rate of NO₃-N was the highest at about 55% and there was no residual NH₃-N.

• Journal of the Korean Society for Environmental Technology
• /
• v.19 no.6
• /
• pp.556-562
• /
• 2018

Due to the enforcement of effluent water regulation the advance sewage treatment system is needed to retrofit and remodelling. In this case the most important issue is the effluent concentrations of TP and there are a lot of system to reduce its concentration. But biological treatment processes have many restrictions to enhance the removal efficiency of TP. In this study the efficient ECO operating condition to improve and retrofit biological sewage wastewater treatment system is as follow; 1) The treatment efficiency of BOD, TN and TP at the current density of $15mA/cm^2$ was higher than the treatment efficiency at $5mA/cm^2$ in the electrodes arranged with Al-SUS(Stainless Steel) regardless of the reaction time, The TP concentration was 0.1 mg/L or less. Especially, when the reaction time was maintained at 10 min, the TP concentration was 0.06 mg/L or less irrespective of the current density. 2) The change of TP concentration is not influenced by the change of current density and rather the concentration of treated water changes according to the reaction time. In the case of electro coagulation reaction, a few seconds to several minutes are required. However, the reaction time of electro coagulation and oxidation was studied to be more than 10 minutes. 3) As a result, it has been studied that the economical current density of the electro coagulation oxidation process for TN and TP treatment of domestic wastewater is $15mA/cm^2$ or less and the reaction time is 10 minutes.

• KEPCO Journal on Electric Power and Energy
• /
• v.2 no.3
• /
• pp.383-389
• /
• 2016

Kissing of sub-conductors due to magnetic forces has been investigated in a 154 kV bundled overhead transmission line. With increasing ampacity of the conductors and enlarging the distance between spacers, lager magnetic force was measured. When the phase ampacity was 2,000 amps and the distance between two adjacent spacers was 68 m, for instance, the conductors became unstable and vibrated with a frequency of several herts. Furthermore, when the ampacity was 2,250 amps and the distance between spacers was 136 m, the two sub-conductors were contacted. Analysing the magnetic forces with distance of spacers, the safe distance of spacers to avoid contact of sub-conductors was presented. The change of the safe distance is discussed due to various parameters, such as residual stresses and wind pressures, in the real transmission lines.

• Proceedings of the Korean Vacuum Society Conference
• /
• 2012.02a
• /
• pp.368-368
• /
• 2012

무기물 나노입자를 포함하는 유기물/무기물 나노복합체는 플렉시블 전자 소자에 적용이 가능하기 때문에 차세대 비휘발성 메모리 소자에 대한 응용연구가 활발히 진행되고 있다. 본 논문에서는 $CuInS_2$ (CIS)/ZnS 코어-쉘 나노 입자를 포함한 poly(N-vinylcarbazole) (PVK) 고분자 박막을 기억 매체로 사용하는 유기 쌍안정성 소자(organic bistable devices, OBD) 메모리 소자를 제작하고 전기적 성질에 대하여 관찰하고 전하 수송 메카니즘에 대하여 규명하였다. 화학적 방법으로 형성한 CIS/ZnS 코어-쉘 나노 입자와 PVK를 toluene 용매에 녹인 후 초음파 교반기를 사용하여 나노 복합 소재를 형성하였다. 하부 전극으로 indium-tin-oxide (ITO)가 증착되어 있는 유리 기판 위에 나노 복합 소재를 스핀코팅 방법으로 도포한 후 열을 가해 잔류 용매를 제거하였다. CIS/ZnS 코어-쉘 나노 입자가 분산되어 있는 PVK 나노 복합 소재로 구성된 박막위에 상부 전극으로 Al을 열증착하여 메모리 소자를 제작하였다. 전류-전압 (I-V) 측정 결과에서 저전압에서는 전도도가 낮은 OFF 상태를 유지하다 어느 특정 양의 전압에서 전도도가 갑자기 증가하여 높은 전도도의 ON 상태로 전이되는 쌍안정성이 관찰되었다. 전류의 ON/OFF 비율은 약 $10^3$이며 역방향 바이어스를 가해주었을 때 특정 음의 전압에서 전도도가 ON 상태에서 OFF 상태로 전환되는 전형적인 OBD 메모리 소자의 I-V 특성을 나타났다. 메모리 전하 수송 메커니즘 분석 결과 쓰기 과정은 thermionic emission (TE), space-charge-limited-current (SCLS) 모델과 지우기 과정은 Fowler-Nordheim (FN) 터널링 모델로 설명이 되었다. 제작된 소자에 대해 기억 시간 측정 결과는 ON과 OFF 상태의 전류가 장시간에도 변화가 거의 없는 소자의 안정성을 보여주었다. 이 실험 결과는 CIS/ZnS 코어-쉘 나노 입자가 분산되어 있는 PVK 나노 복합 소재를 사용하여 안정성을 가진 OBD 메모리 소자를 제작할 수 있음을 보여주고 있다.

• Korean Journal of Materials Research
• /
• v.8 no.10
• /
• pp.945-949
• /
• 1998

Ta(OC2H5)5와 NH3를 이용하여 Cycle-CVD법으로 산화탄탈륨 막을 증착하였다. Cycle-CVD법에서는 Ta(OC2H5)5와 NH3사이에 불활성 기체를 주입한다. 하나의 cycle은 Ta(OC2H5)5주입, Ar주입, NH3 주입, Ar 주입의 네 단계로 이루어진다. Cycle-CVD법으로 산화탄탈륨 막을 증착할 때, 온도 $250-280^{\circ}C$에서 박막의 증착 기구는 원자층 증착(Atomic Layer Deposition:ALD)이었다. $265^{\circ}C$에서 Ta(OC2H5)5:Ar:NH3:Ar:NH3:Ar의 한 cycle에서 각 단계의 주입 시간을 1-60초:5초:5초:5초로 Ta(OC2H5)5 주입 시간을 변화시키면서 산화탄탈륨 막을 Cycle-CVD법으로 증착하였다. Ta(OC2H5)5주입시간이 증가하여도 cycle 당 두께가 $1.5\AA$/cycle로 일정하였다. $265^{\circ}C$에서 증착된 박막의 누설 전류는 2MV/cm에서 2x10-2A/$\textrm{cm}^2$이었고 열처리후의 산화탄탈륨 막의 누설 전류값은 $10-4A\textrm{cm}^2$ 이하고 감소하였다. 증착한 산화탄탈륨 막의 성분을 Auger 전자 분광법으로 분석하였다. 2$65^{\circ}C$에서 증착한 막의 성분은 탄탈륨 33at%, 산소 50at%, 탄소 5at%, 질소 12at% 이었으며 90$0^{\circ}C$, O2300torr에서 10분 동안 열처리한 박막은 탄탈륨 33at%, 산소 60wt%, 탄소 4at%, 질소 3at%이었다. 박막의 열처리 온도가 높을수록 불순물인 탄소와 질소의 박막 내 잔류량이 감소하였다. 열처리 후의 박막은 O/Ta 화학정량비가 증가하였으며 Ta의 4f7/5와 4f 5/2의 결합 강도가 열처리 전 박막보다 증가하였다. 열처리 후 누설 전류가 감소하는 것은 불순물 감소와 화학정량비 개선 및 Ta-O 결합 강도의증가에 의한 것으로 생각된다.

• Resources Recycling
• /
• v.10 no.4
• /
• pp.18-23
• /
• 2001

Air pollutants, phenol was generated in case of thermal regeneration of used activated carbon loaded with phenol and because of this problem, removal process of phenol were studied. Electrolytic oxidation of samples, used S.company granular activated carbon (WS-GAC), used C.company granular activated carbon (WC-GAC) and used L.company granular activated carbon (WL-GAC) loaded with phenol carried out by potentiostatic method in this study. In case of experiment was to come into operation in condition of samples containing 100 mg/g phenol, supporting electrolyte was 1.0% sodium chloride solution, Ti-Ir (10$\times$10$\textrm{cm}^2$) electrode and electrode distance was 2 cm, current density was $1.25 A/dm^2$, Obtained from the results of electrolytic oxidation experiments were not detected residual phenol. And then we knew about reaction time of electrolytic oxidation, current density, concentration of supporting electrolyte and electrode and electrode distance were 60 minutes, 1.25 A/dm$^2$, 1.0%, 2 cm.