• Journal of the Korean Wood Science and Technology
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• v.27 no.2
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• pp.38-45
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• 1999

This study was to figure out proper Formaldehyde/Urea molar ratio of UF resin with satisfactory bonding strength of plywood and properties of particleboard. The six kinds of UF resins were manufactured with F/U molar ratio 1.0, 1.2, 1.4, 1.6, 1.8, and 2.0. The boards were made of three kinds of raw materials : Veneer, Sliver-Particle and Strand-Particle. Manufacturing condition of plywood : amount of mixing resin was 150g/$m^2$. The fourty secs/mm simple-pressing schedule in the pressure 10kgf/$m^2$ was applied for 480mm${\times}$700mm board at the temperature of $110^{\circ}C$ in a hot press. Manufacturing condition of particleboard : Target density was 0.65g/$cm^2$. The stepwise 9 minutes- multi-pressing schedule in the maximum pressure 40kgf/$cm^2$, the minimum pressure 15kgf/$cm^2$ was applied for $480mm{\times}634mm{\times}12mm$ board at the temperature of $150^{\circ}C$ in a hot press. The results are as follows : I. In bonding strength, plywood which was made by F/U molar ratio 1.2 showed the highest value. Other molar ratio resin also gave the satisfied value of KS standard, 7.5kgf/$cm^2$. 2. In internal bond strength of particleboard, Sliver-Particleboard(SLPB) and Strand-Particleboard(STPB) varied respectively from 5.9kgf/$cm^2$ to 4.8kgf/$cm^2$, from 6.7kgf/$cm^2$ to 5.4kgf/$cm^2$. SLPB with F/U=1.2 and STPB with F/U=1.6 had higher IB value. Also, both SLPB and STPB showed lower IB value in F/U molar ratio 2.0 and 1.0. 3. SLPB and STPB with six kinds of UF resin respectively satisfied bending strength of KS standard 150 Type(130kgf/$cm^2$) and 200 Type(180kgf/$cm^2$). Bending strength data for both of SLPB and STPB showed little or no loss from F/U=1.8 to F/U=1.2. Also, STPB was approximately two times higher than that of SLPB. Therefore, the raw material's shape had more effect on bending strength than the FlU molar ratio. 4. F/U=1.6 and 1.4 showed the lower thickness swelling in SLPB and STPB. All of STPBs satisfied thickness swelling of KS standard, under 12%.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2001.11a
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• pp.26-27
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• 2001

SNCR 기술을 이용한 NOx 저감은 반응온도 850～$1100^{\circ}C$에서 효과적이였으며, 몰비($NH_3$/NOx), $O_2$ 농도에 상당히 영향을 받고 있었다. 최적온도 $950^{\circ}C$, 몰비 1.5에서 약65%의 NOx 제거효율을 얻을 수 있으며, 온도구배가 없고 $O_2$ 농도가 2～4%로 낮아질 경우 더 높은 제거효율이 기대된다. SCR 기술에 의한 NOx 저감을 위해 $V_3$$O_{5}$/-$WO_3$/$TiO_2$ 상용촉매를 사용하였으며, 반응 온도는 200～$500^{\circ}C$ 범위로 확인되었으며, 약 84%의 NOx 제거효율이 몰비 1.5 에서 얻어졌다. $O_2$ 농도가 21%로 높아짐에 따라 상당히 효율이 떨어짐이 밝혀졌다. SNCR/SCR combined 시스템은 몰비=2.0, $T_{SNCR}$/=$850^{\circ}C$, $T_{SCR}$ /=$350^{\circ}C$ 반응조건에서는 약 93%의 NOx 저감효율을 보여주어 SNCR, SCR 단위기술보다 더 효과적이었다.

• Journal of the Korean Ceramic Society
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• v.37 no.11
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• pp.1105-1113
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• 2000

Bioglass 조성 중 45S5 (46.1SiO$_2$.24.4$Na_2$O.26.9CaO.2.6P$_2$O$_{5}$ : 몰비)를 기본 조성으로 하여 46P4 (46.2SiO$_2$.49.5CaO.4.3P$_2$O$_{5}$ : 몰비), 46SF (46.1SiO$_2$24.4$Na_2$O.16.1CaO.2.6P$_2$O$_{5}$.10.8CaF : 몰비) 그리고 55SF (55.1SiO$_2$.9.2$Na_2$O.27.8CaO.3.4P$_2$O$_{5}$.4.5CaF : 몰비)를 제조하여 tris-완충용액 및 유사 생체용액(simulated body fluid)에서 반응시킨 후 생체활성유리의 표면에 생성되는 아파타이트 결정형에 관하여 연구하였다. 45S5 유리를 tris-완충용액에 반응시켰을 경우 6시간 반응시부터 수산화 아파타이트가 생성되었으나 유사 생체용액에 반응시켰을 경우에는 24시간까지도 수산화 아파타이트 결정이 생성되지 못하고 비정질 상태의 칼슘 인산염만 형성되었다. tris-완충용액에 각 조성의 유리를 200시간 반응시킨 경우 불소를 함유하지 않은 유리에서는 잎사귀 모양의 수산화 아파타이트가, 불소를 함유한 유리에서는 구상의 플루오르 아파타이트가 형성되었다. 그러나 유사 생체용액에 각 조성의 유리를 200시간 반응시켰을 경우 불소를 함유하지 않은 유리에서는 누에고치형의 수산화 아파타이트가 형성되었고 불소를 함유한 유리에서는 무정형의 칼슘 인산염이 생성되었다.

• Korean Journal of Materials Research
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• v.9 no.9
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• pp.878-882
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• 1999

Structural properties of $Al_xGa_1-_xN$ epilayers grown on (0001) sapphire substrate by plasma induced molecular beam epitaxy are investigated in the range of AlN molar fraction from 0.16 to 0.76. The AlN molar fraction estimated by X-ray diffraction agrees well with that of Rutherford backscattering spectroscopy, showing a good linear relationship. The uniform Auger electron microscopy depth profile and linear dependence of average atomic concentration of all the constituents of AlGaN epilayers on AlN molar fraction imply that the epitaxial growth of $Al_xGa_1-_xN$ layers with variation of AlN molar fraction is well controlled without the compositional fluctuation in depth of the epilayer. It is observed by atomic force microscopy that the surface grain shape of $Al_xGa_1-_xN$ epilayer changes from roundish to coalesced one with increasing AlN molar fraction.

• Journal of the Korean Ceramic Society
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• v.36 no.3
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• pp.274-283
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• 1999

1.1-nm tobermorite의 수열합성에 SiO2원으로 zeolite광물을 출발물질로하여 소석회와 Ca(Si+Al)의 몰비 0.8~1.0로 150$^{\circ}$~23$0^{\circ}C$,8~48시간 동ㅇㄴ 포화증기압하에서 수열반응을 시킨 결과, 반응초기단계에서 tobermorite가 생성되었고, 고결정성 1.1-nm tobermorite의 최적합성조건은 0.8몰, 23$0^{\circ}C$, 48시간이었다. 출발물질중 Al의 존재로 tobermorite는 Ca/(Si+Al)몰비 0.8이 1.0보다 결정화가 급속히 이루어지고 있으나 Al를 함유치 않은 석영의 경우에는 Ca/Si 몰비 1.0이 0.8에서 보다 결정화가 빠르게 진행되었다 1.1-nm tobermorite는 $700^{\circ}C$에서 일주일간 가열처리하여도 저면간격이 변화하지 않는 열적거동이 이상형임을 보여주었다. 특히 출발물질중 Al의 존재는 1.1-nm tobermorite의 결정화와 안정화를 촉진시켜주며 Al이온이 tobermorite구조중의 Si이온과 동형치환을 한다.

• Proceedings of the Korean Nuclear Society Conference
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• 1998.05a
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• pp.369-373
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• 1998

증기발생기에서 부식에 의한 전열관 손상은 전열관과 관판사이의 틈새에서 대부분 발생되고 이 틈새에서의 수질환경에 좌우된다. 틈새에서는 과열도가 높아 미량의 불순물이 농축되면서 틈새수화학 (crevice chemistry)은 증기발생기 내부수 수화학과는 달라진다. 전열관 손상을 억제하기 위해서는 틈새수질을 적절히 제어하여야 하는데 이는 틈새수화학을 정확히 분석평가할 수 있는 기술을 기반으로 하여야 한다. .기존의 틈새수질을 계산하는 방법으로는 증기발생기 내부수에 비해 틈새에서 화학종들이 얼마나 농축되는지를 가정하는 농축도 (concentration factor) 방법이 있으나 가정에 의한 불확실성으로 인해 틈새수질을 정확히 해석할 수 없었다. 그러나 원전 증기발생기의 잠복불순물 방출시험 자료로부터 틈새수질을 보다 정확히 평가할 수 있는 새로운 개념의 몰비지수(molar ratio index) 방법이 최근 EPRI에서 제시되었고 EPRI 산하의 많은 발전소에서 적용중이다. 본 연구에서는 PWR 원전 증기발생기의 틈새수화학을 평가할 수 있는 기술을 개발하기 위해 잠복불순물 방출시험 자료로부터 틈새에서의 몰비지수를 계산할 수 있는 CRAP (CRevice-chemistry Analysis Program) 전산프로그램을 작성하였다 CRAP를 국내원전에 적용하여 증기발생기 및 그 틈새에서의 수화학을 평가하였다.

• Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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• 1999.11a
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• pp.331-334
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• 1999

본 논문에서는 경남산 고령토를 이용하여 고 실리카 제올라이트인 ZSM-5를 조제하는 방법에 대하여 검토한다. KOH를 알칼리 종으로 하여 ZSM-5를 합성하였다. 또한 수열합성을 위한 장치를 제작하여 회전속도 및 반응온도를 제어하였다. Si$_2$/Al$_2$O$_3$의 몰비와 $K_2$O/SiO$_2$의 몰비에 따른 결정생성물의 영역을 밝혔다. 또한, 생성된 ZSM-5를 SEM 및 X선 회절장치로 확인하였다. 또한, 반응시간에 따른 고체회수율 및 ZSM-5의 펴크강도를 관찰하였다. 또한, ZSM-5의 생성을 위한 반응시간을 알았고, ZSM-5가 소멸되기 시작하는 시간을 알았다. 또한 ZSM-5는 SiO$_2$/A1$_2$O$_3$의 몰비의 증가 및 반응시간의 증가에 의해 $\alpha$-Quartz로 전환되어짐을 알았다.

• Korean Chemical Engineering Research
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• v.58 no.1
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• pp.84-91
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• 2020

The efficiency of the synthetic magnesium silicate used in basic polyols and edible oil purification is evaluated by its purification ability and filtration rate and is affected by the particle size and surface area of magnesium silicate. In this study, it was investigated the change on the particle size of magnesium silicate was influenced by the reaction temperature, injection rate, injection order (Si, Mg) and Mg/Si reaction mole ratio. The synthesized magnesium silicate was compared and analyzed for the synthesis, grinding, and refining processes. In the synthesis process, the reaction temperature and feed rate did not affect the average particle size change of magnesium silicate, while the reaction molar ratio of Mg / Si and the order of injection acted as main factors for the change of average particle size. The average particle size of magnesium silicate increased by 8.7 ㎛ from 54.4 ㎛ to 63.1 ㎛ at Mg injection when Mg molar ratio increased from 0.125 to 0.500, and increased by about 4.8 ㎛ from 47.3 ㎛ to 52.1 ㎛ at Si injection. The average particle size according to the order of injection was 59.1 ㎛ for Mg injection and 48.4 ㎛ for Si injection and the difference was shown 10.7 ㎛, therefore the filtration rate was about 2 times faster under the condition of Mg injection. That is, as the particle size increases, the filtration time is shortened and washing filtration rate can be increased to improve the productivity of magnesium silicate. The cake form of separated magnesium silicate after filtration becomes a solid through drying process and is used as powdery adsorbent through the grinding process. As the physical strength of the dried magnesium silicate increased, the average particle size of the powder increased and it was confirmed that this strength was affected by the reaction molar ratio. As the reaction molar ratio of Mg / Si increased, the physical strength of magnesium silicate decreased and the average particle size after grinding decreased by about 40% compared to the average particle size after synthesis. This reduction of strength resulted in an improvement of the refining ability due to the decrease of the average particle size and the increase of the amount of fine particle after the pulverization, but it resulted in the decrease of the purification filtration rate. While the molar ratio of Mg/Si was increased from 0.125 to 0.5 at Mg injection, the refining ability increased about 1.3 times, but the purification filtration rate decreased about 1.5 times. Therefore, in order to improve the productivity of magnesium silicate, the reaction molar ratio of Mg / Si should be increased, but in order to increase the purification filtration rate of the polyol, the reaction molar ratio should be decreased. In the synthesis parameters of magnesium silicate, the order of injection and the reaction molar ratio of Mg / Si are important factors affecting the changes in average particle size after synthesis and the changes of particle size after grinding due to the changes of compressive strength, therefore the synthetic parameter is an important thing that determines productivity and refining capacity.

• Clean Technology
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• v.18 no.4
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• pp.404-409
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• 2012

In this study, the effects of mixing intensity and coagulant dosages on the characteristics of floc growth for phosphorus removal were investigated. The experiments were conducted under Al/P molar ratio of 1.0, 1.5 and 2.0; rapid mixing intensity with G value of 100, 300, and 500 $s^{-1}$. The characteristics of floc growth were measured by flocculation index (FSI) and the removal efficiencies of phosphorus by using different size filters. The removal efficiencies of soluble phosphorus increased as Al/P molar ratio and rapid mixing intensity increased. However, the highest removal efficiencies of T-P were observed at G value of 300 $s^{-1}$. When Al/P molar ratio was lower than 1.0, the value of FSI at G value of 500 $s^{-1}$ was the largest. However, when Al/P ratio was larger than 1.0, the value of FSI at G value 300 $s^{-1}$ was the largest. Effects of mixing intensity and Al/P molar ratio on coagulation for phosphorus removal of synthetic and real wastewater effluent were observed to be similar.

• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 2004.04a
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• pp.370-375
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• 2004

KMnO$_4$에 의한 TCE 용액의 분해에서 Headspace를 가진 반응 용기는 liquid sample을 headspce의 관측값으로 반응의 특성을 나타낼 수 없다. 이런 특성에 의해 in-situ KMnO$_4$ 이용은 TCE의 제거 효율에서 자연적인 휘발을 고려해야한다. 1:2.45 몰비에서 liquid sample의 결과 반감기는 약 80분이고 160분에 약 67%의 제거율을 보인다. 1:12.27 몰비의 경우 반감기는 10분이고 90분에 95%의 제거효율을 보인다.