• 대한소아치과학회지
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• 제27권2호
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• pp.370-378
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• 2000

심미성 수복재로서 임상에서 널리 사용되는 복합레진은 구강내에서 장기간 유지되도록 하기 위하여 그 물성을 향상시킬 필요가 있다. 복합레진의 단점 중 하나로 낮은 마모저항성을 들수 있으며, 이와 관련된 하나의 인자로 수복물의 표면하 분해(subsurface degradation)가 고려되고 있다. 본 연구에서는 알카리성 용액(0.1N NaOH)에 현재 임상에서 많이 이용되는 Clearfil APX (CL, Kuraray). Heliomolar (H,Vivadent), Surefil (S, Dentsply), Tetric Ceram (TC, Vivadent), TPH (Dentsply), Z100 (3M)의 6종의 복합레진을 보관하였을 때 각 제품의 분해저항성을 평가하고자 하였다. 각 제품당 3개의 시편을 제작하여 무게측정을 한 후 0.1N NaOH용액에 저장하여 $60^{\circ}C$에서 보관하였다. 2주후 제거하여 HCl로 중화, 세척 후 $60^{\circ}C$에서 건조하였다. 무게손실, 분해층 깊이, Si 농도등을 기준으로 분해저항성을 평가하여 다음과 같은 결과를 얻었다. 1. 각 제품의 무게손실량은 $0.45\sim3.64%$ 까지 다양하며 Z100, TC, H, S, CL, TPH 순으로 많았다. 2. 각 제품의 표면하 분해층 깊이는 제품마다 다양하여, $10.85\sim73.38{\mu}m$의 범위였고, H, Z100, S, TC, TPH, CL 순으로 깊었다. 3. 각 제품으로부터 용출된 Si 양은 Z100군 2060ppm으로 가장 많고, H, TPH, CL, TC, S순으로 많았다. 4. 무게손실량과 표면하 분해층 깊이사이에 높은 상관관계를 보였다. (r=0.81, p,0.05) 5. 주사전자현미경하 관찰시 NaOH 용액에 보관한 후 레진기질과 필러사이의 결합의 파괴를 관찰할 수 있었다.

• Environmental Engineering Research
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• 제12권1호
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• pp.1-7
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• 2007

Most of the herb residue producing from oriental medical clinics(OMC) and hospitals(OMH) is wasted in Korea. To develop of adsorbent for removing heavy metal from wastewater, the various pre-treatment methods of the herb residue were evaluated by potentiometric titration, Freundlich isotherm adsorption test and the kinetic adsorption test. The herb residue was pre-treated for increasing the adsorption capacity by cleaning with distilled water, 0.1 N HCl and 0.1 N NaOH and by heating at $370^{\circ}C$ for 30 min. It showed a typical weak acid-weak base titration curve and a short pH break like commercial activated carbon during photentiometric titration of pre-treated herb residue. The log-log plots in the Freundlich isotherm test were linear on the herb residue pre-treated with NaOH or HCl like commercial activated carbon. The adsorption capacity(qe) in the Freundlich isotherm test for $Cr^{6+}$ was 1.5 times higher in the pre-treated herb residue with HCl than in activated carbon. On the other hand the herb residue pre-treated with NaOH showed the good adsorption capacities for $Pb^{2+}$, $Cu^{2+}$ and $Cd^{2+}$ even though those adsorption capacities were lower than that of activated carbon. In kinetic test, most of heavy metals removed within the first 10 min of contact and then approached to equilibrium with increasing contact time. The removal rate of heavy metals increased with an increase of the amount of adsorbent. Likewise, the removal rates of heavy metals were higher in the herb residue pre-treated with NaOH than in that pre-treated with HCl. The adsorption preference of herb residues pre-treated with NaOH or HCl was $Pb^{2+}>Cu^{2+}$ or $Cd^{2+}>Cr^{6+}$ in the order. Conclusively, the herb residue can be used as an alternative adsorbent for the removal of heavy metals depending on pr-treatment methods.

• 한국염색가공학회지
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• 제11권2호
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• pp.55-63
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• 1999

The purpose of this study was to investigate the purification of chitin and chitosan for textile finishing agent from crab shell. Weight loss rate(removing Ca and protein), degree of deacetylation, solubility and MIC(Minimum growth inhibitory concentration) value of chitosan and molecular weight of the treated crab shell were measured. The results of this study were as follows : 1) Weight loss rate(removing Ca) of crab shell treated with HCI increased with the concentration of HCI and treatment time, but it became constant over 60 min. of treatment time. 2) Weight loss rate(removing protein) of crab shell treated with NaOH(0.5N∼2N) increased with the concentration of NaOH and treatment temperature and time, but it became constant above loot of temperature and over 200 min. of treatment time. 3) Degree of deacetylation of chitin treated with NaOH increased with the concentration of NaOH(40∼60％), but molecular weight decreased and thus MIC value increased. 4) Concentration of acetic acid should be above 0.3％ to dissolve chitosan easily. Solubility for chitosan was the highest with formic acid, and the next was acetic acid, hydrochloric acid, lactic acid and sulfuric acid in order.

• 자원환경지질
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• 제24권3호
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• pp.219-226
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• 1991

High quality quartz crystals are grown in 0.5N NaOH + LiOH solution on the seed crystal at $370-395^{\circ}C$ and $1200-1300kg/cm^2$ condition. Growth rates are determined by the crystal thickness grown on the seed crystals with Z(0001) and X($11\bar{2}0$) direction. Relatively high growth rate of Z(0001) direction gradually changes as the temperaure difference (${\Delta}$ Ti) between growth and dissolution zones from 25 to $10^{\circ}C$. The X axis direction is affeced by ${\Delta}$ Ti, and +X($11\bar{2}0$) direction shows a high growth rate than -X($\bar{1}\bar{1}20$) direction. According to the variation with kinds of solutions used, the crystal growth that in NaOH solution is found to be slower than that in $Na_2CO_3$ solution. However, for the case in the NaOH solution mixed with LiOH, it shows a favorable growth rate in terms of grown crystal quality.

• 한국식품영양과학회지
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• 제43권9호
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• pp.1462-1466
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• 2014

알칼리 추출법을 이용하여 쌀귀리로부터 단백질을 추출하고 추출수율을 최적화하기 위한 알칼리 농도 조건 및 침전 pH 조건을 반응표면분석을 통해 검토하였다. 추출수율은 추출용매인 알칼리 농도가 증가할수록 그리고 침전 pH 4.9 부근에서 높은 경향을 보였으며, 알칼리 농도가 침전 pH에 비하여 보다 큰 영향을 미치는 것으로 나타났다. 알칼리 추출 공정으로 얻어진 귀리 단백질 농축물의 질소용해지수는 등전점 부근인 pH 5에서 최소값을 나타내었고, pH 3 이하, pH 7 이상에서는 급격히 증가하였다. 알칼리 추출 공정의 최적화를 위한 회귀분석 결과, 알칼리 농도 0.06 N, 침전 pH 4.7에서 최대 수율 85.89%로 예측되었으며 예측모델식과 실제 측정값을 비교하였을 때 유의적인 차이가 크게 나타나지 않아 설계된 실험모델식은 적합한 것으로 나타났다. 따라서 기존의 연구들은 알칼리 추출법을 이용한 귀리 단백질 추출 시 알칼리 농도와 침전 pH가 각기 다름을 보였지만, 본 연구를 통하여 귀리 단백질 농축물 제조를 위한 알칼리 추출 공정의 최적 조건은 알칼리 농도 0.06 N, 침전 pH 4.7인 것으로 확인되었다.

• 한국식품영양학회지
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• 제26권3호
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• pp.601-607
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• 2013

알칼리 가수분해에 따른 보리 ${\beta}$-glucan의 이화학적 특성변화를 살펴보기 위하여 새쌀보리, 새찰쌀보리 및 흰찰쌀보리에 0.2~1.0 N NaOH를 처리하였으며, 총 및 수용성 ${\beta}$-glucan의 함량 및 순도, 수용성 ${\beta}$-glcuan의 분자량, 점도 및 재용해율을 살펴보았다. 3품종 보리의 총 ${\beta}$-glucan 함량은 7.77~8.40% 범위이었으며, 알칼리 가수분해 농도가 증가함에 따라 6.89~7.54% 범위로 감소하였다. 수용성 ${\beta}$-glucan의 함량은 무처리의 4.16~4.80% 범위에서 알칼리 가수분해 농도가 증가함에 따라 4.30~4.82% 범위로 유의적인 차이가 없었다. 수용성 ${\beta}$-glucan의 순도는 3품종 모두 30.91~35.79% 범위이었으나, 알칼리 가수분해에 의해 74.02~81.41%까지 증가하였다. 분자량은 메성보리보다 찰성보리가 더 컸으며, 알칼리 가수분해 농도가 증가함에 따라서 크게 감소하였다. ${\beta}$-Glucan 수용액의 점도는 알칼리 가수분해 농도가 증가함에 따라 감소하였으며, 메성보리보다 찰성보리가 높았고, 흰찰쌀보리보다 새찰쌀보리가 높았다. 재용해율은 무처리의 50~55% 범위에서 알칼리 가수분해 농도가 증가함에 따라 증가하여 1.0 N NaOH 처리구에서 80.00~87.66% 범위로 증가하였다.

• 한국식품영양과학회지
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• 제24권1호
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• pp.105-113
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• 1995

게 가공 폐기물을 부가가치가 높은 키틴 자원으로 활용코자, 이들 폐기물로 부터 키틴을 효율적으로 분리할 수 있는 조건을 설정하고 이로 부터 제조된 키틴의 물리화학적 성질을 조사하였다. 탈회분은 원료중량의 15배에 해당하는 1N HCI로 실온에서 30분간 교반함으로서, 탈단백질은 탈휘분된 시료에 원료중량의 15배에 해당하는 5% NaOH용액으로 $65^{\circ}C$에서 1시간 동안 교반함으로서 가장 효율적으로 이루어졌다. 탈색소는 원료중량의 10배에 해당하는 0.32% NaOCI로 3분간 처리시 가장 바람직하였다. 침지에 의한 탈회분 및 탈단백질은 교반에 비해 추출 효율성이 낮고 장시간을 요하였다. 백색의 최종 키틴제품은 질소함량이 6.45%, 회분은 0.15%이었으며, 5% lithium chloride를 함유한 N,N-dimethylacetamide-용액(DMAc-5% LiCI)에서 0.1% 키틴의 점도는 12.8cP를 나타냈다. 또한 DMAc-5% LiCI에서 키틴의 용해도는 58.4%를 나타냈으며, bulk density는 입자 크기가 20~40mesh 일때 0.27g/ml, 100mesh 이하일 때는 0.43g/ml를 나타내었다. 입자 크기에 따른 키틴의 질소 및 회분함량에는 별 차이가 없었으며, 키틴의 수율은 입자의 크기가 클수록 증가하는 경향이었다. 키틴 제조시 탈색공정은 키틴의 점도를 감소시켰으며 용해도에는 별 영향이 없었다.

• 대한화학회지
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• 제17권3호
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• pp.224-228
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• 1973

Rhodotorula sp.로 $C_{12}{\sim}C_{14}$의 n-alkane 混合物에서 無機系 窒素源인 窒酸鹽과 암모늄鹽 그리고 有機係 窒素源인 urea들의 그 化學形의 差異에 따라 醱酵時間과 收率面에서 어떻게 影響을 미치는가와 窒酸나트륨으로서 炭素源의 炭素에 對한 窒素의 添加比率의 差異에 따라 미치는 影響 等을 調査해 보았다. 그 結果 最高生長에 達하는데 要하는 時間은 窒酸나트륨과 黃酸암모늄이 各各 40 hrs.와 45hrs인데 比해 urea는 이들보다 훨씬 긴 66hrs.가 걸렸고 收率面에 있어서는 0.1N-NaOH의 消費量으로서 兩無機鹽이 各各 0.36과 0.38ml인데 比해 urea는 0.78ml나 되었다. Medium 中의 窒素對 炭素 比率의 影響은 medium에 加하는 n-alkane 混合物을 1%(vol.)에서 窒酸나트륨으로서 N/C가 0.2일 때가 가장 優秀한 結果를 나타내었고 대개 炭素에 對한 窒素의 比率이 낮을 때보다는 높은 때가 더 좋은 生長效果를 보였다.

• Journal of Periodontal and Implant Science
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• 제30권1호
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• pp.187-203
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• 2000

The precipitation of calcium phosphate on implant surface has been known to accelerate osseointegration and to enhance osseous adaptation. The present study was performed to examine whether the precipitation of calcium phosphate on Ti-6Al-4V alloy could be affected by the immersion in NaOH solution and heat treatment. Ti-6Al-4V alloy plates of $15{\times}3.5{\times}1mm$ in dimension were polished sequentially from #240 to #2,000 emery paper and one surface of each specimen was additionally polished with $0.1{\mu}m$ alumina paste. Polished specimens were soaked in various concentrations of NaOH solution(0.1, 1.0, 3.0, 5.0, 7.0, 10.0 M) at $60^{\circ}C$ for 24 hours for alkali treatment, and 5.0 M NaOH treated specimens were heated for 1 hour at each temperature of 400, 500, 600, 700, $800^{\circ}C$. After the alkali and heat treatments, specimens were soaked in the Hank's solution with pH 7.4 at $36.5^{\circ}C$ for 30days.The surface ingredient change of Ti-6Al-4V alloy was evaluated by thin-film X-ray diffractometer(TF-XRD) and the surface microstructure was observed by scanning electron microscope(SEM), and the elements of surface were analyzed by X-ray photoelectron spectroscopy(XPS). The results were obtained as follows ; 1. The precipitation of calcium phosphate on Ti-6Al-4V alloy was accelerated by the immersion in NaOH solution and heat treatment. 2. In Alkali treatment for the precipitation of calcium phosphate on Ti-6Al-4V alloy, the optimal concentration of NaOH solution was 5.0 M. 3. In heat treatment after alkali treatment in 5.0 M NaOH solution, the crystal formation on alloy surface was enhanced by increasing temperature. In heat treated alloys at $600^{\circ}C$, latticed structure and prominences of calcium phosphate layer were most dense. On heat treated alloy surface at the higher temperature(${\geq}700^{\circ}C$), main crystal form was titanium oxide rather than apatite. The above results suggested that the precipitation of calcium phosphate on the surface of Ti-6Al-4V alloy could be induced by alkali treatment in 5.0 M-NaOH solution and by heat treatment at $600^{\circ}C$.

• 환경위생공학
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• 제15권1호
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• pp.62-68
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• 2000

This study was investigated to the recovery of alumina from the first calcined waste pottery using alkaline sintering. This study was based on calcination result of a commercial ${\alpha}-Al2_O_3$ with NaOH powder. $NaAlO_2$ was formed by calcination of ${\alpha}-Al_2O_3$ with NaOH and conversion of $NaAlO_2$ from ${\alpha}-Al_2O_3$ was 91.4% at calcination condition ; weight ritio of $NaOH/{\alpha}-Al2_O_3$ 1.5, $800^{\circ}C$, and 90min. The first calcined waste porrery from the manufacturing Procedure of H Ltd. was grinded to 170/270mesh by a ball mill and calcined over $500^{\circ}C$ with NaOH powder. The calcined sample was dissolved in $25^{\circ}C$ water and sodiumaluminosilicate solid was formed. After filtration, the contained aluminum was leached out by dissolving sodiumaluminosilicate solid in 1N HCl. We estimated the efficiency of Al extraction from waste pottery by ICP analysis and NaOH was added to the filtrate and then aluminum compound was precipitated with $Al(OH)_3$ and recovered. The investigation was carried out with the variables ; the calcination temperature($500-900^{\circ}C$), the calcination time(30~90min), and the weight ratio of NaOH/waste pottery(0.5~1.5). The treatment efficiency of the waste pottery and the recovery of Al as 97.9%, 91.9% were obtained under the optimum conditions as followed ; the weight ratio of NaOH/waste pottery was 1.5 and the calcination conditions were $900^{\circ}C$ and 60min.