• Journal of the Korean Applied Science and Technology
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• v.36 no.1
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• pp.355-361
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• 2019

The red pigment extracted from Serratia marcescens 2354 (ATCC 25419) was prodigiosin (PG), which was dissolved in methanol and measured for ultraviolet and visible light absorption spectra. It was the typical absorption spectrum of PG in an acid solution with ${\lambda}_{max}=537nm$. When the concentration of PG was increased from $1.0{\times}10-5M$ to $9.0{\times}10-5M$ in the methanol solution, the absorption intensity at 537 nm was increased, the absorption intensity at 467 nm was decreased, and the isosbestic point at 500 nm was observed. This phenomenon can be regarded as a result of reversible acid-base equilibrium reaction considering 537 nm and 467 nm of PG absorption band in acid and base solution respectively and isosbestic point of 500 nm. On the other hand, when the concentration of PG was reduced from $6.0{\times}10-4$ to $1.0{\times}10-4M$ in acetic acid buffer solution at pH 4.75, a new absorption band with ${\lambda}$ max at 500 nm appeared. This absorption band appears only in the aqueous solution of pH 4.75 and does not appear in the pure methanol solution of the same pH. This is due to the conversion of the PG molecule from the ${\alpha}$-isomer to the ${\beta}$-isomer by $H_2O$. In other words, it was confirmed that the color change of the PG can be caused by the concentration of the solution and the characteristics of the solvent.

• Journal of the Korean Society of Safety
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• v.7 no.2
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• pp.63-70
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• 1992

The aim of this research is to obtain a basic quantitative understanding of the effect of a noncondensable gas on the absorption of water vapor by a $H_2O$ / LiBr combination with n-octanol as the surfactant. Nonflowing aqueous solutions of LiBr (40,45,50 mass％) were exposed to saturated water vapor following the addition of an n-octanol sufactant (0.01 and 0.6 mass％). A small amount of a noncondensable gas (air) was allowed into the absorber (0.03 volume％) and its effect was analyzed by measuring the amount of water vapor absorbed. This study will aid to predict the performance of heat pump and safety operating condition when the noncondensable gas is not allowed in the absorber The results indicate that, in the presence of small amounts of a noncondensable gas, vapor absorption enhancement ratios are less than half o( those obtained under the same experimental conditions when a noncondensable gas is not present (1). The presence of a noncondensable gas causes the partial vapor pressure of air to increase at the vapor / liquid interface, which results in an instability of vapor absorption rate nd. hence, in an inhibition of interfacial disturbance.

• Korean Journal of Materials Research
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• v.6 no.2
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• pp.188-196
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• 1996

LiOH 용액에서 핵연료피복관용 Zr합금의 부식이 가속되는 현상을 규명하기 위하여 autoclave를 이용하여 순수물, 다른 농도의 Li 용액 및 여러 가지 알카리 수산화물 조건에서 부식시험을 실시하였다. LiOH 용액에서 부식이 가속되는 현상은 용액 내에 Li 농도가 2.2ppm 이상에서부터 일어나기 시작하며 30ppm 이상에서는 급격한 가속 현상이 일어난다. 부식반응 동안에 발생되는 수소 흡수현상은 220ppm Li에서는 물에 비해 약 2배의 높은 수소흡수율을 나타내며 산화막은 주로 수소화물이 모여 있는 지역에서 우선적으로 성장한다. Li가속 부식기구와 관련하여 본 연구 결과는 지금까지 다른 연구자들이 제안한 부식 기구들과는 일치하지 않았다. LiOH 용액 내에서는 수소흡수와 수소화물 형성이 가속되고 이로 인해 산화막의 성질이 비보호성의 산화막으로 변함으로서 부식은 가속된다는 새로운 모델을 제시하였다.

• Journal of the Korean Chemical Society
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• v.27 no.1
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• pp.18-23
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• 1983

To understand the abnormal absorption behavior of rare earths in cation exchange resins, the absorption for Ce(III), Tb(III) and $Cl^-$ ions in Dowex 50W-X2 have been investigated by spectrophotometry in the concentration range of $1{\sim}12$ M HCI and $HCl-HClO_4$ mixed solutions. The amount of $Cl^-$ ion absorbed shows that the ratio of amount of $Cl^-$ ions to that of rare earths does not exceed 10% in the concentration range of $6{\sim}8M$ HCl and decreased gradually to 3% at 2M HCl and 6% at 12M HCl. The ratio is further decreased with the fraction of $HClO_4$ in $HCl-HClO_4$ mixed solutions and the decrease is presumably due to the weak tendency to form a complex between rare earths and $Cl^-$ ions in a cation exchange resin. The effect of $ClO_4^-$ is expected to play a more important role than that of $Cl^-$ ions in the large absorption of rare earths.

• Applied Chemistry for Engineering
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• v.21 no.1
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• pp.71-75
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• 2010

The efficient performance of absorber is of great importance for the absorption heat pump cycle. The experimental study of absorber with spiral tube of tangential feeding of liquid phase has been investigated using methanol-glycerine as a working fluid. The effect of change in absorber operating conditions was analyzed to improve the performance. The increase in solution flow rate and cooling flow rate positively affects the absorber performance while an increse in the solution concentration negatively affects the absorber performance. The results showed that mass absorption flux was in the range of $0.2{\sim}0.6kgm^{-2}sec^{-1}$, the solution heat transfer coefficient between 1.6 and $4.2kwm^{-2}K^{-1}$, the absorber thermal load from 0.9 to 1.5kw and the mass transfer coefficient from 0.9 to 1.7 m/sec.

• Clean Technology
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• v.7 no.4
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• pp.273-280
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• 2001

An absorber is a major component in the absorption refrigeration systems and its performance greatly affects the overall system performance. In this study, experimental analyses on heat transfer characteristics for removal of absorption heat in ammonia-water bubble mode absorber were performed. Heat transfer coefficients were estimated as the variations of input gas flow rate, solution flow rate, temperature, concentration, absorber diameter and height, and input flow direction. The increase of gas and solution flow rate affects positively in heat transfer. However, the increase of solution temperature and concentration affects negatively. Moreover, under the same Reynolds Numbers, countercurrent flow is superior to cocurrent flow in heat transfer performance. In addition, from these experimental data, empirical correlations which can explain easily the characteristics of heat transfer are derived.

• Journal of the Korean Chemical Society
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• v.33 no.2
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• pp.203-207
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• 1989

The methyl red stock solution was added to sample solution and the absorbance values of this solution were measured at the maximum absorption wavelengths of the acidic form, the basic form, and the isosbestic point of the indicator. From the measurements of absorbance, the pH of this solution was calculated. The range of absorbance at the isosbestic point was maintained within 0.1 ${\sim}$ 0.3. The error of pH measurement was within ${\pm}0.08$ pH unit in the pH range of sample solution of $pK_I{\pm}1$.

• 한국신재생에너지학회:학술대회논문집
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• 2007.06a
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• pp.313-316
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• 2007

본 연구에서는 Cu와 In 성분을 포함하는 메탄올 용액을 닥터 블레이딩 방법으로 코팅한 후 이를 Se Evaporator 열처리하여 CIS 광흡수층을 제조하였다. $Cu(NO_{3})_{2}$, $INCl_{3}$ 를 출발 물질로 선정하고, 이를 메탄올 용매에 녹여 전구체 용액을 만든 후, 여기에 유기물 바인더 물질을 첨가하여 닥터 블레이드 코팅에 적합한 점도를 맞춘 후, 이를 Mo/glass 기판에 코팅하였다. 코팅된 Cu, In 함유 유기물 혼합체를 공기중에서 1차 열처리 한 후 Evaporator 를 이용해 Selenization 하여 태양전지용 CIS 광흡수층을 만들었다. 본 연구에서는 전구체 합성, 유기물 첨가, 공기중 열처리 및 Se 열처리 각 단계에서 광흡수층 막의 형상, 결정구조, 화학조성의 변화과정을 분석하여 CIS 박막의 형성 과정을 고찰하였다. 특히 Se 증발 온도가 CIS막의 특성과 조성에 미치는 영향을 분석하여, 최적의 셀렌화 조건을 도출하고자 하였다.

• 한국신재생에너지학회:학술대회논문집
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• 2006.11a
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• pp.570-572
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• 2006

본 연구에서는 Cu와 In 성분을 포함하는 메탄을 용액을 닥터 블레이딩 방법으로 코팅한 후 이를 Se 분위기에서 열처리하여 CIS 광흡순층을 제조하였다 $Cu(NO_3)_2,\;InCl_3$를 출발 물질로 선정하고, 이를 메탄을 용매에 녹여 전구체 용액을 만든 후 여기에 유기물 바인더 물질을 첨가하여 닥터 블레이드 코팅에 적합한 점도를 맞춘 후. 이를 Mo/glass 기판에 코팅하였다. 코팅된 Cu, In 함유 유기물 혼합체를 공기중에서 1차 열처리 후 Se 분위기에서 열처리하면 태양전지용 CIS 광흡수층을 얻게 된다 특히 본 연구에서는 전구체 합성, 유기물 첨가, 공기중 열처리 및 Se 열처리 각 단계에서 광흡수층 막의 형상, 결정구조, 화학조성의 변화과정을 분석하여 CIS 박막의 형성 과정을 고찰하였다.

• Korean Chemical Engineering Research
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• v.51 no.2
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• pp.240-244
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• 2013

Although forward osmosis desalination technology has drawn substantial attention as a next-generation desalination method, the energy efficiency of its draw solution treatment process should be improved for its commercialization. When ammonium bicarbonate is used as the draw solute, the system consists of forward-osmosis membrane modules, draw solution separation and recovery processes. Mixed gases of ammonia and carbon dioxide generated during the draws solution separation, need to be recovered to re-concentrate ammonium bicarbonate solution, for continuous operation as well as for the economic feasibility. The diluted ammonium bicarbonate solution has been proposed as the absorbent for the draw solution regeneration. In this study, experiments are conducted to investigate performance and features of the absorption corresponding to absorbent concentration. It is concluded that ammonium bicarbonate solution can be used to recover the generated ammonia and carbon dioxide. The results will be applied to design and operation of pilot-scale forward-osmosis desalination system.