• 공업화학
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• 제27권2호
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• pp.199-204
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• 2016

입상 활성탄을 사용하여 수용액으로부터 Rhodamine-B 염료의 흡착에 대해 조사하였다. 회분식 실험은 흡착제의 양, pH 초기농도와 접촉시간과 온도를 흡착변수로 사용하여 수행하였다. 흡착평형자료는 Langmuir 등온식에 잘 맞았다. 평가된 Langmuir 분리계수($R_L$ = 0.0164~0.0314)로부터 이 흡착공정이 적절한 처리방법이 될 수 있음을 알았다. 흡착속도실험결과는 유사 1차 반응속도식에 잘 맞는 것으로 나타났다. 음수값의 Gibbs 자유에너지(-4.51~-13.44 kJ/mol)와 양수값의 엔탈피(128.97 kJ/mol)는 흡착이 자발적이고 흡열공정으로 진행된다는 것을 나타냈다. 등량흡착열은 흡착된 염료분자들의 측면상호작용에 따라 표면부하량이 증가할수록 커졌다.

• 설비공학논문집
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• 제17권8호
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• pp.746-753
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• 2005

Adsorption chillers have been receiving considerable attentions as they are energy-saving and environmentally benign systems. In order to evaluate adsorption rates, experiments were performed in the batch type adsorption apparatus. Three types of silica gels were investigated under an assortment of experimental conditions that are representatives of the actual operating environments in the adsorber of adsorption chillers. Experimental results revealed the effects of silica gel particle size, bed temperature, and fin pitch of fin tube on the adsorption rate. The $0.25\~1.18mm$ particle size of silica gel with high adsorption rate was selected as a suitable adsorbent. The measured adsorption rate became bigger with decreasing particle size. From the comparison of adsorption rate, it is found that the fin tube has about $21\%$ higher value than that of the bare tube. The effect of heat and mass flux is found to be more significant in the fin tube than in the bare tube.

• 공업화학
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• 제28권2호
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• pp.206-213
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• 2017

활성탄을 사용하여 수용액으로부터 crystal violet 염료의 흡착에 대해 조사하였으며, 흡착제의 양, 초기농도와 접촉시간 및 온도를 흡착변수로 사용하여 수행하였다. 흡착평형관계는 Langmuir 등온식에 잘 맞았다. 평가된 Langmuir 분리 계수($R_L=0.02{\sim}0.106$)를 바탕으로 이 흡착공정이 효과적인 처리(0 < $R_L$ < 1)가 가능하다는 것을 알았다. 흡착동력학 데이터는 유사 2차 반응속도식에 잘 맞는 것으로 나타났다. Gibbs 자유에너지(-1.61~-11.66 kJ/mol)와 엔탈피(147.209 kJ/mol)는 흡착공정이 자발적이고 흡열반응으로 진행된다는 것을 나타냈다. 등량흡착열은 표면덮임이 증가됨에 따라 흡착제-흡착질의 상호작용이 제한되어 표면부하량이 증가할수록 작아졌다.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2006년도 하계학술발표대회 논문집
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• pp.1119-1124
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• 2006

The objectives of this paper are to investigate the performance of silica gel-water adsorption refrigeration system with heat recovery process from the system experiment. This system can be driven by waste heat at near ambient temperature from $60^{\circ}C$ to $90^{\circ}C$. The cooling capacity and coefficient of performance(COP) were measured from various experimental conditions. An experimental results revealed the influence of operating temperatures(hot, cooling and chilled water), water flow rates, and adsorption-desorption cycle times on cooling capacity and COP. Under the standard conditions of $80^{\circ}C$ hot water, $25^{\circ}C$ cooling water, $14^{\circ}C$ chilled water inlet temperatures and 420sec cycle time, a cooling capacity of 1.14kW and a COP for cooling of 0.55 can be achieved.

• 한국태양에너지학회:학술대회논문집
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• 한국태양에너지학회 2012년도 춘계학술발표대회 논문집
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• pp.364-369
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• 2012

The development of solar thermal energy used adsorption desalination technology have been examined as a viable option for supplying clean energy. In this study, the modelling of the main devices for solar thermal energy used and adsorption desalination system was introduced. Silica gel type adsorption desalination system is considered to be a promising low-temperature heat utilization system. The design is divided into three parts. First, the evaporator for the vaporization of the tap water is designed, and then the reactor for the adsorption and release of the steam is designed, followed by the condenser for the condensation of the fresh water is designed. In addition, new features based on the energy balance are also included to design absorption desalination system. In this basic research, One-bed(reactor) adsorption desalination plant that employ a low-temperature solar thermal energy was proposed and experimentally studied. The specific water yield is measured experimentally with respect to the time controlling parameters such as heat source temperatures, coolant temperatures, system switching and half-cycle operational times. Desalination is processes that permeate our daily lives, but It requires substantial energy input, powered either from electricity or from thermal input. From the environmental and sustainability perspecives, innovative thermodynamic cycles are needed to produce the above-mentioned useful effects at a lower specific energy input. This article describes the development of adsorption cycles for the production of desalting effects. We want that this adsorption system can be driven by low temperature heat sources at 60 to $80^{\circ}C$, such as renewable, solar thermal energy.

• 공업화학
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• 제30권2호
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• pp.190-197
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• 2019

활성탄을 사용하여 수용액으로부터 메틸 그린 염료의 흡착에 대해 초기농도와 접촉시간 및 온도를 흡착변수로 사용하여 조사하였다. 흡착평형관계는 Freundlich 등온식에 잘 맞았다. 평가된 Freundlich 분리계수(1/n = 0.212~0.305)로부터 이 흡착공정이 효과적인 처리영역(0 < $R_L$ < 1)에 속하는 것을 알았다. BET식으로부터 얻은 등온포화용량은 온도가 증가할수록 커졌다. Dubinin-Radushkevich식으로 구한 흡착에너지값(E = 316.869~340.049 J/mol)으로부터 흡착공정이 물리흡착공정임을 알았다. 흡착속도실험결과는 유사 2차 반응속도식에 잘 맞는 것으로 나타났다. 자유에너지(-5.421~-7.889 kJ/mol)와 엔탈피(31.915 kJ/mol)는 흡착공정이 자발적이고 흡열반응으로 진행되었다고 알려주었다. 등량흡착열은 평형흡착량이 증가함에 따라 커졌으며, 표면 덮임이 증가됨에 따라 흡착제-흡착질의 총 상호작용도 증가하였다.

• 한국광물학회지
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• 제9권1호
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• pp.17-25
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• 1996

Usual experimental adsorption isotherms as a function of relative humidity were constructed from adsorbed water contents in soils, which were kept more than 2 days in vacuum desiccators with constant humidities controlled by sulfuric acids of various concentrations. From the experimental data, the adsorption surface areas were calculated on the basis of the existing adsorption theory, such as Langmuir, BET, and Aranovich. Based on the Gibbs function describing chemical potential of perfect gas, the relative humidities in the desiccators were transformed into their chemical potentials, which were assumed to be the same as the potentials of equilibratedly adsorbed water in soils. Moreover, the water potentials were again transformed into the equivalent capillary pressures, heads of capillary rise, and equivalent radius of capillary pores, on the basis of Laplace equation for surface tension pressure of spherical bubbles in water. Adsorption quantity distributions were calculated on the profile of chemical potentials of the adsorbed water, equivalent adsorption and/or capillary pressures, and equivalent capillary radius. The suggested theories were proved through its application for the prediction of temperature rise of sulfuric acid due to hydration heat. Adsorption heat calculated on the basis of the potential difference was dependant on various factors, such as surface area, equilibrium constants in Langumuir, BET, etc.

• 설비공학논문집
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• 제27권2호
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• pp.94-102
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• 2015

A hydroscopic polymer is used as the adsorbent in an adsorption refrigeration system. A pair of plate-type heat exchangers, thinly coated with the polymer, is simulated using a two-dimensional transient model to predict performance of the system. It is predicted that the system would yield 0.57 kW SCP and 0.47 COP at $80^{\circ}C$ heating and $30^{\circ}C$ cooling temperatures. In comparison with a conventional silica gel-water system, the COP is comparable but SCP is about three times larger. The slow mass diffusion rate of the polymer should be improved for better performance.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 2000년도 제15차 학술회의논문집
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• pp.309-309
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• 2000

The main objective of this study is to understand the regeneration step of the PTSA(Pressure and thermal swing adsorption) process below the atmospheric pressure by rigorous dynamic simulation. This target process is to recover toluene using activated carbon as an adsorbent. To do this, the dynamic simulations for the regeneration step are performed at 360, 490, 590mmHg and at high temperature after the simulation of the adsorption step at latm and 298K. A mathematical model was developed to simulate the column dynamics of the adsorption systems. This model is based on non-equilibrium, non-isothermal and non-adiabatic conditions, and axial dispersion and heat conduction are also considered. Heat transfer resistances are considered in gas-solid, gas-column wall and column wall-outside air. The LDF(Linear Driving Force) approximation model describes the mass transfer rate between the gas and solid phase. This study shows that the recovery of toluene by PTSA is more preferable than that by general TSA.

• 대한환경공학회지
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• 제37권4호
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• pp.210-217
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• 2015

Red mud의 염산처리와 열처리에 의한 불소의 제거 특성을 살펴보고자 동역학적 흡착, 평형흡착, pH, 흡착제의 주입량에 따른 흡착특성, 그리고 칼럼을 이용한 연속식 조건에서의 불소흡착 특성을 살펴보았다. Red mud의 산처리는 HCl 0.8 M 농도에서 효과적이었고, 열처리 온도가 높음에 따라 흡착량이 감소하였다. 0.8 M로 산처리한 Red mud (0.8 M-ATRM)의 동역학적실험 결과 초기농도 50 mg-F/L는 30분대에 평형농도에 도달하였고, 초기농도 500 mg-F/L에서는 1시간대 흡착평형을 나타내었다. 0.8 M-ATRM은 단층흡착을 가정한 Langmuir 모델에 잘 부합하였고, 최대흡착량($Q_m$)은 23.162 mg/g으로 나타났다. 또한 낮은 pH에서 높은 불소 흡착경향을 나타내었다. 이는 높은 pH에서 불소와 $OH^-$가 경쟁관계를 형성하기 때문으로 판단된다. 0.8 M-ATRM의 주입량이 증가 할수록 제거율은 높아졌지만, 단위질량당 흡착량은 감소하였다. 본 연구에서 사용된 0.8 M-ATRM은 가격이 저렴할 뿐만 아니라 불소에 높은 흡착능을 나타내어 수중 불소 제거에 효과적인 흡착소재로 판단된다.