• Journal of Korean Society of Environmental Engineers
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• v.22 no.3
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• pp.547-556
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• 2000

A study have been conducted for the adsorption and desorption characteristics of Cu ion using manganese nodule as adsorbent. For 100 ppm Cu ion solution, the adsorbed amount of Cu ion was more than 90 % at equilibrium state. Adsorption was equilibrated in 42 hours the adsorption reaction was shown to be first order reaction. For the desorption reaction of Cu ion in the region of solution pH 3.5~9.5, the desorption was completed in the acidic region, but it has been decreased as the pH was raised. Also, the desorption rate was higher in the acidic region compared with alkaline region. The desorbed amount was decreased as the reaction temperature increased, therefore, the desorption reaction was thought to be exothermic. Also, several thermodynamic properties were calculated based on experimental results and compared with theoretically driven values. To see the effect of complexing agent on the desorption of Cu ion, EDTA was introduced and the des orbed amount increased in the presence of EDTA.

• Proceedings of the Korean Nuclear Society Conference
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• 1998.05b
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• pp.808-813
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• 1998

EDTA 의 농도 및 온도가 일정한 조건에서 수용액의 pH 를 변화시켜 가며, 토양으로부터 Co$^2$$^{+}$ 이온의 탈착특성을 살펴보았다. 실험범위에서, pH 4 일 때 $CO_2$$^{+}$ 이온의 탈착율이 가장 양호하였으며, pH 가 상승함에 따라 탈착율이 감소되는 것으로 나타났다. 또한, 반응중 철 성분이 용해되어 나오는데 이는 반응 초기 수소이온에 의한 용해와 반응중 탈착된 Co$^2$$^{+}$ 이온에 의한 용해로 설명하였다.

• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 2004.09a
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• pp.248-251
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• 2004

일반적으로 유기오염 물질의 경우 sequestration 또는 aging 현상에 의해 탈착저항성을 띠게 되는 것으로 알려져 있다. 그러나 중금속의 경우 흡/탈착반응은 탈착저항성이 없는 가역적 반응이라는 보고가 있는 반면 홉/탈착 반응은 비가역적이며 탈착저항성이 존재한다는 보고도 있다. 본 연구에서는 해양 연안 퇴적물에 대한 납의 흡/탈착 실험을 통하여 탈착 저항성을 화인하고 연속추출 실험을 수행함으로써 탈착 저항성 부분의 크기를 규명하고자 하였다. 그리고 각기 다른 pH(4, 6)에서 흡착 실험을 수행함으로써 pH에 따른 흡착친화도를 규명하였다. 그 결과 퇴적물에 대한 납의 흡착량은 높은 pH(6)에서 더 많았고, 각 pH 범위에서 납은 탈착저항성을 가지는 것으로 나타났으며, 연속추출결과 Organic Material bound부분에 66% 정도가 흡착되어 있음을 알 수 있었다.

• Journal of the Mineralogical Society of Korea
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• v.22 no.4
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• pp.289-295
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• 2009

The characteristics of phosphate desorption on kaolinite was studied by batch adsorptiondesorption experiments. Desorption procedure was carried out through sequential extraction method at pH 4. The phosphorous contents were measured using UV-VIS-IR spectrophotometer with 820 nm wavelength. The adsorption-desorption reaction of P on kaolinite was irreversible, and most of adsorbed P on kaolinite were not easily dissolved to aqueous solution, but may might be fixed on kaolinite surface. The desorption isotherms were well fitted with the Freundlich and Temkin equations in the case of short reaction and long reaction time, respectively. The desorption reaction was divided into the early fast reaction and the later slow reaction. The percentage of desorption generally decreased with increasing adsorbed P concentration and increasing desorption reaction time.

• Journal of the Mineralogical Society of Korea
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• v.15 no.2
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• pp.104-113
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• 2002

The sorption of Cd$^{2+}$ on calcite was studied in aqueous solutions of several electrolytes. The Cd$^{2+}$ concentration, 10$^{-8}$ M, was kept well below saturation with respect to CdCO$_3$(s). Sorption behavior of Cd$^{2+}$ in different ionic strengths of NaClO$_4$solutions shows that sorption is independent of ionic strength. This result suggests that Cd$^{2+}$ sorption on calcite surface is of a specific nature, and adsorption is controlled by an inner-sphere type of surface complex. Two stages in the sorption behavior could be identified: an initial rapid uptake, followed by slower uptake reaching a maximum steady state by 145 hrs. No evidence was observed for surface precipitation, although it can not be entirely ruled out. Desorption of Cd$^{2+}$ from the calcite surface after resuspension into Cd-free solution is initially very rapid, but depends partly on the previous sorption history. Desorption behavior of Cd$^{2+}$ show that an initial rapid desorption followed either by slow uptake reaching a maximum, as in the adsorption experiments, or slowing desorption to reach a steady state minimum. This irreversible behavior of Cd$^{2+}$ sorption and desorption may act as one of the controls for regulating the mobility of dissolved Cd$^{2+}$ natural aqueous systems. Calculated adsorption partition coefficients suggest that overall sorption and desorption process in the concentration range are controlled by d single mechanism.ingle mechanism.

• Clean Technology
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• v.16 no.1
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• pp.33-38
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• 2010

The characteristics of desorption reaction and the heating values of used activated carbons collected from the companies of Shiwha/Banwal industrial complex were investigated. The desorption characteristics of used activated carbons were analyzed based on the data obtained from a thermogravimetric analyzer. The activation energies and reaction orders for desorption reaction of used activated carbons were calculated by employing Freeman-Carroll method. Heating values of volatile organic compounds(VOC) desorbed from used activated carbons were estimated based on the data obtained from a total hydrocarbon analyzer. It was found that the reaction orders of desorption of used activated carbons were 0.1~0.8, their desorption activation energies, 6.9~26.4 kJ/mol, and VOC heating values, 0.4~10.7 kcal/kg.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2005.11a
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• pp.97-98
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• 2005

본 연구결과 흡${\cdot}$탈착공정에서 완충물질인 Q-vesol 경우 흡${\cdot}$탈착능력은 고농도 benzene일 경우, 85 wt%, 95 wt% 보였으며, 고농도 hexane일 경우 81 wt%, 96 wt%의 흡${\cdot}$탈착효율을 보여 저농도 VOCs 경우 보다 흡${\cdot}$탈착 능력이 우수함 을 알 수 있었다. 그리고 hexane보다 benzene 이 흡착반응이 빠름을 알 수 있었으며 또한 탈착 반응은 현저히 느리다는 것을 본 실험연구 결과 알 수 있었다. 이것은 흡${\cdot}$탈착공정에서 Q-vesol 경우, 완충효과가 우수한 것으로 확인되었다.

• Applied Chemistry for Engineering
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• v.21 no.5
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• pp.505-508
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• 2010

The characteristics of desorption reaction for spent activated carbon produced from the manufacture of other chemical products in Shiwha/Banwal industrial complex were investigated. TGA (Thermogravimetric Analyzer) was used to study for characteristics of desorption and kinetics. Then Friedman method and Freeman-carroll method were used to find the activation energy and the order of reaction. Activation energy by Friedman method was 24.82~46.49 kJ/moL. And then activation energy and order of reaction by Freeman-carroll method were 8.77~32.26 kJ/moL and 0.11~1.69.

• Resources Recycling
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• v.30 no.2
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• pp.24-30
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• 2021

Dismantling tests were performed to separate components from waste printed circuit boards (PCBs) using HCl solution with Sn4+. Then, the effects of agitation speed, reaction temperature, initial Sn4+ concentration, and HCl concentration on the dismantling of components were investigated. No significant effect on the dismantling speed was observed upon changing the agitation speed from 100 to 300 rpm. However, the dismantling rate increased with increasing reaction temperature, Sn4+ concentration, and HCl concentration. In the all-component dismantling tests, when the dismantling ratio increased to 100%, no solder was observed on the boards, and the Sn4+ concentration was ~1,500 mg/L. The dismantling ratio of the components from the PCB increased to 100% within 2 h when 1 mol/L HCl solution with 10,000 mg/L Sn4+ was used at an agitation speed and temperature of 200 rpm and 90 ℃, respectively.

• Resources Recycling
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• v.31 no.6
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• pp.25-35
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• 2022

The adsorption/desorption behavior and separation conditions of vanadium and tungsten ions were investigated using a gel-type anion-exchange resin. In the adsorption experiment with the initial acidity of the solution, the adsorption rate of vanadium was remarkably low in strong acids and bases. Additionally, the adsorption rate of tungsten was low in a strong base. An increase in the reaction temperature increased the adsorption reaction rate and maximum adsorption. The effect of tungsten on the maximum adsorption was minimal. The adsorption isotherms of vanadium and tungsten on the ion-exchange resin were suitable for the Langmuir adsorption isotherms of both the ions. For tungsten, the adsorption isotherms of vanadium and tungsten were polyoxometalate. Both ion-exchange resins were simulated using similar quadratic reaction rate models. Vanadium was desorbed in the aqueous solutions of HCl or NaOH, the desorption characteristics of vanadium and tungsten depended on the desorption solution, and tungsten was desorbed in the aqueous solution of NaOH. It was possible to separate the two ions using the desorption process. The desorption reaction reached equilibrium within 30 min, and more than 90% recovery was possible.