• 한국환경농학회지
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• 제14권3호
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• pp.302-311
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• 1995

Benfuresate 및 oxolinic acid를 공시농약으로 선정하여 포장조건하에서 각각의 농약을 토성이 다른 논 및 밭토양에 시용하여 시기별로 잔류량을 측정한후 6가지 kinetic models을 도입하여 잔류유형을 나타내는 최적(最適) model을 선정하고 각 model로부터 구한 반감기를 비교 평가했다. Benfuresate 및 oxolinic acid의 잔류유형은 6가지 model에 의해 유의성 있게 설명되고 있었으나 $t\frac{1}{2}$ 산출을 위해 Power Function(PF), Elovich(EL), Parabolic(PB)등의 경험식을 적용하는것은 무리가 있었다. 실험식중 결정계수($r^2$), 표준오차(SE) 및 유의성을 기준으로 평가할 때 second-order(SO)>first-order(FO)>zero-order(ZO) kinetic model 순(順)이었다. 그러나 FO model의 경우, single FO kinetics 보다는 빠른 분해단계와 느린 분해단계로 구성된 multiple FO kinetics model이 잔류유형을 더 유의성있게 나타냈고, 이 경우 SO model과 비슷한 $r^2$값을 보여 주었다. 따라서 2가지 공시농약의 잔류유형을 나타내는 최적 model은 multiple FO 또는 SO model로 평가되었다. Benfuresate의 경우 single FO model로 산출한 반감기($t\frac{1}{2}$)는 월곡통과 청원통에서 각각 49, 63일로 SO model로부터 구한 $t\frac{1}{2}$인 39, 55일 보다 $20{\sim}13%$가 길었다. Oxolinic acid의 경우 FO model로부터 구한 $t\frac{1}{2}$은 용계통, 이현통에서 각각 25, 26일로 SO model로부터 구한 $t\frac{1}{2}$ 보다 $87{\sim}51%$ 긴 것으로 평가되었다. 이런 결과는 농약의 잔류유형을 나타내는 최적 model이 농약의 종류 및 환경조건에 따라 다를 수 있고 이에 따른 $t\frac{1}{2}$도 변화폭이 크기 때문에 FO model을 일률적으로 적용하는 대신 최적 model을 선정하고 이로부터 $t\frac{1}{2}$를 산출하는 것이 바람직한 것으로 생각된다.

• Bulletin of the Korean Chemical Society
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• 제8권5호
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• pp.408-414
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• 1987

The rate of bromine-exchange reaction between antimony tribromide and ${\alpha}-phenyl-n-butyl$ bromide in nitrobenzene has been determined, using antimony tribromide labelled with Br-82. The results indicate that the exchange reaction follows the first-order kinetics with respect to the organic bromide, and either the second- or first-order kinetics with respect to antimony tribromide depending on its concentration. The third-order rate constant obtained was 7.50 ${\times}10^{-2}l^2mol^{-2}s^{-1}$ at 28$^{\circ}$C. Similar study on the bromine-exchange reaction between antimony tribromide and ${\alpha}$-phenyl-i-butyl bromide has also been carried out. The results of the study show the same kinetic orders as the ones observed with $\alpha$-phenyl-n-butyl bromide. The third-order rate constant observed was 2.40 ${\times} 10^{-2} l^2mol^{-2}s^{-1}$ at 28$^{\circ}$C. The activation energy, the enthalpy of activation and the entropy of activation for the two exchange reactions mentioned above have been determined. The reaction mechanisms for the exchange reactions are discussed.

• Bulletin of the Korean Chemical Society
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• 제20권9호
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• pp.1031-1034
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• 1999

Tin oxide films have been grown employing the chemical vapor deposition technique under reduced pressure conditions using tetramethyltin as the precursor and oxygen as the oxidant. An activation energy derived for the deposition reaction under representative deposition conditions has a value of 89±3 kJ mol-1, suggesting a typical kinetic control. Deposition rates of tin oxide films exhibit a near first order dependence on tetramethyltin partial pressure and a zeroth order dependence on oxygen partial pressure. This study provides the first quantitative information about the growth kinetics of tin oxide films from tetramethyltin by the cold-wall low-pressure chemical vapor deposition.

• 한국환경과학회지
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• 제26권3호
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• pp.363-371
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• 2017

This study evaluates the adsorption properties of Sr ions in an aqueous solution of the synthetic zeolite (Z-Y1) prepared using coal fly ash generated from a thermal power plant. In order to investigate the adsorption characteristics, the effects of various parameters such as the initial concentrations of Sr ion, contact time, and solution pH were investigated in a batch mode. The Langmuir and Redlich-Peterson model fitted the adsorption isotherm data better than the Freundlich model. The maximum adsorption capacity of Sr ions, as determined the Langmuir model, was 181.68 mg/g. It was found that by varying the Sr ion concentration, pH, and temperature, the pseudo-second-order kinetic model describes the adsorption kinetics of the Sr ion better than the pseudo-first-order kinetic model. The calculated thermodynamic parameters of ${\Delta}H^0$ and ${\Delta}G^0$ showed that the adsorption of Sr ions on Z-Y1 was occurred through a spontaneous and an endothermic reaction. We found that the adsorption of Sr ions by Z-Y1 was more affected by pH than by temperature and Sr ion concentration.

• Bulletin of the Korean Chemical Society
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• 제35권8호
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• pp.2471-2476
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• 2014

The aim of the present study is to explore the possibility of utilizing loess for the adsorption of total phosphorous (T-P) and total nitrogen (T-N) in water. Batch adsorption studies were performed to evaluate the influences of various factors like initial concentration, contact time and temperature on the adsorption of T-P and T-N. The adsorption data showed that loess is not effective for the adsorption of T-N. However, loess exhibited much higher adsorption capacity for T-P. At concentration of $1.0mgL^{-1}$, approximately 97% of T-P adsorption was achieved by loess. The equilibrium data were fitted well to the Langmuir isotherm model. The pseudo-second-order kinetic model appeared to be the better-fitting model because it has higher $R^2$ compared with the pseudo-first-order and intra-particle kinetic model. The theoretical adsorption equilibrium $q_{e,cal}$ from pseudo-second-order kinetic model was relatively similar to the experimental adsorption equilibrium $q_{e,exp}$. The thermodynamic parameters such as free energy ${\Delta}G$, the enthalpy ${\Delta}H$ and the entropy ${\Delta}S$ were also calculated.

• 한국수소및신에너지학회논문집
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• 제22권4호
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• pp.534-545
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• 2011

This paper describes the evaluation of kinetic parameters for pyrolysis and carbon char oxidation of residual oil. The non-isothermal pyrolysis of residual oil was carried out with TGA (Thermo-Gravimetric Analyzer) at heating rate of 2, 5, 10 and $20^{\circ}C/min$ up to $800^{\circ}C$ under N2 atmosphere. The first order and nth order pyrolysis models were used to fit the experimental data, and the nth order model was turned out to follow the experimental data more precisely than the first order model. For carbon char oxidation experiment, TGA and four heating rates used in pyrolysis experiment were also adapted. The kinetic parameters for the residual carbon char particle were obtained with three char oxidation model, that is, volume reaction, grain and random pore model. Among them, the random pore model described the char oxidation behaviour quite well, compared to other two models. The non-linear regression method was used to obtain kinetic parameters for both pyrolysis and carbon char oxidation of residual oil.

• 유기물자원화
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• 제15권3호
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• pp.113-120
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• 2007

최종 메탄수율, 동력학적 상수 및 최대 메탄발생 속도 등 돈분의 메탄생성 특성을 평가하기 위하여 혐기성 회분식 실험을 수행하였다. 돈분의 혐기성 분해 동력학적 거동 평가시 1차 반응으로 기정하였으며 최종 메탄수율, 동력학적 상수 및 최대 메탄발생 속도는 각각 0.27~0.44L $CH_4/gVS$, $0.161{\sim}0.280d^{-1}$ 및 0.043~0.120L $CH_4/d$로 나타났다. 돈분 자체를 식종물질로 사용하는 경우 장기간의 초기 순응기간이 소요되었으나 최종 메탄수율에는 차이가 없는 것으로 나타났다. 돈분의 혐기성 처리는 효과적이나 고형물의 함량이 높은 경우 이상 혐기성 소화가 단상 혐기성 소화에 비해 효과적인 것으로 판단된다.

• 유기물자원화
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• 제9권1호
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• pp.119-126
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• 2001

PAHs로 오염된 토양을 슬러리 생물반응기로 처리할 경우, 재순환수와 계면활성제 첨가가 PAHs 제거율에 미치는 영향을 살펴보고자 하였다. 대부분 실험결과에서 1차 반응모델이 0차 반응모델보다 phenanthren과 pyrene의 제거율을 설명하는데 높은 상관계수를 나타냈다. 재순환수 및 CMC(critical micelle concentration)이상으로 계면활성제를 첨가한 실험에서 첨가하지 않은 경우 보다 phenanthrene과 pyrene의 제거율이 향상되었다.

• 한국의학물리학회지:의학물리
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• 제4권2호
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• pp.49-58
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• 1993

열자극 과정의 수치해석적인 방법을 이용하여 열자극 세기곡선의 kinetic order, 활성화 에너지, 이탈 진동수 그리고 초기 트랩 밀도를 구하기 위하여 혼합된 열자극 세기곡선으로 분해하였고, 비선형 최소 자승법으로 분해된 열자극 곡선 세기와 측정된 세기의 차이를 최소화시켰다. 감마선 선량계로 사용되고 있는 $\alpha$-Al$_2$ $O_3$ 에감마선을 조사시킨 후 ,300K～600K의 온도 구간에서 측정된 $\alpha$-Al$_2$ $O_3$의 열자극 발광 세기곡선은 정점 온도가 381K, 415K, 441K, 460K, 488K 그리고 506K인 6개의 독립된 열자극 발광세기곡선으로 분해되었으며, 381K의 정점온도를 갖는 분해된 열자극 발광 세기곡선의 kinetic order, 활성화 에너지 그리고 이탈 진동수는 각각 1, 1.12eV 그리고 6.79X$10^{12}$sec$^{-1}$로써, 이 결과는 다른 측정법에 의한 값과 유사하였다.

• 대한화학회지
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• 제62권2호
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• pp.79-86
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• 2018

This study reported the adsorption of Cu(II) ions onto activated carbon prepared from Myristica Fragrans shell (MFS AC) over independent variables of contact time, activating chemical (NaOH) concentration, initial adsorbate concentration, initial pH of adsorbate solution and adsorption temperature. The MFS AC structure, morphology and total surface area were characterized by FTIR, SEM and BET techniques, respectively. The Cu(II) ions adsorption on the MFS AC (activated using 0.5 M NaOH) fitted best to Freundlich adsorption isotherm (FAI), and the FAI constant obtained was 0.845 L/g at $30^{\circ}C$ and pH 4.5. It followed the pseudo first order of adsorption kinetic (PFOAK) model, and the PFOAK based adsorption capacity was 107.65 mg/g. Thermodynamic study confirmed the Cu(II) ions adsorption should be exothermic and non-spontaneous process, physical adsorption should be taken place. The total surface area and pore volume based on BET analysis was $99.85m^2/g$ and 0.086 cc/g, respectively.