• 공업화학
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• 제19권1호
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• pp.31-36
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• 2008

혐기성소화가스(ADG)를 원료로 수소를 제조하여 연료전지에 활용할 경우 ADG에 포함된 황화합물이 개질기의 촉매와 연료전지의 전극에 독으로 작용하므로 금속이온이 담지된 활성탄을 이용하여 황화합물을 제거하였다. 수분과 산소농도에 따라 고정층 흡착량이 변화하였으며, 산소 0.2 vol%, RH 90% 이상일 때 가장 높은 흡착량을 나타내었다. 본 연구에서는 KI 첨착한 활성탄에서 황화합물의 흡착특성을 고정층에서 동특성 실험을 통해 관찰하고 그 결과를 기준으로 흡착탑을 설계 제작 현장실험을 실시하였다.

• Membrane and Water Treatment
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• 제11권2호
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• pp.131-139
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• 2020

The current study focused on the preparation of low-cost PVC-based adsorbing membrane. Metakaolin, as available adsorbent, was embedded into the PVC matrix via solution blending method. The as-prepared PVC/metakaolin mixed matrix membranes were characterized using scanning electron microscopy (SEM), energy-dispersive X-ray spectroscopy (EDS), attenuated total reflectance-Fourier transform infrared (ATR-FTIR) spectroscopy, atomic force microscopy (AFM), pure water permeability and contact angle measurements. The results confirmed the improvement of PWP and hydrophilicity due to the presence of metakaolin in the PVC matrix. Additionally the structure of PVC membrane was changed due to the incorporation of metakaolin in the polymer matrix. The static adsorption capacity of all samples was determined through dye removal. The effect of metakaolin dosage (0-7%) and pH (4, 8, 12) on dye adsorption capacity was investigated. The results depicted that the highest adsorption capacity was achieved at pH of 4 for all samples. Additionally, adsorption data were fitted on Langmuir, Freundlich, and Temkin models to determine the appropriate governing isotherm model. Finally, the dynamic adsorption capacity of the optimum PVC/metakaolin membrane was studied using dead-end filtration cell. The dye removal efficiency was determined for pure PVC and PVC/metakaolin membrane. The results demonstrated that PVC/metakaolin mixed matrix membrane had a high adsorption capacity for dye removal from aqueous solution.

• 한국환경과학회지
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• 제21권6호
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• pp.687-694
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• 2012

Zeolite 4A was synthesized by fusion method from coal fly ash discharged at the thermal power plants. The synthesized zeolite(FAZ) was characterized through particle size analyzer, XRD, XRF and SEM. $N_2$ adsorption-desorption measurement was used to examine surface and pore structures. The adsorption experiments were carried out under dynamic conditions of trace $SO_2$ in $N_2$ to investigate $SO_2$ adsorption capacity of FAZ. The experiments were conducted to characterize the breakthrough characteristics of $SO_2$ in a fixed bed under different operating conditions including temperature(50-$125^{\circ}C$), concentration of $SO_2$(3000-10000 ppm) and FAZ with 4 kinds of commercial zeolite. The adsorption capacity of FAZ was 53.84 $mgSO_2/g$ adsorbent, larger than that of the same type commercial zeolite(WK4A).

• Carbon letters
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• 제7권4호
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• pp.249-258
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• 2006

Treatment of water hyacinth with sulphuric acid produces carbonaceous materials that have been used to remove Cu(II) and Cd (II) ions from aqueous solutions. Untreated water hyacinth was also used for the subject of comparison. The textural properties of the carbonaceous materials were determined from nitrogen adsorption at 77 K. The optimum pH for the sorption of Cu (II) and Cd (II) ions on the investigated sorbents was determined. Dynamic adsorption measurements have been taken at 298 K whereas equilibrium measurements were carried out at 298, 313 and 323 K. The adsorption of nitrogen at 77 K on the untreated sample was too low and the surface areas of the treated samples 2, 3 and 4 were found between $70-208\;m^2/g$. The total pore volumes of these samples which were determined for the carbonaceous materials investigated were found to be 0.076-0.140 ml/g. The kinetic adsorption data of Cu (II) and Cd(II) were applicable to both pseudo - first and pseudo-second order but fit more the latter order. The equilibrium adsorption data were found to fit Freundlich and Langmiur equations. The values of DG, DH and DS are all negative indicating the feasibility and the spontaneous nature of the sorption of Cu (II) and Cd (II) ions by the sorbents investigated.

• Korean Chemical Engineering Research
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• 제50권1호
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• pp.149-154
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• 2012

바이오필터담체가 충전된 흡착칼럼 운전 시의 흡착 및 탈착거동에 대하여 조사하였다. 에탄올을 휘발성유기화합물(VOC)로서 함유하는 폐가스를 처리하기 위한 연속동적흡착 실험을 바이오필터공정과 같은 90% 이상의 상대습도에서 수행하였다. 에탄올 1,000 ppmv(or 2,050 mg ethanol/$m^3$)를 포함하는 폐가스 2 L/min을 흡착칼럼에 공급하였을 때에 흡착칼럼 출구에서의 파과점과 흡착평형에 이르는 시간은 1단 시료구에서 보다 각각 10배와 3배 만큼 지연되었다. 한편 에탄올 2,000 ppmv(or 4,100 mg ethanol/$m^3$)를 포함하는 폐가스의 경우에는 각각 9배와 3배 지연되었다. 이와 같이 흡착칼럼 출구에서 지연기간의 비는 공급농도와 무관하게 서로 거의 일치하였음이 관찰되었다. 또한 1단 시료구와 출구에서 비교한 유입폐가스의 에탄올농도의 10%를 보이는 탈착시간 지연비도 약 1.5배로서 거의 일치하였다. 한편 미생물활성과 멸균공정의 흡착평형에 대한 영향에 대하여 조사하였다. 멸균된 입상 활성탄으로 충전된 vial의 기상 에탄올 농도는 멸균되지 않은 입상 활성탄으로 충전된 경우와 거의 일치하였다. 그러나 퇴비(compost)나 입상 활성탄/퇴비 혼합물의 경우에는 멸균 안한 경우가 멸균한 경우보다 기상에서의 에탄올 농도가 현저하게 높았다.

• 대한토목학회논문집
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• 제12권2호
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• pp.265-274
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• 1992

하천에 사고로 대량으로 유입된 유독성 유기오염물인 anthracene의 농도를 예측하기 위한 수학적 모형이 제안되었다. 이 수학적 모형은 물리적, 화학적 및 생물학적 반응을 고려한 6개의 미분방정식으로 구성되어 있으며, 5개의 입력변수와 9개의 반응계수를 포함하고 있다. 주어진 조건하에 제안된 수학적 모형을 대상으로 dynamic simulations와 민감도 분석을 수행한 결과 유입된 이 오염물의 농도를 검출한계내로 예측이 가능하였고, 용존 빛 부유고형물에 흡착된 이 오염물의 농도변화에 가장 큰 영향을 주어 가장 정확히 추정하여야할 주요 반응계수는 확산계수와 이동계수 및 흡착계수이었다. 이 연구에서 제안된 수학적 모형은 anthracene 뿐만아니라 이와 유사한 화학적 특성의 유기오염물의 경우에도 활용이 가능할 것으로 기대된다.

• 한국산업보건학회지
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• 제15권1호
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• pp.8-18
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• 2005

Adsorption capacity for the charcoal were tasted in this study to verify the performance of them for the use of the sampling media in industrial hygiene field. Two set of experiments were conducted. The first experiment was to test performance of the tested charcoal tube that were assembled in the laboratory with the use of the GR grade charcoal. The other tests were investigate the adsorption capacity of the charcoal tested in this study and charcoals embedded in the commercial charcoal tubes. Known air concentration samples for benzene, toluene, and o-xylene were prepared by the dynamic chamber. 1. At low air concentration levels (0.1${\times}$TLV), there was no significant differences between the tested charcoal tubes and the SKC charcoal tubes. This implies that there is no defect with the adsorption capacity of the charcoal. 2. At high concentration with 60 minutes sampling, the breakthrough were found only in the tested charcoal while no breakthrough were shown in the SKC charcoal. 3. From the breakthrough tests for the charcoal, the micropore volume(Wo) were calculated by the curve fitting with the use of Dubinin/Radushkevich(D/R) adsorption isotherm equation. The calculated values were 0.687cc/g for SKC, 0.504cc/g for Sensidyne, and 0.419cc/g for the tested charcoal(Aldrich). 4. Adsorption capacities were obtained from the isotherm curves shown adsorption capacities at several levels of the challenge concentration. All range of the air concentration concerned in industrial hygiene, the SKC charcoal showed approximately two times of adsorption capacity compared to the tested charcoal.

• Environmental Engineering Research
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• 제8권2호
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• pp.98-106
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• 2003

• 대한환경공학회지
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• 제27권6호
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• pp.620-625
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• 2005

연속식 흡착장치를 사용하여 활성탄의 세공구조와 아세톤 중기의 흡착특성과의 상관관계를 고찰하였다. 실험에서 비교한 활성탄 중 젠체 세공구조에서 직경 $10{\AA}$ 이하의 세공이 가장 많이 발달한 Takeda의 ACT 활성탄이 가장 긴 파과시간을 가지고 있었다. 평형흡착량은 파과시간에는 비례했지만, BET 비표면적에는 비례한다고 볼 수 없었기 때문에 BET 비표면적 만으로 흡착능을 평가하는 것은 어려웠다. 누적표면적과 평형흡착량과의 상관관계는 $10{\AA}$ 이하에서 가장 컸고, 세공범위가 클수록 감소했다.

• Korean Journal of Chemical Engineering
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• 제35권12호
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• pp.2384-2393
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• 2018

Porous alginate-based hydrogel beads (porous ABH) have been prepared through a facile and sustainable template-assisted method using nano-calcium carbonate and nano-$CaCO_3$ as pore-directing agent for the efficient capture of methylene blue (MB). The materials were characterized by various techniques. The sorption capacities of ABH towards MB were compared with pure sodium alginate (ABH-1:0) in batch and fixed-bed column adsorption studies. The obtained adsorbent (ABH-1:3) has a higher BET surface area and a smaller average pore diameter. The maximum adsorption capacity of ABH-1:3 obtained from Langmuir model was as high as $1,426.0mg\;g^{-1}$. The kinetics strictly followed pseudo-second order rate equation and the adsorption reaction was effectively facilitated, approximately 50 minutes to achieve adsorption equilibrium, which was significantly shorter than that of ABH-1:0. The thermodynamic parameters revealed that the adsorption was spontaneous and exothermic. Thomas model fitted well with the breakthrough curves and could describe the dynamic behavior of the column. More significantly, the uptake capacity of ABH-1:3 was still higher than 75% of the maximum adsorption capacity even after ten cycles, indicating that this novel adsorbent can be a promising adsorptive material for removal of MB from aqueous solution under batch and continuous systems.