• Title/Summary/Keyword: 흡착률

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Adsorption Property of Shrimp Shell Chitosan to Water Soluble Proteins (수용성 단백질에 대한 새우껍질 Chitosan의 흡착 특성)

  • 손병일;김경삼
    • The Korean Journal of Food And Nutrition
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    • v.13 no.3
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    • pp.242-248
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    • 2000
  • 수산물 가공시 흘러나오는 폐수 중에 함유되어 있는 수용성 단백질을 chitosan에 흡착시키기 위하여 albumin과 hemoglobin, albumin-myoglobin 혼합단백질을 이용하여 chitosan과의 흡착 및 chitosan 제조조건에 따른 흡착효과와 chitosan의 수용성 단백질 흡착에 미치는 인자를 살펴본 결과는 다음과 같다. Chitosan위 탈아세틸화 조건을 60, 70, 80%로 달리하여, albumin, hemoglobin, albumin-myoglobin 혼합용액에 적용했을때 chitosan의 탈아세틸화도가 높을수록 chitosan과 단백질 사이의 흡착률은 높게 나타났다. 초음파 처리에 의하여 chitosan의 분자량이 작을수록 chitosan과 단백질 사이의 흡착률은 높게 나타났다. pH변화에 따른 chitosan과 수용성 단백질의 흡착률은 albumin 및 albumin-myoglobin 혼합용액에서는 pH 4.0에서, hemoglobin용액에서는 pH 7.0에서 흡착률이 높게 나타났다 chitosan과 수용성단백질과의 흡착에서 반응시간은 albumin및 albumin-myoglobin 혼합용액에서는 4시간, hemoglobin용액에서는 3시간까지 흡착률이 증가하였고, 그 이후의 시간이 경화하여도 흡착률의 증가는 거의 보이지 않았다. 수용성 단백질 용액에 NaCl 농도를 0.1M에서 1.0M로 증가시켜 첨가했을때 염의 농도가 높을수록 chitosan과 단백질 사이의 흡착이 잘 일어나지 않았다.

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Stabilization Behavior of Heavy Metal ions by Treatment Conditions (처리조건에 따른 중금속 이온의 안정화 거동)

  • 엄태호;김유택
    • Journal of the Korean Ceramic Society
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    • v.40 no.6
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    • pp.583-588
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    • 2003
  • Cation exchange capacity of clay, white clay and zeolite was measured by the adsorption test for 3 different heavy metal (Cd, Cr, Zn) standard solutions whose concentrations were varied by 10, 20, 30 ppm and pH were varied by 3, 5, 7, 9, respectively. The adsorption rate of Cd and Zn increased with increasing pH and slowly increased with increasing pH above pH 5. However, adsorption rate of Cr did not increase with increasing pH. Especially, Cr adsorption rate of the mixture of clay and white clay at pH 5 showed an half decrease compared to that at pH 3. The adsorption rate of mixed heavy metal solutions was in the order of Cd, Zn > Cr; however, the order was changed by Fe>Pb, Cu>Cr>Zn>Cd in case of Cu, Fe and Pb addition.

Adsorption of Diazinon on Humic Substances in Submerged Soil (담수토양중 부식물질에 대한 diazinon의 흡착)

  • Song, Jae-Young;Lee, Kyu-Seung
    • Korean Journal of Environmental Agriculture
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    • v.12 no.1
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    • pp.35-40
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    • 1993
  • In order to find the effect of humic substances affecting to the behavior of diazinon in submerged soil, the adsorption rate of diazinon was investigated with different soil humic substances like as humin, humic acid and fulvic acid. The adsorption rate of diazinon(1.8 ppm) was 12.4% in humin, 11.9% in fulvic acid and 10.4% in humic acid at 1% concentration of humic substances, also were not much differences at 0.1 and 0.5%. But it showed much similar level ($10.2{\sim}10.6%$) at 1.0% concentration in 5ppm diazinon treatment. As a result, because adsorption rate of diazinon on humic substances were about $10{\sim}12%$, disappearance of diazinon in submerged soil may be affected by the other factors such as soil microorganism.

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Properties of Heavy Metal Adsorption of Clay Minerals (점토광물에 의한 중금속 흡착 특성)

  • 엄태호;김유택;이기강;김영진;강승구;김정환
    • Journal of the Korean Ceramic Society
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    • v.39 no.7
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    • pp.663-668
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    • 2002
  • Cation exchange capacity of clay, white clay and zeolite was estimated by performing the powder adsorption test for 6 different heavy metal (Cd, Cr, Cu, Fe, Pb and Zn) standard solutions whose concentrations were varied by 5,10,15 and 20 ppm. The adsorption rate of heavy metals decreased with increasing the concentration of standard heavy metal solutions. The adsorption rate of the clay and the white clay showed more than 80% for the all tested heavy metals except Cr and especially above 99% for the Fe and the Pb. The Cr adsorption rate of the mixture of the clay and the white clay increased, however, that of Zn decreased. The adsorption rate of Cr and Zn showed relatively lower values as compared with those of the other heavy metals because the cation exchange H$\^$+/ ions and heavy metal ions of the clay or the white clay were in competition at low pH region.

Recovery of tin from waste tin plating solution by ion exchange resin (주석도금폐액으로부터 이온교환수지를 이용한 주석 회수)

  • Gang, Yong-Ho;Sin, Gi-Ung
    • Proceedings of the Korean Institute of Surface Engineering Conference
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    • 2015.11a
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    • pp.219-220
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    • 2015
  • 주석도금폐액으로부터 이온교환수지를 이용하여 주석을 회수하는 연구를 하였다. 주석 흡착이 가능한 3종류의 이온교환수지를 사용하여 기초 실험한 결과 tertiary기능기를 가진 이온교환수지는 주석을 흡착하지 못하였고, iminodiacetic 기능기를 가진 이온교환수지는 주석의 흡착률은 높으나, 불순물 함량이 높았으며, ethylhexyl-phosphar의 기능기를 가진 이온교환수지는 주석의 흡착률은 낮으나 pH 조절에 따라 불순물의 제어가 가능하였다.

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수분배기 측면에서 본 진공배기 계산

  • In, Sang-Ryeol
    • Proceedings of the Korean Vacuum Society Conference
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    • 2014.02a
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    • pp.149.2-149.2
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    • 2014
  • 진공용기를 배기하기 시작하면 짧은 시간 동안은 공기의 배기가 주를 이루지만 그 후에는 표면 방출 기체의 배기가 이어지고 표면방출 기체의 대부분은 물이라는 것은 누구나 알고 있는 사실이다. 그러나 배기 계산을 할 때는 막상 물 보다는 공기의 일부로 생각하거나 수분을 다른 기체들과 유사하게 다루는 것에 익숙해져 있다. 이런 계산 결과는 실제 상황을 재현하지 못할 뿐만 아니라 일반적으로 배기능력을 과대평가하게 만들어서 공정 계획대로 진공 시스템을 운전하는 것을 불가능하게 만든다. 물은 일반적인 기체와는 성격이 아주 다르다. 다른 기 체 분자들의 흡착 에너지가 ~0.3 eV이고 기름분자가 ~1 eV 정도인 것에 반해 물은 0.55 eV 내외로 상온에서도 비교적 흡착을 잘하고 또 적당히 방출도 일어나는 특별한 특성 때문에 용기 압력을 지배하면서도 신속한 배기를 방해한다. 만일 이런 물의 흡착률 및 방출률을 제대로 수치화할 수 있다면 배기 계산을 훨씬 현실화할 수 있다. 물의 흡착률은 물분자의 부착계수가 지배하고 방출률은 체류시간에 의해 결정되지만 표면상태에 따라 천차만별이므로 얼마라고 확정하기 어렵다. 우선 이번에는 물의 부착계수 최대값을 0.1 정도로 잡고 흡착량에 따라 직선적으로 줄어드는 것으로 가정하며, 물의 표면 체류시간도 몇 가지 값으로 가정해서 0-D 입자 평형 계산을 수행하여 특정 시스템에서 얻은 실험 결과와 비교하려고 한다. 앞으로 몬테카를로 방법과 연계하여 3차원적 분석을 할 수 있는 코드로 발전시켜 나갈 예정이다.

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A Study on the Relationship between the Pore Volume Distributions of Some Adsorbents Including Charcoal and the Rates of Adsorption of a Number of Cigarette Aerosol Ingredients such as Tar, Nicotine and etc. (활성탄을 포함하는 몇 가지 흡착제의 동공부피 분포와 이들의 흡착제에 대한 타르, 유기산 등 연초 에어로솔 성분의 흡착률과의 관련성)

  • Ick Kyun Kang;Sang Hyun Han;Yong Kwon Kim;Eun Hee Cha
    • Journal of the Korean Chemical Society
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    • v.33 no.4
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    • pp.350-356
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    • 1989
  • The analysis of adsortion behaviors of some cigarett aerosol ingredients such as tar, nicotine, carbon monoxide and a number of organic acids has shown that the rates of adsorption of the adsorbates of lower boiling point had increased in accordance with increasing cumulative pore volume, while that of higher doiling point decreased with increasing pore volume of smaller radius. The adsorbents used here were charcoal, silica gel, alumina, and activated clay. The common principle that the adsorbents of greater specific surface area adsorb the larger amount of adsorbates appeared to be disturbed in the adsortion of higher boiling point adsorbates. This confirmation was made mainly by analyzing the adsorption behaviors with regard to the pore volume distributions evaluated on the bases of desorption isotherms.

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Adsorption/desorption of CO2 on Activated Carbon Fibers Using Electric Swing Adsorption (활성탄소섬유상에서 전기변동법을 이용한 CO2의 흡/탈착)

  • Shim, JaeWoon;Moon, SeungHyun
    • Korean Chemical Engineering Research
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    • v.43 no.3
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    • pp.432-437
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    • 2005
  • An electric swing adsorption (ESA) process for recovering highly pure $CO_2$ from the mixed gases was tested. In this study, activated carbon fibers were used as an adsorbent. The activated carbon fibers showed fast adsorption rate and the high adsorption capacity for $CO_2$ adsorption under the condition of the ambient pressure. Activated carbon fiber with higher specific surface area was suitable to repeated adsorption-desorption cycle process, showing consistent breakthrough curve. Especially, the regeneration method by vacuum combined with ESA improved the performance of desorption process by an additional 17% regeneration efficiency compared to a vacuum only method, and showed the high regeneration efficiency at comparatively low 7-8 Wh energy.

Anion Adsorption Properties of Organobentonites Modified by Cationic Polymers (양이온 폴리머를 이용한 유기벤토나이트의 음이온 흡착특성)

  • 윤지해;황진연;이효민;고상모;유장한
    • Journal of the Mineralogical Society of Korea
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    • v.17 no.2
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    • pp.147-155
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    • 2004
  • Anion adsorption properties of organobentonites modified by two cationic polymers, hexadecyltrimmethylammonium (HDTMA) and cetylpyridinum (CP), were investigated. The organobentonites showed the significant expansion of basal spacing to 42.0 $\AA$ at room temperature. The adsorption experiments were conducted for the 0.2 g of organobentonites with 40 mL solutions of various concentrations of anions such as nitrate, sulfate and phosphate. As a result, the organobentonites showed excellent adsorption capacities for those anions whereas untreated bentonite showed very low adsorption capacity. Adsorption rate of HDTMA-bentonite was about 90% for 100 mg/L solutions of nitrate and phosphate, and that of CP-bentonite was 97% for 100 mg/L solution of nitrate. Adsorption behaviors were slightly different for the different organobentonites and anions. Both organobentonites showed relatively higher adsorption rate for nitrate and phosphate than sulfate. Therefore, these organobentonites showing high anion adsorption capacities can be used far the removal of deleterious anions in the treatment of environmental pollution.

Synthesization and Characterization of Pitch-based Activated Carbon Fiber for Indoor Radon Removal (실내 라돈가스 제거를 위한 Pitch계 활성탄소섬유 제조 및 특성연구)

  • Gwak, Dae-Cheol;Choi, Sang-Sun;Lee, Joon-Huyk;Lee, Soon-Hong
    • Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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    • v.15 no.3
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    • pp.207-218
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    • 2017
  • In this study, pitch-based activated carbon fibers (ACFs) were modified with pyrolysis fuel oil (PFO). Carbonized ACF samples were activated at $850^{\circ}C$, $880^{\circ}C$ and $900^{\circ}C$. A scanning electron microscope (SEM) and a BET surface area apparatus were employed to evaluate the indoor radon removal of each sample. Among three samples, the BET surface area and micropore area of ACF880 recorded the highest value with $1,420m^2{\cdot}g^{-1}$ and $1,270m^2{\cdot}g^{-1}$. Moreover, ACF880 had the lowest external surface area and BJH adsorption cumulative surface area of pores with $151m^2{\cdot}g^{-1}$ and $35.5m^2{\cdot}g^{-1}$. This indicates that satisfactory surface area depends on the appropriate temperature. With the above scope, ACF880 also achieved the highest radon absorption rate and speed in comparison to other samples. Therefore, we suggest that the optimum activation temperature for PFO containing ACFs is $880^{\circ}C$ for effective indoor radon adsorption.