• Journal of Industrial Technology
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• v.27 no.A
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• pp.203-209
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• 2007

본 연구는 목재로서 활용가치가 적은 수피(bark)를 활용하여 수질오염물질을 제거할 수 있는 여과 시스템에 대한 기초연구로서 소나무의 일종인 loblolly pine(Pinus taeda L.) 수피의 인 ($PO_4-P$) 흡착특성을 연구하였다. 실험에 사용된 수피는 입상형태로서 polyallylamine hydrochloride로 전처리하여 회분식 등온 흡착실험을 수행하였다. 회분식 등온흡착실험은 수용액 pH 3~pH 8범위에서, 인의 농도별(10, 20, 30, 40 mg/L)로 수행하였다. pH 5에서 가장 높은 인 제거 효율을 나타냈으며, 수용액의 pH는 실험 후 pH 3으로 감소하였다. 이러한 감소는 수피에 의한 phosphate의 흡착이 Lewis acid-base 반응으로서 이 과정에서 $H^+$의 방출로 인하여 나타난 현상인 것으로 여겨지며, 주된 반응 메카니즘은 더 연구할 필요성이 있다. 인 흡착은 초기에 빠른 속도로 진행되었으며 대략 200분 이후에 평형에 도달하였고, 시간이 지날수록 흡착양이 증가하는 경향을 보였다. 인의 흡착특성 결과는 Langmuir 등온흡착식과 Freundlich 등온흡착식으로 설명될 수 있으며, 등온흡착식 적용결과, 흡착제에 대한 최대 흡착능은 7.14 mg/g 이며 다른 흡착제와 비교하여 더 높았다. 실험결과와 모델에 의한 흡착능을 비교하고자 pseudo second-order model을 적용하여 흡착 동역학 상수를 구하였다. 또한 EDXA분석으로 회분식 흡착실험 후 수피와 인이 결합되어있는 것을 확인할 수 있었다.

• Korean Journal of Environmental Agriculture
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• v.26 no.2
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• pp.124-130
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• 2007

Excess application of paper mill sludge (PMS) in field can limit phosphorus uptake by crops because aluminum presented in the sludge can fix or adsorb available phosphorus which is necessary for crop growth. To investigate phosphorus (P) adsorption characteristics of PMS, we examined P adsorption maximum $(X_m)$ using Langmuir isotherm and P adsorption energy constant $(K_f)$ using Freundlich isotherm for PMS without alum, PMS with alum, and composted PMS with alum through a laboratory incubation test. The maximum P adsorption capacities were 800 ${\mu}g\;g^{-1}$ in soil, 47 $mg\;g^{-1}$ in PMS without alum and 61 $mg\;g^{-1}$ in PMS with alum. P adsorption capacity with alum treatment for PMS increased by 30%. That of PMS compost was 68 $mg\;g^{-1}$ and showed that composting increases 11% of P adsorption. Freundlich constant $K_f$ was 22 in check soil, while $K_f$ values in PMS without alum and in PMS with alum were 398 and 426, respectively. After composting, $K_f$ value of PMS compost significantly increased as 1,819. In conclusions, p adsorption capacity for PMS were increased by alum treatment or composting and therefore excess or continuous land application of alum-amended or composted PMS can limit P uptake for crops by reducing available P in sell.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 1997.10a
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• pp.65-66
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• 1997

우리나라의 대부분 하천과 인공댐의 경우 조류발생에 기여하는 영양염은 질소, 인 그리고 규소 등인데 특히 인이 생산제한 인자로 작용하고 있다. 따라서 인을 적절히 제거할 경우에는 조류 발생에 의한 수질의 악화와 수이용의 저해요인을 배제할 수 있어 이에 대한 연구가 많이 진행되어 왔다. 지금까지와 연구는 인의 화학적 응집 침전법, 생물학적 처리법에 대하여 수행되어 왔으나 설비자금, 운영비, 운전기술, 슬러지 생성 그리고 제거효율 등에서 만족스런 결과가 도출되지 못하여 현장 적용을 하지 못하고 있는 실정이다. 이러한 현실을 감안하여 우리의 자연 환경에서 쉽게 자할 수 있는 황토를 모재로하여 Al3-과 Fe3-, Ca2-을 적절히 배합하여, 주로 인을 선택적으로 제거하 고자 개발된 황토의 흡착능력 그리고 흡착 메카니즘에 대한 기본적인 연구를 하고자 (1) 등온흡착실험을 통하여 흡착용량을 평가하고 (2) 흡착제거속도를 평 가하였고 (3)파과시간 및 흡착특성을 파악하기 위해 column 흡착실험을 하였다 또한 (4) 황토내의 Al3-, Fe3-과 Ca2- 등이 인의 화학적 흡착에 기여하는 정도를 파악하여 흡착메카니즘을 규명하고자 하였다. 먼저 흡착용량실험을 위하여 PO3-4-P 농도 3ppm의 용액 200mf에 황토 0.2g, 0.5g, 1.0g, 2.0g을 각각 투여한 후 충분한 흡착평형이 일어나게 24시간 동 안 130rpm으로 $25^{\circ}C$ 등온반웅조에서 저어주어 흡착평형에 도달하면 상등액을 GF/C Filter로 여과한 후, 여액에 대해 PO3-4-P의 농도를 Ascrobic he건법으로 측정한 결파, Freundlich 등온흡착식에 의하면 K값은 17.34와 16.28이었으며 1/n 값은 1.32와 1.42로 인흡착 성능이 뛰어난 것으로 평가되었다. 둘째, 흡착속도 실험은 PO3-4-P 농도 1.5ppm의 용액 2f에 259의 황토를 투여하고 충분한 혼합이 일어날 수 있도록 170rpm으로 교반하면서 시간별 용액 의 농도 변화를 측정한 결과, 0.45mg/g/m교의 속도로 15분만에 94.3%의 인 제거 효율을 보였다. 셋째, 직경 12mm의 glass column에 황토를 209 채우고 1.5ppm의 PO34P 용액을 2.Sne11in의 유량으로 통수 시킨 후, 시간에 따른 농도 변화를 측정한 결과, 원수 농도의 50%에 해당하는 파과점까지 약 70시간 만에 도달하였다. 넷째, Al3-, Fe3-과 Ca2- 등이 화학적 흡착에 기여하는 정도를 파악하기 위 하여 황토 2g에 대하여 Hieltijes and Lijklema 방법에 의해 Adsorbed-p, Nonapatite inorganic-P(NAI-P), Apatite-p, Organic-P로 구분하여 분석하고, 총인(Total Phosphorus)을 Standard Methods에 따라 Persulfate digestion후 0.45 m membrane 여지 여과하여 여액에 대해 PO3-4-P의 농도를 Ascorbic Acid 법으로 측정한 결과, NAI-P가 가장 큰 비율을 차지하였고, 부원료로 첨가된 금속 양이온 중 Fe3-이온이 흡착에 기여하는 정도가 가장 큰 것으로 평가되었다.

• Korean Journal of Environmental Agriculture
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• v.22 no.2
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• pp.148-152
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• 2003

The phosphorus(P) adsorption capacities of various filter media were investigated in relation to the size and types of fitter media to screen the optimum condition. The objective of this study was to evaluate the constructed wetland longevity by improving P adsorption capacity. The maximum P adsorption capacities of filter media A($4{\sim}10\;mm$), B($2{\sim}4\;mm$) and C($0.1{\sim}2\;mm$) were 8, 10 and 22 mg/kg, respectively, showing those increased as the filter media size decreased. Among the experimental media, the optimum filter media size was $0.1{\sim}2\;mm$. When the filter Medium was supplemented with organic materials which were piled up and decayed in the constructed wetland, the P adsorption capacity was significantly enhanced Under the conditions of optimum fitter media size, the respective Maximum P adsorption capacities of filter media C when supplemented with Ca, Mg, Al and Fe were higher than that of filter media C. However the addition of Ca, Mg, Al and Fe to constructed wetland were not recommended because of the possibility of their secondary pollution. The maximum P adsorption capacity of filter media C was 22 mg/kg, but this was increased to 36 mg/kg when filter media C was supplemented with 2% oyster shell.

• Journal of Sericultural and Entomological Science
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• v.31 no.1
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• pp.45-54
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• 1989

본 연구에서는 견에 대한 산성염료의 염착기구를 규명하기 위하여 전하수가 다른 산성염료에 의한 흡착실험을 수행하여, 견섬유와 피브로인막의 구조와 염료의 구조를 관련시켜서 산성염료의 흡착거동에 관한 해석을 하였다. 산성염료에 sulfonic acid group이 도입됨에 따라서 partition coefficient(Kp)는 감소하였지만 Langmuir type sorption constant(KL)는 증가하였고, 염욕의 pH와 온도의 증가에 따라서도 Kp, KL 값은 증가하였다. 전하수가 1, 2인 Dye I과 Dye II는 견섬유와 피브로인 막에 대하여 stoichiometric adsorption이 잘 적용될 수 있었으나 전하수가 3인 Dye III는 잘 적용되지 않았다. sulfonic acid group이 산성염료에 도입됨에 따라 각각의 sulfonic acid group의 표준친화력은 감소하였고, 모든 엔탈피 값은 음(-)으로 나타난 반면에 엔트로피 값은 양(+)으로 나타났다. 견섬유와 피브로인 막의 흡착 constant를 비교한 결과, 견 피브로인에 대한 산성염료의 흡착거동은 견 피브로인의 구조에 영향을 받는다는 것을 알 수 있다.

• Journal of Korean Society of Environmental Engineers
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• v.37 no.4
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• pp.246-252
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• 2015

In steel factory, hot roller cleaning process produces a lot of iron oxide particles called as mill scale. Major components of these particles are wustite (FeO), magnetite ($Fe_3O_4$), and hematite ($Fe_2O_3$). In this study, we tried to produce pure magnetite from the mill scale because of the largest phosphate adsorption capacity of the magnetite. The mill scale was treated with acid (HCl+$H_2O_2$), base (NaOH), and acid-base ($H_2SO_4$+NaOH). Batch adsorption tests showed the acid and/or base treatment could increase the phosphate adsorption capacity of the iron oxides from 0.28 to over 3.11 mgP/g. Magnetite, which could be obtained by acid and base treatment of the mill scale, showed the best adsorption capacity. From the kinetic analysis, both Freundlich and Langmuir isotherm well described the phosphate adsorption behavior of the magnetite. In Langmuir model, maximum phosphate adsorption capacity was found to be 5.1 mgP/g at $20^{\circ}C$.

• Journal of Korean Society of Water and Wastewater
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• v.27 no.5
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• pp.631-639
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• 2013

The removal of phosphate from surface water is becoming increasingly vital to prevent problems such as eutrophication, particularly near urban areas. Recent requirements to reduce high concentrations of phosphate rely on physicochemical methods and adsorbents that must be effective even under strict conditions. The phosphate removal efficiencies of two adsorbents, Fe-Mn-Si oxide and Fe-Mn oxide, were investigated and the data used to compare kinetics and isotherm models. The maximum adsorption capacities of the two adsorbents were 47.8 and 35.5 mg-$PO{_4}^{3-}/g$, respectively. Adsorptions in both cases were highly pH dependent; i.e., when the pH increased from 3 to 9, the average adsorption capacities of the two adsorbents decreased approximately 32.7 % and 20.3 %, respectively. The Freundlich isotherm model fitted the adsorption of Fe-Mn-Si oxide more closely than did the Langmuir model. Additionally, anionic solutions decreased adsorption because of competition with the anions in the adsorbing phosphate. Although affected by the presence of competing anions or a humic substance, Fe-Mn-Si oxide has better adsorption capacity than Fe-Mn oxide.

• Journal of Korean Society of Environmental Engineers
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• v.32 no.8
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• pp.761-766
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• 2010

This study was aimed to propose La(III)-zeolite composite which can effectively and simultaneously remove ammonia and phosphate in confined water bodies such as lakes and ponds. The optimum ratio of La(III):zeolite for the simultaneous removal of ammonia and phosphate was 0.0048 La(III) g:1 zeolite g. The drying temperature of La(III)-zeolite composite severely affected phosphate adsorption showing optimum condition at room temperature. It was revealed that the optimum dosage of La(III)-zeolite composite was 4.052 g/L at adsorption time of 90 min. The presence of alkalinity in aqueous solution brought positive effect on phosphate adsorption. Detachment of La(III) from La(III)-zeolite composite, which was dried at room temperature, was not observed in aquous solution. It indicates that La(III)-zeolite composite could effectively block phosphate released from sediment.

• Journal of Korean Society of Water and Wastewater
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• v.26 no.5
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• pp.713-721
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• 2012

In many instances phosphorus is a limiting factor for eutrophication in streams, and lakes. Because wastewater treatment plant itself may be the main phosphorus source in a natural water body, removal of phosphorus in final effluent of wastewater treatment processes is required. Amongst various technologies for phosphorus removal in wastewater, adsorption technology was investigated using activated Ca-loess complex. Ca was added in loess to enhance adsorption capacity and intensity of phosphorus. Ca added loess was activated at a high temperature of $400^{\circ}C$ which turned out to be the optimum temperature. Activated Ca-loess complex below $400^{\circ}C$ had not enough strength to be applied as an activated Ca-loess pallet column in wastewater treatment process. Ca-loess complex which activated above $400^{\circ}C$ lost its adsorption capacity as the loess surface was glassified when the activation temperature reached above $400^{\circ}C$20. Even if adsorption capacity of activated Ca-loess was not very high due to the lack of abundant pores on its surface, adsorption intensity was still high because it was activated with added Ca in loess. Activated loess was made by pallets. The activated loess pallets were filled in a column, and were applied in wastewater treatment process. Using an activated Ca-loess pallet column, total phosphorus (T-P) was reduced from about 0.5 mg/l to lower than 0.1 mg/l in wastewater treatment, and ionic phosphorus (phosphate) was completely removed for the four months of pilot plant operation.

• Journal of the Korean GEO-environmental Society
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• v.15 no.12
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• pp.5-13
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• 2014

In this study, exfoliated vermiculite (EV) coated with glycerol was tested for its abiility to remove phosphorus in aqueous solution. The glycerol modified vermiculite (GS) was prepared with EV/glycerol ratio of 1/4 where glycerol contained 4 mol% $H_2SO_4$ and heated until designated temperature. GS heated at $380^{\circ}C$ showed that the specific surface area was $53.1m^2/g$ and mass loss due to oxidation of carbon was maximum from TGA analysis. Removal of phosphorus using GS heated at $380^{\circ}C$ was well explained by Langmuir isotherm model and maximum sorption capacity of 714.3 mg/kg is comparable or greater than those of other clay orignated sorbents for phosphorus.