• 한국환경과학회지
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• 제12권10호
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• pp.1055-1060
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• 2003

Adsorption on goethite of individual component from a solution containing phosphate, sulfate, or copper ion was investigated. Competitive adsorption in the binary and ternary solution systems composed of phosphate, sulfate, and copper ions was also investigated. In competitive adsorption systems with phosphate and sulfate ions, the presence of phosphate ion reduced the adsorption of sulfate ion largely. On the other hand, the presence of sulfate ion caused only a small decrease in phosphate adsorption. This result suggests that phosphate ion is a stronger competitor for adsorption on goethite than sulfate ion, which is consistent with the higher affinity of phosphate for the surface compared to sulfate ion. Compared to the results from single-sorbate systems, adsorption of copper ion in the binary system of sulfate ion and copper ion was found to be enhanced in the presence of sulfate ion. Addition of sulfate ion to the binary system of copper ion and phosphate ion resulted in a small enhancement in copper sorption. This result implies that the presence of sulfate ion promotes adsorption of the ternary complex FeOHCuSO$_4$. The adsorption isotherms could be well described by the Langmuir adsorption equation.

• 한국환경과학회지
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• 제12권9호
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• pp.1011-1016
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• 2003

Adsorption of phosphate, sulfate, and copper ion to goethite was investigated. Goethite was prepared in the alkaline solution. In the single adsorbate systems, the final equilibrium plateau reached within 20 min. The adsorption isotherms of the individual ions could be well described by the Langmuir equation. The maximum adsorption capacities (q$\_$max/) were calculated as 0.483 m㏖/g and 0.239 m㏖/g at pH 3 for phosphate and sulfate ion, and 0.117 m㏖/g at pH 6 for copper ion, respectively, In competitive adsorption system with phosphate and sulfate, phosphate ion was a stronger competitor for adsorption on goethite than sulfate ion, which was consistent with higher affinity of phosphate ion for the surface compared to sulfate ion. The existence of sulfate ion enhanced the adsorption of copper ion but the adsorption of sulfate was inhibited when copper ion was present.

• 한국환경과학회지
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• 제11권3호
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• pp.257-262
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• 2002

The hydroxyapatite(HAp) for the present study was prepared with the wastewater sludge from semiconductor fabrication process and it was crystallized in an electric furnace for 30 min at 90$0^{\circ}C$. The adsorption characteristics of HAp for phosphate ion in aqueous solution has been investigated. The adsorbed ratio of phosphate ion for HAp were investigated according to the reaction time, amount of HAp, concentration of standard solution, pH of solution, and influence of concomitant ions. The amount of adsorbed phosphate ion decreased with the increase of pH due to the mutual electrostatic repulsion between adsorbed phosphate ions and competitive adsorption between phosphate ion and OH- ion in aqueous solution. The maxium amount of the adsorption equilibrium for phosphate ion was about 24 mg/g of HAp. The HAp would likely to be a possible adsorbent for the removal of phosphate ion in the waste water.

• 상하수도학회지
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• 제27권1호
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• pp.121-128
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• 2013

The concern for dissolved phosphate in water/wastewater has been increasing because of the risk for eutrophication. A variety of conventional and advanced technologies were applied to meet the enforced new regulation of phosphate around the world. However, there still remained a lot of challenge because most introduced/developed method, for example, biological and physic-chemical treatment is not easy to satisfy the new regulation of phosphate in water. In order to meet the new regulation, the application of ion exchanger has been tried which showed that the removal efficiency for phosphate was strongly determined by in the presence of the competing ion, especially sulfate. As results, a new class of ion exchanger governed by ligand exchange was developed and investigated to increase the selectivity for phosphate. The current study using organic/inorganic anion exchanger developed with Lewis acid-base interaction confirms the selectivity for phosphate over sulfate. According to isotherm test and column test, the value of the maximum phosphate uptake (Q) showed 64 mg/g as $po{_4}^{3-}$ and the breakthrough for phosphate occurs after 1000 min and completely finishes at 2500 min, respectively.

• 상하수도학회지
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• 제19권4호
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• pp.404-410
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• 2005

A series of batch type adsorption experiments were performed to remove aquatic phosphorus, where the layered double hydroxide (HTAL-CI) was used as an powdered adsorbent. It showed high adsorption capacity (T-P removal: 99.9%) in the range of pH 5.5 to 8.8 in spite of providing low adsorption characteristics (pH<4). The adsorption isotherm was approximated as a modified Langmuir type equation, where the maximum adsorption amount (50.5mg-P/g) was obtained at around 80mg-P/L of phosphorus concentration. A phosphate ion can occupy three adsorption sites with a chloride ion considering the result that 1 mol of phosphate ion adsorbed corresponded to the 3 moles of chloride ion released. Although the chloride ion at less than 1,000mg-CI/L did not significantly affect the adsorption capacity of phosphate, carbonate ion inhibited the adsorption property.

• Journal of Plant Biology
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• 제21권1_4호
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• pp.33-38
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• 1978

Phosphate absorption from a Na2H32PO4 solution by Oryza sativa L. was studied in order to elucidate kinetic mechanisms of ion transport. The rates of phosphate absorption from different concentraitons indicated the presence of dual mechanisms in root tips, one in the low (1$\times$10-6 to 8$\times$10-5M) and the other in the high (1$\times$10-4 to 8$\times$10-3M). A phosphate compensation point of phosphate transport was revealed with a 1$\times$10-6M solution of Na2H32PO4. The kinetic model that ion transport involves an exchange reaction of absorption and desorptin is prosposed as follows: where C represents an ionic-specific organic carrier in the membrane; M, Mo and Mi are the mineral ions, M-outside and M-inside; MC is a carrier-ion complex; and the K's represent rate constants. In this model, the Mi velocity, v, is given by: {{{{v= {dMi} over {dt}= {(K1K3Mo-K2K4Mi) Ct} over {(K2＋K3)＋K1Mo＋K4Mi} }} where Ct is equal to C＋MC, and t is time.

• 한국진공학회지
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• 제7권s1호
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• pp.30-36
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• 1998

The plasma-spray technique is currently the most frequently used method to produce calcium phosphate coatings. Hydroxyapatite(HAp), one form of calcium phosphate, is preferred by its ability to form a direct bond with living bone, resulting in improvements of implant fixation and faster bone healing. Recently, concerns have been raised regarding the viable use and long-term stability of plasma-spray HAp coatings due to its nature of comparatively thick, porous, and poor bonding strength to metal implants. Thin layers (maximum of few microns) of calcium phosphate were formed by an e-beam evaporation with and without ion bombardments. The Ca/P ration of film was controlled by either using the evaporants having the different ration of Ca/P with addition of CaO, or adjusting the ion beam assist current. The Ca/P ration had great effects on the structure formation after heat treatment and the dissolution bahavior. The calcium phosphate films produced by IBAD exhibited high adhesion strength.

• 한국산학기술학회논문지
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• 제8권2호
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• pp.372-379
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• 2007

전로슬래그는 폐수 중에 함유된 인산염을 고형물 형태로 제거하는데 유용하게 사용될 수 있다 본 연구는 전로슬래그를 이용하는데 있어서 폐수의 초기 조건에 따라 전로슬래그로 인한 폐수의 pH, 알칼리도 그리고 양이온 용출변화에 따른 인산염 제거 등에 관하여 연구하였다. 실험대상 폐수의 pH를 0.5 단위로 7.0부터 8.5까지 다른 초기조건에서 폐수의 pH는 10시간 내에 급격하게 pH 11이상까지 상승하였다. 알칼리도는 pH보다는 급격하게 상승하지는 않았지만 반응시간 10 시간이 경과한 후 꾸준하게 상승하였다. 인산염 제거는 pH상승, 알칼리도 상승과 함께 반응시간 10시간까지 급격하게 제거되다가 서서히 제거되는 양상을 보였다. 반응시간 27시간 경과 후 그리고 36 시간 경과 후 전로슬래그에 함유된 마그네슘 이온 용출 농도를 측정한 결과 2.0 mg/L과 4.3 mg/L 수준까지 지속적으로 용출 되었다. 본 실험 결과 전로슬래그에 함유된 마그네슘이 용출되었기 때문에 물속에 암모니아가 존재한다면 인산염과 함께 스트루바이트 형태의 결정체로 인이 제거될 수 있음을 확인하였다.

• 한국응용과학기술학회지
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• 제37권5호
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• pp.1222-1228
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• 2020

Tin bis(monohydrogen orthophosphate) monohydrate 물질의 흡착 성질에 관하여 KCl 수용액을 통하여 조사하였다. 금속이온 농도와 pH를 변화시키면서 어떻게 달라지는지 화학평형에 바탕을 두고 data를 분석하였다. 금속이온들의 흡착 data는 Langmuir 흡착식에 넣어 Langmuir 수치들을 얻는 데 사용되었다. Tin phosphate는 산성에서 이온교환 화합물로 작용하였으며, 2가의 전이금속이온에 대해 Cu⁺² > Co⁺² > Ni⁺²의 순서로 선택적 흡착성질을 나타내었다. 약한 산성 이온 교환체에서와 같이 금속이온의 교환은 tin phosphate의 선택성을 결정하는데 결정적 역할을 하였다. 모든 경우에서 흡착의 정도는 온도와 농도의 증가와 함께 증가하였다. Lnngmuir 수치들은 흡착과정 동안의 엔트로피, 엔탈피, 자유에너지 변화량같은 열역학적 함수들을 계산하는데 이용되었다.

• 자원리싸이클링
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• 제12권4호
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• pp.38-43
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• 2003

인산염은 유기물의 성장에 필요한 중요한 영양물질이나 아주 미량이 필요하여 폐수 중의 인산염은 오염물질로 작용하며 수생 생태계에 영향을 미친다. 따라서 고농도의 인산염에 대하여 칼슘을 이용한 침전법를 사용하여 인산염의 제거에 관한 연구를 수행하였으며 폐수의 재이용 방면에 대해 고찰하였다. 인산염의 침전 제거 시 pH 조건은 pH 6에서 pH 12로 고려하였는데, pH 12에서 가장 좋은 효율을 나타내었다. 또한 인산염은 침전반응에 의하여 칼슘을 침전반응 당량비의 0.5배 투입한 경우까지 제거율이 급격히 증가하는 경향을 나타내었으며 인산염의 잔존량은 0.0027 mM 까지 낮추는 효과를 가져왔다. 불소가 오염물로 존재하는 상황에서 인산염을 제거하기 위한 실험은 pH 및 농도비에 따라 진행되었으며 pH가 증가할수록 인산염의 제거율은 증가하였다. 또한 인산염 : 불소의 농도비가 증가하여도 인산염의 제거율은 크게 영향을 받지 않은 것이 관찰되었다.