• 제목/요약/키워드: continuous adsorption process

검색결과 73건 처리시간 0.023초

아민화 아크릴계 이온교환섬유의 폐수 중 Linear Alkylbenzene Sulfonate 흡착에 관한 연구 (Studies on the Adsorption of Linear Alkylbenzene Sulfonate from Waste Water by Fibrous Aminated Acrylic ion-Exchanger)

  • 황택성;박진원;김원종
    • 폴리머
    • /
    • 제26권4호
    • /
    • pp.516-522
    • /
    • 2002
  • 4급 암모늄기를 관능기로 갖는 아민화 아크릴계 이온교환섬유를 이용하여 연속식 흡착공정 중 linear alkylbenzene sulfonate(LAS)의 흡착특성을 확인하였다. 아민화 아크릴계 이온교환섬유의 LAS흡착성능은 온도가 증가함에 따라 증가하였으며 $40^{\circ}C$에서 최적 흡착성능을 나타내었다. 또한 컬럼 베드 충진비(L/D)의 변화에 따른 LAS 이온의 흡착능은 L/D>2에서 최대 흡착능을 나타내었다. pH 변화에 따른 LAS이온 흡착능은 pH가 증가함에 따라 증가하는 경향을 나타내었고, pH 7에서 최대 흡착능을 나타내었다. 유속변화에 따른 LAS 흡착능은 유속이 증가할수록 낮아졌으며 농도가 높을수록 떨어졌다.

Sequential adsorption - photocatalytic oxidation process for wastewater treatment using a composite material TiO2/activated carbon

  • Andriantsiferana, Caroline;Mohamed, Elham Farouk;Delmas, Henri
    • Environmental Engineering Research
    • /
    • 제20권2호
    • /
    • pp.181-189
    • /
    • 2015
  • A composite material was tested to eliminate phenol in aqueous solution combining adsorption on activated carbon and photocatalysis with $TiO_2$ in two different ways. A first implementation involved a sequential process with a loop reactor. The aim was to reuse this material as adsorbent several times with in situ photocatalytic regeneration. This process alternated a step of adsorption in the dark and a step of photocatalytic oxidation under UV irradiation with or without $H_2O_2$. Without $H_2O_2$, the composite material was poorly regenerated due to the accumulation of phenol and intermediates in the solution and on $TiO_2$ particles. In presence of $H_2O_2$, the regeneration of the composite material was clearly enhanced. After five consecutive adsorption runs, the amount of eliminated phenol was twice the maximum adsorption capacity. The phenol degradation could be described by a pseudo first-order kinetic model where constants were much higher with $H_2O_2$ (about tenfold) due to additional ${\bullet}OH$ radicals. The second implementation was in a continuous process as with a fixed bed reactor where adsorption and photocatalysis occurred simultaneously. The results were promising as a steady state was reached indicating stabilized behavior for both adsorption and photocatalysis.

연속반응기에서 Agar를 담체로 고정한 조류 Spirulina의 중금속 흡착특성 (Biosorption Characteristics of Heavy Metal in the Continuous Reactor Packed with Agar Immobilized Algae, Spirulina)

  • 신택수;연익준;김재용
    • 환경위생공학
    • /
    • 제13권1호
    • /
    • pp.174-184
    • /
    • 1998
  • Biosorption characteristics were investigated to discuss the use of agar entrapped Spirulina to remove of heavy metal ions from polluted waters. Agar immobilized algae were used as bioadsorbent in continuous reactor for heavy metal ions removal. The process solution contains Pb, Cu, and Cd as single ion and binary ions. In the adsorption of single heavy metal ions by agar immobilized Spirulina, the adsorption reached within 1hr and observed diffusion limitation differed from the free algal cell adsorption. The optimum pH for the adsorption of heavy metals was 4.5 but the influence of pH decreased less than that of free algal cell. Also, the adsorption characteristics of single heavy metal ions with agar immobilized Spirulina fitted the BET isotherm. Both of experiments of free algal cell and agar immobilized algae showed higher removal efficiency in the single ion solutions than binary ions solutions. The experimental results in the packed column with agar immobilized algae were over 90% of removal efficiency for the Pb, Cu, and Cd in single ion solutions.

  • PDF

Applicability of Composite Beads, Spent Coffee Grounds/Chitosan, for the Adsorptive Removal of Pb(II) from Aqueous Solutions

  • Choi, Hee-Jeong
    • 공업화학
    • /
    • 제30권5호
    • /
    • pp.536-545
    • /
    • 2019
  • An experiment was conducted to evaluate the adsorptive removal of Pb(II) from an aqueous solution using a mixture of spent coffee grounds and chitosan on beads (CC-beads). Various parameters affecting the adsorption process of Pb(II) using CC-beads were investigated. Based on the experimental data, the adsorption kinetics and adsorption isotherms were analyzed for their adsorption rate, maximum adsorption capacity, adsorption energy and adsorption strength. Moreover, the entropy, enthalpy and free energy were also calculated by thermodynamic analysis. According to the FT-IR analysis, a CC-bead has a very suitable structure for easy heavy metal adsorption. The process of adsorbing Pb(II) using CC-beads was suitable for pseudo-second order kinetic and Langmuir model, with a maximum adsorption capacity of 163.51 (mg/g). The adsorption of Pb(II) using CC-beads was closer to chemical adsorption than physical adsorption. In addition, the adsorption of Pb(II) on CC-beads was exothermic and spontaneous in nature. CC-beads are economical because they are inexpensive and also the waste can be recycled, which is very significant in terms of the continuous circulation of resources. Thus, CC-beads can compete with other adsorbents.

이온교환 칼럼 충진비의 변화가 도금폐수 중 니켈이온 흡착에 미치는 영향 (Effect of Packing Density of ion-Exchange on the Nickel Adsorption Column in Electroplating Rinse Water)

  • 황택성;이진혁
    • 폴리머
    • /
    • 제26권5호
    • /
    • pp.551-558
    • /
    • 2002
  • 술폰산형 섬유이온교환체를 이용하여 도금 폐수 중 니켈 이온 분리를 위해 각각의 조건에 따른 니켈 이온에 대한 흡착 특성을 관찰하였다. 술폰산형 섬유이온교환체의 함수율은 술폰화도 극성이 클수록 크게 나타났으며 이온교환용량은 술폰화도가 증가함에 따라 증가하였으며 술폰화도 16%에서 3.38 meq/g로 높게 나타났다. 니켈이온의 흡착은 pH 변화에 따라 크게 변화하지 않았고 모든 흡착은 10분 이내에 약 7.5 mg/min의 흡착속도로 매우 빠르게 평형에 도달하였다. 재생 시 흡착용량은 7회까지 3.15 meq/g으로 거의 100% 가까이 탈착되었으며 그 이상에서는 2.01 meq/g으로 약간 감소하는 것으로 보아 본 연구에 사용한 이온교환체는 내구성에 문제가 없는 것으로 판단되었다. 한편 흡착평형 시간은 L/D의 값이 증가함에 따라 선형적으로 증가하였으며, 최대 흡착용량은 각각 2.71∼3.01 meq/g으로 약간 증가하였고 L/D의 변화에 크게 영향이 없는 것으로 보아 L/D<2로 흡착칼럼의 설계가 가능할 것으로 사료되었다. 또한 이온교환 섬유의 충전비가 일정할 때 pH 변화에 따른 니켈 이온의 흡착량은 산성 pH에서는 큰 변화가 없는 것으로 보아 도금수세액의 pH가 산성인 점을 고려할 때 pH 5 이하가 적합한 것으로 판단되었다.

Wastewater treatment using a hybrid process coupling adsorption on marl and microfiltration

  • Maimoun, Bakhta;Djafer, Abderrahmane;Djafer, Lahcene;Marin-Ayral, Rose-Marie;Ayral, Andre
    • Membrane and Water Treatment
    • /
    • 제11권4호
    • /
    • pp.275-282
    • /
    • 2020
  • Hranfa's marl, a local natural mineral, is selected for the decontamination by adsorption of aqueous effluents in textile industry. Its physicochemical characterization is first performed. It is composed mainly of Calcite, Quartz, Ankerite and Muscovite. Its specific surface area is 40 ㎡ g-1. Its adsorption performance is then tested in batch conditions using an industrial organic dye, Bemacid Red E-TL, as a model pollutant. The measured adsorption capacity of Hranfa's marl is 16 mg g-1 which is comparable to that of other types of natural adsorbents. A hybrid process is tested coupling adsorption of the dye on marl in suspension and microfiltration. An adsorption reactor is inserted into the circulation loop of a microfiltration pilot using ceramic membranes. This makes possible a continuous extraction of the treated water provided that a periodic replacement of the saturated adsorbent is done. The breakthrough curve obtained by analyzing the dye concentration in the permeate is close to the ideal one considering that no dye will cross the membrane as long as the adsorbent load is not saturated. These first experimental data provide proof of concept for such a hybrid process.

토양의 규산 흡착 카이네틱에서 2단계 흡착 기작 (Two Stage Process Mechanism of Silica Adsorption by Soil in Adsoption Kinetics)

  • 이상은;정광용
    • 한국토양비료학회지
    • /
    • 제29권2호
    • /
    • pp.107-112
    • /
    • 1996
  • 토양의 규산 흡착기작을 밝히고자 continuous stirred-flow(연속진탕흘림) 법을 이용하여 시간 경과에 따른 규산 흡착량 변화에 대한 실험을 $25^{\circ}C$, pH 3수준(5, 6.5, 8)에서 실시하였다. 규산 흡착량은 실험기간내 최대 흡착량을 보이지 않고 계속 증가 하였다. 시간에 따른 규산의 흡착과정을 2단계로 구분 하였고, 1단계 반응과정은 아래의 지수함수식에서 고도의 유의성있는 상관관계를 보였다 $$R_{ad}=K_a*(Q_{OH}^S)^n$$ 여기서 $R_{ad}$는 규산흡착속도($Si\;{\mu}mal/min$), $Q_{OH}^S$는 알칼리 투여를 통하여 생성된 토양표면 음전하량, $K_a$와 n 은 상수이다. 1단계 반응과정의 n값은 1.1로 한자리 결합(monolantate ligand bonding)에 의한 흡착과정인 것으로 나타났다. 2단계 과정은 아래 식에서 고도의 유의성있는 상관관계를 보였다. $$R_{ad}=K_b*(pH)$$ 이때 $K_b$ 는 비례상수로, pH 증가에 따른 규산 흡착 속도의 증가 추세가 지수 함수적으로 감소하는 경향을 보였다.

  • PDF

Regeneration and modeling of fixed-bed adsorption of fluoride on bone char

  • Hugo D. Garcia;Rigoberto Tovar;Carlos J. Duran;Virginia Hernandez;Ma. R. Moreno;Ma. A. Perez
    • Advances in environmental research
    • /
    • 제12권1호
    • /
    • pp.17-40
    • /
    • 2023
  • This article presents studies of the adsorption process in a continuous system of fluoride solutions at a concentration of 30 mg/L using a bone char packed in fixed-bed columns, as well as regeneration studies in the same system using HNO3, HCl and NaOH at 0.01, 0.1 and 1 M. The Thomas Model, Artificial Neural Networks (ANNs), Numerical Integration and Mass Transfer Zone were used for the modeling of asyemmetrical breakthrough curves obtained from the fluoride adsorption on bone char. The maximum adsorption capacity of the breakthrough curves was estimated, and various design parameters of the columns were obtained for the different operating conditions. Results showed that an improvement in the modeling capabilities of the Thomas model can be obtained using ANNs. Moreover, ANNs are useful for determining reasonable and accurate design parameters of packed-bed adsorption columns. This modeling approach can be useful for the process system engineering of dynamic adsorption systems involved in the field of water treatment and purification. It is important to highlight that the obtained results indicate that, when using HCl or HNO3 at a concentration of 0.1 M, a large number of adsorption-desorption cycles are obtained and, therefore, the highest values of adsorption capacity, which leads to a reduction in operation costs.

활성탄집진시설의 시간변화에 따른 총탄화수소의 집진효율성 및 경제성에 관한 연구 (A Study on Collection Efficiency And Economy of Total Hydrocarbons in Accordance with Time Changes at Activated Carbon Collection Facility)

  • 김성중;한대희;우인성
    • 대한안전경영과학회지
    • /
    • 제16권2호
    • /
    • pp.231-236
    • /
    • 2014
  • In this study, the changes in collection efficiencies due to the time changes of activated carbons were ascertained, and in order to identify the magnitude of adsorption, the before-use and after-use iodine adsorption values were analyzed. In addition, as a result of examining the characteristics of continuous process and non-continuous process and as a result of investigating whether the emission standards would be maintained, the continuous process and printing facilities were seen as not being able to maintain the emission standards. Also were found, in the case of non-continuous process,-taking into consideration the special nature of the job -for 4${\o}$ palletized charcoal, a collection efficiency near 50% was shown even after 96 hours. Also, when the inlet concentration was about 300ppm, it is thought that the emission standards would be maintained if the activated carbons are replaced within at least 96 hours in the case of 4${\o}$ palletized charcoal and the use was deemed pointless in the case of carbon. The results of this study are expected to provide assistance in selecting replacement periods for activated carbons and in selecting absorbents at the project sites, and are expected to be of significant help in the selection of precipitators that can collect total hydrocarbons for compliance of the emission standards.

AOPP-g-AN 섬유이온교환체를 이용한 간수로부터 우라늄 이온 흡착특성에 관한 연구 (A Study of Adsorption Characteristics of Uranium ion Using Amidoximated PP-g-AN Fibrous ion-exchanger in Brine Water)

  • 황택성;최재은;이재천
    • 폴리머
    • /
    • 제26권1호
    • /
    • pp.121-127
    • /
    • 2002
  • Acrylonitrile을 그라프트시킨 아미드옥심화 polypropylene 섬유이온교환체(AOPP-g-AN)의 충전 bed 높이를 변화시켜 간수 중 우라늄 이온 흡착 특성 및 흡착 공정 특성을 관찰하였다. 아미드옥심형 섬유이온교환체의 팽윤율은 그라프트율 100%, 물과 과산화수소 용매에 대하여 각각 8.54, 8.87 g/g을 나타내었다. 이온교환용량은 그라프트율이 증가함에 따라 증가하였으며, 그라프트율 100%에서 3.99 meq/g으로 최대를 나타내었다. 회분식 흡착에서 우라늄 흡착은 10분 이내에 초기 흡착 평형에 도달하며, 흡착 속도는 9.50 mg/min으로 나타났다. 최종 흡착 용량은 3.95 meq/g이었으며, pH에 따른 흡착 특성 변화는 관찰되지 않았다. 충전비에 따른 연속식 흡착시 흡착 용량은 L/D=1에서 3.92 meq/g으로 최대를 나타내었으며, L/D<2에서 편류 및 불균일 흡착에 의한 2단계 과정으로 파과가 나타남을 확인하였다. 실제 간수에 대한 우라늄 흡착 실험 결과, 흡착 용량 및 파과시간은 각각 3.63 meq/g, 26 min으로 모의용액과 비교 시 주목할만한 흡착능 저하는 관찰되지 않았다.