• Polymer(Korea)
• /
• v.25 no.6
• /
• pp.789-795
• /
• 2001

In order to recover nickel ion from waste water containing heavy metals, the PAN fibrous ion-exchanger with primary, secondary amine groups and carboxyl group was synthesized by acid and base hydrolysis. The hydrolysis yield of PAN fiber in acid solution was higher than base solution. The swelling ratio and ion-exchange capacity of PAN fiber which was synthesized in 1N $H_2SO_4$ solution at $80^{\circ}C$ for 7 hrs appeared 71.2% and 1.95 meq/g respectively. We investigated that the adsorption of nickel ion was approached 1.44 meq/g at 50 min and the maximum adsorption capacity of ion-exchanger was 2.48 meq/g. We confirmed that the $Ni^{+2}$ adsorption ability of the synthesized PAN fibrous ion-exchanger in this study is excellent.

• Journal of the Korean Electrochemical Society
• /
• v.15 no.4
• /
• pp.256-263
• /
• 2012

This study was performed to investigate the separation of cesium cations by using an electrochemical ion exchanger of nickel hexacyanoferrate($KNiFe(CN)_6$) film electrode. Potential, current, and charge passing through the cyclic voltammograms were measured in singular and binary solutions of 1.0M $NaNO_3$ and 1.0M $CsNO_3$. Before and after each experiment, the structural morphology and atomic composition of $KNiFe(CN)_6$ were analyzed by SEM and EDS, respectively. The ion selectivity of $KNiFe(CN)_6$ was also observed by the voltammograms and atomic compositions measured in the solution alternated between sodium and cesium. As the result of this study, it was found that the electrically switched $KNiFe(CN)_6$ ion exchanger had the significant advantage of 40 times or longer durability than conventional organic or inorganic ion exchanger. It was also shown that the $KNiFe(CN)_6$ ion exchanger had high selectivity for cesium over sodium.

• Membrane Journal
• /
• v.25 no.5
• /
• pp.431-439
• /
• 2015

The study was evaluated and compared to commercial heterogeneous membrane in order to make cation exchange membrane set up the optimal preparing condition. The research findings show that ion exchange resin was added more than 40 wt% in order to show chemical properties of HPVDF higher than commercial heterogeneous membrane. But ion exchange resin was added less than 40 wt% in order to show mechanical properties of HPVDF higher than commercial heterogeneous membrane. According to conditions above, Electrical resistance was $1.83{\Omega}{\cdot}cm^{-1}$, water uptake was 79%, ion exchange capacity was 1.60 meq/g, and burst strength was 0.97 MPa. Also The TDS remove efficiency was measured by approximately 40%.

• Journal of the Korean Chemical Society
• /
• v.14 no.1
• /
• pp.37-43
• /
• 1970

Durch Umsetzung an vernetzten p-lithiumstyrolhaltigen Copolymeren ist es nicht moglich, Austauscherharze mit Benzoylaceton-oder 8-Hydroxy-chinolingruppen mit praktisch brauchbarer Kapazitat herzustellen. Tetraphenylarsoniumchlorid-Gruppierungen enthaltende Austauscher mit einem Gehalt von etwa 1,3 mval/g an funktionellen Gruppen lassen sich aus vernetzten p-lithiumstyrolhaltigen Copolymeren und Triphenyl-arsinoxid herstellen. Aus einer Quecksilber(II)-chlorid-Losung nehmen in wassrigem Dioxan etwa 60% der im Harz befindlichen funktionellen Gruppen Quecksilberionen auf.

• Applied Chemistry for Engineering
• /
• v.8 no.1
• /
• pp.67-75
• /
• 1997

Heterogeneous cation exchange membrane consisting of cation exchange resin particles (diameter of less than $149{\mu}$) which are finely dispersed in a polyethylene matrix, were produced as forms of sheet. The characteristics were measured after treating hot water or saturated sodium chloride. When membranes were treated with hot water or saturated sodium chloride, cation exchange resin particles swell and expand pushing away the polyethylene matrix of membranes. The above treatment results the formation of narrow cavities between a cation exchange resin particles and polyethylene matrix, and the formation of fine micro-cracks on the polyethylene matrix. Thus, we were obtained good physical and electrochemical properties. On the treatment with hot water or saturated sodium chloride, the optimum conditions for good heterogeneous cation exchange membrane were treatment time of 30min and treatment temperature of $90^{\circ}C$.

• Journal of the Korean Ceramic Society
• /
• v.25 no.3
• /
• pp.237-242
• /
• 1988

Ion exchange behavior of glasses was investigated in this study. The used glasses were Soda-limesilica glasses that was produced by float process. In order to analyse effects of ion exchange, some properties were measured; $K^+$ ion penetration depth, compressive stress, compression layer thickness, amount of $K^+$ ion exchange and density, in case of 43$0^{\circ}C$-8h and 45$0^{\circ}C$-6h, and activation energy is 17.0kcal/mole. Further it can be seen that excessive heat treatment brings about stress relaxation.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1997.10a
• /
• pp.137-138
• /
• 1997

1. 서론 : 이온교환막이란 합성 폴리머의 이온교환수지를 막상으로 만든 것으로 고분자 매트릭스에 특정 전하가 고정되어 있어 이러한 성질 때문에 보통의 격막에서는 볼 수 없는 특징을 가지고 있으며 바닷물의 농축에 의한 소금의 제조, 탈염에 의한 공업용수 및 음료수의 제조, 도금공장의 폐수처리, 식품과 의약품공업, 고체 고분자 전해질에 근거한 수소생성 등에서 폭넓게 이용되고 있다. 본 연구에서는 상용막에 대체가능한 이온교환막을 제조하기 위하여 내열성, 내약품성, 내산성과 우수한 기계적성질 등을 가지고 있어 membrane 소재로 널리 사용되는 polyethersulfone(PES)를 술폰화시켜 sulfonated PES를 합성한 후 양이온 교환막을 제조하여 특성을 분석하였다.

• Journal of the Microelectronics and Packaging Society
• /
• v.9 no.3
• /
• pp.25-29
• /
• 2002

Single ion exchange process was used, and the ion exchange behavior and mechanical properties were investigated in substrate glass for flat panel display. In order to study the effects of ion exchange, ion exchange behavior with ion penetration depth, amount of ion exchange, density and thermal expansion was measured according to the time and temperature. The mechanical properties were evaluated by the three point bending test and curvature change, and then the fracture patterns were investigated by optical microscope.

• Membrane Journal
• /
• v.34 no.2
• /
• pp.132-139
• /
• 2024

The ion exchange resin used to remove total dissolved solids (TDS) is used by being packed in a column, and sufficient contact time between the ionic material and the ion exchange resin is required during the ion exchange process. In this study, the ion exchange resin that exhibits high TDS reduction even with a short contact time through pulverization of the ion exchange resin was characterized. The optimal size of resin considering flowability was over 100 ㎛. The highest pulverizing yield were obtained that 250~500 ㎛ size and 100~250 ㎛ size were 67.3% and 36.9%, respectively. Also, the highest yield and the pulverizing time of 100~500 ㎛ size was 87.1% and 2 minutes, respectively. Under batch test conditions, the time to reach a removal rate of 95% and 99% for 250~500 ㎛ resins was 1.82 and 1.96 times faster than non-pulverized ion exchange resin, respectively. The 100~250 ㎛ resins showed 15.9 times and 6.18 times faster, respectively. Under the column test, a total of 1.74 g of NaCl was removed by non-pulverized ion exchange resins, 1.83 g of NaCl was removed by 250~500 ㎛ resins and 1.63 g of NaCl was removed by 100 and 250 ㎛ resins. As the size of the resin decreased, the capacity slightly decreased. As a result, it was observed that the pulverized ion exchange resins could be a method of achieving high TDS removal performance under short contact time.

• Membrane Journal
• /
• v.29 no.3
• /
• pp.155-163
• /
• 2019

The anion exchange membrane using the blending polymer of poly(ether sulfone) and poly(phenylene sulfide sulfone) was prepared. It was confirmed by EDXS and FT-IR analysis that the prepared anion exchange membrane had the -N- as an anion exchange group. The ionic conductivity in 1 mol/L $H_2SO_4$ aqueous solution was measured. The ionic conductivity of the prepared anion exchange membrane was 0.015~0.083 S/cm, and had a high value compared with AFN and APS as a commercial anion exchange membrane. Permeabilities of the vanadium ions through the prepared anion exchange membrane were tested to evaluate the possibility as a separator in vanadium redox flow battery. Vanadium ion permeation rate in the prepared anion exchange membrane had a low value compared with Nafion 117 as a commercial cation exchange and AFN as a commercial anion exchange membrane.