• Membrane and Water Treatment
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• 제10권2호
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• pp.127-137
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• 2019

The D2EHPA/TBP co-extractants immobilized PolyHIPE membrane can be used for the selective separation of Mn (II) from Co (II). By solvent-nonsolvent method, D2EHPA/TBP co-extractants can be effectively immobilized into PolyHIPE membrane. The pore structure of PolyHIPE membrane and the presence of TBP enhance the stability of immobilized co-extractants. The optimal operating conditions for the separation of Mn (II) and Co (II) are feeding phase at pH 5.5, sulfuric acid concentration in the stripping phase of about 50 g/L and stirring speed at 400 rpm. The D2EHPA/TBP co-extractants ratio of 5:1 shows synergetic effect on Mn/Co separation factor about 22.74. The removal rate and recovery rate of Mn (II) is about 98.4 and 97.1%, respectively, while for Co (II) the transport efficiency is insignificant. The kinetic study of Mn (II) transport shows that high initial flux, $J_f^o=80.1({\mu}mol/m^2s)$, and maxima stripping flux, $J_s^{max}=20.8({\mu}mol/m^2s)$, can be achieved with D2EHPA/TBP co-extractants immobilized PolyHIPE membrane. The stability and reusability study shows that the membrane can maintain a long term performance with high efficiency. High purity of Co (II) and Mn (II) can be recovered from the feeding phase and stripping phase, respectively.

• 멤브레인
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• 제25권2호
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• pp.99-106
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• 2015

Flaring gas에서 $CO_2$ 제거를 위해 폴리술폰 고분자를 이용한 중공사막을 제조하였다. 제조된 중공사막은 1단과 2단 공정의 전산모사와 실제 공정을 통해서 $CH_4$ 농도 99% 이상 $CO_2$ 농도 1% 미만의 운전조건과 성능을 확인하였다. 또한 $25Nm^3/h$ 급 bench scale $CO_2$ 분리막 연속공정에서 100시간의 운전시간 동안 $CO_2$의 농도를 1% 미만으로 안정적으로 운전하였고 이때의 $CH_4$ 회수율은 약 98%였다.

• Membrane and Water Treatment
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• 제13권4호
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• pp.191-199
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• 2022

In industrial production, the development of traditional polyamide nanofiltration (NF) membrane was limited due to its poor oxidation resistance, complex preparation process and high cost. In this study, a composite NF membrane with high flux, high separation performance, high oxidation resistance and simple process preparation was prepared by the method of dilute solution dip coating. And the sulfonated polysulfone was used for dip coating. The results indicated that the concentration of glycerin, the pore size of the based membrane, the composition of the coating solution, and the post-treatment process had important effects on the structure and performance of the composite NF membrane. The composite NF membrane prepared without glycerol protecting based membrane had a low flux, when the concentration of glycerin increased from 5% to 15%, the pure water flux of the composite NF membrane increased from 46.4 LMH to 108.2 LMH, and the salt rejection rate did not change much. By optimizing the coating system, the rejection rate of Na₂SO₄ and PEG1000 was higher than 90%, the pure water flux was higher than 40 LMH (60psi), and it can withstand 20,000 ppm.h NaClO solution cleaning. When the post treatment processes was adjusted, the salt rejection rate of NaCl solution (250 ppm) reached 45.5%, and the flux reached 62.2 LMH.

• Korean Membrane Journal
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• 제8권1호
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• pp.13-20
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• 2006

The production of CO-free hydrogen streams for feeding PEM-Fuel Cells using catalytic zeolite membrane reactors was analysed by means of selective oxidation. Tubular FAU (Na-Y) zeolite membranes, prepared by a secondary growth method and Pt-loaded, were used in a flow-through MR configuration. The catalytic tests were carried out at $200^{\circ}C$ and at different pressures with a simulated dry reformate shifted gas mixture ($H_2$ ca. 60%, CO 1 %, plus $O_2,\;N_2,\;CO_2$). The operative $O_2/CO$ stoichiometric equivalent feed ratio was ${\lambda}= 2$. These catalytic tests, reducing the CO concentration down to $10{\sim}50$ ppm, verified the possibility of MR integration after using a low temperature water-gas shift unit of a fuel processor to convert hydrocarbons into hydrogen-rich gas.

• 멤브레인
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• 제32권5호
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• pp.325-335
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• 2022

본 연구에서는 zeolitic imidazolate framework-9 (ZIF-9)을 합성하고 poly(ether-b-amide)-1657 (Pebax-1657) 내에 함량을 달리하여 Pebax/ZIF-9 혼합막을 제조한 다음 단일기체 (N₂, CO₂)를 투과하여 혼합막에 대한 기체 투과 특성을 조사하였다. 순수 Pebax 막 내에 혼입되는 ZIF-9 함량이 증가함에 따라 N₂ 투과도는 점차 감소하고, CO₂ 투과도는 Pebax/ZIF-9 3 wt% 혼합막까지 증가하다가 그 이후의 함량에서는 감소하였다. 그리고 혼합막들 중 Pebax/ZIF-9 3 wt% 혼합막은 극성 기체인 CO₂에 대해 gate-opening 현상이 일어나면서 선택적으로 CO₂를 받아들여 가장 높은 선택도 69.3을 보였다. 또한 CO₂ 투과도와 CO₂/N₂ 선택도가 모두 증가하여 Robeson upper-bound에 가장 근접하는 결과를 얻었다.

• 한국환경과학회지
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• 제9권4호
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• pp.311-318
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• 2000

To improve $CO_2$pemselectivity, a modified silica membrane was prepared by chemical vapor deposition with tetraethoxysilane(TEOS)-ethanol-water, and TEOS-ethanol-water-HCI solution at 300-$600^{\circ}C$. The silica was effectively deposited in the mesopores of a ${\gamma}$-alumina film coated on a porous $\alpha$-alumina tube by evacuating the reactants through the porous wall. In this membrane, $CO_2$interacts, to some extent, with the pore wall, and $CO_2$/$N_2$selectivity then exceeds the value of the Knudsen diffusion mechanism, while the membrane derived from TEOS alone has no $CO_2$selectivity. The silica membrane prepared from TEOS-ethanol-water-HCI solution showed that $CO_2$permeance was $2.5$\times$10^{-7}mol/s^{-1}.m^{-2}.Pa^{-1} at 30{\circ}C$ and $CO_2$/$N_2$selectivity was approximately 3. The $CO_2$permeance and selectivity was improved by enlarging the surface diffusion with modification of chemical affinity of the silica pores.

• Korean Membrane Journal
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• 제8권1호
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• pp.21-30
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• 2006

A faujasite NaY zeolite membrane was prepared on a tubular ${\alpha}-Al_2O_3$ support by the secondary growth process, and effects of permeation test conditions on the $CO_2/N_2$ separation were investigated. A NaY zeolite membrane with good $CO_2/N_2$ separation was successfully synthesized by using the hydrothermal solution ($Al_2O_3:SiO_2:Na_2O:H_2O$ = 1:6:14:840 in a molar base): at a permeation temperature of $30^{\circ}C$, its $CO_2$ permeance and $CO_2/N_2$ separation factor were $2.5{\times}10^{-7}mol/m^2secPa$ and 34, respectively. The $CO_2$ and $N_2$ permeations were highly dependent on permeation test conditions (feed composition, feeding rate, feed pressure, He sweeping rate and permeation temperature). The results indicated that (i) $CO_2$ and $N_2$ permeations through NaY zeolite membrane are governed by surface and micropore diffusions, respectively, (ii) the preparation of NaY zeolite membrane with a large permeating area is one of the most difficult hurdles for its real applications, and (iii) the retardation of $N_2$ permeation is an effective key to improve $CO_2/N_2$ separation factor in NaY zeolite membrane.

• 공업화학
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• 제25권2호
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• pp.204-208
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• 2014

본 연구는 1차원 반응기 모델을 이용한 수치 시뮬레이션을 통해 수소투과량, 수소선택도, 사용된 촉매의 양, 급송흐름에서의 $H_2O/CO$ 조성비 및 Ar sweep gas가 막반응기(membrane reactor)에서의 수성가스전이반응의 성능에 미치는 영향을 분석하였다. 막반응기에서 평형상태보다 향상된 수소수율을 얻기 위해선 적어도 100 이상의 수소선택도를 가져야 함이 관찰되었으며, 수소투과량이 계속 증가될 경우에는 수소수율의 증가폭이 점차 감소됨이 보였다. 낮은 수소투과량의 경우에는 촉매량이 증가할수록 초기엔 증가된 CO 전환율을 보이다가 점차 그 증가폭이 감소되었으며, 높은 수소투과량의 경우에는 촉매의 양과 무관하게 높은 CO 전환율이 관찰되었다. 급송흐름에서의 $H_2O/CO$ 조성비가 1.5 이상인 경우엔 수소투과량이 막반응기에서의 CO 전환율에 미치는 영향이 미미하였고, 막반응기에서 평형상태보다 향상된 CO 전환율을 얻기 위해선 적어도 $6.7{\times}10^{-6}mol\;s^{-1}$ 의 Ar 몰유속이 필요함이 밝혀졌다.

• 멤브레인
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• 제22권2호
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• pp.128-134
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• 2012

본 연구에서는 hydroxy polyimide (HPI)로 용매 증발법에 의해 제조가 되었다. 비다공성막의 기체투과성능측정 결과로써, $CO_2$ 투과도는 약 85 Barrer이고, $CO_2/N_2$선택도는 23으로 측정되었다. 고분자, 용매, 비용매-첨가제의 3성분계 시스템을 도입하여 평막과 중공사막을 제조하였고, 모폴로지와 기체투과성능을 전계방출형전자주사현미경과 버블플로우메타로 측정하였다. 평막과 중공사막에서 $CO_2$투과도와 $CO_2/N_2$ 선택도는 각각 18.28 GPU, 70 GPU를 6.72, 8.63으로 나타남을 확인하였다. 중공사막이 평막보다 기체투과특성이 우수하다는 것을 확인하였다.

• 멤브레인
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• 제23권5호
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• pp.384-391
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• 2013

DME 제조공정에서 발생하는 혼합가스 중, $CO_2$를 제거하기 위하여 폴리술폰 고분자를 이용하여 지지체 중공사막을 제조하고, Hyflon AD를 코팅하여 복합막을 제조하였다. 제조된 중공사막을 이용하여 Flaring 모사가스에 대한 모듈의 성능을 측정하였다. 분리막 1단 평가 결과 1.2 MPa에서 Stage cut 0.24 이상의 $CO_2$농도는 3% 이하이며, 동일조건에서 $CO_2$ 제거율 및 $CH_4$ 회수율은 각각 약 80%이다. 분리막 2단 평가결과 Product 가스의 $CO_2$ 농도를 5%로 고정하였을 때, stage cut 0.074에서 recycle 되는 $CO_2$ 농도는 공급가스와 같은 농도를 가지며, 이때 $CH_4$의 회수율은 약 99%이다.