• Membrane Journal
• /
• v.22 no.6
• /
• pp.450-460
• /
• 2012

In the submerged membrane-coupled sequencing batch reactor (MSBR) with sponge type media, the effect of media on the removal efficiency and filtration performance were investigated. Dosages of the media in the MSBR were set of 5%, 10%, and 20% based on working volume of reactor. As a control system, the MSBR without media was also operated. The experimental results showed that there was also no difference observed in the removal efficiencies of COD, T-N, and T-P irrespective of the dosages of the media. But TMP (transmembrane pressure) of the MSBR with media increased slowly during the operation time, while that of the MSBR without media increased rapidly at the initial operation. This result was thought that the collisions between flat membrane and moving media gave shear forces which decreased the cake layer on the surface of flat type membrane. Consequently, this study showed that filtration performance of the MSBR with media was greatly enhanced compared with that of the MSBR without media. The MSBR with media suggested in this study can be a good candidate for the wastewater treatment.

• Applied Chemistry for Engineering
• /
• v.25 no.2
• /
• pp.204-208
• /
• 2014

This study investigated the effect of hydrogen permeance and selectivity, catalyst amount, $H_2O/CO$ ratio in a feed stream, and Ar sweep gas on the performance of a water gas shift reaction in a membrane reactor. It was observed that a minimum hydrogen selectivity of 100 was needed in a membrane reactor to obtain a hydrogen yield higher than the one at equilibrium and the hydrogen yield enhancement gradually decreased as the hydrogen permeance increased. The CO conversion in a membrane reactor initially increased with the catalyst amount and reached a plateau later for a membrane reactor with a low hydrogen permeance while the high CO conversion independent of a catalyst amount was observed for a membrane reactor with a high hydrogen permeance. For the $H_2O/CO$ ratio in a feed stream higher than 1.5, a hydrogen permeance had little effect on the CO conversion in a membrane reactor and it was found that a minimum Ar molar flow rate of $6.7{\times}10^{-6}mol\;s^{-1}$ was needed to achieve the CO conversion higher than the one at equilibrium in a membrane reactor.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1999.04a
• /
• pp.135-138
• /
• 1999

• Proceedings of the Membrane Society of Korea Conference
• /
• 2005.11a
• /
• pp.196-199
• /
• 2005

원자력 고온가스의 열물 이용하여 수소를 생산을 하는 IS(Iodine-Sulfur)공정 중 HI분해-분리반응은 높은 열적-화학적 안정성이 요구되는 공정이다. 이러한 공정분위기에서 사용 될 분리막반응기의 촉매를 선정하고자 다양한 담체내에 백금(Platinum)의 함유량이 각각 다른 촉매를 사용하였다. HI 분해실험온도는 $300-500^{\circ}C$ 의 범위이며 일정량의 HI 용액을 기화시켜 촉매반응기에 정량적으로 공급하여, 가스크로마토그래피를 이용하여 분석하였다. 분해온도 변화와 다양한 담체내백금의 함유량 변화에 따른 HI전환율 확인하였으며, 반응 후 촉매에 대한 SEM과 XRD분석의 수행으로 촉매의 내구성과 변화를 확인하였다.

• 한국생물공학회:학술대회논문집
• /
• 2002.04a
• /
• pp.351-354
• /
• 2002

This research discussed about the substrate transport phenomena in anaerobic biofilm. Three anaerobic fixed biofilm reactors were filled with the sludge of anaerobic digestor from Suyoung wastewater treatment plant. After 15 days of biofilm formation periods, suspended solids within the reactors were removed, and each fixed biofilm reactor was supplied with synthetic wastewater of different concentration of 8.00 mgTOC/L, 9.76 mgTOC/L and 18.97 mgTOC/L, respectively. The experimental results in conjunction with substrate transfer phenomena indicated that data - thickness, substrate removal rate. At the low influent substrate concentration(reactor 1 : 8.00 mgTOC/L, reactor 2 : 9.76 mgTOC/L), the rate of substrate utilization($k_v$), effective diffusivity($D_{eff}$) of substrate in biofilm were similar. While $k_v$ and $D_{eff}$ of the high influent substrate concentration(reactor 3 : 18.97 mgTOC/L) were higher than data in the reactors of the low influent substrate concentration.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1992.04a
• /
• pp.35-36
• /
• 1992

화학반응이 주로 고온에서 일어나기 때문에 polymer membrane의 화학반응에의 적용은 거의 없었으며, 연구의 대부분은 열적 안정성이 좋은 inorganic membrane reactor에 대하여 이루어져 왔다. 산 및 산화환원 촉매로써의 12-텅스토인산은 반응물의 종류에 따라 특이한 흡착 특성을 보이며, 헤테로폴리산만이 지니는 특징적인 surface, bulk 특성 때문에 바능물의 종류에 따라 반응은 촉매의 surface and/or bulk에서 일어난다. 무기 축합산인 12-텅스토인산이 지니는 또 하나의 특징은 물, 알콜, ether 같이 산소를 포함하는 organic solvent에 매우 잘 녹는다는 사실이다.

• KSBB Journal
• /
• v.6 no.4
• /
• pp.345-350
• /
• 1991

The purpose of this study is to investigate biomass characteristics and organic removal efficiency by changing superficial upflow velocity and organic loading rate in treating alcoholic distillery wastewater. Since the biomass concentration and the thickness of biofilm are very sensitive to superficial upflow velocity, a high concentration of biomass could be achieved by decreasing superficial upflow velocity that lowered the organic removal efficiency. Therefore, superficial upflow velocity should be controlled as to give optimum conditions and removal efficiency. Generally, activated sludge system shows 70% COD removal efficiency at$1.5kgCOD/m^3{\cdot}day$, but the fluidized-bed biofllm reactor shows 80% COD removal efficiency even at 6kgCOD/$m^2{\cdot}day$.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1998.10a
• /
• pp.82-85
• /
• 1998

1. 서론 : Cyclodextrin(CD) 동족체(homologues)는 $\alpha$-, $\beta$-, $\gamma$-CD로 구분되며, 이들 각각은 $\alpha$-D-glucopyranose 단위체 6,7, 및 8개가 비환원성 환상구조로 연결된 cyclic maltooligosaccaride의 일종으로 외부는 친수성이고, 내부는 소수성인 공동 구조를 갖고 있다. 따라서 각 CD는 동공의 크기가 달라 다른 크기의 소수성 물질들과 선택적인 포접화합물 (inclusion compound)을 형성하는 특징이 있다. CD 동족체는 전분 분해 효소인 cyclodextrin glycosyltransferase(CGTase)에 의해 전분으로부터 생산되는데, 반응용액 내에서의 CD 동족체 농도가 어느 한계값 이상으로 높아지면 생산물 저해와 다른 환원당으로의 분해 때문에 생산성이 감소하여 이의 효과적 생산에 어려움이 있다. 본 연구는 dead-end 및 cross-flow형 막 생물반응기를 사용하여 CGTase에 의한 전분의 CD 동족체로의 분해반응시 생산물 저해를 억제시켜 생산성을 향상시키고, 동시에 조작조건 변화에 따른 생산물인 CD 동족체의 효과적인 연속분리 가능성을 검토하였다.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1992.10a
• /
• pp.5-6
• /
• 1992

무기막은 고분자 계통의 유기막과는 달리 200$\circ$C 이상의 고온에서도 높은 기체 투과도와 구조적 안정성을 보인다. 따라서 무기막을 고온의 촉매 반응에 이용하면 생성물 중 일부를 선택적으로 분리시키므로써 열역학적으로 예측할 수 있는 값 이상의 높은 전환율을 얻을 수 있으며, 또한 반응물 중 일부를 막을 통해 주입하면 반응의 정도를 조절함으로써 원하는 생성물의 수율을 높일 수 있게 된다. 그러나, 현재 실험실에서 많이 연구되고 있는 다공성 유리 또는 다공성 알루미나와 같은 무기막들은 기체 투과도는 높은 반면에 기체 분리가 Knudsen diffusion에 의해 이루어지기 때문에 분리선택도가 낮은 단점이 있다.

• KSBB Journal
• /
• v.16 no.6
• /
• pp.573-578
• /
• 2001

The effects of organic supplement (acetate) and dissolved oxygen concentration on the nitrification rate of wastewater were investigated in the 27.7 L pilot-scale airlift biofilm reactor with the granular activated carbon media of 0.613 mm diameter. The ammonium oxidation rate increased stepwise up to 5 kg N/㎥$.$d at the riser air velocity of 0.063 m/s, when the air velocity and the ammonium loading rate were raised alternately. The nitrite build-up was observed during the early stage of the biofilm formation, which disappeared after the reactor operation of 128 days. As increasing the organic loading rate, the organic oxidation rate increased up to 25.0 kg COD/㎥$.$d with the removal efficiency of 94% but the oxidation rates of ammonium and nitrite decreased. The oxidation rates of ammonium and nitrite increased with the dissolved oxygen concentrations. When the pure oxygen was sparged, the ammonium oxidation rate was almost five times higher than that with air at the same velocity.