• 멤브레인
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• 제11권4호
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• pp.170-178
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• 2001

상전환 방법에 의해 PVC계 MF막을 제조하여 환성슬러지가 포함된 폐수 처리용 MBR (Membrane bioreactor)에 적용하였다. 막 제조시 첨가제의 농도에 따른 막 특성을 확인한 결과 첨가제의 농도가 증가할수록 기공 크기가 증가하였으며 친수화도 역시 향상되었다. MBR의 내부 환경변화에 따른 실험을 통해 제조한 막의 투과 성능 및 막에 발생하는 막 오염 거동을 조사하였다. 사상균의 생성으로 인한 Sludge bulking 시 막 오염 현상이 가속화되었으며, 이 때 각 시료의 Rc을 조사한 결과 CP-0 > CP-1.0 > CP-1.5의 순으로 나타났고, 정상상태와 비교하여 sludge busking시 Rc값은 3.5~7배가지 증가하였다. 표면 특성이나 투과 유속면에서 PVP 1.5 wt% (CP-1.5)를 첨가하였을 때가 가장 적합하였다. 평균 투과 유속은 시료 모두에서 12(${\pm}$2) L/$m^2$hr 정도였으며, 평균 COD 제거율은 98.8% 정도를 나타내었다 MBR 운전에 있어 sludge bulking시 사상균이 차지하는 비율과 미생물의 모양과 크기에 따라 막 오염은 가속화 되었고, 투과 유속 감소를 보였다. 따라서 막 여과 특성은 막의 친수화 정도와 MBR 내부 미생물의 성장 조건과 환경에 의해 결정되는 것을 알 수 있었다.

• 한국물환경학회지
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• 제21권3호
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• pp.242-247
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• 2005

In this study, we investigated the removal efficiencies of pollutants and permeate fluxes depending on chemistry of feed water, various molecular weight cut-offs (MWCOs) and materials of membrane, operating pressure. We used seven MWCO membranes of YC0.5, YM1, YM3, YM10, YM30, YM100 and PM30, humic acid solution and surface water as feed water, and examined variation in permeate flux. Results of TOC removal experiment demonstrate that MWCO lower 1,000daltons could remove humic acid effectively. As increasing solution pH and decreasing divalent cations ($Ca^{2+}$) concentration, TOC removal increased. But $UV_{254}$ removal efficiency increased with higher divalent cation concentration and solution pH. Membrane fouling increased with increasing electrolyte (NaCl), divalent cation concentration and decreasing solution pH. In spite of initial permeate flux of the hydrophobic membrane (PM30) was higher than that of the hydrophilic membrane (YM30), flux decline of PM30 was significant during operation. At higher operating pressure, compactness of the cake layer on the membrane surface increased, resulting in gradual increase in hydraulic resistance.

• 상하수도학회지
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• 제35권6호
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• pp.379-387
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• 2021

In general, trans-membrane pressure (TMP), flux, filtration resistance are used as indicators to evaluate the degree of fouling in MBR. However, they have limitations in determining the level of EPS generation, which is known as an important factor of fouling. Therefore, a new evaluation method is required to monitor the amount of EPS generation. In this study, the applicability of capillary suction time (CST), which is used to measure the dewaterability of sludge, was evaluated as an indirect fouling evaluation index. Statistical analysis was performed to evaluate the effect of EPS on CST, and to determine whether EPS has high similarity with representative fouling evaluation indicators and CST, and quantitatively compared them. As a result, the correlation coefficient between CST and bEPS was 0.7988, which was higher than the correlation coefficient between filtration resistance and bEPS. Since bEPS is a major factor inducing fouling by affecting the formation of the cake layer, it was evaluated that CST, which has a high correlation with bEPS, is suitable to represent EPS. In addition, it was evaluated that the correlation coefficient between filtration resistance and CST was high as 0.7187, which could be used as a fouling evaluation index.

• 상하수도학회지
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• 제28권4호
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• pp.397-409
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• 2014

Algal problem in drinking water treatment is being gradually increased by causing deterioration of water supplies therefore, especially taste and odor compounds such as geosmin and 2-MIB occur mainly aesthetic problem by its unpleasant effects resulting in the subsequent onset of complaints from drinking water consumer. Recently, geosmin and 2-MIB are detected frequently at abnormally high concentration level. However, conventional water treatment without advanced water treatment processes such as adsorption and oxidation process, cannot remove these two compounds efficiently. Moreover, it is known that the advanced treatment processes i.e. adsorption and oxidation have also several limits to the removal of geosmin and 2-MIB. Therefore, the purpose of this study was not only to evaluate full scale nanofiltration membrane system with $300m^3/day$ of permeate capacity and 90% of recovery on the removal of geosmin and 2-MIB in spiked natural raw water sources at high feed concentration with a range of approximately 500 to 2,500 ng/L, but also to observe rejection property of the compounds within multi stage NF membrane system. Rejection rate of geosmin and 2-MIB by NF membrane process was 96% that is 4% of passage regardless of the feed water concentration which indicates NF membrane system with an operational values suggested in this research can be employed in drinking water treatment plant to control geosmin and 2-MIB of high concentration. But, according to results of regression analysis in this study it is recommended that feed water concentration of geosmin and 2-MIB would not exceed 220 and 300 ng/L respectively which is not to be perceived in drinking tap water. Also it suggests that the removal rate might be depended on an operating conditions such as feed water characteristics and membrane flux. When each stage of NF membrane system was evaluated relatively higher removal rate was observed at the conditions that is lower flux, higher DOC and TDS, i.e., $2^{nd}$ stage NF membrane systems, possibly due to an interaction mechanisms between compounds and cake layer on the membrane surfaces.

• 대한환경공학회지
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• 제28권6호
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• pp.613-619
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• 2006

[ $MIEX^{(R)}$ ]와 응집에 의한 분자량 크기별 제거특성에서는 10 kDa 미만의 유기물질에 대해서는 $MIEX^{(R)}$ 처리가 우수한 제거능을 나타내었으나, 10 kDa 이상의 유기물질은 응집 공정에서 높은 제거능을 가지는 것으로 나타났다. 막의 공극 크기에 대한 투과 flux 실험결과 UF 공정에 비하여 MF 공정에서의 투과 flux 감소율이 낮게 나타나고 있으며, MF 공정에 적용된 전처리 공정중 $MIEX^{(R)}+MF$ 공정의 경우 응집+MF 공정에 비하여 투과 flux 감소율이 낮게 나타나고 있다. $MIEX^{(R)}+UF$ 공정의 경우 입자상 물질의 존재 유무에 상관없이 flux 감소율은 거의 유사하게 나타났으나, 응집+UF 공정의 경우에는 용존성 유기물질만이 존재하는 시수에 비하여 입자상 물질이 존재하는 경우 투과 flux 감소율은 작게 나타났다. 응집 공정의 적용 후 다양한 입도분포 변화가 발생하였으며, pH 7에서 $MIEX^{(R)}$ 입자의 제타전위 측정결과 $MIEX^{(R)}$ 입자의 전하는 평균 -2.3 mV로 나타나 전기화학적으로 입자상 물질의 흡착이 가능하며 $MIEX^{(R)}$가 침전됨에 따라 입자상 물질이 sweep되어 입도분포 변화를 보였다.

• 상하수도학회지
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• 제31권6호
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• pp.501-510
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• 2017

In this study, it is estimated that ceramic membrane process which can operate stably in harsh conditions replacing existing organic membrane connected with coagulation, sedimentation etc.. Jar-test was conducted by using artificial raw water containing kaolin and humic acid. It was observed that coagulant (A-PAC, 10.6%) 4mg/l is the optimal dose. As a results of evaluation of membrane single filtration process (A), coagulation-membrane filtration process (B) and coagulation-sedimentation-membrane filtration process (C), TMP variation is stable regardless of in Flux $2m^3/m^2{\cdot}day$. But in Flux $5m^3/m^2{\cdot}day$, it show change of 1-89.3 kpa by process. TMP of process (B) and (C) is increased 11.8, 0.6 kpa each. But, the (A) showed the greatest change of TMP. When evaluate (A) and (C) in Flux $10m^3/m^2{\cdot}day$, TMP of (A) stopped operation being exceeded 120 kpa in 20 minutes. On the other hand, TMP of (C) is increased only 3 kpa in 120 minutes. Through this, membrane filtration process can be operated stably by using the linkage between the pretreatment process and the ceramic membrane filtration process. Turbidity of treated water remained under 0.1 NTU regardless of flux condition and DOC and $UV_{254}$ showed a removal rate of 65-85%, 95% more each at process connected with pretreatment. Physical cleaning was carried out using water and air of 500kpa to show the recovery of pollutants formed on membrane surface by filtration. In (A) process, TMP has increased rapidly and decreased the recovery by physical cleaning as the flux rises. This means that contamination on membrane surface is irreversible fouling difficult to recover by using physical cleaning. Process (B) and (C) are observed high recovery rate of 60% more in high flux and especially recovery rate of process (B) is the highest at 95.8%. This can be judged that the coagulation flocs in the raw water formed cake layer with irreversible fouling and are favorable to physical cleaning. As a result of estimation, observe that ceramic membrane filtration connected with pretreatment improves efficiency of filtration and recovery rate of physical cleaning. And ceramic membrane which is possible to operate in the higher flux than organic membrane can be reduce the area of water purification facilities and secure a stable quantity of water by connecting the ceramic membrane with pretreatment process.

• 한국조경학회지
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• 제46권2호
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• pp.1-13
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• 2018

이 연구는 지금까지 조경 드로잉에서 컴퓨터 테크놀로지가 어떠한 역할을 해왔는가를 검토하고, 근래의 디지털드로잉에서 발견되는 사실적 묘사 경향에 관한 쟁점을 진단한 후 대안적 방향을 모색한다. 조경 드로잉의 매체가 손에서 컴퓨터로 이행하는 시기에 드로잉 테크놀로지는 대체로 손 드로잉의 테크닉을 모방하는 기계 도구의 기능을 담당했다. GIS는 레이어 케이크의 절차를 보다 정확하게 효율적으로 처리했고, CAD는 물리 모형을 시공 도면으로 변환했으며, 그래픽 소프트웨어는 콜라주와 몽타주를 보다 쉽게 만들 수 있도록 도왔다. 근래에 디지털 조경 드로잉에는 경관의 외양을 회화와 같이 사실적으로 묘사하려는 경향이 짙다. 그래픽 소프트웨어를 이용하여 사진 재료의 조립 흔적을 지워내 마치 실재 경관을 포착한 사진처럼 보이도록 제작되고 있다. 이러한 사진과 같은 이미지는 대중과의 의사소통에 수월하지만, 경관의 다감각적 특성을 온전하게 구현하기 힘들고, 좀처럼 현실에서 발생하기 힘든 경관의 가장 이상적인 순간을 묘사하여 수용자를 기만하는 경우가 발생하기도 하며, 자칫 최종 결과물처럼 여겨져 드로잉의 생산에만 집중하게 할 우려가 있다. 이에 대한 대안적 방향으로, 경관의 기능 정보를 삼차원으로 모델링하고, 디지털 테크놀로지를 설계 전반 프로세스에서 설계 아이디어를 발전시키는데 활용하며, 서로 다른 드로잉 테크닉과 테크놀로지를 혼용하여 경관의 다양한 국면을 시각화하는 실험이 필요하다.

• Asian-Australasian Journal of Animal Sciences
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• 제15권4호
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• pp.522-527
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• 2002

The experiment was conducted for a period of 56 days with twelve Bangladeshi bull calves of average body weight of $127.20{\pm}11.34$ kg. The calves were divided into 3 groups having 4 animals in each. The animals were fed urea-treated rice straw designated as A) 4% urea-treated rice straw, B) 4% urea+4% soybean-treated rice straw and C) 4% urea+6% soybean-treated rice straw. In addition, all the animals were supplied 2 kg green grass, 350 g Til-oil-cake and 100 g common salt per 100 kg body weight of animals. Straw was treated with 4% urea solution and soybean meal at 4 and 6% were added to treated straw and kept for 48 h in double layer polythene bags under anaerobic condition. Urea treatment improved crude protein (CP) content of rice straw from 2.68 to 8.70% and it was further increased by 10.74 and 12.12% with the addition of 4 and 6% soybean meal. Dry matter (DM) intake (kg) was higher (p<0.05) in C (4.2) followed by B (4.1) and A (4.0). Crude protein intake was significantly higher (p<0.05) in group B and C than group A. Total live weight gains were 20.2, 24.8 and 25.6 kg for calves of group A, B and C respectively (p<0.01). The addition of soybean meal to treated rice straw did not affect the coefficients of digestibility of DM, OM, EE and NFE. However, CP and CF digestibility were significantly higher in group B and C (p<0.05). The values for digestible crude protein (DCP), digestible ether extract (DEE), digestible nitrogen free extract (DNFE) and total digestible nutrients (TDN) were significantly (p<0.05) higher in diet C and B in comparison to diet A, but there were no significant difference in digestible organic matter (DOM) and digestible crude fibre (DCF) value among the groups. It may be concluded that 4% urea treated rice straw can be fed to growing bull calves with 2 kg green grass and a small quantity of concentrate without any adverse effect on feed intake and growth. Moreover, soybean meal at 4 and 6% can be added to urea treated rice straw at the time of treatment for rapid hydrolyzing of urea, which resulted an improvement in nutrient digestibility and better utilization of rice straw for growth of growing bull calves.

• 멤브레인
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• 제22권3호
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• pp.171-177
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• 2012

정수처리용 세라믹 한외여과 및 광촉매의 혼성공정에서 주기적 질소 역세척 시 휴믹산 농도의 영향을 알아보고, 막오염에 의한 저항($R_f$) 및 투과선속(J), 총여과부피($V_T$) 측면에서 물 역세척의 기존 결과와 비교 고찰하였다. 휴믹산 농도가 낮아질수록 $R_f$는 급격히 감소하고 J는 증가하여, 휴믹산 농도 2 mg/L에서 $V_T$는 가장 높았다. 휴믹산 농도가 2에서 10 mg/L로 높아졌을 때, 180분 운전 후 막오염 저항($R_{f,180}$)은 물 역세척 시 $R_{f,180}$값보다 0.8배 더 증가하였다. 따라서 물 역세척보다 질소 역세척 시 막오염이 휴믹산 농도의 영향을 더 크게 받는다는 것을 알 수 있었다. 탁도 처리효율은 휴믹산 농도와 무관하게 거의 일정하였으나, 휴믹산 처리효율은 휴믹산 2 mg/L에서 최대였다. 이것은 질소 역세척 시 휴믹산 2 mg/L에서 광촉매 구의 흡착과 광산화로 휴믹산이 가장 효과적으로 제거되지만, 4 mg/L에서는 광촉매 구만으로 역부족인 것으로 판단된다. 휴믹산 6 mg/L 이상에서는 막표면의 두꺼운 케이크 층과 심화된 내부 막오염으로, 휴믹산이 한외여과막에 의해 효과적으로 제거된 것이다.

• Journal of Animal Science and Technology
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• 제57권5호
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• pp.17.1-17.6
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• 2015

The present study investigated the nutritional and economic suitability of cashew reject meal (full fat and defatted) as replacement for groundnut cake (GNC) in the diets of laying chickens. A total of eighty four brown shavers at 25 weeks of age were randomly allotted into seven dietary treatments each containing 6 replicates of 2 birds each. The seven diets prepared included diet 1, a control with GNC at $220gkg^{-1}$ as main protein source in the diet. Diets 2, 3 and 4 consist of gradual replacement of GNC with defatted cashew reject meal (DCRM) at 50%, 75% and 100% on weight for weight basis respectively while diets 5, 6 and 7 consist of gradual inclusion of full fat cashew reject meal (FCRM) to replace 25%, 35% and 50% of GNC protein respectively. Each group was allotted a diet in a completely randomized design in a study that lasted eight weeks during which records of the chemical constituent of the test ingredients, performance characteristics, egg quality traits and economic indicators were measured. Results showed that the crude protein were 22.10 and 35.4% for FCRM and DCRM respectively. Gross energy of DCRM was 5035 kcal/kg compared to GNC, 4752 kcal/kg. Result of aflatoxin $B_1$ revealed moderate level between 10 and $17{\mu}g/Kg$ in DCRM and GNC samples respectively. Birds on control gained 10 g, while those on DCRM and FCRM gained about 35 g and 120 g respectively. Feed intake declined (P < 0.05) with increased level of FCRM. Hen day production was highest in birds fed DCRM, followed by control and lowest value (P < 0.05) was recorded for FCRM. No significant change (P > 0.05) was observed for egg weight and shell thickness. Fat deposition and cholesterol content increased (P > 0.05) with increasing level of FCRM. The cost of feed per kilogram decreased gradually with increased inclusion level of CRM. The prediction equation showed the relative worth of DCRM compared to GNC was 92.3% whereas the actual market price of GNC triples that of DCRM. It was recommended that GNC could be completely replaced by DCRM in layer's diets in regions where this by product is abundant. However, FCRM should be cautiously used in diets of laying chickens.