• Biotechnology and Bioprocess Engineering:BBE
• /
• 제6권6호
• /
• pp.426-432
• /
• 2001

Perstractive fermentation is a good way to increase the productivity of bioreactors. Us-ing Propionibacteria as the model system, the feasibility of using supported emulsion liquid mem-brane(SELM) fro perstractive fermentation is assessed in this study. Five industrial solvents were considered as the solvent for perparing the SELM. The more polar a solvent, is the higher the par-tition coefficeint However, toxicity of a solvent also increases with its polarity. CO-1055(indus-trial decanol/octanol blend)has the highest partition coefficient toward propionic acid among the solvents that has no molecular toxicity toward Propionibacteria, A preliminary extraction study was conducted using tetradecane as solvent in a hydrophobic hollow fiber contactor. The results confirmed that SELM eliminates the equilibrium limitation of conventional liquid-liquid extrac-tion and allows the use of a non-toxic solvent with low partition coefficient.

• 분석과학
• /
• 제24권5호
• /
• pp.352-359
• /
• 2011

용매를 사용하지 않고 반복적으로 막 추출한 후 저온농축과 GC-MS로 물 중 BTEX를 분석하는 방법을 시도하였다. 물로부터 비공성막의 silicone 막을 투과한 BTEX를 He 기체를 통해 $-100^{\circ}C$의 저온 농축장치로 보낸 후 열 탈착과 GC-MS로 분석하였다. 물 시료(30 mL)는 10 mL/min로 흘려주었고, 한 번 추출된 시료는 다시 되돌려서 두 번 더 추출하였다. Benzene에 대한 회수율은 가장 높아 약 80%인 반면에, ethylbenzene과 xylenes에 대한 회수율은 3.5-10%로 낮은 편이었다. 그렇지만, RSD는 모두 10% 미만이었고 검량선의 직선성($r^2$)도 0.9976-0.9997로 높은 편이었으며, 방법검출한계도 1.8 ${\mu}g$/L 이었다. 이 방법은 짧은 추출 시간, 용매의 미사용 및 분석의 편의성의 장점을 갖고 있다.

• Korean Chemical Engineering Research
• /
• 제47권2호
• /
• pp.258-261
• /
• 2009

본 연구에서는 추출용매 물 100%을 이용하여 다양한 초음파 에너지(35, 72, 170 KHz)와 추출 시간(30, 60 min)에 의한 고삼으로부터 식물성에스트로겐 제니스테인 및 포르모노네틴의 추출량과 일반성분의 영향을 비교하였다. 전처리 단계는 초음파추출, 여과, 농축, 막분리로 구성되었다. 추출된 용액은 역상 고성능 액체크로마토그래피 (HPLC)를 사용하여 분석하였다. 이동상 조성은 A는 물/아세트산(99.9/0.1 vol%), B는 아세토니트릴/아세트산(99.9/0.1 vol%)이며, A/B를 80/20~65/35 vol%로 60분 동안 선형적으로 변화시켰다. 실험결과에 의하면 일반성분은 탄수화물(0.255~0.413%)을 제외한 나머지 성분들의 함량은 거의 비슷하게 확인되었다. 또한 주파수 170 KHz, 60 min에서 추출량이 3.17 g으로 추출 수율이 가장 우수하였고 천연물관련 화학 및 생물학 연구에 기초자료로 도움이 될 것이다.

• Asian-Australasian Journal of Animal Sciences
• /
• 제24권12호
• /
• pp.1666-1673
• /
• 2011

The presence of sialoglycoproteins (SGPs) in the membranes from goat (Capra aegagrus hircus), buffalo (Bubalus bubalis bubalis) and pig (Sus scrofa domestica) erythrocytes was investigated by partial purification with a chloroform-methanol extraction method followed by Sodium dodecyl sulphate - Polyacrylamide gel electrophoresis in comparison to human (Homo sapiens) erythrocytes. The results show that mammalian erythrocytes possess clear differences in the SGPs numbers and molecular weights although all animals studied in this experiment are from the same class i.e. mammalia. The SGPs number in human, goat, buffalo and pig are four (PAS-1 to PAS-4), ten (PAS-GI to PAS-GX), seven (PAS-BI to PAS-BVII) and four (PAS-PI to PAS-IV) respectively as indicated by staining the polyacrylamide gel with sialoglycoprotein-specific Periodic acid-Schiff's (PAS) stain. The new SGPs could be observed only after the partial purification of membrane fractions named as PAS-HI with molecular weight (Mr) 190 kDa and PAS-HII 150 kDa in human, PAS-BIA in buffalo and PAS-PIA and PAS-PIVA in pig. The gels were also stained with Coomassie brilliant blue (CBB) and Silver stain to check the contamination of other membrane proteins in the purified fractions. The quantitative distribution of SGPs was also determined by densitometry. Present study indicates that there are some basic differences in mammalian erythrocyte membrane SGPs, especially with respect to their number and molecular weights indicating major structural variations.

• Elastomers and Composites
• /
• 제23권1호
• /
• pp.11-17
• /
• 1988

The transport of chromium(VI) ion from waste water through the liquid surfactant membrane containing tri-n-octylamine as a carrier, was analyzed by a slab model and was investigated through experiments. For the experiment of membrane stability, concentrations of surfactant and liquid paraffin oil were analyzed. Extraction experiments were carried out to observe the effect of system variables, such as concentrations of carrier, and initial chromium(VI) ion in external aqueous phase at $25^{\circ}C$. It is concluded that the most stable formation of liquid membrane emulsion was obtained when surfactant concentration is above 3 wt.% and liquid paraffin oil concentration is 50 vol.%. The theoretical equation on the transport of chromium(VI) ion agreed well with the experimental results.

• Membrane and Water Treatment
• /
• 제8권5호
• /
• pp.483-498
• /
• 2017

Novel mixed matrix membranes of Sodium Alginate (NaAlg) were developed by the incorporation ofunmodified, modified Phosphomolybdic acid (PMA) then cross-linked with glutaraldehyde externally. These membranes were prepared by the solution casting technique. Pervaporation (PV) experiments have been performed with pure NaAlg, unmodified NaAlg-PMA5, NaAlg-PMA10, modified NaAlg-mPMA5, and NaAlg-mPMA10 (wt. % of PMA 5 and 10) at 30, 40 and $50^{\circ}C$, to separate water-isopropanol feed mixtures containing 10-30 wt. % of water. Pervaporation results of NaAlg-mPMA10 produced a highest separation factor of 9028 with a flux of $0.269kg/m^2.h$ for 10 wt. % of water containing feed mixture. Both separation factor and flux for water increased significantly with increasing content of mPMA into NaAlg; a significant improvement in PV performance was observed for NaAlg-mPMA5 and NaAlg-mPMA10 membranes when compared to pure NaAlg& PMA-5, PMA-10 membrane.

• 멤브레인
• /
• 제5권1호
• /
• pp.44-57
• /
• 1995

내부산의 탈거제로 탄산나트륨을 함유하는 유화액막의 거동을 묘사하기 위하여 수학적 모델이 제시되었다. 젖산의 회분식 추출 실험 결과가 모델의 계산 결과와 비교되었는데, 모델의 계산 결과는 담체농도, 탈거제농도, 교반속도, 처리비와 같은 변수의 영향을 잘 예측할 수 있었다. 유화액막의 주요 문제 중의 하나인 에멀젼의 팽윤을 줄이기 위하여, 액체 파라핀, n-데칸올, 사이클로헥사논, 스판-85 같은 막 첨가제가 사용되었다. 사용된 모든 첨가제는 팽윤 정도를 줄이는데 어느 정도 효과가 있었다. 사이클로헥사논은 팽윤을 줄일 뿐만 아니라, 젖산의 전달 속도를 크게 증가시키는 것으로 관찰되었다.

• Biotechnology and Bioprocess Engineering:BBE
• /
• 제3권1호
• /
• pp.24-31
• /
• 1998

The separation and concentration of L-phenylalanine (L-Phe) using a supported liquid membrane (SLM) is investigated. A cation complex agent, di-2-ethylhexyl phosphoric acid (D2EHPA), is used as a carrier in the SLM with n-Heptane as a solvent. The reaction order and equilibrium constant in the formation reaction of L-phe-carrier complex are obtained from the extraction experiment. A mathematical model for a carrier mediated counter transport process is proposed to estimate the diffusion coefficient of L-phe-carrier complexly in the liquid membrant. Permeation experiments of L-phe using a SLM are performed under various operating conditions and optimum conditions for the transport of L-phe are obtained. Concentration of L-phe in the strip phase against its concentration is observed. Transport rate of glucose through liquid membrane is less than that of L-phe in the competitive transport of L-phe and glucose. And the existence of glucose reduced the transport rate of L-phe. The performance of separation with continuous strip phase is increased due to the dilution effect in the strip phase.

• 상하수도학회지
• /
• 제30권4호
• /
• pp.441-447
• /
• 2016

Development of shale gas has drawn increasing attention since it is one of promising alternative energy resources. However, contamination of groundwater and surface water during the extraction of shale gas is becoming a serious environmental issues, which brings the needs to treat wastewater generated from hydraulic fracking. In this study, the feasibility of membrane distillation (MD) for the treatment of shale gas wastewater was investigated using a laboratory scale experimental setup. Flat-sheet MD membranes were used to treat produced water from a shale gas well in the United States. Different configurations such as direct contact MD (DCMD) and air gap MD (AGMD) were compared in terms of flux and fouling propensity. The foulants on the surface of the membranes were examined. The results suggest that MD can treat the shale gas produced water containing more than 200,000 mg/L of total dissolved solids, which is impossible by other technologies such as reverse osmosis (RO) and forward osmosis (FO). In this study, we investigated the possibility of processing and characterization of shale gas produce wastewater using membrane distillation. Laboratory scale membrane distillation experimental device was developed. It was compared the flat-sheet direct contact membrane distillation and flat-sheet air gap membrane distillation. AGMD flux in lower than the flux of DCMD, it was expected that the contamination caused by organic matters.

• 멤브레인
• /
• 제5권4호
• /
• pp.129-136
• /
• 1995

본 연구는 에멀젼 액막을 이용한 염색 폐수 내의 염료 이온 제거에 관한 연구이다. Aliquat 336을 함유한 액막과 D2EHPA를 함유한 액막으로 각각 음이온성 염료와 양이온성 염료 제거에 관한 최적 조건을 확립하였으며, 이 조건하에서 실제의 염색 폐수 처리 실험을 행하였다. 직접 염료인 Sirius Red, 반응성 염료인 Reactofix Supra Blue 및 염기성 염료인 Apollo Blue를 대상으로 하여 막상의 계면활성제(Span 80)와 담체(Aliquat 336 or D2EHPA)의 농도, 내수상의 counter ion($Na_2SO_4$) 농도, 그리고 에멀젼 투여량 등을 변화시키며 염료 제거 실험을 행하였다. 반응 5분 후에 추출 평형에 도달하였으며, 각 염료에 대하여 색소 성분의 95% 이상을 제거할 수 있었다. 제막 조건에 가장 큰 영향을 미치는 인자는 담체의 농도로서 일정량 이상의 담체는 막의 물질 전달 저항을 증가시켜 색도 제거 효과를 감소시킴을 알 수 있었다. 또한, 막상의 계면활성제의 양, 내수상의 counter ion의 양 및 투여 에멀젼의 양은 평형 도달 후의 최종 색도보다는 추출 속도에 더 큰 영향을 미침을 알 수 있었다. 실제 염색 폐수를 에멀젼 액막으로 2단계 처리한 결과 550nm에서의 흡광도를 초기 0.53에서 10분 후 0.03까지 낮출 수 있었다.