• Membrane Journal
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• v.19 no.2
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• pp.157-164
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• 2009

Bio-butanol recovery by pervaporation was performed with dense and composite polydimethylsiloxane (PDMS) membranes. The pervaporative behavior of the membranes was investigated as a function of operation temperature $(20{\sim}40^{\circ}C)$ and membrane thickness $(100{\sim}1{\mu}m)$ using a series of aqueous BtOH model solutions $(1{\sim}5wt%)$. With the increment of the BtOH concentration in feed, the Butanol concentration in permeate, pervaporation selectivity of Butanol over water and Butanol permeation flux increased. As the operating temperature of feed solutions increased, the BtOH concentration in permeate, pervaporation selectivity and permeation flux increased markedly. As the thickness of the PDMS membrane decreased, permeation flux increased but pervaporation selectivity decreased. These results were explained in terms of high solubility and low diffusion resistance of BtOH over water toward hydrophobic and rubbery PDMS membranes.

• KSBB Journal
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• v.24 no.5
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• pp.446-452
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• 2009

Oleyl alcohol, butyl butyrate, and two different ionic liquids were evaluated for the extraction of butanol from culture broth without toxic effect to cells. The tested solvents showed more than 50% extraction efficiency, and oleyl alcohol was chosen as the best extractant for butanol among the used extractants with a partition coefficient of 2.89. When oleyl alcohol was used as an extractant, more than 80% of butanol was extracted in the wide range of butanol concentrations (1-20 g/L) and pH values (pH 4-5.5). In extractive fermentation using oleyl alcohol only, there was 11% more butanol production and glucose consumption when compared to that without extractive fermentation, implicating a reduced inhibitory effect of butanol due to butanol removal to the oleyl alcohol phase. In addition, oleyl alcohol did not inhibit cell growth, while a mixture of oleyl alcohol and butyl butyrate with the volume ratio of 9:1~7:3 inhibited either butanol production or cell growth significantly due to the toxicity of butyl butyrate to cells. In conclusion, oleyl alcohol can be used as an efficient and non-toxic solvent for extractive fermentation for butanol production.

• 한국생물공학회:학술대회논문집
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• 2000.04a
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• pp.243-246
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• 2000

Clostridium acetobutylicum Bl8 can produce a large amount of butanol by control characteristics such as glucose concentration, pH and extra nutrient. It is known that this stain is potentially useful in simultaneous ABE fermentation-seperation system because of its low acid $production^{1).}$ The purpose of this study is to determine optimal condition of fermentation to produce maximum butanol in batch and fed-batch by strain Bl8.

• Microbiology and Biotechnology Letters
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• v.41 no.1
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• pp.26-32
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• 2013

Butanol-resistant bacteria were isolated from butanol solvent. The cell growth of isolated strains declined with increasing concentrations of butanol, and isolated strain BRS02 displayed more resistance to 12.5 g/L of butanol than other isolated strains. In addition, strain BRS251, which was resistant to even higher concentrations of butanol, was developed by the mutation of BRS02 using UV. BRS251 could grow in LB medium containing up to 17.5 g/L of butanol, 32.5 g/L of propanol, or 6 g/L of pentanol, whereas the control strain Escherichia coli was found to be tolerant to 7.5 g/L of butanol, 20 g/L of propanol, or 2 g/L of pentanol. The isolated BRS02, a Gram(+) bacterium seen to have a cocci form under the microscope, grew in 6.5% NaCl. According to biochemical tests, BRS02 can metabolize and produce acid with D-galactose, D-maltose, D-mannitol, D-mannose, methyl-${\beta}$-Dglucopyranoside, D-ribose, sucrose, or D-trehalose, as carbon sources. Also, this strain showed resistance to bacitracin, vibriostatic agent O/129, and optochin, alongside positive activities for arginine dihydrolase, ${\alpha}$-glucosidase, and urease. The BRS02 strain was identified as Staphylococcus sp. by analyses of the 16S rRNA gene, phylogenetic tree, and biochemical tests.

• Korean Chemical Engineering Research
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• v.49 no.6
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• pp.816-822
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• 2011

Pervaporation is known to be a low energy consumption process since it needs only an electric power to maintain the permeate side in vacuum. Also, the pervaporation is an environmentally clean technology because it does not use the third material such as an entrainer for either an azeotropic distillation or an extractive distillation. In this study, Silicalite-1 particles are hydrothermally synthesized and polydimethylsiloxane(PDMS)-zeolite composite membranes are prepared with a mixture of synthesized Silicalite-1 particles and PDMS-polymer. They are used to separate n-butanol from its aqueous solution. Pervaporation characteristics such as a permeation flux and a separation factor are investigated as a function of the feed concentration and the weight % of Silicalite-1 particles in the membrane. A 1,000 $cm^3$ aqueous solution containing butanol of low mole fraction such as order of 0.001 was used as a feed to the membrane cell while the pressure of the permeation side was kept about 0.2~0.3 torr. When the butanol concentration in the feed solution was 0.015 mole fraction, the flux of n-butanol significantly increased from 14.5 g/ $m^2$/hr to 186.3 g/$m^2$/hr as the Silicalite-1 content increased from 0 wt% to 10 wt%, indicating that the Silicalite-1 molecular sieve improved the membrane permselectivity from 4.8 to 11.8 due to its unique crystalline microporous structure and its strong hydrophobicity. Consequently, the concentration of n-butanol in the permeate substantially increased from 0.07 to 0.15 mole fraction. This composite membrane could be potentially appliable for separation of n-butanol from insitu fermentation broth where n-butanol is produced at a fairly low concentration of 0.015 mole fraction.

• Journal of the Korean Chemical Society
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• v.52 no.2
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• pp.111-117
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• 2008

critical micelle concentration (CMC) and the counter ion binding constant (B) in a mixed micellar state of the trimethyltetradecylammonium bromide (TTAB) with the polyoxyethylene (23) lauryl ether (Brij 35) at 25oC in water and in aqueous solutions of butanol isomers were determined as a function of 1 (the overall mole fraction of TTAB) by the use of electric conductivity method and surface tensiometer method. Various thermodynamic parameters (Xi, i, Ci, aiM, and Hmix) were calculated by means of the equations derived from the nonideal mixed micellar model. The results say that the effects of butanol isomers on the micellization of TTAB/Brij 35 mixtures have been in the order of n-butanol>iso-butanol>t-butanol> water.

• Journal of the Korean Applied Science and Technology
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• v.36 no.1
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• pp.13-22
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• 2019

The aim of the present investigation was to assess the oxidation inhibition by nitrogen oxide scavenging activity and physiological activities. Bioactive compound of proanthocyanidin $69.000{\pm}2.737mg$ catechin equivalents (CE)/g dry weight. Antioxidant effects (nitric oxide radical scavenging activity, nitrite scavenging activity, ${\beta}$-carotene bleaching assay and lipid peroxidation inhibition activity) of distilled water (DW), 70% ethanol and n-butanol extract of turmeric (Curcuma longa L.). Turmeric extracts yield were DW 17.11%, 70% ethanol 15.26% and n-butanol 4.12%, respectively. Oxidation inhibition activity of the samples exhibited a dose-dependent increase. However, in the current study, none of the samples evaluated showed activity as strong as the BHA and trolox. Total flavonoid content was the highest in the n-butanol extract, followed by 70% ethanol and DW extract. Further, nitrite scavenging activity was the highest for the n-butanol extract. As a result of this experiment, the turmeric can be utilized as a valuable and potential natural oxidation inhibition for the functional food industry.

• Korean Chemical Engineering Research
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• v.53 no.1
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• pp.116-120
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• 2015

Synthesis of butenes through dehydration of 2-butanol was investigated over HY zeolite catalysts. 2-Butanol dehydration reaction was carried out in a fixed bed catalytic reactor. 2-Butanol conversion was increased with increase of $Si/Al_2$ ratio of HY zeolite catalysts, which can be ascribed to increase of acid strength with increase of $Si/Al_2$ ratio. Selectivities to 1-butene, trans-2-butene, and cis-2-butene were not greatly influenced by the change of the $Si/Al_2$ ratio of HY zeolite. As a result, it was advantageous to use a HY zeolite catalyst with 60 $Si/Al_2$ ratio for maximizing the yield of 1-butene in the dehydration of 2-butanol. The optimal reaction temperature for maximizing the yield of 1-butene was $250^{\circ}C$ over HY (60) catalyst.

• Journal of Life Science
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• v.31 no.1
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• pp.59-65
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• 2021

Prunus mume Sieb. et Zucc is distributed throughout Asia and has traditionally been used as medicine and food. P. mume is known to contain large amounts of various organic acids, minerals, and phenol components. To date, the trend of P. mume research has focused only on the effects of antioxidant, anticancer and antibacterial, with only a few studies have focused on angiogenesis. Angiogenesis is a common characteristic of metastatic cancer through which oxygen and nutrients are delivered to the cells and tissues. In the present study, angiogenesis-inhibiting activity was investigated by evaluating the total polyphenol and flavonoid contents of the P. mume butanol fraction (PBF) and their ability to inhibit VEGF-induced human umbilical vein endothelial cells (HUVECs) proliferation, migration, invasion, and capillary formation. The polyphenols (12.81 mg GAE/g) and flavonoids (28.4 mg QE/g) of the PBF exhibited high antioxidant activity. The results of this study showed that PBF did not inhibit the proliferation of HUVECs at concentrations of 25-200 ㎍/ml and did not exhibit toxicity to normal cells. However, PBF inhibited the VEGF-induced mobility, invasion, and capillary formation of HUVECs. These results show that PBF inhibits the angiogenesis of HUVECs induced by VEGF. Therefore, PBF could serve as a therapeutic agent for the inhibition of angiogenesis.

• Membrane Journal
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• v.19 no.1
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• pp.54-62
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• 2009

Pervaporation membrane for butanol separation was prepared by hybrid process. Plasma treatment of commercial poly(dimethylsiloxane) (PDMS) membrane was attempted and combination of plasma treatment and PDMS solution coating on polysulfone, poly(ether imide) supports were also performed. Plasma treatment of PDMS membrane with hexane and silane group compounds was performed to increase the hydrophobicity of the surface, which enhanced the separation factor upto 12.5 at the expense of flux decrease down to $1.15kg/m^2{\cdot}hr$. Contact angle and relative sorption ratio were also related with hydrophobicity of the memrbane. Increase of PDMS prepolymer composition resulted in dense structure of coating layer with better separation factor. Effects of sequence of PDMS coating vs. plasma treatment were examined. It was found that plasma treatment with butanol and n-hexane plasma followed by PDMS coating showed better performance and vice versa for plasma treatment with hexamethyldisilane and hexamethyldisilazane.