• The Korean Journal of Physiology
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• v.23 no.2
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• pp.351-361
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• 1989

The contraction of renal arterial strip by no.epineph.me (NE) or 40 mM $K^+$ were Significantly attenuated after histamine $(10^{-5}\;M)-induced$ contraction. The mechanisms of this phenomenon were investigated in the helical strips of isolated renal artery with the measurement of isometric tension. The arterial strip was immersed in the tris-buffered Tyrode's solution which was equilibrated with 100% $O_2\;at\;35^{\circ}C$. The contraction was induced by NE or 40 mM $K^+$ during the recovery from the histamine-induced contraction which lasted for 15 minutes. The contraction by NE was also attenuated in the $Ca^{2+}-free$ Tyrode's solution and the increase of contraction by addition of 2 mM $Ca^{2+}$ was attenuated as well. This attenuation phenomenon was not observed in the presence of low concentration $(3{\times}10^{-7}\;M)$ of histamine. This attenuation was not affected by destruction of endothelium, pretreatment with papaverine or propranolol. This attenuation was partially inhibited by pretreatment of ouabain or in low $K^+(0.5 mM)$ Tyrode's solution. But the attenuation in the $Ca^{2+}-free$ Tyrode's solution was not inhibited. Furthermore this attenuation was completely blocked by pretreatment of djphenhydramine $(H_1-receptor blocker)$ and potentiated by pretreatment of cimetidine $(H_2-receptor\;blocker)$. This attenuation Phenomenon was disappeared after recovery of 1 hour. From the above results, it is suggested that the attenuation phenomenon may be resulted partially from the activation of $Na^+-K^+$ exchange pump and partially from the depletion of intracellular $Ca^{2+}$ pool after the histamine-induced contraction mediated through $H_1-receptor$ function.

• Journal of the Korean Crystal Growth and Crystal Technology
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• v.17 no.6
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• pp.238-244
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• 2007

Nano-sized ZnO crystals were successfully incorporated using ion exchange method in TMA-A zeolite synthesized by the hydrothermal method. The optimal composition for the synthesis of TMA-A zeolite was resulted in a solution of $Al(i-pro)_3$:2.2 TEOS:2.4 TMAOH:0.3 NaOH:200 $H_2O$. 0.3g of TMA-A zeolite and 5mol of $ZnCl_2$ solution were employed for the preparation of ZnO incorporated TMA-A zeolite. The ZnO incorporated TMA-A zeolite precursors, prepared from the process of mixing, stirring, centrifugal separation and drying, were calcined at temperatures from 400 to $600^{\circ}C$ for 3 h. The crystallization process of ZnO incorporated TMA-A zeolite was analyzed by X-ray diffraction (XRD). The Brunaur-Emett-Teller (BET) surface area of the ZnO incorporated TMA-A zeolite was measured. Subsequently, the morphology and the particle size depending on the temperature and time were observed using scanning electron microscopy(SEM), transmission electron microscopy(TEM) and particle size analyzer.

• Korean Journal of Poultry Science
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• v.16 no.3
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• pp.157-167
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• 1989

Pretreatment of egg white and ion exchange resins was attempted to separate lysozyme from egg white efficiently. Apparent viscosity of egg white could be decreased to 3cp by homogenization for 30 minutes at 2, 000rpm and ultrasonication for 45 minutes. The result of testing adsorption capacity of lysozyme was as follows； CM-Sephadex C-25 ＞Duolite C464＞Amberlite C-50＞Dowex MSC-1＞Amberlite IRC-50＞Amberlite IRC-84. Although CM-Sephadex C-25 showed highest adsorption capacity of lysozyme, egg white could not eluted easily. Duolite Cf64 was selected based on relatively high lysozyme adsorption and good egg white eluting property for separation of egg white lysozyme. Na$^{＋}$ form of Duolite C-464 was most effective on adsorption of Iysozyme. To separate lysozyme from egg white efficiently rinse buffer and eluting solution were selected 0.1M sodium phosphate buffer at pH 6.5 and 10% ammonium sulfate respectively. After separating lysozyme from egg white, foaming power of egg white was decreased to 85.3%. Color of egg white gel was not changed while hardness of egg white gel was decreased by 30% after separating lysozyme. However, elasticity of egg white gel was increased by 13% in lysozyme-separated egg white.

• Food Science and Biotechnology
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• v.15 no.6
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• pp.908-913
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• 2006

Recombinant ${\beta}$-galactosidase from Bifidobacterium longum LL04 was expressed in Escherichia coli and partially purified by ammonium sulphate precipitation and anion-exchange chromatography (Mono-Q). The optimum temperature and pH of the partially purified enzyme were $50^{\circ}C$ and pH 7.0-8.0, respectively, when o-nitrophenyl-${\beta}$-D-galactopyranoside was used as a substrate. The enzyme was stable over the pH range of 5.0-9.0, and was active at $40^{\circ}C$ for more than 60 min at pH 7.0. The enzyme was significantly activated by $Na^+$ and $K^+$. Maximal activity was observed at the concentration of 10 mM for both $Na^+$ and $K^+$. The enzyme activity was strongly inhibited by most bivalent metal ions. The Km and Vmax on ONPG at 37 and $50^{\circ}C$ were 0.72, 167.9, and 0.507 mM, 310.9 U/mL, respectively.

• Korean Journal of Soil Science and Fertilizer
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• v.29 no.4
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• pp.321-327
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• 1996

A back titration method was suggested to determine the exchangeable acidity of soil originated from exchangeable aluminum and adsorbed hydrogen ion in relation to minimizing its titration error. In this method. soils are treated by neutral salt solution whose concentration is the same as soil solution suspended by distilled water. And then. its pH is adjusted at 3, using 1 N HCl solution and back-titrated by 0.1 N NaOH solution containing 1 N NaCl. The results of the suggested back-titration showed the possibility of practical application with linear relationship to that of standard method.

• Resources Recycling
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• v.31 no.5
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• pp.3-19
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• 2022

Electro-membrane technology is a process for separating and purifying substances in aqueous solution by electric energy using an ion exchange membrane with selective permeability, such as electrodialysis (ED) and bipolar electrodialysis (BMED). Electro-membrane technology is attracting attention as an environmental friendly technology because it does not generate by-products during the process and the recovered base or acid can be reused during the process. In this paper, we investigate the principles of ED and BMED technologies and various characteristics and problems according to the cell configuration. In particular, by investigating and analyzing research cases related to the treatment of waste sodium sulfate (Na₂SO₄), which is generated in large amounts during the metal recovery process.

• Food Science and Preservation
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• v.10 no.2
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• pp.246-251
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• 2003

Pretense produced by Bacillus subtilis PANH765 was purified from culture supernatant by using ammonium sulfate fractionation DEAE-cellulose ion exchange chromatography, and gel filtration with Sephacryl S 200 HR and Sepharose CL-6B. DEAE-cellulose ion exchange column chromatography, separated the pretense into one fraction. This fraction was further purified using Sephacryl S 200 HR and Sepharose CL-6B gel titration. The molecular mass of pretense was estimated to be 35.0 kDa by the SDS-PAGE and gel filtration using Sepharose CL-6B. The results indicated that the purified pretense are monomeric proteins. Specific activity and purification folds of pretense were 657 U/mg and 4.35, respectively. The optimum temperature, optimum pit stable at a temperature range and pH ranges for the purified protease were 65$^{\circ}C$, 7.05, 50 ∼ 75$^{\circ}C$ and 6.0 ∼ 7.5, respectively. The pretense activity was decreased by the presence of PMSF and DFP, which the protease activity was increased by the presence of Na$\^$+/, K$\^$+/, Mg$\^$2＋/ and NH$_4$$\^$+/ ions.

• Korean Journal of Soil Science and Fertilizer
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• v.42 no.4
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• pp.239-248
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• 2009

In this investigation, we observed surface morphology and porosity of a macroporous adsorbent made of Na-bentonite and Ca-bentonite as structure formation materials and grounded waste paper as macropore forming material for the development of a permeable reactive barrier to remove heavy metals in groundwater. Therefore, we selected minerals having higher cation exchange capacity among 2:1 clay minerals and other industrial minerals because sintering can significantly influence cation exchange capacity, resulting in drastic decrease in removal of heavy metals. The results showed that the increasing sintering temperature drastically decreased CEC by less than 10 % of the indigenous CEC carried by the selected minerals. One axial compressibility test results showed that the highest value was obtained from 5% newspaper waste pulp for both structure formation materials of Na-bentonite and Ca-bentonite although there were not much difference in bulk density among treatments. The pore formation influenced by sintering temperature and period contributes removal of heavy metals passing through the sintered macroporous media having different water retention capacity.

• Korean Journal of Veterinary Research
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• v.39 no.1
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• pp.62-69
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• 1999

Although it has been reported that hormones or chemicals, which increase in intracellular cAMP, produced $Mg^{2+}$ release from the heart, it is not well characterized whether a specific $Mg^{2+}$ exchanger is involved in cAMP-induced $Mg^{2+}$ efflux in the mammalian hearts. In this work, we studied the relationship between the increase in intracellular cAMP and ion transport system on $Mg^{2+}$ regulation in the perfused rat heart and isolated myocytes. The $Mg^{2+}$ content in the perfusate and supernatant were measured by atomic absorption spectrophotometer. The addition of membrane permeable cAMP analogue to the perfused hearts and myocytes induced a $Mg^{2+}$ efflux in the dose dependent manners. $Mg^{2+}$ efflux was stimulated by cAMP modulators (forskolin, IBMX and Ro20-1724) in the perfused hearts and myocytes. cAMP-induced $Mg^{2+}$ efflux was inhibited by $H_7$, benzamil or imipramine in the perfused hearts and myocytes, but not by EIPA. We confirmed that a significant $Mg^{2+}$ efflux was induced by an increase in intracellular cAMP in the hearts and myocytes. The cAMP-induced increase of $Mg^{2+}$ efflux in the hearts may be involved in ion transport system ($Na^+-Ca^{2+}$ and $Na^+-Mg^{2+}$ exchanger).

• The Korean Journal of Food And Nutrition
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• v.9 no.3
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• pp.247-252
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• 1996

$\beta$-Amylase was purified from sweet potato by acetone fractlonatlon, Sephadex A-50 ion exchange chromatography and Sepgadex G-200 gel chromatographyl The higher enzyme concentration was, the higher heat stability of enzyme became. After 1 hour 30 minute. At 6$0^{\circ}C$ in pH 5, enzyme under concentration of 30$\mu$l/ml lost its activity completely and over the concentration of 100$\mu$g/ml remained 25% of activity. The enzyme was stabilized at range of pH 4~10 and pH stability was increased by glycerol. Five moles of NaCl inhibited completely of the enzyme activity. SDS of 0.05% inhibited the enzyme completely after 12 hours at 37$^{\circ}C$ in pH5. One mole guanidine-HCl and 8M urea inhibited the entire enzyme after 13 hours at 37$^{\circ}C$ in pH 5.