• Title/Summary/Keyword: Ion Exchange Reaction

검색결과 372건 처리시간 0.021초

Byssochlamys fulca가 생성하는 펙틴질 분해효소에 관한 연구 II (Studies on the Pectolytic Enzymes from Byssochlamys fulva II)

  • 남영중;김남수;홍순우
    • 미생물학회지
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    • 제21권2호
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    • pp.86-94
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    • 1983
  • Polygalacturonase of Byssochlamys fulva was purified and characterized. Specific activity increased from 2.21 units/mg protein to 10.47 units/mg protein through $(NH_4)_2SO_4$ treatment, SephadexG-100 gel filtration, and DEAE-Sephadex ion exchange chromatography. Divalent cations, such as $Ca^{++}\;and\;Cu^{++}$, increased polygalacturonase activity greatly. Added as $10^{-3}M$ concentration, $Ca^{++}$ ion enhanced enzyme activity 9.8folds. Optimum temperature was $50^{\circ}C$ and optimum pH was 5.0. Activation energy of reaction was 8.69 Kcal/mole. Michaelis-Menten $constant(K_M)\;and\;V_{max}$ of reaction were $6.27{\times}10^{-3}mole/l\;and\;2.85{$\mu}moles/min$. Polygalacturonase of Byssochlamys fulva preferred polygalacturonic acid to pectin as substrate and was presumed as endo-type on the basis of the relationship between viscosity reduction and substrate degradation. Molecular weight of polygalacturonase was estimated as 55,000.

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Trimeric Chromium Oxyformate Route to Chromia-Pillared Clay

  • 윤주병;황성호;최진호
    • Bulletin of the Korean Chemical Society
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    • 제21권10호
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    • pp.1049-1051
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    • 2000
  • A chromia-pillared clay has been prepared by ion exchange type intercalation reaction between the sodium ion in montmorillonite and the trimeric chromium oxyformate (TCF) ion, and by subsequent heat-treatment. The structural and thermal properties have been systematically studied by thermal analysis, powder XRD, IR spec-troscopy, and XAS. The gallery height of~6.8 $\AA$ upon intercalation of the TCF ion suggests that the $Cr_3O$ plane is parallel to the aluminosilicate layers. Even though the basal spacing of TCF intercalated clay decreases slightly upon heating, the layer structure was retained up to $550^{\circ}C$ as confirmed by XRD and TG/DTA. Ac-cording to the EXAFS spectroscopic analysis, it is identified that the (Cr-Cr) distance of 3.28 $\AA$ between vertex-linked CrO6 octahedra in TCF splits into 2.64 $\AA$, 2.98 $\AA$, and 3.77 $\AA$ due to the face-, edge-, and corner-shared CrO6 octahedra after heating at $400^{\circ}C$, implying that a nano-sized chromium oxide phase was stabilized within the interlayer space of clay.

이온교환체에 의한 담배 주류연 중 카보닐 화합물의 선택적 흡착 특성 및 흡착 메카니즘 구명 (Investigation of Adsorption Mechanism and Selective Adsorption of Carbonyl Compounds of Mainstream Tobacco Smoke by Ion Exchangers)

  • 이존태;김효근;지상운;황건중;이문수;박진원
    • 한국연초학회지
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    • 제26권2호
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    • pp.159-167
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    • 2004
  • This work has been conducted to select appropriate filter materials for removing carbonyl compounds in mainstream tobacco smoke. To investigate of the usability of this filter materials, two types of bead ion exchangers were synthesized and their adsorption characteristics for carbonyl compounds were investigated. Sulfonic acid group-containing cation exchanger and ammonium group-containing anion exchanger were synthesized by the suspension polymerization of glycidylmethacrylate(GMA) and divinylbenzene(DVB) followed by the subsequent functionalization, respectively. The removal efficiency of carbonyl compounds by these two ion exchangers increased in the presence of moisture. However, the amount of carbonyl compounds adsorbed on the anion exchanger was larger than that on the cation exchanger under two levels of water contents tested. This phenomenon seems to arise from the electron delocalization in carbonyl group of the anion exchangers. There was not any significant relationship between the amount of carbonyl compounds adsorbed on ion exchangers and the length of adsorption column. From the large ion exchange capacity and rapid ion exchange reaction rate of the anion exchanger, it is suggested that the anion exchanger may be a good filter material for removing carbonyl compounds in the mainstream tobacco smoke.

가교결합한 Poly((vinylbenzyl)trimethylammonium chloride-2-hydroxyethyl methacrylate)/poly(vinyl alcohol) 음이온 교환막 제조 (Preparation of Anion Exchange Membranes of Cross-linked Poly((vinylbenzyl)trimethylammonium chloride-2-hydroxyethyl methacrylate)/Poly(vinyl alcohol))

  • 김미양;김광제;강호
    • 공업화학
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    • 제21권6호
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    • pp.621-626
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    • 2010
  • 음이온 교환막은 전기투석뿐만 아니라 역전기투석에 의한 전기생산과 축전 탈이온에 의한 정수 분야에 이용될 수 있다. 본 연구에서는 폴리비닐알콜 수용액 상에서 (vinylbenzyl)trimethylammonium chloride와 2-hydroxyethyl methacrylate를 중합한 후 글루타르산과의 에스테르화 반응, 그리고 글루타르알데히드와 가교반응을 통해서 음이온 교환막을 제조하였다. 실험 변수에 따라 음이온 교환막을 제조하고 이온교환막의 전기화학적 물성을 조사하였다. 중합반응에서 음이온 교환성 단량체 비율에 따라 이온교환량과 저항 값이 변하였으며, 에스테르화 반응에서는 글루타르산의 함량의 증가에 따라 함수율과 전도도가 감소하였다. 형성된 필름과 알데히드의 가교반응 시간 변화는 함수율, 전기저항, 이동수 값들에 영향을 미쳤다. 끝으로 제조된 이온 교환막의 chronopotentiometry와 한계전류밀도도 측정하였다.

방사선 동시조사법을 이용한 고관능성 Hybrid Polyolefine 음이온교환섬유의 합성 (Synthesis of High Functionalized Anion Exchange Fibers Using Hybrid Polyolefine by $\gamma-Ray$ Mutual Radiation)

  • 조인희;곽노석;강필현;노영창;황택성
    • 폴리머
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    • 제30권3호
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    • pp.217-223
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    • 2006
  • 방사선 동시조사에 의해 폴리올레핀 복합 섬유 표면에 고관능성 아민화 이온교환섬유를 합성하였다. 총 조사선량이 증가할수록 그래프트율도 증가하였으며 GMA 농도 50%에서 그래프트율은 최대 365%로 최대 값을 나타내었다. 또한 그래프트 반응은 극성용매에서 일어나며 Mohr's salt, 황산의 함량 $1.0\times10^{-3}M$, 0.1 M에서 그래프트율은 최대 190% 이었다. 아민화 반응은 아민화제의 종류에 따라 각기 다르게 나타났으며 메틸아민의 경우 반응성이 가장 좋았으며 트리에틸아민의 반응성이 가장 낮게 나타났다. 이온교환섬유의 함수율과 이온 교환용량은 아민화율이 증가할수록 높게 나타났으며 비표면적은 그래프트 반응과 아민화 반응이 진행됨에 따라 급격히 감소하는 경향을 보였다.

Cryptand 이온교환 수지를 이용한 우라늄(VI) 이온의 흡착 (Adsorption of Uranium(VI) Ion Utilizing Cryptand Ion Exchange Resin)

  • 박성규;김준태
    • 분석과학
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    • 제17권2호
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    • pp.91-97
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    • 2004
  • 1%, 2%, 5% 및 10%의 가교도를 가진 스틸렌 디비닐벤젠 공중합체에 1-aza-15-crown-5 거대고리 리간드를 치환반응으로 결합시켜 cryptand 이온교환 수지들을 합성하였다. 이들 수지의 합성은 염소 함량과 원소 분석 그리고 IR-스펙트럼으로 확인하였다. 우라늄 ($UO{_2}^{2+}$) 이온의 흡착에 미치는 pH, 시간, 수지의 가교도 그리고 용매의 유전상수에 따른 영향들을 조사하였다. 우라늄 이온은 pH 3 이상에서 큰 흡착율을 보였으며, 금속 이온들의 흡착 평형은 2시간 정도였다. 한편, 에탄올 용매에서 수지에 대한 흡착 선택성은 우라늄 ($UO{_2}^{2+}$), 마그네슘 ($Mg^{2+}$), 네오디뮴 ($Nd^{3+}$) 이온이었고, 우라늄 이온의 흡착력은 1%, 2%, 5% 및 10%의 가교도순 이었으며, 용매의 유전상수 크기에 반비례하였다.

이온교환법에 의한 탈질소 공정개발의 기초연구(IV) -연속식 반응기에서의 속도론과 경제성 분석- (Basic Study for Development of Denitrogenation Process by Ion Exchange(IV) -A Kinetic Study in Continuous Column and an Economic Analysis-)

  • 이민규;주창식;채용곤;김승일;이동환;윤태경
    • 한국환경과학회지
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    • 제9권3호
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    • pp.261-266
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    • 2000
  • A kinetic study for nitrate removal by anion exchange resin was performed using continuous column reactors. Kinetic approach from the packed bed showed the reaction rate constant k$_1$ was 0.07~0.17 $\ell$/mgㆍhr and maximum exchange quantity q$_{o}$ was 27.75~31.81 mg/g. The results from the continuous column well agreed with that from the batch reactor. An economic analysis of the water treatment plant by anion exchange resin with a regenerating system was performed to design plant and process. Based on the treatment of 20 mg/$\ell$ nitrate-contained wastewater of 10,000 gallons per day to 2 mg/$\ell$, total capital cost and total annual cost are estimated to be 836 million wons and 211 million wons, respectively.y.

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Adsorption Characteristics of Al (III), Ni (II), Sm (III) Ions on Resin with Styrene Hazardous Material in Reinforcement Water Fire Extinguishing Agent

  • Kim, Joon-Tae
    • 통합자연과학논문집
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    • 제6권3호
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    • pp.151-157
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    • 2013
  • The ion exchange resins were synthesized from 1-aza-18-crown-6 macrocyclic ligand attached to styrene (2th petroleum in 4th class hazardous material) divinylbenzene (DVB) copolymer with crosslinks of 1%, 6%, and 15% by substitution reaction. These synthetic resins were confirmed by chlorine content, elementary analysis, surface area, and IR-spectrum. The object of this study was to seperate the metal ion absorbed in reinforcement water fire extinguishing agent. As the results of the effects of pH, equilibrium arrival time, and crosslink of synthetic resin on metal ion adsorption for resin adsorbent, the metal ions were showed high adsorption at pH 3 or over and adsorption equilibrium of metal ions was about 2 hours. In addition, adsorption selectivity for the resin in water was the order of Al (III) > Ni (II) > Sm (III) ions, adsorbability of the metal ions was in the crosslinks order of 1%, 6%, and 15%.

물 소화약제로부터 Cryptand 이온교환수지의 Mg(II), Al(III) 및 Pb(II) 흡착특성 (Adsorption Characteristic of Mg(II), Al(III), Pb(II) Metal Ions on Cryptand Ion Exchange Resin from Water Fire Extinguishing Agent)

  • 김준태;김관천
    • 환경위생공학
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    • 제23권1호
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    • pp.57-65
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    • 2008
  • Resins were synthesized with 1-aza-15-crown-5 macrocyclic ligand attached to styrene(dangerous matter) divinylbenzene(DVB) copolymer with crosslink of 1, 2, 6 and 15% by substitution reaction. The synthesis of these resins was confirmed by content of chlorine, element analysis, and IR-spectrum. The effects of pH, time and crosslink on adsorption of metal ion from water fire extinguishing agent by the synthetic resin adsorbent were investigated. The metal ion was showed fast adsorption on the resins above pH 3. The optimum equilibrium time for adsorption of metallic ions was about two hours. The adsorption selectivity determined in water was in increasing order of $Mg^{2+}>Al^{3+}>Pb^{2+}$. The adsorption was in the order of 1, 2, 6, and 15% crosslink resin.

벼에 의한 인산흡수의 기작에 관한 연구 (A Kinetic Study of Phosphate Absorption by Rice Roots)

  • 장남기
    • Journal of Plant Biology
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    • 제21권1_4호
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    • pp.33-38
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    • 1978
  • Phosphate absorption from a Na2H32PO4 solution by Oryza sativa L. was studied in order to elucidate kinetic mechanisms of ion transport. The rates of phosphate absorption from different concentraitons indicated the presence of dual mechanisms in root tips, one in the low (1$\times$10-6 to 8$\times$10-5M) and the other in the high (1$\times$10-4 to 8$\times$10-3M). A phosphate compensation point of phosphate transport was revealed with a 1$\times$10-6M solution of Na2H32PO4. The kinetic model that ion transport involves an exchange reaction of absorption and desorptin is prosposed as follows: where C represents an ionic-specific organic carrier in the membrane; M, Mo and Mi are the mineral ions, M-outside and M-inside; MC is a carrier-ion complex; and the K's represent rate constants. In this model, the Mi velocity, v, is given by: {{{{v= {dMi} over {dt}= {(K1K3Mo-K2K4Mi) Ct} over {(K2+K3)+K1Mo+K4Mi} }} where Ct is equal to C+MC, and t is time.

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