• Title/Summary/Keyword: 수소 이온 농도

Search Result 399, Processing Time 0.028 seconds

특수환경 미생물의 산업적 이용

  • 김상진
    • The Microorganisms and Industry
    • /
    • v.14 no.3
    • /
    • pp.41-46
    • /
    • 1988
  • 극한환경을 구성하는 중요한 환경인자는 온도, 수소이온농도, 염도, 압력, 물, 영양물질 등이 있는데 본 총설에서는 그동안 비교적 많이 다루어지지 않았던 알칼리성환경, 건조환경, 저영양환경, 심해환경과 같은 극한환경과 아울러 특수환경인 해양환경, 지하환경 등으로 나누어 설명했다. 고염환경과 고영양환경, 혐기성환경은 다른 저자에 의해 자세히 다루어지고 고온환경, 산성환경, 극지환경 등은 지면상 이유로 제외했다.

  • PDF

Microsomal Proton Transport Activity Measured by Quinacrine Fluorescence from Tomato Roots (Quinacrine 형광을 이용한 토마토 뿌리조직 마이크로솜의 수소이온이동 활성측정)

  • Shin, Dae-Seop;Cho, Kwang-Hyun;Kim, Young-Kee
    • Applied Biological Chemistry
    • /
    • v.45 no.2
    • /
    • pp.53-58
    • /
    • 2002
  • Quinacrine, a pH-sensitive fluorescence probe, which exists either as an unprotonated fluorescence form or a protonated noufluorescence form, can be used to measure the proton transport activity of $H^+-ATPase$. Quinacrine was used to determine the optimal conditions for measuring the activity of microsomal $H^+-ATPase$ prepared from the roots of tomato plants. The amount of quinacrine fluorescence quenching obtained at $0.43{\mu}g/{\mu}l$ of microsomal protein concentration was 25-26%, which shows that the enzyme activity of 100 nmol/min decreases 10% of quinacrine fluorescence. Maximal fluorescence quenching was obtained at pH 7.0-7.2 and 2 mM $Mg^{2+}$ Because the activity of microsomal $H^+-ATPase$ is also maximal at these conditions, the quinacrine fluorescence well represents the activity of $H^+-ATPase$. Vanadate and $NO_3-$, specific inhibitors of plasma and vacuolar $H^+-ATPases$, respectively, were successfully applied to inhibit the quinacrine fluorescence quenching mediated by the corresponding $H^+-ATPases$. These results imply that quinacrine is a useful tool for measuring the proton transport activities of microsomes obtained from the root tissue of tomato plants.

Leaching of Smelting Reduced Metallic Alloy of Spent Lithium Ion Batteries by the Mixture of Hydrochloric Acid and H2O2 (과산화수소를 혼합한 염산용액으로 폐리튬이온배터리의 용융환원된 금속합금의 침출)

  • Moon, Hyun Seung;Tran, Thanh Tuan;Lee, Man Seung
    • Resources Recycling
    • /
    • v.30 no.5
    • /
    • pp.25-31
    • /
    • 2021
  • Smelting reduction of spent lithium-ion batteries results in the production of metallic alloys in which reduced cobalt, nickel and copper coexist. In this study, we investigated the leaching of the metallic alloys containing the above three metals together with iron, manganese, and silicon. The mixture of hydrochloric acid and hydrogen peroxide as an oxidizing agent was employed, and the effect of the concentration thereof, the reaction time and temperature, and pulp density was investigated to accomplish the complete leaching of cobalt, nickel, and copper. The effect of the hydrogen peroxide concentration and pulp density on the leaching was prominent, compared to that of reaction time and temperature, especially in the range of 20 to 80℃. The complete leaching of the metals present in metallic alloys, except silicon, was accomplished using 2 M HCl and 5% H2O2 with a pulp density of 30 g/L for 150 min at 60℃.

Efficient bio-gas desulfurization purification technology development Using ion-exchange fibers (이온교환섬유를 이용한 바이오가스 고효율 탈황정제기술 개발)

  • Tak, Bong-Yeol;Tak, Bong-Sik;Min, Gil-Ho;Lee, Sang-Min;Lee, Won-Gu;Lee, So-A
    • 한국신재생에너지학회:학술대회논문집
    • /
    • 2011.11a
    • /
    • pp.116-116
    • /
    • 2011
  • 바이오 가스 플랜트의 혐기소화 공정에서 발생하는 바이오 가스는 중 유해가스인 황하수소($H_2S$)는 부식성 가스로 수천 PPM농도를 함유하여, 발전기나 가스보일러로 이용하는 경우에는 $H_2S$를 제거하는 탈황공정이 반드시 필요하다. 탈황방식에는 산화철 탈황(건식 탈황)과 생물 탈황이 현재 많이 사용되고 있어나 산화철 탈황은 산화철 pellet이 유화철에 변화하면 탈황능력이 저하되어 pellet을 교환해야 하며 많은 비용이 발생한다. 생물 탈황 방식은 유황산화세균의 서식활동조건(온도, 반응시간, 산소량)확보가 반드시 필요하여 높은 운전기술을 필요로 한다. 본 연구에서는 바이오가스 전처리 기술 중 활성탄 또는 약액을 이용한 기존의 탈황정제방식보다 흡착성능이 뛰어난 이온교환섬유를 이용하여, 황화수소($H_2S$)를 95% 이상 제거할 수 있는 고효율 섬유상 이온촉매 악취제거 시스템 개발을 수행하였다. 이온교환섬유는 방사선 조사를 이용하여 부직포에 라디칼을 인위적으로 형성시켜(그라프트 중합) 양이온 또는 양이온을 교환할 수 있도록 제조된 섬유상의 흡착제로, 이온교환 섬유의 화학적 이온교환과 물리적 흡착 및 탈착반응이 동시에 발생되고, 활성탄/실리카켈 보다 흡착능력이 2~4배 높다. 또한 이온섬유의 재생기능을 이용하여 장기적 다양한 악취($H_2S$, $NH_3$, 아민계, 메르갑탄류, 알데히드 등) 및 유해가스(VOCs, NOx, SOx) 등을 95% 이상 제거할 수 있다.

  • PDF

Selective Reduction with Zinc Borohydride. Reaction of Zinc Borohydride with Selected Organic Compounds Containing Representative Functional Groups (수소화붕소아연에 의한 선택환원. 수소화붕소아연의 대표적 유기화합물과의 반응)

  • Yoon Nung Min;Ho Jun Lee;Hye Kyu Kim;Jahyo Kang
    • Journal of the Korean Chemical Society
    • /
    • v.20 no.1
    • /
    • pp.59-72
    • /
    • 1976
  • The addition of one mole of zinc chloride to 2.33 moles of sodium borohydride in tetrahydrofuran at room temperature gave a clear chloride-free supernatant solution of zinc borohydride after stirring three days and standing at room temperature.The approximate rates and stoichiometry of the reaction of zinc borohydride with 54 selected organic compounds were determined in order to test the utility of the reagent as a selective reducing agent. Aldehydes and ketones were reduced rapidly, aromatic ketones being somewhat slowly, and the double bond of cinnamaldehyde was not attacked. Acyl halides were reduced rapidly within one hour, but acid anhydrides were reduced at a moderate rate. Carboxylic acids, both aliphatic and aromatic, were slowly reduced to alcoholic stage. Esters were inert to this reagent but a cyclic ester, γ-butyrolactone, was slowly attacked. Primary amides were reduced slowly with partial evolution of hydrogen, whereas tertiary amides underwent neither reduction nor hydrogen evolution. Epoxides and nitriles were all inert, as well as nitro, azo, and azoxy compounds. Cyclohexanone oxime and phenyl isocyanate were reduced slowly but pyridine was inert. Disulfide, sulfoxide, sulfone and sulfonic acids were stable to this reagent.

  • PDF

Determination of Cr(Ⅲ) Iron by Chemiluminescence Method (화학발광법을 이용한 Cr(Ⅲ)이온의 정량)

  • Lee, Sang Hak;Ju, Ik Su
    • Journal of the Korean Chemical Society
    • /
    • v.46 no.2
    • /
    • pp.145-150
    • /
    • 2002
  • A Method to determine Cr(III)ion in aqueous solution by chemiluminescence method using a stopped flow system has been studied. The method is based on the increased chemiluminescence intensity with the addition of Cr(III) to a solution of lucigenin a nd hyrogen peroxide. The effects of pH, injection volumes of reagent and sample, and concentration of lucigenin and hyrogen peroxide on the chemiluminescence intensity have been investigated. The calibration curve for Cr(III) ion was linear over the range from 1.0${\times}$$10^{-6}$ to 1.0${\times}$$10^{-3}$M and the detection limit was 5.2${\times}$$10^{-8}$M under the optimal experimental condition of 437nm, 12.8,and 1.0${\times}$$10^{-6}$ and 2.0M for emission wavelength, pH, and concentration of lucigenin and hyrogen peroxide, respectively.

Kinetic Study of Proton Exchange between Al($H_2O$)$_6^{3+}$ Ion and Bulk Water Molecules (Ⅰ) (Al($H_2O$)$_6^{3+}$ 이온과 물 용매 분자 사이에서의 수소 이온 교환의 반응속도론적 연구 (Ⅰ))

  • Moon-Hwan Cho;Jin-Ho Kim;Chang-Ju Yoon
    • Journal of the Korean Chemical Society
    • /
    • v.32 no.5
    • /
    • pp.436-442
    • /
    • 1988
  • The $^1H-nmr$ lineshapes of $H_2O$ in the solution containing $Al^{3+}$ ion have been measured as a function of temperature and $H^+$-ion concentration. Above [$H^+$] = 0.06, the lineshape were analyzed by the uncoupled two-site exchange model. From the proton exchange rate between hexaaquaaluminium ion and bulk water as a function of H-ion concentration. These kinetic data could be fitted to a following linear rate law; that is; 1/${\tau}$ = k$_1$/12 + $k_2$[$H^+$]/6. The following proton exchange parameters were obtained; $k_1^{298}$ = 38.5s$^{-1}$ ${\{Delta}H_1^{\neq}$ = $42.9kJ mole^{-1}$ ${\{Delta}S_1^{\neq}$ = -48.6J $mole^{-1}K^{-1}$ $k_2^{298}$ = $172s^{-1}mole^{-1}$ ${\{Delta}H_2^{\neq}$ = 27.8kJ $mole^{-1}$ ${\{Delta}S_2^{\neq}$ = -90.3J $mole^{-1}K^{-1}$ These activation parameters are indicating an associative interchange, Ia, mechanism for the acid-hydrolysis of hexaaquaaluminium ion and the proton exchange between the hydration spheres of $Al^{3+}$ and $H^+$.

  • PDF

Cavern Environment in SimBook Cave (심복굴의 동굴 환경)

  • Kim, Choo-Yoon
    • Journal of the Speleological Society of Korea
    • /
    • no.67
    • /
    • pp.35-42
    • /
    • 2005
  • Simbook cave is a livestone cave formed at the Cambrian period. Simbook cave is situated in Kalkum -Ri, YeonPyeong-Meon, Kuisan-Kun, ChungBok province. The temperature of the Simbook cave is about $12\~16^{circ}C$, humidity $90\~95\%$, pH$7\~8$, Water temperature $13\~16^{circ}C$, Carbon dioxide $700\~900$ppmv, hardness 110mg/$\ell$. In Conclusion, Simbook cave does not have values of topography, environment, and tourism resource.

Cavern Environment in Uro Cave (우로굴의 동굴환경)

  • 김추윤
    • Journal of the Speleological Society of Korea
    • /
    • no.62
    • /
    • pp.11-16
    • /
    • 2004
  • Uro cave is a livestone cave formed at the Cambrian period. Uro cave is situated in Urosil, HogyeMyen, Moonkyunssi, HyungBok province. The temperature of the Uro cave is about 12~$15^{\circ}C$, humidity 90~95%, pH 7~8, Water temperature 12~$15^{\circ}C$, Carbon dioxide 500~900ppmv, hardness 110mg/$\ell$ in Conclusion, Uro cave does not have values of topography, environment, and tourism resource.

A Study on the Removal of Nitrate Nitrogens by Redox Reaction of Zinc Ball (아연볼의 산화·환원 반응을 통한 연속식 질산성질소 처리에 관한 연구)

  • Kim, Joon Hwan;Kim, Jong Hwa;Song, Ju Yeong
    • Journal of the Korean Applied Science and Technology
    • /
    • v.34 no.3
    • /
    • pp.487-494
    • /
    • 2017
  • Since nitrate nitrogen is quite stable in aqueous solution, considerable skill is required to remove it. Low concentrations of nitrate nitrogen are easily removed, while high concentrations of nitrate nitrogen are difficult to remove. This study is to show that nitrate nitrogen in the form of gaseous nitrogen can be removed by using zinc ball with a diameter of about 3mm and to test the removal characteristics of nitrate nitrogen under various reaction conditions. As a result of this study, the treatment efficiency of nitrate nitrogen by continuous treatment with zinc ball was about 80%. However, there is a problem that the wastewater must be maintained in an acidic atmosphere of about pH 2, and the treated wastewater must be neutralized and discharged.