• Title/Summary/Keyword: 산화개질

Search Result 233, Processing Time 0.02 seconds

Determination of Biogenic Amines using an Amperometric Biosensor with a Carbon Nanotube Electrode and Enzyme Reactor (Carbon Nanotube 전극과 효소반응기로 구성된 Amperometric Biosensor를 이용한 Biogenic Amines 검출)

  • Kim, Jong-Won;Jeon, Yeon-Hee;Kim, Mee-Ra
    • Journal of the East Asian Society of Dietary Life
    • /
    • v.20 no.5
    • /
    • pp.735-742
    • /
    • 2010
  • Biogenic amines are synthesized by microbial decarboxylation for the putrefaction or fermentation of foods containing protein. Although biogenic amines such as histamine, tyramine, and putrescine are required for many physiological functions in humans and animals, consumption of high amounts of biogenic amines can cause toxicological effects, including serious gastrointestinal, cutaneous, hemodynamic, and neurological symptoms. In this study, a novel amperometric biosensor wasdeveloped to detect biogenic amines. The biosensor consisted of a working electrode, a reference electrode, a counter electrode, an enzyme reactor with immobilized diamine oxidase, an injector, a peristaltic pump and a potentiostat. A working electrode was fabricated with a glassy carbon electrode (GCE) by coating functionalized multi-walled carbon nanotubes (MWCNT-$NH_2$) and by electrodepositing Prussian blue (PB) to enhance electrical conductivity. A sensor system with PB/MWCNT-$NH_2$/GCE showed linearity in the range of $0.5 {\mu}M{\sim}100 {\mu}M$ hydrogen peroxide with a detection limit of $0.5 {\mu}M$. The responses for tyramine, 2-phenylethylamine, and tryptamine were 95%, 75%, and 70% compared to that of histamine, respectively. These results imply that the biosensor system can be applied to the quantitative measurement of biogenic amines.

Strength Development Characteristics of Clay Stabilized with Electric Furnace Steel Slag (전기로 제강슬래그로 안정화된 연약점토의 강도 발현 특성)

  • Hyeongjoo Kim;Taegew Ham;Taewoong Park;Taeeon Kim
    • Journal of the Korean GEO-environmental Society
    • /
    • v.25 no.5
    • /
    • pp.29-37
    • /
    • 2024
  • This study aimed to investigate the changes in chemical components that occur when weak clay is mixed with steel slag modified with calcium oxide, and to understand the expression characteristics of compressive strength according to hydrophilicity and curing time. XRF testing, SEM imaging, vane shear strength and uniaxial compressive strength testing were conducted. Calcium (Ca) released from the steel slag increases the Ca content in clay by increasing the number of crystal particles and forming a coating layer known as calcium silicate hydrate (CaO-SiO2-H2O) through chemical reactions with SiO2 and Al2O3 components. The weak clay stabilized with steel slag is classified into an initial inactive zone where strength relatively does not increase and an activation zone where strength increases over curing time. The vane shear strength of the initial inactive area was found to be 4.4 to 18.4 kN/m2 in the state of the weight mixing ratio Rss 30% (steel slag 30% + clay 70%). In the case of the active area, the maximum uniaxial compressive strength increased to 431.8 kN/m2 after 480 hours of curing time, which increased due to the apparent adhesion strength of clay through pozzolanic reaction. Therefore, considering the strength expression characteristics of stabilized mixed clay based on the mixing ratio (Rss) during the recycling of steel slag can enhance its practicality in civil engineering sites.

Conceptual Design and Hydrodynamic Properties of a Moving Bed Reactor for Intrinsic $CO_2$ Separation Hydrogen Production Process ($CO_2$ 원천분리 수소 제조 공정을 위한 이동층 반응기의 개념 설계 및 수력학적 특성)

  • Park, Dong-Kyoo;Cho, Won-Chul;Seo, Myung-Won;Go, Kang-Seok;Kim, Sang-Done;Kang, Kyoung-Soo;Park, Chu-Sik
    • Clean Technology
    • /
    • v.17 no.1
    • /
    • pp.69-77
    • /
    • 2011
  • The intrinsic $CO_2$ separation and hydrogen production system is a novel concept using oxidation and reduction reactions of oxygen carrier for both $CO_2$ capture and high purity hydrogen production. The process consists of a fuel reactor (FR), a steam reactor (SR) and an air reactor (AR). The natural gas ($CH_4$) is oxidized to $CO_2$ and steam by the oxygen carrier in FR, whereas the steam is reduced to hydrogen by oxidation of the reduced oxygen carrier in SR. The oxygen carrier is fully oxidized by air in AR. In the present study, the chemical looping moving bed reactor having 200 L/h hydrogen production capacity is designed and the hydrodynamic properties were determined. Compared with other reactors, two moving bed reactors (FR, SR) were used to obtain high conversion and selectivity of the oxygen carrier. The desirable solid circulation rates are calculated to be in the range of $20{\sim}100kg/m^2s$ from the conceptual design. The solid circulation rate can be controlled by aeration in a loop-seal. To maintain the gas velocity in the moving beds (FR, SR) at the minimum fluidization velocity is found to be suitable for the stable operation. The solid holdup in moving beds decrease with increasing gas velocity and solid circulation rate.