• Title/Summary/Keyword: H2 energy

Search Result 6,780, Processing Time 0.039 seconds

Characteristics of Flame Hardening Process for 12Cr Steels (12Cr 강의 이동 화염경화 공정 특성)

  • Kim Gwang-Ho;Lee Min-Ku;Kim Kyeong-Ho;Kim Whung-Whoe;Rhee Chang-Kyu;Kim Gil-Mu
    • Journal of the Korean institute of surface engineering
    • /
    • v.39 no.2
    • /
    • pp.49-56
    • /
    • 2006
  • In this study, the movable flame hardening process of 12Cr steel for a uniform hardness and desirable residual stress have been investigated. For this, the temperature cycles have been controlled accurately as a function of the three processing variables, the flame intensity $I_f$, the scanning velocity $V_s$, and the initial flame holding time $t_h$, where the standard surface temperature $T_{s,\;max}$, was maintained at $960^{\circ}C$. The optimized conditions were $V_s=0.68mn/s\;and\;t_h=67sec$ for the $C_3H_8:O_2\;=\;5:20l/min,\;V_s=0.80mm/s$ and $t_h=56sec$ for the $C_3H_8:O_2=6:24l/min,\;V_s=1.01mm/s\;and\;t_h=48sec$ for the $C_3H_8:O_2=7:28l/min,\;and\;V_s=1.15mm/s$ and $t_h=39sec$ for the $C_3H_8:O_2$=8:32 l/min. The optimally flame-hardened surface exhibited uniform distributions of the hardness and residual compressive stress over the treated area with moderate levels of $470{\sim}490HV_{0.2}$in hardness and $-300{\sim}-450MPa$ in residual stress, which were acceptable on the basis of the acceptance criteria of Siemens AG-KWU and GE Power Generation Engineering.

Removal of Cobalt ion by Foam Flotation(I): Precipitate Flotation (거품부상법을 이용한 코발트이온제거(I): 침전부상법)

  • Jung, In Ha;Park, Hee Seoung;Moon, Je Sun;Yim, Sung Paal;Bae, Ki Kwang
    • Applied Chemistry for Engineering
    • /
    • v.10 no.1
    • /
    • pp.41-45
    • /
    • 1999
  • Simulated liquid waste containing 50 ppm cobalt ion was treated by precipitate flotation using the surfactant of sodium lauryl sulfate. The effects of initial cobalt ion concentration, pH, surfactant concentration, removal time, gas flow rate and foreign ions were estimated on removal efficiency. 35% $H_2O_2$ was added for pre-treatment stage before precipitate flotation. As the result of pre-treatment, optimum removal pH and the pH of treated water being discharged were lowed and optimum removal pH range was broadened. For the result of this experiment, 99.8% removal efficiency was obtained at the condition of 50ppm of initial cobalt ion concentration, pH 9.5, 70 mL/min of gas flow rate, and 30 min of removal time. Attraction between precipitate and surfactant was supposed to be influenced by solubility and chemical affinity among species in sloution as well as zeta potential. The influence of foreign ions such as, $NO_3{^-}$, ${SO_4}^{-2}$, $Na^+$, $Ca^{+2}$ on the removal efficiency was also observed. Removal efficiency by precipitate flotation containing 0.1 M of ${SO_4}^{-2}$ ion decreased to 90% due to the decrease of zeta potential and interruption of precipitation.

  • PDF

Application of Two Centre Huckel Method for C-C Bond Fission and Hydrogen Abstraction of Saturated Hydrocarbons (二中心 Huckel 法의 應用. 포화탄화수소의 C-C 切斷 및 水素의 反應性)

  • Park, Byung-Kak;Lee, Mu-Sang
    • Journal of the Korean Chemical Society
    • /
    • v.16 no.2
    • /
    • pp.59-63
    • /
    • 1972
  • In connection with two electron binding energy of each bond of saturated hydrocarbons, C-C bond fission and hydrogen abstraction from C-H bond are discussed by means of two center Huckel method. A beautiful correlation could be noticed between the observed bond dissociation energy and the calculated bond energy except for n-butane. Bond dissociation energies between C-C bond were also related to C-C bond fission. We could also find a very close relation between the relative easiness of hydrogen abstraction and the calculated binding energy of C-H bond. In other words, C-H bonds of tertiary hydrogen have been noticed as most weakely bonded and hence the tertiary hydrogen would most easily from the paraffins. In addition, the C-H binding energy is discussed applying ionic character of C-H bond which is derived from its dipole moment (0.4D)

  • PDF

Room temperature deposition of SiN thin film using pulsed $SiH_4-N_2$ plasma and the effect of duty ratio on refractive index (펄스드 $SiH_4-N_2$ 플라즈마를 이용한 SiN 박막의 상온 증착과 굴절률에의 Duty ratio 영향)

  • Kwon, Sang-Hee;Kim, Byung-Whan;Woo, Hyung-Su;Lee, Hyung-Gu
    • Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
    • /
    • 2009.06a
    • /
    • pp.25-26
    • /
    • 2009
  • Pulsed-PECVD를 이용하여 상온에서 실리콘 나이트라이드(SiN) 박막을 증착하였다. 본 연구에서는, 60-100%의 duty ratio 변화에 따른 굴절률을 살펴보고, 굴절률에 대한 이온에너지의 영향을 분석했다. RF 소스파워는 900W로 고정하였고 $SiH_4-N_2$를 이용하였다. 이온에너지에 대한 정보는 non-invasive 이온 분석기를 이용하여 수집하였다. 측정된 이온에너지 변수는 high ion energy, low ion energy, high ion energy flux, low ion energy flux이며, 이를 이용해 또 다른 변수인 ion energy flux ratio를 계산하였다. Duty ratio의 감소에 따라 굴절률은 일반적으로 감소하였다. 또한 duty ratio의 감소에 따라 high ion energy는 증가하였다. 한편, 60-80%에서 굴절률은 이온에너지 flux의 비에 강한 의존성을 보였으며, 60%를 제외한 모든 duty ratio 구간에서 굴절률은 Nl에 강하게 영향을 알고 있는 것으로 유추되었다. 굴절률은 1.508와 1.714 사이에서 변화하였다.

  • PDF

Lyophobized Ordered Mesoporous Silica Additives for Li-O2 Battery Cathode

  • Roev, Victor;Ma, Sang Bok;Lee, Dong Joon;Im, Dongmin
    • Journal of Electrochemical Science and Technology
    • /
    • v.5 no.2
    • /
    • pp.58-64
    • /
    • 2014
  • The surface of an ordered mesoporous silica (OMS) was functionalized using 1H,1H,2H,2H-perfluorooctyltrimethoxysilane at $20^{\circ}C$ and $60^{\circ}C$. It was shown that only elevated temperature allows lyophobic properties on the walls of OMS, eventually preventing pore flooding with nonaqueous electrolytes. The functionalized OMSs (OMS-F) were characterized with various techniques: wettability test, $N_2$ sorption measurement, high-resolution transmission electron microscopy (HR-TEM). Cathodes of $10mg/cm^2$ loading were prepared with a commercial Pt/C catalyst and polyvinylidene fluoride (PVDF, 2.5 wt.%) binder using a typical doctor blade method on a commercial gas diffusion layer (GDL) in the presence or in the absence of OMS-F additives. Subsequent discharge-charge curves were taken in a 1M LiTFSI-TEGDME electrolyte at 60oC in pure oxygen atmosphere. It was found that the discharge capacity was significantly affected by OMS-F: 5 wt.% of additive extended discharge capacity by a factor 1.5. On the other hand, a similar OMS material but synthesized at $20^{\circ}C$ did not show lyophobic properties and deteriorated cathode capacity.

A Study of Hydroxyapatite Production from Waste Oyster Used Mechanochemical Treatment

  • Kim, Sun-Tae;Oh, Chi-Jung;Kim, Wan-Tae;Kim, Young-Sig;Kim, Myong-Jun
    • Proceedings of the IEEK Conference
    • /
    • 2001.10a
    • /
    • pp.469-471
    • /
    • 2001
  • Dry grinding of a mixture of CaCO$_3$ and Ca(H$_2$PO$_4$)$_2$.$H_2O$ was conducted using a planetary ball mill in order to investigate solid state reaction for a synthesis of hydroxyapatite(Ca$_{10}$(PO$_4$)$_{6}$(OH)$_2$, HAp) through mechanochemical treatment method. The raw materials, which are composed of waste oyster and calcium biphosphate Ca(H$_2$PO$_4$)$_2$.$H_2O$, were mixed and then treated mechanochemically. The synthesis of hydroxyapatite(Ca$_{10}$(PO$_4$)$_{6}$(OH)$_2$, HAp) from the mixture was almost completed by about 60 minute grinding. The formation of HAp monophase in the ground mixture was characterized through X-ray diffraction (XRD) analysis. Moreover, the formation of HAp monophase depending on the grinding time was improved by increasing the grinding time.ime.ime.

  • PDF

Preferential CO Oxidation over Ce-Promoted Pt/γ-Al2O3 Catalyst (Ce가 첨가된 Pt/γ-Al2O3 촉매의 선택적 CO 산화반응 특성)

  • Kim, Kihyeok;Koo, Keeyoung;Jung, Unho;Yoon, Wanglai
    • Transactions of the Korean hydrogen and new energy society
    • /
    • v.23 no.6
    • /
    • pp.640-646
    • /
    • 2012
  • The effect of Ce promotion over 1wt% $Pt/{\gamma}-Al_2O_3$ catalysts on the CO conversion and $CO_2$ selectivity was investigated in preferential CO oxidation (PrOx) to reduce the CO concentration less than 10 ppm in excess $H_2$ stream for polymer electrolyte membrane fuel cell (PEMFC). Ce-promoted 1wt% $Pt/{\gamma}-Al_2O_3$ catalysts were prepared by incipient wetness impregnation method and the loading amount of Pt was fixed at 1wt%. The content of Ce promoter which has excellent oxygen storage and transfer capability due to the redox property was adjusted from 0 to 1.5wt%. Ce-promoted 1wt% $Pt/{\gamma}-Al_2O_3$ catalysts exhibit high CO conversion and $CO_2$ selectivity at low temperatures below $150^{\circ}C$ due to the improvement of reducibility of surface PtOx species compared with the 1wt% $Pt/{\gamma}-Al_2O_3$ catalyst without Ce addition. When Ce content was more than 1wt%, the catalytic activity was decreased at over $160^{\circ}C$ in PrOx because of competitive $H_2$ oxidation. As a result, 0.5wt% Ce is optimal content not only to achieve high catalytic activity and good stability at low temperatures below $150^{\circ}C$ in the presence of $CO_2$ and $H_2O$ but also to minimize the $H_2$ oxidation at high temperatures.

Oxidation of CVD β-SiC in Impurity-Controlled Helium Environment at 950℃ (950℃ 불순물을 포함한 헬륨 환경에서 CVD β-SiC의 산화)

  • Kim, Dae-Jong;Kim, Weon-Ju;Jang, Ji-Eun;Yoon, Soon-Gil;Kim, Dong-Jin;Park, Ji-Yeon
    • Journal of the Korean Ceramic Society
    • /
    • v.48 no.5
    • /
    • pp.426-432
    • /
    • 2011
  • The oxidation behavior of CVD ${\beta}$-SiC was investigated for Very High Temperature Gas-Cooled Reactor (VHTR) applications. This study focused on the surface analysis of the oxidized CVD ${\beta}$-SiC to observe the effect of impurity gases on active/passive oxidation. Oxidation test was carried out at $950^{\circ}C$ in the impurity-controlled helium environment that contained $H_2$, $H_2O$, CO, and $CH_4$ in order to simulate VHTR coolant chemistry. For 250 h of exposure to the helium, weight changes were barely measurable when $H_2O$ in the bulk gas was carefully controlled between 0.02 and 0.1 Pa. Surface morphology also did not change based on AFM observation. However, XPS analysis results indicated that a very small amount of $SiO_2$ was formed by the reaction of SiC with $H_2O$ at the initial stage of oxidation when $H_2O$ partial pressure in the CVD ${\beta}$-SiC surface placed on the passive oxidation region. As the oxidation progressed, $H_2O$ consumed and its partial pressure in the surface decreased to the active/passive oxidation transition region. At the steady state, more oxidation did not observable up to 250 h of exposure.