• Title/Summary/Keyword: 수소잔류물

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Chemical structure and PVC shape after dehydrochlorination of PVC (탈염화수소후의 PVC형상과 화학구조)

  • 신선명;전호석
    • Resources Recycling
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    • v.13 no.3
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    • pp.37-42
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    • 2004
  • PVC powder was dehydrochlorinated by hydrothermal reaction at reaction time 0∼5 hr, reaction temperature $200∼250^{\circ}C$ in 0∼2M NaOH solution, and shape and structure of the PVC residue was investigated. The shape of the residue was changed largely according to NaOH concentration. Most of the residue was cohered in the aqueous solution, and many pores less than 10 $\mu\textrm{m}$ were formed on the surface. Dense network structure was well developed inside the residue. On the other hand, the residue in the NaOH solution was not cohered and its shape is roughly spherical. In the IR spectrum of the residue both in water and NaOH solution at $250^{\circ}C$, aromatic rings and absorption peak by C=C double bond were observed. From the results, it was observed that aromatic circle reaction and bridge reaction occured inter and intra molecules.

가열탈기체가 확산에 미치는 영향에 대한 수치해석

  • Choe, Ho-Seon;Ha, Tae-Gyun
    • Proceedings of the Korean Vacuum Society Conference
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    • 2016.02a
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    • pp.119.2-119.2
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    • 2016
  • 가열탈기체 처리하면 표면의 물 분자를 빠르게 탈리시켜 단시간에 배기하는 동시에 진공용기 재료 내부의 수소 확산속도를 가속하므로 처리 후 수소 기체방출도 현저하게 낮출 수 있다. 가열탈기체 후의 진공계에서는 물 분자는 일부만 남고 진공용기 재료 내부에서 확산 되어 나온 수소가 잔류가스의 대부분이 된다. 이러한 가열탈기체 처리의 효과에 대해서는 익히 알려져 있으나 정량적으로 예측하기는 쉽지 않았다. 본 연구에서는 가열탈기체 조건이 수소 확산에 미치는 영향에 초점을 맞추어, 진공용기의 재료 및 두께에 따라 목표 진공도에 도달하기 위한 가열탈기체 처리 온도와 시간의 최적 조합을 수치 해석적으로 계산하고 비교하였다.

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Characterization of Product Gas and Residues from Arc Cracking of Waste Lubricating Oil (폐윤활유의 아크 열분해 생성물 및 잔류물 특성 연구)

  • 김인태;김정국;송금주;서용칠;김준형
    • Resources Recycling
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    • v.8 no.5
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    • pp.34-43
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    • 1999
  • An elecmc arc cracking reaclor is developed for the productiol~o f ieusuble fuel gas by the thennal destruction of waste oil. The churaclensucs of product gas and ~esiduesf rom arc crachng of wnste lubr~cat~nogil are sludird. Thc product gas is mainly coruposcd of hydrogen 135-4076), acetylene (13-4076), ethylene 13-476) and olher hgdrocnrbons. The contenr of carbon monomde, one or the main product in a conventional low-temperature Lhennal cracking umt, 1s very slnvll in lhis atc cracking expcnmcnt. Total calocctic wlue of product gas shows 11,000-13.000 kcizlkg, which is hiph cnough to use as a ~ L I I I Cga~ s . and the concentralions oC loxic gases arc well below the rcguliltury emission critena The GCIMS analysis of llquld-phase residues shows that the high rnalccular welgllt hydrocilrbons in the waste oil arc cracked into the low malecular weight hydrocarbons snd hydroem,. The dehydrogcnntion is found lo be Lhe main cracking rcacuon due lo the high temperalure ~ ~ ~ d ubcyc edle ctric arc. The average parucle size of soot as the solid-phase residue is 10 3 wm, and the conlents of cabon a ~ hdea vy metals are abovc 60% and under 0.01 ppm, respecttrely. Thc utllizvtion or sool, as industl-id1 rcsource seems lo he reasible aIter refimng.

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Humidity Dependence of the Residual Stress of Diamond-like Carbon Film (습도에 따른 다이아몬드성 카본필름의 잔류응력 변화에 대한 연구)

  • Lee Young-Jin;Kim Tae-Young;Lee Kwang-Ryeol;Yang In-Sang
    • Journal of the Korean Vacuum Society
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    • v.13 no.4
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    • pp.157-163
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    • 2004
  • Dependence of residual compressive stress of diamond-like carbon (DLC) films on relative humidity was investigated. Polymeric, graphitic and diamond-like carbon films were prepared by r.f.-PACVD using methane or benzene with the negative self bias voltage of the substrate ranging from -100 to -800 V. In-situ measurements of the residual stress were carried out in an environment chamber where the relative humidity was varied from 10% to 90%. In dense DLC film of high residual compressive stress and hardness, we could not observe any change in the residual compressive stress with relative humidity. However, in the cases of graphitic and polymeric DLC films, abrupt change in the residual stress occurred by changing the relative humidity. The quantity of the stress change was inversely proportional to the film thickness, which means that the stress change with humidity is not due to the penetration of the water molecule into the film structure, but due to surface interaction between water molecules and film surface.

KSTAR 2009 실험을 통하여 얻어진 플라즈마 대항부품 내 부의 수소 흡착량과 향후 고주파 가열에 미치는 효과 분석

  • Gwak, Jong-Gu;Kim, Seon-Ho;Wang, Seon-Jeong;Na, Hun-Gyun;Park, Jae-Min
    • Proceedings of the Korean Vacuum Society Conference
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    • 2010.02a
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    • pp.296-296
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    • 2010
  • 핵융합로에서 플라즈마 대항부품(Plasma facing components) 내부에 흡착되는 수소에 대한 조절은 삼중수소의 흡착으로 인한 운전시간 제한뿐만 아니라 원활한 토카막 방전유지를 위하여 매우 중요한 문제이다. 특히 고주파 가열에서는 수소를 소수종으로 사용하는 경우 수소 농도에 대한 수 % 이내의 정밀한 조절이 필요하므로 플라즈마 대항부품 내부의 수소 함유량에 대한 조절이 매우 중요하다. 2009 KSTAR 실험에서는 인보드와 아웃보드에 흑연재질의 플라즈마 대항부품을 사용하였다. 이들은 설치후 진공배기 이전까지 장시간 공기에 노출되었으므로 상당량의 수소와 물이 흡착되었으리라고 예상되었다. 본 발표에서는 잔류가스분석기 및 분광법을 이용하여 토카막 방전중의 수소와 중수소의 비율을 측정하였고 이들을 토카막 방전유지시간, 방전세정과정 등을 매개변수로 분석하였다. 한달여의 토카막 실험을 통하여 플라즈마 대항부품에 대한 활발한 세정활동이 이루어졌음에도 불구하고 중수소에 대한 수소의 농도는 50 % 근방의 값을 유지하였다. 2010년도 실험에서는 신규 설치되는 디버터도 흑연을 사용할 계획이므로 플라즈마 대항부품의 수소흡착량은 더욱 증가할 것이다. 따라서 2010년도에 KSTAR 플라즈마에서 효과적인 고주파 가열을 달성하기 위하여는 강력한 세정 활동을 포함한 수소의 농도 제거활동이 선행되어야한다.

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Occurrence of Pyrobitumen in the Lower Cretaceous Jinju Formation, Korea (하부 백악기 진주층에서 산출되는 고열역청(pyrobitumen)의 산상)

  • Choi, Taejin;Lim, Hyoun Soo;Lee, Jae Il;Lee, Yong Il
    • Journal of the Korean earth science society
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    • v.43 no.5
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    • pp.639-646
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    • 2022
  • Occurrence of black opaque hydrocarbon (pyrobitumen) in some Cretaceous Jinju sandstones of the Sindong Group, Gyeongsang Basin in Korea is first reported in this study. The pyrobitumen is developed on chlorite pore-lining cement, or impregnated into the outer zone of chlorite cement. Therefore, it seems to have been formed after the precipitation of chlorite cement, indicating the former presence of crude oil. The liquid hydrocarbons migrated into sandstones during moderate burial and these sandstones seem to have acted as a liquid hydrocarbon reservoir. The presence of pyrobitumen in the Jinju Formation indicates that this formation underwent deep burial after liquid hydrocarbon migration. As reservoir temperatures increased further, hydrocarbons were cracked and a solid pyrobitumen residue remained in the reservoir.

Use of Hydrogen Peroxide with Ozone to Simultaneously Reduce MIB and Quench Ozone Residual in Existing Water Treatment Plants Sourcing Water from the Han River (한강을 원수로 하는 오존/과산화수소 고도정수처리공정에서의 MIB제거 및 잔류오존 농도에 관한 연구)

  • McAdams, Stephen R.;Koo, Bon Jin;Jang, Myung Hoon;Lee, Sung Kyoo
    • Journal of Korean Society on Water Environment
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    • v.28 no.5
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    • pp.704-716
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    • 2012
  • This paper provides a detailed account of pilot testing conducted at South Lake Tahoe (California), the Ddukdo (Seoul) water treatment plant (WTP) and the Bokjung (Seongnam) WTP between February, 2010, and February, 2012. The objectives were first, to characterize the reactions of ozone with hydrogen peroxide (Peroxone) for Han River water following sand filtration, second to determine empirical ozone and hydrogen peroxide doses to remove a taste-and-odor surrogate 2-methylisoborneol (MIB) using an advanced oxidation process (AOP) configuration and third, to determine the optimum dosing configuration to reduce residual ozone to a safe level at the exit of the process. The testing was performed in a real-time plant environment at both low- and high seasonal water temperatures. Experimental results including ozone decomposition rates were dependent on temperature and pH, consistent with data reported by other researchers. MIB in post-sand-filtration water was spiked to 40-50 ng/L, and in all cases, it was reduced to below the specified target level (7 ng/liter) and typically non-detect (ND). It was demonstrated that Peroxone could achieve both MIB removal and low effluent ozone residual at ozone+hydrogen peroxide doses less than those for ozone alone. An empirical predictive model, suitable for use by design engineers and operating personnel and for incorporation in plant control systems was developed. Due to a significant reduction in the ozone reaction/decomposition at low winter temperatures, results demonstrate the hydrogen peroxide can be "pre-conditioned" in order to increase initial reaction rates and achieve lower ozone residuals. Results also indicate the method, location and composition of hydrogen peroxide injection is critical to successful implementation of Peroxone without using excessive chemicals or degrading performance.

Variation of Hydrogen Residue on Metallic Samples by Thermal Soaking in an Inert Gas Environment (불활성 가스하 열건조에 따른 금속시험편의 수소잔류물 거동 분석)

  • Lee, Yunhee;Park, Jongseo;Baek, Unbong;Nahm, Seunghoon
    • Transactions of the Korean hydrogen and new energy society
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    • v.24 no.1
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    • pp.44-49
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    • 2013
  • Hydrogen penetration into a metal leads to damages and mechanical degradations and its content measurement is of importance. For a precise measurement, a sample preparation procedure must be optimized through a series of studies on sample washing and drying. In this study, two-step washing with organic solvents and thermal soaking in inert gas were tried with a rod-shaped, API X65 steel sample. The samples were machined from a steel plate and then washed in acetone and etyl-alcohol for 5 minute each and dried with compressed air. After then, the samples were thermally soaked in a home-made nitrogen gas chamber during 10 minute at different heat gun temperatures from 100 to $400^{\circ}C$ and corresponding temperature range in the soaking chamber was from 77 to $266^{\circ}C$ according to the temperature calibration. Hydrogen residue in the samples was measured with a hot extraction system after each soaking step; hydrogen residue of $0.70{\pm}0.12$ wppm after the thermal soaking at $77^{\circ}C$ decayed with increase of the soaking temperature. By adopting the heat transfer model, decay behavior of the hydrogen residue was fitted into an exponential decay function of the soaking temperature. Saturated value or lower bound of the hydrogen residue was 0.36 wppm and chamber temperature required to lower the hydrogen residue about 95% of the lower bound was $360^{\circ}C$. Furthermore, a thermal desorption spectroscopy was done for the fully soaked samples at $360^{\circ}C$. Weak hydrogen peak was observed for whole temperature range and it means that hydrogen-related contaminants of the sample surface are steadily removed by heating. In addition, a broad peak found around $400^{\circ}C$ means that parts of the hydrogen residue are irreversibly trapped in the steel microstructure.

20인치 크라이오 워터펌프 (CWP) 배기성능 종합평가

  • In, Sang-Ryeol;Lee, Dong-Ju;Han, Myeong-Hui
    • Proceedings of the Korean Vacuum Society Conference
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    • 2016.02a
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    • pp.119.1-119.1
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    • 2016
  • 크라이오 워터펌프(CWP)는 크라이오 펌프(CP)와 달리 10 K 활성탄 어레이는 장착하지 않고 100 K 정도로 냉각시킨 배플만을 사용하여 물의 배기속도를 최적화 하는 데 초점을 맞춘 진공펌프다. 용기 압력이 10-9 mbar 대가 될 때까지는 잔류기체의 90% 이상이 수분이므로 다른 기체들의 배기 보다는 물을 잘 배기하는 것이 배기시간을 단축하고 도달 진공도를 낮추는 첩경이라는 아이디어에 근거를 두고 있다. CWP는 물 흡착확률을 거의 1에 가깝게 만들어서 오리피스 컨덕턴스에 육박하는 이상적인 펌프를 제작할 수 있지만 용도상 직부형(close type), 통과형(in-line type) 및 내장형(in-vessel type) 등 세 가지 다른 형태에 따라 성능도 약간씩 다르다. CWP는 모든 기체에 반응하는 정통적인 CP에 비해 훨씬 간단하고 저렴하게 만들 수 있으면서도 진공 시스템에 큰 영향을 미칠 수 있지만 물 이외의 기체들을 배기할 펌프가 필요하다는 측면에서 활용에 제약이 있다. 만일 TMP를 이미 사용하고 있거나 작은 TMP를 추가로 달아서 충분히 작동이 가능한 시스템이면서 수분 발생이 많은 곳이나, 또 활성탄의 오염이나 산소 분위기 등 CP 투입이 꺼려지는 환경이라면 CWP 사용이 좋은 선택이 될 수 있다. CWP의 물 배기용량은 CP의 알곤이나 질소 배기용량에 준하는 크기로 0.5g/cm2 이상임이 실험적으로 입증되었다. 따라서 일반적인 상황에서 정상 작동시 대부분의 기체는 TMP로 배출하고 잔류 수분만 포집하므로 CP처럼 주기적인 재생이 필요 없다. 필요하다면 CWP는 금속 표면에 응축된 물을 드라이펌프 작동만으로 쉽게 제거할 수 있고 혹시 오염 물질이 붙어도 세척이 용이하다. 이런 사용상 융통성과 여러 가지 장점에도 불구하고 그동안 물배기에 대한 인식이 미흡하고, 또 부수적이고 추가적인 비용이 드는 것으로 생각되어 주목을 받지 못했지만 디스플레이와 반도체 산업을 필두로 물 분압을 낮추고 생산수율을 높이는 것에 점점 더 관심이 높아지면서 CWP에 대한 수요도 높아지고 있다. 본 보고에서는 20인치 통과형 CWP를 만들고 14인치 TMP에 얹어 복합 진공배기시스템을 구성한 후 물 배기속도와 알곤, 질소 및 수소 배기속도를 측정하고 예측치와 비교했다. 아울러 물 배기용량 측정 및 CWP의 온도제어와 펌프재생 특성 평가 결과도 정리했다.

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Persistence and degradation of herbicide molinate in paddy-soil environment (논토양 환경 중 제초제 molinate의 잔류성과 분해특성)

  • Park, Byung-Jun;Park, Hyeon-Ju;Lee, Byung-Moo;Ihm, Yang-Bin;Choi, Ju-Hyeon;Ryu, Gab-Hee
    • The Korean Journal of Pesticide Science
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    • v.9 no.1
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    • pp.60-69
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    • 2005
  • The herbicide molinate has been detected with high frequency in the main river during the growing season in Korea. To elucidate the exposure of molinate in agricultural environment, the persistence and the degradation characteristics of molinate were investigated in paddy ecosystems. The half-lives of molinate were 4.1 days with soil aquatic system, and 4.2 days in only aquatic system. Initial dissipation rate of molinate in water was greater with soil aquatic system than that of only aquatic system. Photolysis of molinate was occurred about 31.0% of molinate treated in pure water, when irradiated at 5,530 $J/cm^2$ by the xenon lamp, but its hydrolysis was stable. For the accelerated photolysis of molinate in aqueous solution, several photosensitizers were screened, showing that the hydroperoxide($H_2O_2$) and acetone were prominent among the chemical tested. When hydroperoxide and zinkoxide(ZnO) were used as photosensitizer, their photolysis were accelerated greater than 98% and 58% in aqueous solution, respectively. Elution rate of molinate as granular formulations in aqueous system was more than 90% in 30 hour at $35^{\circ}C$. Molinate concentration pattern in paddy water was rapidly decrease from treatment till 7 days in paddy rice field and its half-lives were 3.7 days($Y=1.9258{\times}e^{-0.1865X}$(r=-0.9402)).