• 열처리공학회지
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• 제17권2호
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• pp.87-93
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• 2004

Nitrocarburizing was carried out with various $CH_4$ gas composition with 4 torr gas pressure at $570^{\circ}C$ for 3 hours and post oxidation was carried out with 100% $O_2$ gas atmosphere with 4 torr at different temperatures for various time. In the case of plasma nitrocarburizing, It is that the ratio of ${\varepsilon}-Fe_{2-3}$(N, C) and ${\gamma}^{\prime}-Fe_4$(C, N), which comprise the compound layer phase, depend on concentrations of $N_2$ gas and $CH_4$ such that when the concentration of $N_2$ and $CH_4$ increased, the ratio of ${\gamma}^{\prime}-Fe_4$(C, N) decreased, but the ratio of ${\varepsilon}-Fe_{2-3}$(N, C) increased. The thickness of compound layer consistently increased as gas concentration increased regardless of $N_2$ and $CH_4$ expect when the concentration of $CH_4$ was 3.5 volume%, it decreased insignificantly. When oxidizing for 15min in the temperature range of $460{\sim}570{^\circ}C$, the study found small amount of $Fe_3O_4$ at the temperature of $460{^\circ}C$ and also found that amounts of $Fe_2O_3$. and $Fe_3O_4$ on the surface and amount of ${\gamma}^{\prime}-Fe_4$(C, N) in the compound layer increased as the increased over $460^{\circ}C$, but the thickness of the compound layer decreased. Corrosion resistance was influenced by oxidation times and temperature.

• 공업화학
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• 제5권5호
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• pp.843-850
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• 1994

$[NP(OC_6H_5)_{1.7}(OC_6H_4P(Ph)_2$=$CHCH_2CH_2CH_3)_{0.3}]_n$과 같은 포스파젠 고분자에 부착된 Wittig 시약을 $[NP(OC_6H_5)_{1.7}(OC_6H_4Br)_{0.3}]_n$에 n-butyllithium, diphenylchlorophosphine, 그리고 n-butyl iodide 등으로 처리하여 만들었다. 고분자의 반응들은 [$NP(OC_6H_5)_5(OC_6H_4P(Ph)_2$)]와 같은 고리형 삼중체를 이용한 모델반응 조건들을 고려해 이루어졌다. 포스파젠 고분자에 부착된 Wittig 시약과 benzophenone을 반응시켜 원하는 알켄과 고분자에 부착된 phosphine oxide를 성공적으로 만들었다.

• Korean Chemical Engineering Research
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• 제50권3호
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• pp.527-534
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• 2012

FCC 연료가스로부터 에틸렌 회수를 위한 흡착공정을 개발을 위하여 활성탄(AC)과 탄소분자체(CMS)로 충진된 흡착탑의 흡착 동특성을 비교하였다. FCC 연료가스로는 6성분($CH_4/C_2H_4/C_2H_6/C_3H_6/N_2/H_2$,32:15:14:2:12:25 vol.%) 혼합가스를 이용하였으며, 흡착탑의 흡착 및 탈착파과 실험을 실시하였다. 활성탄 흡착탑의 경우 파과는 $H_2$ < $N_2$ < $CH_4$ < $C_2H_4$ < $C_2H_6$ 순서로 나왔으며, CMS 흡착탑의 경우는 $H_2$< $CH_4$ < $N_2$ < $C_2H_6$ < $C_2H_4$ 순서를 보였다. CMS 흡착탑은 활성탄 흡착탑보다 성능이 나쁘나, 속도분리의 특성으로 $CH_4$와 $N_2$뿐만 아니라 활성탄에서 제거하기 어려운 $C_2H_6$ 이상의 성분들을 흡착단계에서 제거할 수 있다. 흡착탑의 재생은 감압과정만으로는 두 흡착제 충진탑에서 충분히 재생되기 어려우며, 진공재생이 필요하다. 따라서 CMS를 이용하는 흡착공정은 전처리 공정으로 설계하고, 활성탄을 이용하는 흡착공정을 주요 분리기로 설계하는 압력진공순환식 흡착공정(PVSA)이 에틸렌 회수에 제안될 수 있다.

• 한국환경보건학회지
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• 제33권3호
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• pp.217-226
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• 2007

The purpose of this study is to estimate the emission factor of $non-CO_2$ global warming gases such as $N_2O$ and $CH_4$ by measuring concentrations from stacks of waste incinerators and cement production plants. Based on the established monitoring methods, $N_2O$ concentration measured from stacks in incinerator were between 0.62 and $40.60\;ppm_v$ (ave. $11.50\;ppm_v$). The concentration of $N_2O$ was dependent on the incinerator types. However, the concentrations of $CH_4$ gas were between 2.65 and $5.68\;ppm_v$ (ave. $4.22\;ppm_v$), and did not show the dependency on the incinerator types. In the cement production plant, the concentration ranges of $N_2O$ from the stack were from 6.90 to $10.80\;ppm_v$ (ave. $8.60\;ppm_v$), and $CH_4$ were between 1.80 and $2.20\;ppm_v$ (ave. $2.60\;ppm_v$). Using measured concentrations, the emission amounts of $N_2O$ and $CH_4$ from stacks per year were calculated. The results were is 4.2 ton $N_2O/yr$ in the incinerators, and 53.7 ton $N_2O/yr$ in the cement facilities. The big difference is from the flow rate of flue gas in the cement facilities compared to the incinerators. By the same reason, the $CH_4$ emission amounts in cement plant and incinerator was found to be 339 ton $CO_2/yr$ and 34.1 ton $CO_2/yr$, respectively. Finally, the emission factor of $N_2O$ in the incinerators were calculated using the measured concentration and the amount of incinerated wastes, and was $42.5\sim799.1\;g/ton$ in kiln and stoker type, $11.9\sim79.9\;g/ton$ in stoker type, 90.1 ton/g in rotary kiln type, 174.9 g/ton in fluidized bed type, and 63.8 g/ton in grate type, respectively. Also, the emission factors of $CH_4$ were found to 65.2-91.3 g/ton in kiln/stoker type, 73.9-122 g/ton in stoker type, 109.5 g/ton rotary kiln, and 26.1 g/ton in fluidized bed type. This result indicates that the emission factor in incinerators is strongly dependent on the incinerator types, and matched with result of IPCC (International Panel on Climate Change) guideline.

• 공업화학
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• 제19권6호
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• pp.624-628
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• 2008

$N_2O$는 주요 온실가스 성분의 하나로서 광화학 스모그의 유발, 산성비의 전구체 등 온실효과에 상당한 기여를 하고 있는 물질이다. 이러한 $N_2O$ 및 질소산화물을 제거하기 위하여 환원제를 이용한 Selective Catalytic Reduction (SCR) 반응 공정이 널리 사용되고 있다. 본 연구에서는 Hydrotalcite 형태의 전구체로부터 Mixed Metal Oxide 촉매를 제조하고 그를 사용하여 $N_2O$ 분해를 위한 메탄 SCR 반응 및 CO의 생성효과를 비교 연구하였다. 실험결과 $CH_4$ 환원제의 첨가는 $N_2O$의 분해 반응에 긍정적인 영향을 미치며, 최적화된 $O_2/CH_4$ 비율의 조건에서 메탄의 부분산화에 의한 SCR 반응이 가장 높은 효율을 나타내는 것을 확인할 수 있었다.

• Asian-Australasian Journal of Animal Sciences
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• 제18권6호
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• pp.873-878
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• 2005

Emissions of nitrous oxide (N$_2$O) and methane (CH$_4$) from poultry enteric fermentation were investigated using a respiration chamber. Birds were placed in a respiration chamber for certain intervals during their growing period or for the whole life cycle. The accumulated gas inside the chamber was sampled and analyzed for N$_2$O and CH$_4$ production. A curve for gas production during a life cycle was fitted. The calculated area under the curve estimated the emission factor of poultry enteric fermentation on a life cycle basis (mg bird$^{-1}$ life cycle$^{-1}$). This method can be used to estimate CH$_4$ or N$_2$O emissions from different types of avian species taking into account factors such as diet, season or thermal effects. The CH$_4$/N$_2$O emission factors estimated for commercial broiler chickens, Taiwan country chickens and White Roman Geese were 15.87/0.03, 84.8/16.4 and 1,500/49 (mg bird$^{-1}$ life cycle$^{-1}$), respectively, while the calculated CH$_4$/N$_2$O emission from enteric fermentations were 3.03/0.006, 14.73/2.84 and 9.5/0.31 (Mg year$^{-1}$), respectively in Taiwan in the year of 2000. The described method is applicable to most poultry species and the reported emission factors were applicable to meat type poultry only.

• 한국재료학회:학술대회논문집
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• 한국재료학회 2003년도 춘계학술발표강연 및 논문개요집
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• pp.42-42
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• 2003

Ni/Si 기판상에 CH$_4$, H$_2$, $N_2$의 혼합기체를 사용하여 $700^{\circ}C$에서 5분 동안 MPECVD법으로 탄소나노튜브 성장시켰다. 이 과정에서 CH$_4$, H$_2$에 대한 $N_2$의 유량비를 여러 가지 값으로 변화시켜 그 성장 양상을 살펴보았다. 혼합기체 내 질소의 함량에 따라 나노튜브의 성장길이와 quality가 달라짐을 SEM과 Raman spectroscopy 측정을 통하여 확인하였다. 나노튜브의 성장 시 혼합기체 내 주입하는 질소량에 의해 나노튜브의 성장길이가 변화됨을 SEM을 통해 관찰할 수 있었고 혼합기체 내 질소의 비율이 커질수록 carbonaceous particle 등의 감소로 인한 나노 튜브의 quality가 향상됨을 Raman spectra를 통해 확인할 수 있었다. 또한 TEM과 SEM 관찰을 통해 성장된 탄소나노튜브가 대나무(bamboo) 구조를 가진 수직 배향된 다중벽 탄소나노튜브임을 확인하였다.

• 폴리머
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• 제32권3호
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• pp.239-245
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• 2008

Block copolymers of the general formula $[(-CO-R'-CO-HN-Ar-NH-CO-R'-CO)_xNH(CH_2)_3-(Me_2SiO)_y(CH_2)_3NH_2]_n$, [n=18.00 to 1175.0] where $R'=CH_2CH(CH_2GeCl_3)$;$CH_2CHGeCl_3CH_2$; and $Ar=-C_6H_4$;$-(o.CH_3C_6H_4)_2$;$-o.CH_3OC_6H_4)_2$;$-(o.CH_3C_6H_4)$ were prepared by a polycondensation reaction of polyamide containing a pendant trichlorogermyl group and terminal acid chloride $Cl(-CO-R'-CO-NH-Ar-NH-CO-R'-CO-)_xCl$ with aminopropyl-terminated polydimethylsiloxane $H_2N(CH_2)_3(Me_2SiO)_y-(CH_2)_3NH_2]$, (PDMS). These polymers were characterized by elemental analysis, $T_g$, FT-IR, $^1H$-NMR, solid state $^{13}C$-NMR, and molecular weight determination. The thermal stability of these copolymers was examined using thermal analysis techniques, such as TGA and DSC. Their molecular weights as determined by laser light scattering technique ranged $5.13{\times}10^5$ to $331{\times}10^5\;g/mol$. These polymers display their $T_g$ in the range of 337 to $393^{\circ}C$ with an average decomposition temperature at $582^{\circ}C$.

• 멤브레인
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• 제28권4호
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• pp.233-242
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• 2018

본 연구는 GO (graphene oxide)를 활용한 기체 분리막 연구를 위해 PEBAX [poly(ether-block-amide)]에 GO를 첨가하여 PEBAX-GO 고분자 복합막을 제조하고, 이 복합막을 통해 $H_2$, $N_2$, $CH_4$, $CO_2$에 대한 기체투과 특성을 연구하였다. 기체투과 실험결과 PEBAX-GO 복합막에 대해 $N_2$, $CH_4$, $CO_2$의 기체투과도는 GO 함량이 증가함에 따라 점차 감소하였다. 반면 $H_2$의 기체투과도는 GO 함량이 증가함에 따라 증가하였고, GO 함량 30 wt%에서는 21.43 barrer로 단일막에 비하여 약 5배가 증가하였는데 GO는 $H_2$에 대해 다른 기체들에 비해 빠르고 선택적인 기체운송 channel로 더 용이하게 작용하였기 때문이다. 증가된 선택도($H_2/N_2$)와 선택도($H_2/CH_4$)는 투과기체 크기에 의한 확산선택도가, 증가된 선택도($CO_2/N_2$)와 선택도($CO_2/CH_4$)는 $CO_2$와 GO의 -COOH와의 친화성으로 용해선택성이 더 크게 영향을 미친 것으로 나타났다.

• 대한전기학회논문지:전기물성ㆍ응용부문C
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• 제49권4호
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• pp.203-209
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• 2000

This paper proposes the improvement of the etch rate of GaN using a magnetized inductively coupled $CH_4/H_2/Ar$plasma. The gradient magnetic field with the axial direction is investigated using Gauss-meter and the ion current density is measured using double Langmuir probe. The applied magnetic field changes the ion current density profile in the radial direction, resulting in producing the higher density in the outer region than in the center. GaN dry etching process is carried out based on the measurements of the ion current density. The each rate of 2000 /min is achieved with $CH_4/H_2/Ar$ chemistries at 800 W input power, 250W rf bias power, 10 mTorr pressure and 100 gauss magnetic field.