• 한국응용과학기술학회지
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• 제26권2호
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• pp.179-185
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• 2009

The esterification of the reactants of Jatropha oil and methanol added by propyleneglycol was done using p-TSA catalyst. And then the emulsification of triglyceride and methanol was conduced by 1.0vol% GMS. The emulsified reactants were transesterified at $65^{\circ}C$ using TMAH and mixed catalyst (50wt%-TMAH+50wt%-NaOH) respectively. The esterification conversion at the 1:8 molar ratio of free fatty acid to methanol using 8.0wt% p-TSA was 94.7% within 80min. The overall conversion at the 1:8 molar ratio of mixed fat(50wt% Beef Tallow) to methanol and $65^{\circ}C$ using mixed catalyst was 95.4% The cloud point of Biodiesel decreased with the addition of petroleum diesel.

• 한국응용과학기술학회지
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• 제25권3호
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• pp.275-281
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• 2008

The esterification of free fatty acid in Jatropha oil added by propylene glycol using p-TSA catalyst was done, and then the transesterification of Jatropha oil added by 1.0vol% GMS as an emulsifier using TMAH, and mixed catalyst(60wt%-TMAH+ 40wt%-KOH) respectively was followed at $60^{\circ}C$. The esterification conversion at the 1:8 molar ratio of free fatty acid to methanol using 8.0wt% p-TSA was 94.7% within 60min. The overall conversion at the 1:8 molar ratio of Jatropha oil to methanol and $60^{\circ}C$ using mixed catalyst was 95.4%. The kinematic viscosity of Biodiesel using TMAH and mixed catalyst in 24h met the ASTM D-6751 above $30^{\circ}C$, and showed a little more than its criterion.

• 폴리머
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• 제36권5호
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• pp.593-598
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• 2012

본 연구에서는 Al계 화합물 혼합촉매 시스템의 L-lactide 용액중합을 실시하여 단일 Al계 화합물과 Al계 혼합화합물의 용액중합 특성의 차이를 비교하였다. $Al(O-i-Pr)_3$와 triisobutylaluminium(TIBA)를 혼합한 촉매의 경우 생성된 polylactide(PLA)의 분자량은 $Al(O-i-Pr)_3$의 조성이 증가할수록 대체적으로 감소하였다. 분자량 분포곡선은 혼합촉매 시스템의 경우 고분자량 부분에서 shoulder가 형성되었으며 TIBA가 80%인 경우에는 거의 bimodal 형태의 곡선을 가졌다. Trimethylaluminium(TMA)와 TIBA를 혼합한 촉매를 이용한 결과 TMA의 조성비가 증가할수록 전환율은 감소하였다. Trioctylaluminium(TOA)와 TIBA를 혼합한 촉매를 이용하여 생성된 PLA의 전환율은 TOA의 양이 증가함에 따라 점점 감소하였다. 분자량 분포곡선은 TOA 조성비가 40%부터 크게 줄기 시작하여 unimodal 특성을 보였다. 이러한 다양한 조합의 Al계 혼합촉매 시스템을 통해 GPC 곡선에서 PLA의 고분자량 shoulder을 형성할 수 있다.

• 폴리머
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• 제36권1호
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• pp.53-58
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• 2012

본 연구에서는 Al 계 화합물 혼합촉매 시스템의 L-lactide 벌크중합을 통해 단일 Al계 화합물과 혼합된 Al계 화합물의 중합 특성의 차이를 확인하였다. Al 화합물 촉매를 조성비를 변화시킨 혼합촉매를 사용하여 벌크중합한 polylactic acid (PLA)는 FTIR, DSC, GPC 등으로 분석하였다. 선정된 Al계 화합물로는 aluminum isopropoxide($Al(O-i-Pr)_3$), trimethylaluminum(TMA), trioctylaluminum(TOA), triisobutylaluminum(TIBA)이었으며 TIBA를 기준 촉매로 선정하여 나머지 세 Al화합물을 각각 혼합하여 사용하였다. $Al(O-i-Pr)_3$와 TIBA를 혼합한 촉매의 경우 혼합촉매 내 $Al(O-i-Pr)_3$의 양이 증가함에 따라 전환율도 증가하였고 생성된 PLA의 분자량은 13000까지 증가하였으며 분자량분포도도 약간의 증가를 보였다. 분자량 분포곡선은 혼합촉매 시스템의 경우 고분자량 부분에서 약간의 tail 또는 shoulder 형태가 형성되었다. TOA와 TIBA를 혼합한 촉매를 이용하여 L-lactide를 벌크중합한 결과 전환율은 혼합촉매 내 TOA의 양이 증가함에 따라 낮아졌다. TOA와 TIBA를 혼합한 촉매를 이용하여 벌크중합한 PLA의 분자량은 혼합촉매 내 TOA 조성이 60 mol%까지 분자량이 14000 g/mol까지 증가하다가 감소하였다. 이러한 Al계 혼합촉매 시스템을 통해 PLA의 고분자량 tail이나 shoulder을 생성할 수 있었으며 이를 통해 PLA의 기계적 물성을 향상시킬 수 있는 역할을 기대할 수 있다.

• 한국응용과학기술학회지
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• 제24권2호
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• pp.190-195
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• 2007

The transesterifications of beef tallow and the mixture of beef tallow and rapeseed oil were conducted at $65^{\circ}C$ respectively using TMAH, NaOH and their mixed catalysts. The reactants were emulsified with 1vol% emulsifier and propylene glycol. The overall conversion of beef tallow was 95% at such optimum conditions as the 1:8 of molar ratio and 0.8 wt% TMAH. The overall conversion of mixed fat at the 1:8 of molar ratio and mixed catalyst of 70 wt% TMAH 30 wt% NaOH was close to 97% which appeared at 0.8 wt% TMAH in 80min. And the kinematic viscosity of biodiesel mixture using the mixed catalyst was $6.5mm^2/s$ at $40^{\circ}C$.

• 한국응용과학기술학회지
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• 제28권2호
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• pp.178-184
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• 2011

The analysis of reaction kinetics provided that the reaction order was the $1^{st}$ of triglyceride and the rate constant was 0.067 $min^{-1}$. The transesterification of camelina oil using 0.6 wt% mixed catalyst which consists of 40 v/v% of potassium hydroxide (1 wt%) and 60 v/v% of tetra methyl ammonium hydroxide (0.8 wt%), was carried out at $65^{\circ}C$ on the tubular reactor packed with static mixer. The conversion was shown to be 95.5% at the 6:1 molar ratio of methanol to oil, flow rate of feed of 3.0 mL/min and 24 of element of static mixer. The volume of washing water emitted by 0.6 wt% mixed catalyst was the half of the volume emitted by 1 wt% potassium hydroxide.

• Bulletin of the Korean Chemical Society
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• 제35권8호
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• pp.2431-2437
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• 2014

In this study, Ni, Ni-Cu and Ni/Cu catalysts were deposited onto C-fiber textiles via the electrophoretic deposition method, and the growth characteristics of carbon nanofibers on the deposited catalyst/C-fiber textiles were investigated. The catalyst deposition onto C-fiber textiles was accomplished by immersing the C-fiber textiles into Ni or Ni-Cu mixed solutions, producing the substrate by post-deposition of Ni onto C-fiber textiles with pre-deposited Cu, and passing it through a gas mixture of $N_2$, $H_2$ and $C_2H_4$ at $700^{\circ}C$ to synthesize carbon nanofibers. For analysis of the characteristics of the synthesized carbon nanofibers and the deposition pattern of catalysts, SEM, EDS, BET, XRD, Raman and XPS analysis were conducted. It was found that the amount of catalyst deposited and the ratio of Ni deposition in the Ni-Cu mixed solution increased with an increasing voltage for electrophoretic deposition. In the case of post-deposition of Ni catalyst onto substrates with pre-deposited Cu, both bimetallic catalyst and carbon nanofibers with a high level of crystallizability were produced. Carbon nanofibers yielded with the catalyst prepared in Ni and Ni-Cu mixed solutions showed a Y-shaped morphology.

• Korean Chemical Engineering Research
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• 제56권2호
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• pp.269-274
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• 2018

All the $Ni-Co-Ce-ZrO_2$ mixed oxides are prepared by co-precipitations methods. Methanation of CO and $H_2$ reaction is screened tested over different fractions of cerium (2, 4, 7 and 12 wt.%) over $Ni-Co/ZrO_2$ bimetallic catalysts are investigated. The mixed oxides are characterized by XRD, CO-Chemisorption, TGA and screened methanation of CO and $H_2$ at $360^{\circ}C$ for 3000 min on stream at typical ratio $CO:H_2=1:1$. In $Ni-Co/CeZrO_2$ series 2 wt.% Ce loading catalyst shows most promising catalyst for $CH_4$ selectivity than $CO_2$, which directs more stability with less coke formation. The high activity is attributed to the better bimetallic synergy and the well-developed crystalline phases of NiO, $ZrO_2$ and $Ce-ZrO_2$. Other bimetallic mixed oxides NCoZ, $NCoC^{4-12}Z$ has faster deactivation with low methanation activity. Finally, 2 wt.% Ce loading catalyst was found to be optimal coke resistant catalyst.

• 한국응용과학기술학회지
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• 제34권4호
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• pp.883-891
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• 2017

고분자 전해질 연료전지의 연료에 포함된 일산화탄소의 선택적 산화를 위하여, 귀금속 촉매를 대체하기 위한 CuO-$CeO_2$ 복합 산화물 촉매를 졸-겔법과 공침법으로 제조하였다. 졸-겔법으로 촉매 제조 시 Cu/Ce의 비와 가수분해 비를 변화시켰다. 제조한 촉매의 활성은 귀금속 촉매($Pt/{\gamma}-Al_2O_3$)와 비교하였다. Cu/Ce의 비를 변화시키면서 제조한 촉매 중 Cu/Ce의 비가 4:16인 촉매가 가장 높은 CO 전환율(90%)과 선택도(60%)를 나타내었다. 촉매의 제조에서 가수분해 비가 증가할수록 촉매 표면적이 증가하였고, 아울러 촉매 활성 또한 증가하였다. 공침법으로 제조한 촉매와 1wt% $Pt/{\gamma}-Al_2O_3$ 촉매의 가장 높은 CO 전환율은 각각 82% 및 81%인 반면, 졸-겔법으로 제조한 촉매의 경우는 90%가 얻어졌다. 이는 졸-겔법으로 제조한 촉매가 공침법으로 제조한 촉매나 귀금속 촉매보다 더 높은 촉매활성을 보임을 의미한다. CO-TPD 실험을 통하여, 낮은 온도($140^{\circ}C$)에서 CO를 탈착하는 촉매가 본 반응에서 더 높은 촉매활성을 보임을 알 수 있었다.

• 한국응용과학기술학회지
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• 제26권4호
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• pp.394-399
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• 2009

The esterification of palmitic acid in Jatropha Oil using 8wt% p-TSA catalyst was done at the 1:8 molar ratio of oil to methanol and $65^{\circ}C$. The conversion of palmitic acid appeared to be 95.3% in 60min. After that, the continuous transesterification of the oil using 0.5wt% KOH, 0.8wt% TMAH mixed catalyst[40vol% KOH(0.5wt%) + 60vol% TMAH(0.8wt%)] and 1.1wt% TMAH was conducted with the flow rates and the molar ratios at $65^{\circ}C$. The overall conversion of Jatropha Oil increased with the decrease of flow rate and showed 95.6% with 9ml/min of flow rate at the 1:8 molar ratio of oil to methanol and $65^{\circ}C$. But it showed 87% with 15ml/min of flow rate at the same conditions. The recovery of methanol(%) appeared to be 86% at the 1:8 molar ratio of oil to methanol, mixed catalyst and $65^{\circ}C$.