• Bulletin of the Korean Chemical Society
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• 제23권11호
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• pp.1513-1518
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• 2002

Kinetic studies on the water-gas shift reaction catalyzed by magnetite/chromium oxide and copper/zinc oxide were carried out by using an in situ photoacoustic spectroscopic technique. The reactions were performed in a closed-circulation reactor system using a differential photoacoustic cell at total pressure of 40 Torr in the temperature range of 100 to $350^{\circ}C.$ The CO2 photoacoustic signal varying with the concentration of CO2 during the catalytic reaction was recorded as a function of time. The time-resolved photoacoustic spectra obtained for the initial reaction stage provided precise data of CO2 formation rate. The apparent activation energies determined from the initial rates were 74.7 kJ/mol for the magnetite/chromium oxide catalyst and 50.9 kJ/mol for the copper/zinc oxide catalyst. To determine the reaction orders, partial pressures of CO(g) and H2O(g) in the reaction mixture were varied at a constant total pressure of 40 Torr with N2 buffer gas. For the magnetite/chromium oxide catalyst, the reaction orders with respect to CO and H2O were determined to be 0.93 and 0.18, respectively. For the copper/zinc oxide catalyst, the reaction orders with respect to CO and H2O were determined to be 0.79 and 0, respectively.

• 자원리싸이클링
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• 제13권2호
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• pp.9-15
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• 2004

석유화학공정으로부터 폐기되는 폐산화철촉매를 이용하여 도금합성폐수중 크롬회수에 관한 연구를 회분식과 연속식으로 실시하였다. 도금합성제수 중 $CrO _{4}^{-2}$ 형태의 음이온으로 존재하는 6가 크롬은 폐산화철촉매의 등전점(pH 3.0)이하에서 폐촉매와 물리적 흡착을 한다. 한편, 6가 크롬은 pH 3.0 이상에서도 폐촉매의 수산화철과 산화환원반응에 의해 일부 환원되어 $Cr(OH)_3$로 침전한다. 컬럼을 이용한 크롬 연속회수실험에서 크롬합성폐수의 pH가 0.5∼2.0일 때 폐촉매의 크롬흡착량은 2.0∼2.3g/L이며, pH가 3.0에서는 1.5g/L이었다. 폐수 중 크롬농도가 50∼500mg/L로 높아질수록 폐촉매에 흡착한 크롬누적량은 1.29∼8.56g/L로 증가하지만, 유속이 30∼80 ml/mm으로 증가하여도 크롬 흡착누적량은 2.21∼2.49 mg/L로 거의 유사하였다.

• Elastomers and Composites
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• 제50권2호
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• pp.103-109
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• 2015

In this study, epoxy/anhydride mixing ratio for the highly silica filled compounds with chromium (III) octoate catalyst was investigated at a low curing temperature ($71^{\circ}C$ for 40 hr) by evaluating the compressive strength with the weight ratio ranges from 0.3/1.0 to 1.0/1.0 of epoxy part (Part A)/anhydride part (Part B). In case of epoxy/anhydride compounds used surface unmodified silica by coupling agent, these compounds need excess anhydride unlike the weight ratio in the conventional epoxy/anhydride compounds. In curing behavior, the epoxy/anhydride compounds containing chromium (III) octoate showed high conversions at $71^{\circ}C$ for 40 hr, even if a dipropylene glycol (DPG) was not used as a polymerization initiator. Also, DPG leads to a poor epoxy network structure. In conclusion, the appropriate weight ratio of Part A/Part B of highly silica filled epoxy/anhydride compounds with chromium (III) octoate catalyst is 0.5/1.0 and the maximum amounts of silica is 1470 phr of epoxy resin.

• 대한화학회지
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• 제23권3호
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• pp.152-160
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• 1979

Furfural의 수소화반응에 쓰이는 구리-크롬산화물계 촉매에서 바륨, 스트론륨 등의 첨가효과 및 그 기능에 관하여 조사하였다. X-선 회절에 의하면 $BaCrO_4$, $SrCrO_4$등의 생성을 확인할 수 있었으나, 촉매표면적에는 차이가 없었다. 그러나 이들의 첨가로 촉매능은 개선되어 첨가전보다 반응시간에 따른 활성저하폭이 훨씬 적어졌다. 바륨이 첨가된 또는 실기카에 분산시킨 촉매는 CO흡착으로 분산된 Cr(V)의 EPR 스펙트럼을 보여주었으며 표면의 산화-혼원과정에서 가역적인 스펙트럼을 나타내었다. 바륨의 첨가로 촉매활성점이 분산되어 존재함으로서 furfural의 수소화반응에서 향상된 촉매능을 보여주는 것으로 생각된다.

• Bulletin of the Korean Chemical Society
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• 제35권9호
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• pp.2835-2838
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• 2014

• Bulletin of the Korean Chemical Society
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• 제13권6호
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• pp.605-612
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• 1992

Chromium oxide/zirconia catalysts were prepared by dry impregnation of powdered $Zr(OH)_4$ with ($NH_4$)$_2$CrO$_4$aqueous solution. The characterization of prepared catalysts was performed using FTIR, XPS, XRD and DTA methods, and by the measurement of surface area. The addition of chromium oxide to zirconia shifted the transitions of $ZrO_2$ from amorphous to tetragonal phase and from tetragonal to monoclinic phase to higher temperature due to the strong interaction between chromium oxide and zirconia, and the specific surface area of catalysts increased in proportion to the chromium oxide content. Since the $ZrO_2$ stabilizes supported chromium oxide, chromium oxide was well dispersed on the surface of zirconia, and ${\alpha}$-$Cr_2O_3$ was observed only at the calcination temperature above 1173 K. Upon the addition of only small amount of chromium oxide (1 wt% Cr) to $ZrO_2$, both the acidity and acid strength of catalyst increased remarkably, showing the presence of two kinds of acid sites on the surface of $CrO_x$/$ZrO_4$-Bronsted and Lewis.

• 한국재료학회지
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• 제11권8호
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• pp.703-707
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• 2001

크롬의 첨가에 따른 Raney 니켈의 특성을 파악하여 우수한 성능을 나타낼 수 있는 알칼리형 연료전지용 수소극의 촉매를 제조하였다. 또한 제조된 촉매를 이용, 실제 전극으로 제작하여 전류밀도를 측정한 뒤 최적의 전극재료의 제조조건을 확립하였다. 먼저 Ni-Al합금 제조시 크롬의 첨가량을 달리하여 Raney 니켈을 제조한 뒤 이를 이용하여 수소극을 제작, 전기화학적 특성을 고찰한 결과 크롬 첨가량이 증가함에 따라 mass activity도 증가하여 크롬 첨가량이 1 wt% 인 경우 최고 3.688 A/g을 나타내었다. 전기화학적 측정시 half cell의 운전온도는 8$0^{\circ}C$이었으며 전해질은 6N KOH이었다. Raney 니켈 촉매의 입자크기와 비표면 적을 조사한 결과 크롬의 첨가량이 증가함에 따라 Raney 니켈 촉매의 입자크기는 12.11 $\mu\textrm{m}$에서 크롬의 첨가량이 1.25 wt%인 경우 11.07 $\mu\textrm{m}$로 감소하였고 비표면적은 0.653 $\m^2$/g에서 0.685 $\m^2$로 중가함을 알 수 있었다. 평균입자 크기가 커짐에 따라 잔존 알루미늄의 함량은 증가함을 알 수 있었다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2228-2231
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• 2007

Water gas shift reactor in fuel processing is an important part that converts carbon monoxide into hydrogen. Fuel processing system for PEMFC usually has two stages of WGS reactors, which are high temperature and low temperature shifter. In this study we prepared noble metal catalysts and compared their performances with that of a commercial iron chromium oxide catalyst. Noble metal catalysts and the commercial catalyst showed quite different temperature dependence of carbon monoxide conversion. The conversion of carbon monoxide at the commercial catalyst was very low at medium temperature(${\sim}300^{\circ}C$) and increased rapidly as temperature increased while the conversion at noble metal catalysts was high in the medium temperature range and decreased as temperature increased, which is thermodynamically expected. Their characteristics agreed well with the literature published, and we are accomplishing further study for improvement of the noble metal catalysts.

• 공업화학
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• 제3권4호
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• pp.663-669
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• 1992

분말의 $Zr(OH)_4$를 $(NH_4)_2CrO_4$수용액에 함침시킨 후 공기중에 소성하여 질코니아에 담지된 산화크롬 촉매를 제조하였다. 제조된 $CrO_x/ZrO_2$ 촉매상에 cumene을 반응시켜 산화-환원 거동을 연구한 결과 크롬의 산화상태가 +6인 chromate형태로 질코니아 표면에 존재할 때는 강한 산점이 생성되어 cumene의 탈알킬화 반응에 촉매활성을 나타내었다. 그러나 많은 양의 $Cr^{6+}$종은 반응중에 탈수소로 생성된 $H_2$에 의하여 환원되어 $Cr^{3+}$종으로 변환되었으며 $Cr^{3+}$종은 cumene을 탈수소화시켜 ${\alpha}$-methyl styrene을 생성하는 반응에 활성점으로 작용하였다. 환원된 $Cr^{3+}$종은 $O_2$로 처리하면 다시 $Cr^{6+}$종으로 되고 따라서 산화된 촉매는 cumene의 탈알킬화 반응에 활성을 나타내었다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2010년도 추계학술대회 초록집
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• pp.115.2-115.2
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• 2010

Autothermal reforming(ATR) processes of hydrocarbon liquids such as diesel fuels are spotlighted as methods to produce hydrogen for Fuel cell. However, the use of heavy hydrocarbons as feedstocks for hydrogen production causes some problems which increase the catalyst deactivation by the carbon deposition. Coking can be inhibited by increasing the water dissociation on the catalyst surface. This results in catastrophic failure of whole system. Performance degradation of diesel autothermal reforming leads to increase of undesirable hydrocarbons at reformed gases and subsequently decrease the performance. In this study, perovskite-based catalysts were investigated as alternatives to substitute the noble metal catalyst for the ATR of diesel. The investigated perovskite structure was based on LaCrO3. and metals were added at the A-site to enhance oxygen ion mobility, transition metals were doped on the B-site to enhance the reformation. Substituted Lanthanum chromium perovskite were made by aqueous combustion synthesis, which can produce high surface area. And for the homogeneous fuel supply, we made ultrasonic injection system for reforming. We compared durability of evaporation system and ultrasonic system for fuel injection.