• 공업화학
• /
• 제3권4호
• /
• pp.663-669
• /
• 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.

• 공업화학
• /
• 제1권1호
• /
• pp.35-43
• /
• 1990

일련의 $TiO_2-SiO_2$촉매를 $TiCl_4$와 $Na_2SiO_3$혼합용액을 공침전시켜 제조하였으며 이중 일부의 촉매는 1N $H_2SO_4$로 처리하여 촉매표면을 개질하였다. 개질된 촉매의 촉매활성은 개질 안된 촉매보다 높은 촉매활성을 나타내었으며 cumene dealkylation 반응에서 보다 2 - propanol dehydration 반응에서 더욱 효과가 크게 나타났다. 개질 안된 촉매의 상기 두 반응에 대한 촉매활성은 산의 양과 관계가 있었다. $TiO_2-SiO_2$촉매는 비교적 많은 양의 약한 산자리와 작은 양의 강한 산자리를 가졌기 때문에 cumene dealkylation 반응에서 보다 2 - propanol dealkylation 반응에 더 높은 촉매활성을 나타내었다. 촉매활성에 미치는 $H_2SO_4$의 개질효과는 $TiO_2$ 함량에 비례하였으며 $92-TiO_2-SiO_2/SO_4^2$가 2 - propanol dealkylation 반응에 가장 큰 촉매활성의 증가를 나타내었다.

• Bulletin of the Korean Chemical Society
• /
• 제22권12호
• /
• pp.1309-1315
• /
• 2001

Zirconium sulfate supported on zirconia catalysts were prepared by impregnation of powdered $Zr(OH)_4$ with zirconium sulfate aqueous solution followed by calcining in air at high temperature. The characterization of prepared catalysts was performed using Fourier transform infrared (FTIR), X-ray diffraction (XRD), differential scanning calorimetry (DSC), and by the measurement of surface area. The addition of zirconium sulfate to zirconia increased the phase transition temperature of $ZrO_2$ from amorphous to tetragonal due to the interaction between zirconium sulfate and zirconia, and the specific surface area and acidity of catalysts increased in proportion to the zirconium sulfate content up to 10 wt% of $Zr(SO_4)_2$. Infrared spectra of ammonia adsorbed on $Zr(SO_4)2}ZrO_2$ showed the presence of Bronsted and Lewis acid sites on the surface. $10-Zr(SO_4)_2}ZrO_2$ calcined at $600^{\circ}C$ exhibited maximum catalytic activities for 2-propanol dehydration and cumene dealkylation. The catalytic activities for both reactions were correlated with the acidity of catalysts measured by ammonia chemisorption method.

• Bulletin of the Korean Chemical Society
• /
• 제24권2호
• /
• pp.159-160
• /
• 2003

• 공업화학
• /
• 제7권2호
• /
• pp.245-251
• /
• 1996

일련의 $BeO-SiO_2$ 촉매를 염화베릴리움과 sodium silicate 혼합 용액을 공침전법으로 제조하였다. $SiO_2$에 BeO를 첨가하면 표면적, 산의 양, 산세기, 산촉매활성이 증가하여 BeO 함량이 20mol%일 때 최대를 나타내었다. X-선 회절로 조사한 결과 $400{\sim}500^{\circ}C$에서 소성된 촉매는 무정형으로 존재하였으며 $Br{\ddot{o}}nsted$ 산점과 Lewis 산점 모두를 가지고 있었다. Cumene의 dealkylation 반응에 대한 촉매활성은 촉매의 산의 양과 밀접한 관계를 가졌다.

• Bulletin of the Korean Chemical Society
• /
• 제25권5호
• /
• pp.657-664
• /
• 2004

Titanium sulfate supported on $TiO_2$was prepared by impregnation of powdered $TiO_2$with an aqueous solution of titanium sulfate followed by calcining in air at high temperature. For Ti$(SO_4)_2/TiO_2$ samples calcined at 300 $^{\circ}C$, no diffraction lines of titanium sulfate are observed at $Ti(SO_4)_2$loading up to 30 wt%, indicating good dispersion of $Ti(SO_4)_2$ on the surface of $TiO_2$. The acidity of the catalysts increased in proportion to the titanium sulfate content up to 20 wt% of $Ti(SO_4)_2$. 20 wt% $Ti(SO_4)_2/TiO_2$ calcined at 300 $^{\circ}C$ exhibited maximum catalytic activities for 2-propanol dehydration and cumene dealkylation. The catalytic activities for these reactions, were correlated with the acidity of catalysts measured by ammonia chemisorption method.

• Bulletin of the Korean Chemical Society
• /
• 제24권12호
• /
• pp.1785-1792
• /
• 2003

Zirconia modified with $MoO_3$ was prepared by impregnation of powdered $Zr(OH)_4$ with ammonium heptamolybdate aqueous solution followed by calcining in air at high temperature. Spectroscopic studies on prepared catalysts were performed by using FTIR, Raman, XRD, and DSC and by measuring surface area. Upon the addition of molybdenum oxide to zirconia up to 15 wt%, the specific surface area increased in proportion to the molybdate oxide content, while acidity measured by irreversible chemisorption of ammonia exhibited a maximum value at 3 wt% of $MoO_3$. Since the $ZrO_2$ stabilizes the molybdenum oxide species, for the samples equal to or less than 30 wt%, molybdenum oxide was well dispersed on the surface of zirconia and no phase of crystalline $MoO_3$ was observed at any calcination temperature above $400^{\circ}C$. The catalytic activities for cumene dealkylation were roughly correlated with the acidity of catalysts measured by ammonia chemisorption method, while the catalytic activities for 2-propanol dehydration were not correlated with the acidity because weak acid sites are necessary for the reaction.

• Bulletin of the Korean Chemical Society
• /
• 제11권5호
• /
• pp.403-406
• /
• 1990

Two types of new silica catalysts modified with benzenesulfonic acid derivatives were prepared by esterification or phenylation followed by sulfonation. Both catalysts thus prepared were tested as acid catalysts for 2-propanol dehydration and cumene dealkylation reactions. B catalyst () were more active than A catalyst (). Highter catalytic activity for B catalyst may be accounted for by higher resistance to water, higher acid strength, more acidity, and better thermal stability as compared with A catalyst.

• Bulletin of the Korean Chemical Society
• /
• 제27권6호
• /
• pp.821-829
• /
• 2006

A series of catalysts, $NiO/La_2O_3-ZrO_2/WO_3$, for acid catalysis was prepared by the precipitation and impregnation methods. For the $NiO/La_2O_3-ZrO_2/WO_3$ samples, no diffraction lines of nickel oxide were observed, indicating good dispersion of nickel oxide on the catalyst surface. The catalyst was amorphous to X-ray diffraction up to 300 ${^{\circ}C}$ of calcination temperature, but the tetragonal phase of $ZrO_2$ and monoclinic phase of $WO_3$ by the calcination temperatures from 400 ${^{\circ}C}$ to 700 ${^{\circ}C}$ were observed. The role of $La_2O_3$ in the catalyst was to form a thermally stable solid solution with zirconia and consequently to give high surface area and acidity. The high acid strength and high acidity were responsible for the W=O bond nature of complex formed by the modification of $ZrO_2$ with $WO_3$. For 2-propanol dehydration the catalyst calcined at 400 ${^{\circ}C}$ exhibited the highest catalytic activity, while for cumene dealkylation the catalyst calcined at 600 ${^{\circ}C}$ showed the highest catalytic activity. 25-$NiO/5-La_2O_3-ZrO_2/15-WO_3$ exhibited maximum catalytic activities for two reactions due to the effects of $WO_3$ modifying and $La_2O_3$ doping.

• Bulletin of the Korean Chemical Society
• /
• 제28권8호
• /
• pp.1265-1272
• /
• 2007

A solid acid catalyst, NiSO4/CeO2-ZrO2 was prepared simply by promoting ZrO2 with CeO2 and supporting nickel sulfate on CeO2-ZrO2. The support of NiSO4 on ZrO2 shifted the phase transition of ZrO2 from amorphous to tetragonal to higher temperatures because of the interaction between NiSO4 and ZrO2. The surface area of 10-NiSO4/1-CeO2-ZrO2 promoted with CeO2 and calcined at 600 oC was very high (83 m2/g) compared to that of unpromoted 10-NiSO4/ZrO2 (45 m2/g). This high surface area of 10-NiSO4/1-CeO2-ZrO2 was due to the promoting effect of CeO2 which makes zirconia a stable tetragonal phase as confirmed by XRD. The role of CeO2 was to form a thermally stable solid solution with zirconia and consequently to give high surface area and acidity of the sample, and high thermal stability of the surface sulfate species. 10-NiSO4/1- CeO2-ZrO2 containing 1 mol% CeO2 and 10 wt% NiSO4, and calcined at 600 oC exhibited maximum catalytic activities for both reactions, 2-propanol dehydration and cumene dealkylation.