Investigation of toluene formation on Pt/Al2O3 catalyst in n-hexane dehydrocyclization

Formation of toluene, a chain lengthening product, has been observed on Pt/Al₂O₃ catalyst in n-hexane dehydrocyclization. Toluene formation is influenced by the catalyst pretreatment processes and the reaction temperature. A correlation has been found between the ageing phenomena and toluene formation.

---

- Pt/Al₂O₃ — . . .

     

Catalytic incineration of n-hexane on Pt/Al2O3

The catalytic incineration of n-hexane over a Pt/Al₂O₃ catalyst has been studied using a fixed bed reaction. The reaction was carried out in dry air between 250 and 350 °C and at 1 atm pressure. The concentration of n-hexane was between 25 and 300 ppm. The reaction was found to be zero order in n-hexane concentration and the activation energy was found to be 21 kcal/mol. The zero order kinetics can be explained by a surface redox cycle known as Mars-van Krevelen mechanism in which the oxidation of surface Pt is the rate-controlling step.

---

- Pt/Al₂O₃ . , 250–350°C 1 . - 25–300 .. - –21 /. , — , , , Pt.

     

低温下Pt/Al_2O_3和Pd/Al_2O_3光辅助乙二醇水相重整制氢研究

采用浸渍还原法制备了氧化铝负载的Pt和Pd纳米颗粒催化剂,用于光辅助乙二醇水相重整制氢反应。结果表明,光照能够有效降低乙二醇水相重整制氢的活化能,Pt/Al_2O_3比Pd/Al_2O_3具有更高的H_2转换频率(TOF)和更低的CO选择性。采用XRD、TEM、UV-vis等技术对催化剂的结构和形貌进行了表征,原位漫反射红外光谱(DRIFTS)表明,光照能促进乙二醇分子O-H键的断裂。理论计算表明,Pt/Al_2O_3催化乙二醇重整制氢反应产物中较低的CO选择性主要归因于CO在Pt表面较小的反应能垒,能够较快与H_2O解离的O反应生成CO_2。     

Pt/Al2O3 and Pt/Ba?Al2O3 catalysts studied by temperature programmed desorption of oxygen: Evidence for a low temperature desorbing species

For fresh and aged Pt/Al₂O₃ catalysts, TPD of oxygen is fairly well related to the noble metal surface areas and to the catalytic activity in butane combustion, whereas for aged Pt/Ba−Al₂O₃ solids, the catalytic activity is still preserved despite a tremendous sintering of the metallic phase and seems to be connected to a surface barium superoxide.     

Sulfuration of Pt/Al2O3, Pt?Re/Al2O3 and Pt?Ir/Al2O3 catalysts

Three reforming catalysts Pt/Al₂O₃, Pt–Ir/Al₂O₃ and Pt–Re/Al₂O₃ have been sulfurated by H₂S and tested by their activities in benzene hydrogenation. By treatment at 500°C under hydrogen flow only a part of the initial activity of the non-sulfurated catalyst is retained. So only a part of the adsorbed sulfur is easily removed in these conditions. The remaining sulfur for each of the catalysts (Pt/Al₂O₃, Pt–Ir/Al₂O₃ and Pt–Re/Al₂O₃) gives the same atomic ratio of 0.5 sulfur atom per accessible metallic atom.

---

Pt/Al₂O₃, Pt–Ir/Al₂O₃ Pt–Pe/Al₂O₃ . 500°C H₂ . . ., . (Pt/Al₂O₃, Pt–Ir/Al₂O₃ Pt–Pe/Al₂O₃) 0,5.

     

Kinetics of catalytic combustion in air over Pt/Al2O3/Al catalyst

Summary Catalytic combustion of toluene, propylene and CO over Pt/Al₂O₃ /Al catalyst was investigated. Strong inhibition effects are observed when the mixture of toluene, propylene and CO is oxidized. A reaction mechanism of catalytic combustion over Pt/Al₂O/Al is proposed. The results from kinetic models are in good agreement with the experimental data.     

Sulfurization of Pt/Al2O3?Cl catalysts. IV. Adsorption sites of H2S on Al2O3, Al2O3?Cl and Pt/Al2O3?Cl

Chemisorption of H₂S on Al₂O₃, Al₂O₃–Cl and Pt/Al₂O₃–Cl has been studied by gravimetry and IR spectroscopy. The influence of the amount of Cl on the H₂S adsorption equilibrium value and the nature of the adsorption sites at low and high coverages are discussed.

---

H₂S Al₂O₃, Al₂O₃–Cl Pt/Al₂O₃–Cl . Cl H₂S, .

     

Temperature programmed reduction and oxidation of Ir/Al2O3 catalysts

3 % Ir/Al₂O₃ catalysts have been studied by means of temperature programmed reduction and oxidation. With growing degree of metal oxidation (higher T_ox) reducibility of the catalysts at low temperatures decreases.

---

3% Ir/Al₂O₃ . ( ) .

     

Studies on the active sites for dehydrocyclization reaction over Pt?Al2O3 catalysts

The work represents a search for direct evidence of the existence of low temperature and high temperature active sites over Pt–Al₂O₃ for dehydrocyclization reaction. It is suggested that the former consists of dispersed metallic Pt and the latter of super-dispersed metallic Pt or isolated atomic Pt and ionic Pt.

---

- - Pt/Al₂O₃ . , Pt, Pt, Pt.

     

Kinetic studies of Pt/Al2O3 catalyst pellets with nonuniform activity

Catalysts with nonuniform distribution of the catalytically active component (Pt) over their porous support (Al₂O₃) have been studied. A nonuniform activity distribution changes not only the reaction rate but also the kinetics can be different on these catalysts.

---

(Pt) (Al₂O₃). , , .

     

X-ray study of Re/Al2O3 and Re+Pt/Al2O3 catalysts using synchrotron radiation

Uning synchrotron radiation, L_III rhenium absorption spectra have been studied for Re/Al₂O₃ and Re+Pt/Al₂O₃ catalysts obtained by impregnation. For individual rhenium compounds a linear dependence between the shift of absorption edge and the state of rhenium oxidation has been found. The absorption spectra of reduced catalysts are significantly broadened as compared with those of individual compounds of the same valency. This points to the presence of rhenium compounds in different oxidation states.

---

L_III- , Re/Al₂O₃ Re+Pt/Al₂O₃, . . . .

     

A kinetic study of the methanation of CO2 over Ni?Al2O3 catalyst

CO₂ methanation has been studied over Ni–Al₂O₃ and the intrinsic kinetic data obtained are related by a powerlaw type rate expression, which established a good agreement between calculated and experimental values of conversion.

---

CO₂ Ni/Al₂O₃. . .

     

Ni-Mo/Al_2O_3催化剂上硫转移反应的研究

制备了以γ-Al2O3为载体的Ni-Mo催化剂,并用于FCC汽油的加氢硫转移反应。对Ni-Mo/Al2O3催化剂上的硫转移反应机理进行了研究,考察了不同反应条件对硫转移反应的影响。实验结果表明,硫醇与烯烃的反应在催化剂表面的加氢活性位上进行,小分子的硫醇发生加氢脱硫,生成吸附态H2S,吸附态的H2S与烯烃反应,生成大分子硫醇和硫醚;另外小分子硫醇还可直接与烯烃发生反应,生成硫醚。提高反应温度、压力、氢油比或降低空速,均可提高催化剂的硫转移反应活性,轻质硫转化率得到明显提高,且单烯选择性还能维持在98%左右。     

Al2O3负载Pt催化剂的合成及其甲醇低温催化燃烧性能研究

采用一步合成法制备了Al₂O₃负载Pt催化剂Pt/Al₂O₃,以甲醇催化燃烧作为目标反应研究了其催化性能,考察了还原剂浓度、表面活性剂用量、表面活性剂浓度和煅烧温度对Pt/Al₂O₃甲醇低温催化燃烧性能的影响。结果表明,当还原剂浓度为0.1 mol/L、表面活性剂(CTAB)用量为8.53 g/g_cat.、表面活性剂浓度为0.1 mol/L、煅烧温度为600℃时,所得催化剂的活性最高,25℃下甲醇催化燃烧的转化率达到52%。而改进一步合成法制备的负载型催化剂Pt/Al₂O₃具有更高的甲醇催化燃烧活性,25℃下甲醇催化燃烧的转化率为84%。     

Hydrogen effects on the electric conductivity of a Pt/Al2O3 catalyst

Hydrogen desorption, hydrogen spillover and reduction processes have been evidenced using a new experimental strategy based on AC electric conductivity measurements during TPD and TPR experiments on a 0.5% Pt/Al₂O₃ catalyst.     

Isomerization and secondary metathesis of 2-butenes over a MoO3/Al2O3 catalyst

Transformation of cis- and trans-2-butene at 40°C was investigated over a MoO₃/A₂O₃ catalyst reduced with hydrogen and subjected to different pretreatments. Isomerization is accelerated by hydrogen preadsorbed either at low or high temperatures. The cometathesis of 2-butenes with the 1-butene intermediate, however, is enhanced only by hydrogen preadsorbed at low and suppressed by hydrogen adsorbed at high temperatures.

---

- -2- 40°C MoO₃/Al₂O₃, . , , . 2- 1- , ; , .

     

Ni/γ-Al2O3催化剂上萘加氢生成十氢萘的催化反应研究

采用Ni/Al₂O₃催化剂,在高压固定床反应器中考察了反应温度、压力、空速和氢油体积比比等因素对萘饱和加氢反应行为的影响,尤其是反应条件对反式十氢萘和顺式十氢萘选择性的影响。研究表明,反式十氢萘和顺式十氢萘的选择性与反应操作条件密切相关;反式十氢萘与顺式十氢萘的比例随着氢油比和温度的升高而增加,而随着压力和空速的增加而减小。在反应温度260-290℃、反应压力为5-7 MPa、空速为1-1.5 h^-1及氢油体积比大于250时,十氢萘的选择性最高可达99%以上,萘的转化率接近100%,产物中反式和顺式十氢萘的比例最高,可达4.0左右。对Ni/γ-Al₂O₃催化剂稳定性进行了考察,初步发现催化活性组分的烧结或流失是催化剂失活和影响产物中反式十氢萘和顺式十氢萘比例的主要原因。     

Hydrocarbon conversion over Pt?Re/Al2O3-ZSM-5 bifunctional catalysts. II. Sulfur resistance of Pt?Re/Al2O3 modified with ZSM-5

The sulfur resistance of Pt–Re/Al₂O₃-ZSM-5 catalyst has been investigated for normal heptane reforming. It was found that while sulfur acts as a poison for Pt–Re/Al₂O₃, it can play an important role in activity maintenance and aromatics production when ZSM-5 zeolite is present.

---

Pt–Re/Al₂O₃-ZSM-5 -. , , Pt–Re/Al₂O₃, ZSM-5.

     

Catalytic activity of the Al2O3?Cr2O3?Fe2O3 system II. Influence of nitrogen bases on hydrocarbon aromatization

The physico-chemical properties of the Al₂O₃–Cr₂O₃–Fe₂O₃ catalyst system have been correlated with n-hexane dehydrocyclization. Using a poisoning technique, the ionic and radical steps of the reaction have been determined.

---

- Al₂O₃–Cr₂O₃–Fe₂O₃ -. , .