CO2气氛下负载型Cr2O3催化剂上乙苯脱氢制苯乙烯反应

 采用浸渍法制备了负载型Cr2O3/Al2O3和Cr2O3/SiO2催化剂,并考察了催化剂在CO2气氛下催化乙苯脱氢制苯乙烯反应的活性. 结果表明,Cr2O3/Al2O3的催化活性高于Cr2O3/SiO2. 这可能是由于Cr2O3在Al2O3载体表面的分散度大大高于在SiO2表面的分散度. 催化剂的催化活性与Cr2O3的负载量有关,在w(Cr2O3)=25%时,Cr2O3/Al2O3的催化活性最高. CO2气氛对乙苯脱氢反应有明显的促进作用; 在CO2气氛下,Cr6+物种可能是催化乙苯脱氢反应活性位的前驱体.     

改性三氧化二铬催化1,1,3,3-四氯丙烯氟化高选择性合成反式-1-氯-3,3,3-三氟丙烯研究

反式-1-氯-3, 3, 3-三氟丙烯 (HCFO-1233zd (E))是近年来正在研发的第四代发泡剂,其大气臭氧消耗潜能值为0.00024,温室效应潜能值为7.0,毒性低,常态下不燃,使用安全;它也是合成含氟精细化工品的中间体,以及合成氟树脂和氟弹性体的单体。本论文制备了Al,Zn,Co改性的Cr2O3催化剂,将其成功应用于1, 1, 3, 3-四氯丙烯（HCC-1230za）与氟化氢反应中,高选择性地合成HCFO-1233zd (E),复合催化剂Zn / Cr2O3显示高稳定性,其中HCC-1230za转化率高达99.4％,HCFO-1233zd（E）的选择性高达98.2％。反应条件诸如反应物HF / HCC-1230za 的摩尔比和反应温度等对产物分布有显着影响。在相对较低的温度（200?C）和较大的HF / HCC-1230za 摩尔比（10：1）下,对HCFO-1233zd（E）的选择性有利。通过XRD,XPS,BET和V70吡啶吸附红外光谱技术对复合催化剂Zn / Cr2O3进行了表征。 XRD结果表明,催化剂中大多数无定形Cr2O3和高度分散微晶相Cr2O3共同导致催化剂的高活性和高稳定性。HCC-1230za的转化率与预氟化处理催化剂Zn / Cr2O3的比表面积有关,催化剂的比表面积越高,催化活性越高。XPS光谱表明,在预氟化过程中,表面铬氧化物可能与F原子强烈相互作用,从而导致Cr原子的化学环境发生广泛变化。V70吡啶吸附红外光谱和氨-程序升温脱附技术结果证明尚未失活的催化剂Lewis 酸和Br?nsted酸中心的数目和强度与新制备的催化剂相比明显提高。     

Pt coated Cr2O3 thin films for resistive gas sensors

The resistive response of atomic layer deposited thin epitaxial α-Cr₂O₃(0 0 1) films, to H₂ and CO in air, was studied. The films were covered with Pt nanoislands formed by electron-beam evaporation of a sub-monolayer amount of the material. The gas measurements were performed at 250°C and 450°C. These temperatures led to different proportion of chemical states, Pt²⁺ and Pt⁴⁺, to which the Pt oxidized. The modification was ascertained by the X-ray photoelectron spectroscopy method. As a result of the modification, the response was fast at 250°C, but slowed at 450°C. A disadvantageous abundance of Pt⁴⁺ arising at 450°C in air could be diminished by high-vacuum annealing thus restoring the response properties of the system at 250°C.      

3DOM InVO4-supported chromia with good performance for the visible-light-driven photodegradation of rhodamine B

Three-dimensionally ordered macroporous (3DOM) monoclinic InVO₄ and its supported chromia (yCrO_x/3DOM InVO₄, y denotes as the weight percentage of Cr₂O₃, y = 5, 10, 15, and 20 wt%) photocatalysts were fabricated using the ascorbic acid-assisted polymethyl methacrylate-templating and incipient wetness impregnation methods, respectively. Physicochemical properties of the materials were characterized by means of a number of analytical techniques. Photocatalytic activities of the samples were evaluated for the degradation of rhodamine B (RhB) in the presence of H₂O₂ under visible-light illumination. Compared to 3DOM InVO₄ and 15CrO_x/bulk InVO₄, yCrO_x/3DOM InVO₄ showed much better visible-light-driven photocatalytic performance for RhB degradation, with the 15CrO_x/3DOM InVO₄ sample performing the best. It is concluded that the CrO_x loading, higher surface area and surface oxygen vacancy density and lower bandgap energy as well as the better quality of 3DOM structure were responsible for the good photocatalytic performance of 15CrO_x/3DOM InVO₄ for the degradation of RhB.     

Characterization and Dehydrogenation Activity of SBA-15 and HMS Supported Chromia Catalysts

ＩｎｔｒｏｄｕｃｔｉｏｎＥｎｏｒｍｏｕｓｓｔｕｄｙｈａｓｂｅｅｎｄｅｖｏｔｅｄｔｏＭ4 1Ｓ ,ｔｈｅｆｉｒｓｔｆａｍｉｌｙｏｆｍｅｓｏｐｏｒｏｕｓｍｏｌｅｃｕｌａｒｓｉｅｖｅｓｒｅｐｏｒｔｅｄｉｎ1992 ,1,2 ｉｎｃｌｕｄｉｎｇｔｈｅｉｒｍｏｄｉｆｉｃａｔｉｏｎｓａｎｄａｐｐｌｉｃａｔｉｏｎｓｉｎｃａｔａｌｙｓｉｓ .Ｔｈｅａｔｔｒａｃｔｉｖｅｐｒｏｐｅｒｔｉｅｓｏｆｔｈｅｓｅｍａｔｅｒｉａｌｓａｒｅｔｈｅｉｒｈｉｇｈｓｐｅｃｉｆｉｃｓｕｒｆａｃｅａｒｅａ (>10 0 0ｍ2 /ｇ) ,ｗｅｌｌ ｄｅ ｆｉｎｅｄｓｔｒ…     

Oxidation kinetics study of the iron-based steel for solid oxide fuel cell application

Kinetics of oxidation of Fe-Cr steel containing 25 wt.-percent Cr was studied as a function of temperature (1023–1173 K) for up to 480 h in flowing air, which corresponds to SOFC cathode environment operating conditions. The oxidation process was found to be a parabolic, suggesting that the diffusion of ionic defects in the scale is the slowest, rate determining step and it occurs predominantly by short-circuit diffusion paths. Comparison of the determined activation energy of oxidation of the studied steel with literature data indicates that at 1098–1173 K the chromia scale grows by the outward solid-state diffusion of chromium interstitials, whereas at 1023–1098 K — through a significant contribution of counter-current oxygen/chromium diffusion along Cr₂O₃ grain boundaries. The oxide scales were composed mainly of Cr₂O₃ with a continuous thin Mn_1.5Cr_1.5O₄ spinel layer on top of the chromia scale. The oxidation test results on Fe-25Cr steel demonstrate the applicability of the commercial type DIN 50049 stainless steel as interconnect for SOFC. This revised version was published online in July 2006 with corrections to the Cover Date.     

氧化铬柱层状铌酸的合成和表征

本文报道先用正丙胺预支撑层状铌酸,然后同氯化四甲铵水溶液进行离子交换,最后再与醋酸铬(Ⅲ)水溶液反应可得含铬(Ⅲ)聚合离子支撑的层状铌酸。进一步焙烧所得含铬(Ⅲ)聚合离子支撑的层状铌酸可得氧化铬柱层状铌酸。该材料具有较高的热稳定性(>700℃)和BET比表面(66.7 m²/g),是一类中等偏弱的新型多孔固体酸(平均孔径为3.3 nm,总酸量为188.3 μmol/g,且主要为Lewis酸)。     

Isobutane dehydrogenation over chromia alumina catalysts prepared from MIL-101: Insight into chromium species on activity and selectivity

Various mesoporous chromia alumina catalysts were prepared by five different methods based on a metal-organic framework MIL-101 and their catalytic performances over isobutane dehydrogenation were investigated. The highly dispersed chromium species were produced on catalyst KCr Al-I1 with largest specific surface area of 198 m2 g-1prepared with aluminium isopropoxide(Al(i-OC3H7)3) by ultrasonic impregnation method. However, the catalyst KCr Al-I2 synthesized by stirring impregnation possessed crystalline α-Cr2O3 phase, which was poorly dispersed. Two types of Cr-rich and Al-rich Crx Al2-xO3 solid solutions, designated as Cr Al-I and Cr Al-II phase, were formed over the catalysts KCr Al-I3(prepared by Al(i-OC3H7)3with nitric acid regulation), KCr Al-C4(prepared by aluminium chloride hexahydrate) and KCr Al-N5(prepared by aluminium nitrate nonahydrate). Catalytic evaluation results revealed that KCr Al-I1 exhibited the high isobutane conversion due to its highly dispersed chromium species. However, KCr Al-I3, KCr Al-C4 and KCr Al-N5 showed the higher isobutene selectivity(95.2%-96.4%) on account of the formation of chromia alumina solid solutions in the catalysts. Moreover, the solid solution over the chromia alumina catalysts could greatly suppress the coke formation.     

Isobutane dehydrogenation over chromia alumina catalysts prepared from MIL-101:Insight into chromium species on activity and selectivity

Various mesoporous chromia alumina catalysts were prepared by five different methods based on a metal-organic framework MIL-101 and their catalytic performances over isobutane dehydrogenation were investigated. The highly dispersed chromium species were produced on catalyst KCrAI-I1 with largest specific surface area of 198 m2-g-1 prepared with aluminium isopropoxide （Al（i-OC3HT）3） by ultrasonic im- pregnation method. However, the catalyst KCrAI-I2 synthesized by stirring impregnation possessed crystalline a-Cr203 phase, which was poorly dispersed. Two types of Cr-rich and Al-rich CrzA12_zO3 solid solutions, designated as CrAI-I and CrAI-II phase, were formed over the catalysts KCrAI-I3 （prepared by Al（i-OC3HT）3 with nitric acid regulation）, KCrA1-C4 （prepared by aluminium chloride hexahydrate） and KCrA1-N5 （prepared by aluminium nitrate nonahydrate）. Catalytic evaluation results revealed that KCrAI-I1 exhibited the high isobutane con- version due to its highly dispersed chromium species. However, KCrAI-I3, KCrA1-C4 and KCrA1-N5 showed the higher isobutene selectivity （95.2%-96.4%） on account of the formation of chromia alumina solid solutions in the catalysts. Moreover, the solid solution over the chromia alumina catalysts could greatly suppress the coke formation.