CoAPO-11分子筛在己烯骨架异构化反应中的应用及失活

 用水热法合成了CoAPO-11分子筛,并考察了温度和空速对分子筛上1-己烯骨架异构化反应的影响. 结果表明,1-己烯转化率以及产物异己烯的选择性和收率均随空速的增加而降低; 而随着温度的升高1-己烯转化率也升高,异己烯的选择性和收率则先增加后减小,在300 ℃附近有一最大值. 另外从分子筛的晶相、孔道尺寸以及酸性的变化等方面探讨了再生后的分子筛催化性能下降的原因.     

丙烯环氧化反应中TS-1催化剂失活研究

采用丙烯气相进料,在预混段中先与双氧水的甲醇溶液混合后进入固定床反应器,考察了进料液中pH值、丙二醇单甲醚、乙硫醇以及铁锈等对丙烯环氧化连续反应中TS-1分子筛催化剂性能的影响。结果表明,进料液体pH值对催化剂的催化性能有影响,适宜的进料液体pH值在7左右;副产物丙二醇单甲醚含量的增加不会对催化剂性能产生影响;乙硫醇量的增加使环氧丙烷选择性下降,但不会引起催化剂的失活;而进料液体中铁锈的引入会导致催化剂中部分孔堵塞,使催化剂部分失活。当进料液中的pH值用0.1mol/L的氨水调节为7左右,在反应温度55℃,反应压力0.7MPa,TS-1催化剂具有较好的稳定性,经130h的连续试验考察,双氧水的转化率和环氧丙烷的选择性约为90%。     

TiO2光催化剂失活机理研究进展

评述了TiO₂多相光催化剂在处理环境污染物领域的催化剂失活研究进展,主要探讨了气固多相光催化反应过程影响催化剂活性的因素,液固多 相光催化反应的催化剂失活的几种途径,以及解决催化剂失活问题的办法,最后对该领域的研究提出建议.     

环己酮氨肟化反应中TS-1催化剂的积炭失活

 采用连续淤浆反应器,在环己酮质量空速为6 h-1和温度为70 ℃的条件下,对 TS-1 催化剂上环己酮氨肟化制环己酮肟反应过程中的活性变化规律进行了考察,并用热重-差热分析、程序升温脱附、 N2物理吸附、程序升温氧化和傅里叶变换红外光谱等测试手段对不同运转时间及再生后的催化剂进行了表征. 结果表明,催化剂运转时间在60 h以内时活性稳定,然后迅速下降; 积炭是引起催化剂失活的主要原因. 催化剂表面的积炭主要沉积在 TS-1 的微孔内,含碳物种有两种类型: 易除炭存在于Ti中心附近,可在350 ℃下氧化除去; 难除炭沉积于强酸中心 Si-OH 处,需在700 ℃下才能除去. 催化剂失活前后的骨架结构未发生显著变化,经烧炭再生后活性可恢复到新鲜催化剂的水平.     

Deactivation of precolumns for capillary GC by a thin layer of OV-1701

Deactivation of precolumns with an ultra thin film of OV-1701 provided inertness at least equal to silylation, but better resistance to water. Dynamic coating of the raw fused silica capillary is, furthermore, much faster than the hydrothermal treatment/silylation procedure.     

钛硅分子筛在环己酮肟气相贝克曼重排反应中的失活

 对比了不同孔径的钛硅分子筛催化剂Ti－MCM－41（Si／Ti摩尔比＝27）和TS－1（Si／Ti摩尔比＝25）对环己酮肟气相贝克曼重排反应的催化性能，分析了它们在重排反应中的积碳量和孔体积的变化．结果表明，这些钛硅分子筛催化剂的失活主要是由积碳引起的，且积碳速率受催化剂孔径的制约．在重排反应过程中，TS－1催化剂微孔孔道内的积碳量随反应时间线性增加，微孔体积随反应时间线性下降；而二次孔内的积碳量随反应时间呈指数增加，孔体积随反应时间呈指数递减．     

乙苯脱氢制苯乙烯工业催化剂的失活原因

用混合法制备了工业乙苯脱氢催化剂,考察了新鲜催化剂和使用34个月后的催化剂的催化性能,并应用多种表征手段详细研究了所制备的工业催化剂在使用前后体相和表面的变化情况.活性测试结果发现,催化剂使用34个月后,活性下降12%,消炭后催化剂活性有所提高,但很快又恢复到失活后的水平.表征结果发现,积炭、钾的流失和催化剂活性相的烧结都不是导致催化剂失活的根本原因,而助催化剂钾的不均匀分布和催化剂活性相中Fe3 的还原可能是催化剂失活的主要原因.     

甲醇制烯烃催化剂失活模型

在固定床反应器中,研究了甲醇制烯烃反应中当SAPO-34分子筛处于失活期时催化剂活性的变化情况,主要考察催化剂活性随反应温度、空速和运行时间的变化,通过对实验数据的分析拟合,得到了催化剂活性与失活时间、反应温度、空速的经验关联式(失活模型),对失活模型的检验表明,该模型与实验数据较为吻合,表明了该式的准确性。 通过对失活模型的分析,获得了当失活速率达到最大时的失活时间与反应时间、空速的关联式,失活过程应服从不均匀表面失活机理,并且当催化剂处于失活区时,失活时间对活性的影响要大于空速和温度。     

Deactivation of external acid sites of H-mordenite by silica-modification in the isopropylation of biphenyl

Although extensive isomerization of 4,4'-diisopropylbiphenyl (4,4'-DIPB) occurred at 300^oC over H-mordenite, high selectivity for 4,4'-DIPB among DIPB isomers was observed over silica-modified H-mordenite. This is due to the prevention of the isomerization of 4,4'-DIPB by the deactivation of external acid sites. This revised version was published online in June 2006 with corrections to the Cover Date.     

有机-无机杂化溶胶-凝胶涂层对不锈钢毛细管柱的脱活作用研究

 用甲基三乙氧基硅烷和四乙氧基硅烷水解缩合后形成的有机 无机杂化溶胶 凝胶 (sol gel)涂层对国产气相用不锈钢毛细管柱进行脱活。通过气相法研究了不同老化温度下所得脱活涂层的行为。结果表明这种涂层不但对不锈钢柱内壁活性点有很好的遮盖作用 ,而且本身具有相当的分离能力。在 2 5 0℃下老化的涂层可使碳原子数在 12以下的正构烷烃达到基线分离 ,与未用涂层的不锈钢裸柱相比 ,吸附活性大大降低 ;但随着老化温度的升高 ,涂层在缩聚老化过程中产生不均匀微孔 ,对被分离物的作用力加强。     

Reversible Deactivation of Enzymes by Redox‐Responsive Nanogel Carriers

Novel redox‐responsive polymeric nanogels that allow highly efficient enzyme encapsulation and reversible modulation of enzyme activity are developed. The nanogel synthesis and encapsulation of enzyme are performed simultaneously via in situ crosslinking of pyridyldisulfide‐functionalized water‐soluble reactive copolymers, which are synthesized via reversible addition–fragmentation chain transfer copolymerization. Obtained nanogels with loaded cellulase demonstrate very good colloidal stability in aqueous solutions. The enzymatic activity of cellulase is greatly reduced when encapsulated in the nanogels and rapidly recovered in 10 × 10⁻³ m dithiothreitol solution. Fluorescence resonance energy transfer (FRET)‐based experiments indicate that the recovered enzymatic activity is mainly ascribed to the release of the enzyme due to the degradation of the disulfide crosslinking network after addition of dithiothreitol (DTT), instead of the enhanced substrate transport rate. The developed enzyme immobilization method opens new possibilities for reversible activation/deactivation of enzymes and opens up new directions for targeted protein therapy and biotechnology applications.

     

催化剂积炭失活宏观反应动力学的研究

 针对催化剂使用中积炭失活的一般性特点,借鉴库存集成电路长期稳定性预测研究结果,对现有的催化剂失活反应动力学方程进行了修正,并以渣油加氢脱硫反应为例加以验证. 修正后的失活反应动力学微分方程为-da/dt=kdad·tm,其积分式为a=1+(d-1)kdm+1tm+1-1d-1. 当m=0时,便成为常规的失活反应动力学方程; 当m≠0时,可将反应时间t视为一种虚拟反应组分.     

Deactivation studies of bifunctional Fe-HZSM5 catalyst in Fischer-Tropsch process

A physical mixture of alkali-promoted iron catalyst with binder based on Fischer-Tropsch synthesis and an acidic co-catalyst （HZSM5） for syngas conversion to hydrocarbons was studied in a fixed bed micro reactor. Deactivation data were obtained during the synthesis over a 1400 h period. The deactivation studies on iron catalyst showed that this trend followed the phase transformation Fe2.2C （ ε′） → Fe5C2 （χ） → Fe3C （θ）, and the final predominant phase of the catalyst was Fe3C （θ）. Deactivation of zeolite component in bifunctional catalyst may be caused by coking over the zeolitic component, dealumination of zeolite crystals, and migration of alkali promoters from iron catalyst under synthesis conditions. The deactivation rate of iron catalyst was also obtained.     

Deactivation kinetics of a COcoupling reaction after addition of H2 to the system

The influence of hydrogen on the catalytic coupling reaction of CO was tested ar reaction temperatures of 105 120^oC and a residence time of 1.8 s. The formation rate of diethyl oxalate (DEO) decreases with the addition of hydrogen to the system. Increasing hydrogen concentration and reaction temperature, the apparent rate of main reaction or the yield of DEO decreases more quickly. But the deactivation rate does not change with the relative activity. By correlating the experimental data, the deactivation kinetics was obtained. This revised version was published online in June 2006 with corrections to the Cover Date.     

多相催化体系的反应机理和失活模式(英文)

Solving the problem of catalyst deactivation is essential in process design. To do this, various aspects of the kinetics of processes with catalyst deactivation, and their different mechanisms, are discussed. Catalyst deactivation often cannot be avoided, but more knowledge on its mechanism can help to find kinetic means to reduce its harmful consequences. When deactivation is caused by coke, the generation of coke precursors is the determining step in the deactivation kinetics. Different types of deactivation were distinguished that lead to different evolution of the process. The phenomenon of non-uniform coking can be linked to catalyst surface non-uniformity. For the class of catalysts with more than one type of active sites, an explanation was suggested for the observed trends in the deactivation modes. For catalytic proc-esses using catalyst particles of industrial size, the influence of intraparticle diffusion resistance is important. The analysis showed that for a number of processes, the decrease of the reaction rate due to deactivation is less under diffusion control. For certain reaction mechanisms, there exist operation conditions where the rate of the process under diffusion control exceeds the rate in the kinetic control regime. A signifi-cant problem is the change of selectivity in the course of catalyst deactivation. The selectivity may either decrease or increase, and depends on the reaction mechanism during deactivation. The changes are larger when there is no diffusion resistance. The intentional poisoning of catalysts and its influence on catalyst activity and selectivity for the process of ethylene oxide production was discussed.     

Study on the Deactivation Kinetics of Pd（PPh3）2Cl2 in the Monocarbonylation of Benzyl Chloride

The deactivation kinetics of Pd(PPh3)2Cl2 in the monocarbonylation of benzyl chloride to synthesize phenylacetic acid is studied in this paper. Solid 1-(2-pyridylazo)-2-naphthol (PAN) is used as the colouring agent, and the concentration of Pd(PPh3)2Cl2 in the system is measured through absorptiometry. The result shows that the optimum condition of the chromogenic reaction between Pd2+ and PAN is: 0.5 ml of 0.04% PAN added to 10 ml of Pd2+ solution (1.0×10-6-2.0×10-5 mol/L), and heated in a constant temperature water bath at 40℃ for about 30 min, with pH of the solution being about 3.0. The molar coefficient of absorption is 1.384×104 L/(mol·cm); the orders of the hydrolytic reaction to the concentration of Pd(PPh3)2Cl2, PPh3, phenylacetic acid and NaOH are 0.5, minus 0.8, 2 and 1.2, respectively. The activation energy (E) of the hydrolytic reaction is 75.59 kJ/mol, and the pre-exponential factor is 1.68×1012.     

芳氧基取代酞菁锌的合成及光物理化学性质

合成得到3-(5-氨基-萘氧基)邻苯二甲腈(C18H11N3O)、4-(5-氨基-萘氧基)邻苯二甲腈(C18H11N3O)、3-联苯氧基邻苯二甲腈(C20H12N2O)及4-联苯氧基邻苯二甲腈(C20H12N2O)4种未见报导的取代邻苯二甲腈,以此为前躯体合成了四[α-(5-氨基-萘氧基)]酞菁锌(C72H44N12O4Zn)、四[β-(5-氨基-萘氧基)]酞菁锌(C72H44N12O4Zn)、四[α-(联苯氧基)]酞菁锌(C80H48N8O4Zn)和四[β-(联苯氧基)]酞菁锌(C80H48N8O4Zn)4种未见报导的芳氧基取代酞菁锌配合物。通过测定它们的紫外-可见吸收光谱、荧光发射光谱,获得其最大吸收波长及其摩尔消光系数、最大发射波长、荧光量子产率(ΦF)、单线态氧量子产率(ΦΔ)及光降解速率常数并与其类似物进行了比较,探讨了它们的光物理光化学性质的构效关系。研究结果表明四[α-(联苯氧基)]酞菁锌在红光区具有大的摩尔消光系数,且具有较高的ΦΔ,有望开发成为光动力治疗用光敏剂。     

浆态相甲醇合成催化剂的失活机理

 浆态床甲醇合成过程具有重要的工业应用价值,影响该过程工业化的根本原因是催化剂易失活. 以合成气为原料,医用液体石蜡为溶剂,在5 MPa, 260 ℃和 1100 ml/(g·h)的反应条件下于浆态床反应器中考察了铜基甲醇合成工业催化剂C301的稳定性,并采用程序升温还原、 X射线衍射、透射电镜、扫描电镜、 扫描电镜能谱、元素分析和N2物理吸附等表征方法对不同失活程度的催化剂的物相组成和形貌进行了表征. 结果表明,在本实验条件下,失活催化剂无中毒现象,但随着反应时间的延长,催化剂晶粒长大,比表面积减小,积炭和热烧结现象较明显,但不伴随活性组分铜的流失.     

Ab initio study of the photochemistry of aminopyrimidine

Complete active space self‐consistent field (CASSCF), multi‐reference configuration interaction calculations (MR‐CISD), and equation of motion coupled‐cluster with singles and doubles (EOM‐CCSD) calculations are presented in order to elucidate the photodeactivation pathways of 6‐aminopyrimidine after vertical excitation to the S₁ ¹nπ* state. Vertical excitation energies are reported up to the S₇ state. Two S₁ excited state minima, both of ¹nπ* character, and three strongly puckered ¹ππ* minima on the crossing seam (MXS) between the S₀ and the S₁ potential energy surface were found. Nonadiabatic reaction paths are discussed by linearly interpolating between the two minima and all MXS, which explain and extend observations made in recent surface‐hopping dynamics CASSCF investigations [Barbatti and Lischka, J Phys Chem A 2007, 111, 2852]. © 2008 Wiley Periodicals, Inc. Int J Quantum Chem, 2008