Quantified MS analysis applied to combinatorial heterogeneous catalyst libraries

A high-throughput screening system for secondary catalyst libraries has been developed by incorporation of an 80-pass reactor and a quantified multistream mass spectrometer screening (MSMSS) technique. With a low-melting alloy as the heating medium, a uniform reaction temperature could be obtained in the multistream reactor (maximum temperature differences are less than 1 K at 673 K). Quantification of the results was realized by combination of a gas chromatogram with the MSMSS, which could provide the product selectivities of each catalyst in a heterogeneous catalyst library. Because the catalyst loading of each reaction tube is comparable to that of the conventional microreaction system and because the parallel reactions could be operated under identical conditions (homogeneous temperature, same pressure and WHSV), the reaction results of a promising catalyst selected from the library could be reasonably applied to the further scale-up of the system. The aldol condensation of acetone, with obvious differences in the product distribution over different kind of catalysts, was selected as a model reaction to validate the screening system.     

Pd-diimine: a highly selective catalyst system for the base-free oxidative Heck reaction

Pd(OAc)(2)/3 is an efficient catalyst system for the base-free oxidative Heck reaction that outperforms the currently available catalysts for the more challenging substrates studied. The catalyst system is highly selective, and works at room temperature with dioxygen as the oxidant.     

Methionine‐functionalized chitosan–Pd(0) complex: A novel magnetically separable catalyst for Heck reaction of aryl iodides and aryl bromides at room temperature in water as only solvent

We report a novel catalyst system with an immobilized palladium metal‐containing magnetic nanoparticle core (ImmPd(0)‐MNPs) for the Heck reaction. ImmPd(0)‐MNPs was found to be an exceptionally mild and versatile catalyst for the Heck reaction of aryl iodides and bromides at room temperature. The catalyst was simply recovered using an external magnet from the reaction mixture and recycled six times. The results showed that the catalyst was very active and stable. Moreover, the reaction was carried out in water as a green and environmentally acceptable solvent. In terms of scope and mildness, ImmPd(0)‐MNPs is an improvement over previously reported catalysts for Heck coupling methods.     

Kinetic modelling and simulations studies for propanoic acid esterification process

The esterification of propanoic acid with n-butanol to produce n-butyl propionate and water in the influence of an Amberlite catalyst was investigated using a batch reactor. The catalyst was chosen based on its ability to perform in this reaction. The temperature of the reaction runs between 363.15 K and 403.15 K, while the propanoic acid to n-butanol molar ratio is around 1:1 and 1:4. The selection of the catalyst loading is dependent on the volume of the reaction mixture. The catalyst dosage was kept within a 1%–3% by weight range. The kinetics of conversion have been researched in relation to the reaction temperature, mole ratio, catalyst size, stirrer speed, and catalyst quantity. The catalyst dosage and reaction temperature, according to the study, have a substantial influence on how soon the system achieves equilibrium. The pseudo homogeneous kinetic model is developed and tested against experimental results. Under the specified conditions, model predictions and empirical observations accord well. Arrhenius equation was used for calculation of rate constants and energy of activation. The forward reaction's frequency factor & activation energy are 18.554 L/mol.min and 30350 J/mol, correspondingly. Since the equilibrium constant increases as the temperature rises, the reaction is endothermic.     

FCC汽油低温改质过程的烯烃转化及催化剂积炭

利用微反-色谱联合实验装置和连续式小型提升管催化裂化实验装置研究了催化裂化汽油低温改质过程中烯烃转化和催化剂积炭的过程和规律。通过对模型化合物和催化裂化汽油改质过程中催化剂活性、催化裂化汽油窄馏分、反应温度、剂油比和反应时间对烯烃转化和催化剂积炭的研究表明，大部分烯烃转化和催化剂积炭的反应发生在油剂接触极短的反应时间内，并随着催化剂活性、反应物活性、剂油比和反应温度的提高而增加。在油剂接触后很长的反应时间内，生焦量、积炭速率和烯烃的转化程度都很小，烯烃转化损失率降低，因此，催化裂化汽油在低温改质的条件下可以通过延长反应时间来提高烯烃的转化率。因此，催化裂化汽油改质的最佳工艺条件为，390℃～440℃，剂油比6，催化剂活性61～65，长反应时间，轻馏分进料。     

钼酸胺催化剂对煤-油共处理反应性的影响

用共振搅拌反应器研究了钼酸胺催化剂对煤-油共处理中煤总转化率及产物的影响。研究表明，低温时(390 ℃)，催化剂能促进前沥青烯向小分子苯可溶物转化；高温时(480℃)，有催化剂时煤的转化率低于无催化剂时煤的转化率，而且在产物中苯可溶物产率与前沥青烯产率全部减少，说明产物发生了缩聚反应。在高温时(390 ℃)随反应时间的延长，煤转化率下降，同时在产物中苯可溶物产率与前沥青烯产率呈下降趋势。反应温度越高，反应时间越长，缩聚越严重。反应体系有供氢溶剂不能抑制缩聚反应。     

Preparation of Hydrogenated Nitrile Rubber

Hydrogenated nitrile rubber is an oil and solvent resistant rubber and particularly give more resistant to heat, ozone, light. It is generally prepared from nitrile rubber by selective hydrogenation using a suitable catalyst system. In the present work a prepared method was adapted for the hydrogenation reaction of nitrile rubber using homogeneous tris(tri-phenlphosphine)chlorhodium(I) catalyst (RhCl(PPh3)) system. The hydrogenation reaction was carriedout at different temperature, pressure, time and catalyst concentration, the concentration, the conditions of hydrogenation are stated in table 1.     

镍基催化剂上硫醇与异戊二烯硫醚化反应的研究

在上流式气-液-固三相固定床微型反应装置上，对Ni／Al2O3催化剂上硫醇与异戊二烯硫醚化反应进行了研究，并考察了反应温度、压力、空速、临氢条件对催化剂二烯硫醚化反应性能的影响。结果表明，异戊二烯与硫醇在镍基催化剂的作用下，可以发生反应生成高沸点的硫醚化合物，反应温度和空速对催化剂二烯硫醚化活性有明显的影响，提高反应温度和降低空速有利于提高硫醇在二烯硫醚化反应过程中的转化率，在临氢反应条下，可以提高催化剂二烯硫醚化反应的活性和稳定性。     

环钯-[PPh4]Br体系催化氯代芳烃的Heck芳基化反应研究

以氯代芳烃为底物，季鏻盐[PPh4]Br为助催化剂，用于环钯催化的Heek芳基化反应．结果表明，在环钯-[PPh4]Br催化体系中，以Na2CO3作为碱性试剂，使用0．3mol％Pd的环钯催化剂催化氯苯的Heek反应，就可得到比较高的产率（88％）和转化率（90％）．对于大部分卤代芳烃Heck反应而言，环钯-[PPh4]Br是一种有效的催化体系，即使是对含推电子基团的不活泼的氯代芳烃，在此体系中也能获得比较好的结果．此外，文中还探讨了反应温度、[PPh4]Br／Pd比值及催化剂回用对反应活性的影响．     

Indications for a surface temperature excess in heterogeneous catalysis

We explored the surface temperature excess DeltaT = T(r) - T(m) (real reaction temperature T(r), measured catalyst temperature T(m)) on the basis of experimental data, a gradually curved Arrhenius plot for CO oxidation reactions over Pd/gamma-Al(2)O(3) catalysts. Such a plot could be an indication of the surface temperature excess in the 2-dimensional reaction surfaces of catalysts. The positive or negative surface temperature excess could be developed to be a general explanation for a gradually curved Arrhenius plot of a gas-solid catalytic system. This is a new insight into solving the puzzle on such common phenomena in heterogeneous catalysis. By using the reciprocal of the real reaction temperature T(r) in the hypothetical 2-D reaction surface, instead of the experimentally determined catalyst temperature T(m) or the gas temperature T(g), the gradually curved Arrhenius plot becomes linear. We investigated the implications of such a difference among T(r), T(m), and T(g). The surface temperature excess could be the effect of coupling between the fluxes of a chemical reaction and heat transport in the 2-D reaction surface. Its order of magnitude is 10 K for the present model system.(1) The surface temperature excess increases exponentially with the reaction temperature.     

A New Method of Low Temperature Methanol Synthesis

Low temperature methanol synthesis is a promising technique for the practical methanol industry. New developments of a new kind of low temperature methanol synthesis were reviewed, including the effects of feed gas, reaction solvent, supercritical media and catalyst modification. The reaction mechanism and kinetics were also summarized primarily. Carbon dioxide played an important role in this new kind of low temperature methanol synthesis. It reacted with hydrogen adsorbed on catalyst surface to form HCOOM, an important reaction intermediate. Alcohol solvent in the low temperature methanol synthesis performed not only a media, but also a homogeneous catalyst. The reaction of the adsorbed formate species with alcohol on Cu/ZnO catalyst surface proceeded according to the Rideal mechanism rather than Langmuir–Hinshelwood mechanism to form alkyl formate. The formation of alkyl formate from alcohol solvent and hydrogenation of such an alkyl formate were the key steps in low temperature methanol synthesis reaction. These results provided new insights into low temperature methanol synthesis.     

红外光谱法对COS水解催化剂氧中毒行为的研究

采用一套玻璃真空系统，对COS、H2S、O2各自的吸附行为进行了研究，通过红外谱图发现COS是解离吸附，由H2S＋O2的共吸附与H2S＋O2＋COS的共吸附结果可以看出，只有H2S与O2共存时，才会导致催化剂的失活，且导致COS水解催化剂失活的主要原因是单质硫和微量的硫酸盐沉积于催化剂的表面，温度越高，失活越严重，红外光谱得出的结果与微反得出的结果一致，并提出了失活机理。     

Catalytic coprocessing of waste plastics and petroleum residue into liquid fuel oils

Waste plastics of different types were catalytically coprocessed with petroleum residue of light Arabian crude oil in the presence of a number of catalysts. The purpose of the study was to explore effects of various conditions such as catalyst type, amount of catalyst, reaction time, pressure and temperature on the product distribution. The waste plastic studied included low-density polyethylene (LDPE), high-density polyethylene (HDPE), polystyrene (PS) and polypropylene (PP). A series of single (waster plastic with catalyst) and binary (waste plastic and residue with catalyst) reactions were carried out in an autoclave reactor under variable reaction conditions. The reaction conditions used were 1, 3 and 5 wt.% catalysts, 30–120 min reaction time, 400–430 °C reaction temperature and 500–1200 psi hydrogen pressure. The product distribution achieved for residue/plastic/catalyst system showed higher yields of liquid fuels as compared to residue/plastic system. Hydrocarbon gases were formed as well along with heavy oils, insoluble gums and coke. At the reaction conditions of 3 wt.% NiMo catalyst, 90 min reaction time, 1200 psi hydrogen gas pressure, 430 °C temperature and residue to plastic feed ratio of 3:2 (wt.) afforded maximum conversion of the plastics into liquid fuel oils.     

铁系高温变换催化剂上水煤气变换反应本征动力学的研究

采用活塞流管式积分反应器,在1.0 MPa压力下,对环境友好铁系无铬NBC-1型高温变换催化剂上变换反应本征动力学数据进行了测试。根据测定得到的数据,对幂函数动力学模型进行了模型参数估计和模型检验,得到了高度显著的动力学回归方程。从动力学方程可以得出:该高温变换催化剂上变换反应活化能比较低,因此其低温活性较好；该催化剂上H2O组分对反应速率的影响比较大；CO2对变换反应速率的抑制作用很大,因此为提高变换反应速率,应当设法减小CO2的不利影响；H2组分对反应速率的影响很小,在实际应用过程中,可以忽略。     

强酸性阳离子交换树脂负载金属离子改性催化合成乙酸丁酯

用两种强酸性阳离子交换树脂进行金属离子负载改性制备酯化催化剂,考察了金属盐种类,盐浓度,沉浸时间,沉浸温度等因素对催化剂性能的影响.用在优化条件下制备的催化剂催化乙酸和正丁醇酯化反应体系,反应1h乙酸的转化率达到69%.     

Low-Temperature Catalytic Oxidation of Sulfide Ions in Aqueous Solutions on a Ni-Oxide System

Catalytic oxidation of sulfide ions in aqueous solutions by air oxygen has been investigated using a Ni-oxide system as a catalyst. The kinetics and the selectivity of the oxidation process were studied by varying the pH, catalyst amount and reaction temperature. A reduction/oxidation mechanism of the reaction has been supposed comprising interaction between the surface active oxygen of the catalyst and HS^– and reoxidizing of the reduced catalyst by the dissolved oxygen. The results obtained show that the Ni-oxide system is a promising catalyst for practical application.     

Hydrolysis and polycondensation of acid-catalyzed Phenyltriethoxysilane (PhTES)

The effects of acid catalyst, water content and reaction temperature on the hydrolysis and polycondensation of phenyltriethoxysilane (PhTES) were studied using ²⁹Si NMR spectroscopy. The sol catalyzed by hydrochloric acid showed the simultaneous progress of hydrolysis and polycondensation. In addition, the reaction rate was almost independent of reaction temperature. On the other hand, the polycondensation in the PhTES-derived sol mixed with an excess amount of water and acetic acid as a catalyst proceeded after completion of the hydrolysis. In the acetic acid-catalyzed system, the degree of the hydrolysis and polycondensation largely depends on the reaction temperature.     

含钒杂多酸催化发烟硫酸中甲烷液相部分氧化反应

 以H5PV2Mo10O40 为催化剂,在发烟硫酸中进行了甲烷液相部分氧化,考察了催化剂用量、反应温度、反应时间和发烟硫酸浓度等工艺条件对反应收率的影响. 甲烷在反应中首先转化为硫酸甲酯,硫酸甲酯随后水解为甲醇. 对于甲烷液相部分氧化反应,发烟硫酸中游离的SO3是非常重要的影响因素. 在工艺条件为催化剂用量7.0 mmol, 反应温度473 K, 反应压力3.5 MPa, 反应时间3 h和发烟硫酸中SO3含量50%时,甲烷转化率可达48.5%, 目的产物甲醇收率为41.5%.     

光热催化还原二氧化碳反应器研究进展

光热催化还原技术是二氧化碳资源化的研究热点之一。设计高效的新型催化剂材料,是构建有效的光热催化反应体系的重要内容,而开发与催化材料适配的反应器,则可以最大化地发挥催化剂的性能,是光热催化放大反应的关键。本文综述了光热催化反应器的不同形式,讨论了光热催化关键变量温度、光照、给料类型和运行方式对反应器设计的影响。总结了反应器设计的局限性和挑战性,为光热催化还原二氧化碳的技术发展提出了展望。     

Catalytic epoxidation of polyisobutylene-co-isoprene with hydrogen peroxide

Polyisobutylene-co-isoprene (PIBI) can be epoxidized with hydrogen peroxide in the presence of methyltrioctylammonium tetrakis (diperoxotungsto) phosphate(3-) as the catalyst in a biphasic system. The effects of the reaction time and temperature, the ratio of the organic phase to the aqueous phase, the concentration of the catalyst and polymer and stirring intensity, respectively, are studied on the conversion of double bonds to oxirane groups. ¹H-NMR analysis confirms the absence of ring opening side reactions in this epoxidation reaction system. The kinetics of the reaction are discussed. The rate constants are measured at four temperatures and the activation energy for the reaction is determined as 54.2kJ/mol. The optimum reaction temperature is about 60°C.