摘要:
A method for effective and inexpensive synthesis of a zero-valence transition metal complex as a starting material for synthesis of a catalyst usable in, for example, production of polyolefins through ring-opening metathesis polymerization of olefins and synthesis of epothilones through ring closing metathesis reaction thereof, and further effective and inexpensive synthesis of an organometallic compound useful as such a catalyst from the zero-valence transition metal complex. In particular, a method of synthesizing zero-valence transition metal complex (C) through reaction between bivalent transition metal complex (A), the bivalent transition metal complex (A) selected from among bivalent ruthenium complexes (A ) and bivalent osmium complexes (A ), and olefin (B), characterized in that after reaction under reducing conditions, the obtained crude products are subjected to hot extraction with a saturated hydrocarbon as an extraction solvent. Further, there is provided a method of synthesizing an organometallic compound, characterized in that the zero-valence transition metal complex (C) is subjected to a one-step reaction with specified compound (D) and neutral ligand (E).
摘要:
Hydroisomerization of hydrocarbon feeds is effected over a Group VIII metal containing catalyst, the catalyst also containing a hydrocracking suppressant such as a Group IB metal or sulfur.
摘要:
A two-stage process for obtaining a substantial amount of olefinic product from a residua feedstock. The first stage is comprised of a thermal process unit containing a reaction zone comprised of a horizontal moving bed of fluidized hot particles operated at temperatures from about 500 to 600 °C and having a short vapor residence time, and the second stage thermal conversion zone operated at a temperature of about 700 °C to about 1100 °C, and also having a short vapor residence time.
摘要:
There is provided a process for the net catalytic oxidative dehydrogenation of alkanes to produce alkenes. The process involves simultaneous equilibrium dehydrogenation of alkanes to alkenes and combustion of the hydrogen formed to drive the equilibrium dehydrogenation reaction further to the product alkenes. In the present reaction, the alkane feed is dehydrogenated over an equilibrium dehydrogenation catalyst in a first reactor, and the effluent from the first reactor is then passed into a second reactor containing a reducible metal oxide which serves to selectively combust hydrogen in an oxidation/reduction (REDOX) reaction. This particular mode of operation is termed a separate reactor, REDOX mode.
摘要:
A method for selective dehydrogenation of a compound, comprising contacting a compound of formula (I), wherein each R1, R2, R3 and R4 is independently selected from the group consisting of H, (C1-C20) alkyl, (C3-C20) cycloalkyl, (C6-C20) aryl, (C7-C20) alkylaryl, (C7-C20) aralkyl groups, as well as substituted (C1-C20) alkyl, (C3-C20) cycloalkyl, (C6-C20) aryl, (C7-C20) aralkyl and (C7-C20) arylalkyl moieties, optionally further substituted with -OR, wherein R is R1, R2, R3 or R4; and wherein R1 and R2 or R3 and R4 may be joined as part of a ring structure, at a dehydrogenation temperature in the presence of a catalyst comprising about 0.01 wt % - 19.9 wt % Pd and about 0.01 wt % - 19.9 wt % Cu on a carbon support, wherein the total amount of (Pd + Cu) on the support is about 0.02 wt % to 20 wt %, the weight ratio of Pd:Cu is about 1:1 to 10:1, and the carbon support has a surface area of at least about 100 m2/g and is essentially free of reactive sulfur. A selective dehydrogenation catalyst having the composition described supra is disclosed as is a method of preparing the same. This catalyst is highly selective for dehydrogenating a variety of substrates while minimizing the formation of unwanted hydrogenolysis by-products.
摘要:
A process for making diethynylbenzene by a "one-pot" reaction in which mixed isomers of divinylbenzene (DVB) and bromine are combined in a solvent consisting of sulfolane, at a rate that does not cause the temperature of the reaction to rise above 50°C., the intermediate brominated product is dehydrobrominated, and diethynylbenzene is separated from the dehydrobromination reaction mixture, is disclosed.
摘要:
1. A L zeolite of total SiO2 /Al2 O3 molar ratio at least equal to 8, having a potassium content lower than 2.9% by weight, a sodium content lower than 0.5% by weight, crystalline parameters vector a and vector c respectively lower than 1.836 nm and 0.754 nm, a nitrogen adsorption capacity, measured at 77 K, under a P/Ps partial pressure of 0.19, higher than 11% by weight, a benzene adsorption capacity at 30 degrees C under a P/Ps partial pressure of 0.25, higher than 8.5% by weight, said L zeolite having a lattice of secondary pores (mesopores) whose radii range from 0.8 nm to 20 nm, the volume of the secondary pores amounting to 5-70% of the total pore volume.
摘要翻译:1.总SiO 2 / Al 2 O 3摩尔比的AL沸石至少等于8,钾含量低于2.9重量%,钠含量低于0.5重量%,结晶参数载体a和载体c分别低于1.836 nm和0.754nm,在77K下,在P / Ps分压为0.19,高于11重量%,在P / Ps分压为0.25的30℃下的苯吸附容量为77K, 所述L沸石具有半径范围为0.8nm至20nm的二次孔格(中孔)晶格,二次孔的体积为总孔体积的5-70%。
摘要:
Disclosed is a method for providing improved hydrogenation activity by pretreating a catalyst in a three-step manner before selective hydrogenation of unsaturated hydrocarbons in an aromatic fraction in the presence of an oxide-type bimetallic (nickel-molybdenum) supported catalyst. The pretreatment of the catalyst comprises sulfidation, oxidation at a temperature above 250°C and reduction.