摘要:
An improved dehydrogenation process that comprises the dehydrogenation of dehydrogenatable hydrocarbons by the utilization of an iron oxide based dehydrogenation catalyst composition having a low titanium content under low steam-to-oil process conditions.
摘要:
A catalyst which is based upon an iron oxide and a compound of a lanthanide, of which iron oxide at least a portion is made by a process which involves heat decomposition of an iron halide, the lanthanide being in a quantity in the range of from 0.07 to 0.15 mole per mole iron oxide present in the catalyst, calculated as Fe2O3; a process for the preparation of the catalyst; a process for the dehydrogenation of an alkylaromatic compound which process involves contacting a feed containing the alkylaromatic compound with the catalyst; and a method of using an alkenylaromatic compound for making polymers or copolymers, in which method the alkenylaromatic compound has been prepared by the dehydrogenation process.
摘要:
Catalysts for dehydrogenating ethylbenzene to styrene which comprise iron oxide, oxides of alkaline and alkaline-earth metals, oxides of the lanthanide series, oxides of metals of the sixth group, prepared from a paste of iron oxide impregnated with an aqueous solution of a cerium salt, treated with aqueous KOH and calcined, after drying, to preform potassium ferrate, to which the other components or precursors of the catalyst are then added.
摘要:
A method for preparing methacrolein comprises subjecting isobutylene or a tertiary butanol to gas phase catalytic oxidation with molecular oxygen in the presence of a catalyst which comprises a mixture of a composition (I) represented by the following general formula I:
Mo a Bi b Fe c X d Y e Z f O g I
wherein X represents at least one element selected from the group consisting of Ni and Co; Y represents at least one element selected from the group consisting of K, Rb, Cs and Tl; Z represents at least one element selected from the group consisting of those belonging to Group 2, 3, 4, 5, 6, 7, 11, 12, 13, 14, 15 and 16 of Periodic Table in accordance with IUPAC nomenclature (1989); and a, b, c, d, e, f and g each represents an atomic ratio of each corresponding element, when a is assumed to be 12, b is 0.1 to 10, c is 0 to 20, d is 0 to 20, e is 0 to 2, f is 0 to 4 and g is the number of oxygen atoms which is required for satisfying the valencies of the foregoing elements and a composition (II) represented by the following general formula II:
Ln h MO i O j II
wherein Ln represents at least one element selected from the group consisting of rare earth elements; h, i and j each represents an atomic ratio of each corresponding element, when i is assumed to be 1, h is 0.2 to 1.5 and j is the number of oxygen atoms which is required for satisfying the valencies of the foregoing elements. According to this method, the end product is obtained with a high yield and selectivity.
摘要翻译:一种制备甲基丙烯醛的方法包括在催化剂存在下使用异丁烯或叔丁醇进行气相催化氧化,所述催化剂包含由以下通式I表示的组合物(I)的混合物:Moa Bib Fec X d Y e Zf Og I其中X表示选自Ni和Co中的至少一种元素; Y表示选自K,Rb,Cs和T1中的至少一种元素; Z表示选自根据IUPAC命名(1989)的属于元素周期表的第2,3,4,5,6,7,11,12,13,14,15和16族的那些元素中的至少一种元素。 ; a,b,c,d,e,f和g各自表示各对应元素的原子比,当a为12时,b为0.1〜10,c为0〜20,d为0〜20, e为0〜2,f为0〜4,g为满足上述成分的化合价所需的氧原子数,以及下述通式II表示的组成(II):Ln h MOi O j II 其中Ln表示选自由稀土元素组成的组中的至少一种元素; h,i和j各自表示每个相应元素的原子比,当i假设为1时,h为0.2至1.5,j为满足上述元素的价态所需的氧原子数。 根据该方法,以高产率和选择性获得最终产物。
摘要:
Olefins such as propylene and isobutylene are converted to the corresponding unsaturated nitriles, acrylonitrile, and methacrylonitrile, respectively, by reacting a mixture of the olefin, ammonia, and molecular oxygen-containing gas in the presence of a catalyst containing the oxides of bismuth, molybdenum, iron, nickel and magnesium, at least one element selected from the group comprising potassium and cesium, and optionally one element selected from the group comprising cobalt, phosphorus, manganese, tellurium, sodium, cerium, chromium, antimony and tungsten wherein the sum of cesium and potassium is at least 0.1 to 0.4.
摘要:
A process and catalyst have been developed for hydrotreating halogen containing olefinic feedstock including resins. The process and catalyst dehalogenates both saturated and unsaturated feedstock. The catalyst is not deactivated by prolonged exposure to a halogen. The composition of the catalyst includes oxides from Group VIIIA, tungsten oxide or molybdenum oxide and a basic promoter oxide from Group IA, Group IIA, Lanthanides and Actinides.
摘要:
Ammoxidation of propane or isobutane with NH₃ and 0₂ using (1) a mole ratio of paraffin:NH₃ in the range from 2 to 16 and a mole ratio of paraffin:O₂ in the range 1 to 10 and (2) a mixture of particulate catalyst compositions, the first being especially effective to promote formation of an unsaturated nitrile and an olefin from the paraffin, and the second catalyst composition being especially effective to promote the conversion of the olefin to the unsaturated nitrile. Catalytic compositions useful in the process are disclosed.
摘要:
Ammoxidation of propane or isobutane with NH₃ and 0₂ using (1) a mole ratio of paraffin:NH₃ in the range from 2 to 16 and a mole ratio of paraffin:O₂ in the range 1 to 10 and (2) a mixture of particulate catalyst compositions, the first being especially effective to promote formation of an unsaturated nitrile and an olefin from the paraffin, and the second catalyst composition being especially effective to promote the conversion of the olefin to the unsaturated nitrile. Catalytic compositions useful in the process are disclosed.