摘要:
Catalysts for ammonia synthesis based on ruthenium, directly supported over graphite having BET specific surface area in excess of 10 m2/g, preferably in excess of 100 m2/g and more preferably in excess of 280 m2/g, the graphite being characterised by X-ray diffraction pattern containing the diffraction lines characteristic of the crystalline graphite only, with exclusion of relevant bands due to amorphous carbon, to which catalysts barium, caesium and potassium are added as promoters. The graphitic supports allow to avoid the known pre-treatments and post-treatments needed in the case of supports obtained by partial graphitisation of active carbons and during use they are affected negligibly by the methanation shown by the supports obtained from active carbons. Furthermore, the catalysts of the present invention are characterised by a very high activity, even with ruthenium loadings well below the known loading.
摘要:
The present invention relates to a catalyst for the dehydrogenation of ethylbenzene to styrene and to a process for the preparation thereof. The catalyst contains iron oxide, potassium oxide and calcium oxide, preferably also cerium oxide and molybdenum oxide, and is characterised by a magnesium content (expressed as MegO) lower than 0.001 %.
摘要:
Linear mono-olefines are prepared by contacting linear paraffins having from 6 to 16 carbon atoms per molecule with a porous dehydrogenation catalyst comprising beryllium oxide as a support and from 0.01 to 10% by weight of noble metal as active component.
摘要:
Catalysts for ammonia synthesis based on ruthenium, directly supported over graphite having BET specific surface area in excess of 10 m2/g, preferably in excess of 100 m2/g and more preferably in excess of 280 m2/g, the graphite being characterised by X-ray diffraction pattern containing the diffraction lines characteristic of the crystalline graphite only, with exclusion of relevant bands due to amorphous carbon, to which catalysts barium, caesium and potassium are added as promoters. The graphitic supports allow to avoid the known pre-treatments and post-treatments needed in the case of supports obtained by partial graphitisation of active carbons and during use they are affected negligibly by the methanation shown by the supports obtained from active carbons. Furthermore, the catalysts of the present invention are characterised by a very high activity, even with ruthenium loadings well below the known loading.
摘要:
Process for the preparation of catalysts suitable for the production of linear olefins by dimerization or co-dimerization of linear olefins having small numbers of carbon atoms, characterized by depositing one or more metals chosen from among those belonging to group VIII of the periodic system of elements on a natural or synthetic crystalline zeolite by ion exchange to a quantity of deposited metal of from 0.1 to 50% by weight with respect to the zeolite itself, by bringing the resulting product into contact with an organic or inorganic base in the liquid or gaseous form at a temperature in the range from -35 to 250.degree. C for a time of at least 30 minutes, and by eliminating the excess of the base and heat-treating at temperatures in the range from 50 to 450.degree. for at least 30 minutes, and a process for the preparation of linear olefins having from 6 to 24 carbon atoms in the molecule, characterized by the introduction of one or more linear olefins having from 3 to 12 carbon atoms in the molecule to the catalysts obtained, and by operating at temperatures of from 130 to 260.degree. C and at pressures of from 2 to 70 atmospheres.