IMPROVED SELECTIVE AMMOXIDATION CATALYSTS Russian patent published in 2018 - IPC B01J23/887 C07C253/26 B01J35/00 B01J37/03 C07C255/08 

Abstract RU 2668554 C2

FIELD: chemical or physical processes.

SUBSTANCE: present invention relates to a catalyst composition for use in the ammoxidation of an unsaturated hydrocarbon to a corresponding unsaturated nitrile containing a complex of metal oxides, the relative ratios of the listed elements in said catalyst being represented by the following formula: Mom Bia Feb Ac Dd Ee Ff Gg Ceh Nii Coj Mnk Mgl 0#, wherein A is at least one element selected from the group consisting of sodium, potassium, rubidium and cesium; and D is at least one element selected from the group consisting of zinc, calcium, strontium, cadmium and barium; E is at least one element selected from the group consisting of chromium, tungsten, boron, aluminium, gallium, indium, phosphorus, arsenic, antimony, vanadium and tellurium; F is at least one element selected from the group consisting of lanthanum, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, scandium, yttrium, titanium, zirconium, hafnium, niobium, tantalum, aluminium, gallium, indium, thallium, silicon, germanium and less than about 10 ppm lead; G is at least one element selected from the group consisting of silver, gold, ruthenium, rhodium, palladium, osmium, iridium, platinum and mercury; and where a is 0.05 to 7, b is 0.1 to 7, c is 0.01 to 5, d is 0 or 0.1 to 12, e is 0 to 5, f is 0 to 5, g is 0 to 0.2, h is 0.01 to 5, i is 0.1 to 12, j is 0 or 0.1 to 12, k is 0 or 0.1 to 12, l is 0 or 0.1 to 12, m is 10 to 15, # is the number of oxygen atoms required to satisfy the valence requirements of the other constituent elements present; where z = d + i + j + k + 1; and wherein 0.45≤a / h <1.5, and 0.3≤(a + h) / z, and 0.8≤h / b≤5; with 0.2 <i / (i + j + k + l). Versions of the above catalyst composition are also provided.

EFFECT: technical result is improving the performance of the catalyst while achieving high degree of conversion of propylene and/or isobutylene to nitriles.

18 cl, 2 dwg, 4 tbl, 23 ex

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RU 2 668 554 C2

Authors

Brazdil James F.

Toft Mark A.

Besecker Charles J.

Seely Michael J.

Dates

2018-10-02Published

2014-05-29Filed