Catalyst for fluidized bed ammoxidation reaction, and method for producing acrylonitrile
US-2018318803-A1 · Nov 8, 2018 · US
US9358528B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9358528-B2 |
| Application number | US-201514935514-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 9, 2015 |
| Priority date | May 29, 2014 |
| Publication date | Jun 7, 2016 |
| Grant date | Jun 7, 2016 |
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A catalytic composition useful for the conversion of an olefin selected from the group consisting of propylene, isobutylene or mixtures thereof, to acrylonitrile, methacrylonitrile, and mixtures thereof. The catalytic composition comprises a complex of metal oxides comprising bismuth, molybdenum, iron, cerium and other promoters, wherein the ratio of bismuth to cerium ratio in the composition is greater than or equal to 0.45 and less than or equal to 1.5.
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The claimed invention is: 1. A process for the conversion of an olefin selected from the group consisting of propylene, isobutylene or mixtures thereof, to acrylonitrile, methacrylonitrile, and mixtures thereof, respectively, by reacting in the vapor phase at an elevated temperature and pressure said olefin with a molecular oxygen containing gas and ammonia in the presence of a catalyst wherein the relative ratios of the listed elements in said catalyst are represented by the following formula: Mo m Bi a Fe b A c D d E e F f G g Ce h O x 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 nickel, cobalt, manganese, zinc, magnesium, calcium, strontium, cadmium and barium; E is at least one element selected from the group consisting of chromium, tungsten, boron, aluminum, 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, aluminum, 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 a, b, c, d, e, f, g, h and x are, respectively, the atomic ratios of bismuth (Bi), iron (Fe), A, D, E, F, G, cerium (Ce) and oxygen (O), relative to “m” atoms of molybdenum (Mo), wherein a is from 0.05 to 7, b is from 0.1 to 7, c is from 0.01 to 5, d is from 0.1 to 12, e is from 0 to 5, f is from 0 to 5, g is from 0 to 0.2, h is from 0.01 to 5, m is from 10 to 15, and x is the number of oxygen atoms required to satisfy the valence requirements of the other component elements present; wherein 0.5≦a/h≦1.5 and 0.3≦(a+h)/d≦1 and 0.8≦a/h≦5. 2. A process for the conversion of an olefin selected from the group consisting of propylene, isobutylene or mixtures thereof, to acrolein/acrylic acid, methacrolein/methacrylic acid, and mixtures thereof, respectively, by reacting in the vapor phase at an elevated temperature and pressure said olefin with a molecular oxygen containing gas in the presence of a catalyst wherein the relative ratios of the listed elements in said catalyst are represented by the following formula: Mo m Bi a Fe b A c D d E e F f G g Ce h O x 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 nickel, cobalt, manganese, zinc, magnesium, calcium, strontium, cadmium and barium; E is at least one element selected from the group consisting of chromium, tungsten, boron, aluminum, 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, aluminum, 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 a, b, c, d, e, f, g, h and x are, respectively, the atomic ratios of bismuth (Bi), iron (Fe), A, D, E, F, G, cerium (Ce) and oxygen (O), relative to “m” atoms of molybdenum (Mo), wherein a is from 0.05 to 7, b is from 0.1 to 7, c is from 0.01 to 5, d is from 0.1 to 12, e is from 0 to 5, f is from 0 to 5, g is from 0 to 0.2, h is from 0.01 to 5, m is from 10 to 15, and x is the number of oxygen atoms required to satisfy the valence requirements of the other component elements present; wherein 0.5≦a/h≦1.5 and 0.3≦(a+h)/d≦1 and 0.8≦a/h≦5. 3. The process of claim 1 , wherein 0.65≦a/h<1.5. 4. The process of claim 1 , wherein 0.7≦a/h<1.5. 5. The process of claim 1 , wherein 0.8≦a/h<1.5. 6. The process of claim 1 , wherein 0.90≦a/h<1.5. 7. The process of claim 1 , wherein 0.90≦a/h<1.2. 8. The process of claim 2 , wherein 0.65≦a/h<1.5. 9. The process of claim 2 , wherein 0.7≦a/h<1.5. 10. The process of claim 2 , wherein 0.8≦a/h<1.5. 11. The process of claim 2 , wherein 0.90≦a/h<1.5. 12. The process of claim 2 , wherein 0.90≦a/h≦1.2.
Mixed oxides other than spinels, e.g. perovskite · CPC title
containing in addition other metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 · CPC title
Constitutive chemical elements of heterogeneous catalysts · CPC title
with chromium, molybdenum or tungsten · CPC title
Propene · CPC title
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