Method for carrying out a heterogeneously catalysed reaction
US-2019099731-A1 · Apr 4, 2019 · US
US10865179B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10865179-B2 |
| Application number | US-201816648286-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 12, 2018 |
| Priority date | Sep 19, 2017 |
| Publication date | Dec 15, 2020 |
| Grant date | Dec 15, 2020 |
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A method for preparing methyl methacrylate from methacrolein and methanol. The method comprises contacting a mixture comprising methacrolein, methanol and oxygen with a heterogeneous catalyst comprising a support and a noble metal, wherein oxygen concentration at a reactor outlet is from 1 to 7.5 mol % and wherein pH at a reactor outlet is no greater than 7.5.
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The invention claimed is: 1. A method for preparing methyl methacrylate from methacrolein and methanol; said method comprising contacting in a reactor a mixture comprising methacrolein, methanol and oxygen with a heterogeneous catalyst comprising a support and a noble metal, wherein the noble metal comprises gold, wherein the catalyst has an average diameter of at least 300 microns, wherein oxygen concentration at a reactor outlet is from 1 to 7.5 mol % and wherein pH at a reactor outlet is no greater than 7.5. 2. The method of claim 1 in which the reactor is an axial flow reactor having a liquid-phase superficial velocity of 0.5 to 20 mm/s and an average partial pressure of oxygen greater than 50 kPa. 3. The method of claim 2 in which the catalyst has an average diameter from 400 microns to 10 mm. 4. The method of claim 3 in which the catalyst is contained in a catalyst bed which is at a temperature from 40 to 120° C. 5. The method of claim 4 in which pH in the reactor is from 3 to 7.2. 6. The method of claim 5 in which oxygen concentration at a reactor outlet is from 1.6 to 6 mol %. 7. The method of claim 1 in which the support is selected from the group consisting of γ-, δ-, or θ-alumina, silica, magnesia, titania, zirconia, hafnia, vanadia, niobium oxide, tantalum oxide, ceria, yttria, lanthanum oxide and combinations thereof. 8. The method of claim 7 in which methanol and methacrolein are fed to a reactor containing the catalyst bed in a molar ratio from 1:1 to 10:1, respectively. 9. The method of claim 8 in which at least 90 wt % of the noble metal is in the outer 70% of catalyst volume.
Silver or gold · CPC title
Egg shell like · CPC title
with rare earths or actinides · CPC title
characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title
by oxidation of primary alcohols · CPC title
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