Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Propionic Acid | HCID 1032 | — |
| Reactant | Methyl Methacrylate | HCID 6658 | — |
| Reactant | Dimethyl Ether | HCID 8254 | — |
| Reactant | Indole-3-Butyric Acid | HCID 8617 | — |
| Catalyst | Vanadium | HCID 23990 | — |
| Solvent | Acetic Acid | HCID 176 | — |
| Solvent | Ethyl ketone | HCID 7288 | — |
| Solvent | 1,2-Dimethoxyethane | HCID 8071 | — |
| Product | Acetaldehyde | HCID 177 | — |
| Product | Ethyl Propionate | HCID 7749 | — |
Reaction Steps
Experiments were conducted to evaluate catalyst compositions containing vanadium, which is known to be effective for oxidative dehydrogenation of IBA to MAA in the synthesis of methyl methacrylate from propionic acid and dimethyl ether. A sample of the catalyst chunks from Example 32 was crushed and sieved, and 1.46 grams (5.0 cm3) loaded into a reactor tube. The reactor effluent was analyzed online by gas chromatography. Results are given in Table 8. In Example 33, the temperature was set at 300° C. and GHSV was 920 hr−1. The 1% V2O5/SiO2 catalyst gave 30% conversion of PA and 23% conversion of DME. The catalyst gave a high selectivity to acetaldehyde, ethyl propionate, diethylketone and acetic acid byproducts at 300° C. In Example 34, the catalyst temperature was increased to 330° C. The 1% V2O5/SiO2 catalyst gave 20% PA conversion and maintained a substantial byproduct selectivity. The oxidative dehydrogenation activity of this catalyst is seen in its selectivity to acrylic acid of 1.3% at 330° C.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US06329549B1 |
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| Source dataset | uspto-grants-2001_12 |
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| ORD ID | ord-2750a49c722441208b03d5d87bfeef87 |
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| Source note | uspto-grants-2001_12 |
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