Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Ammonia | HCID 222 | — |
| Reactant | Oxygen | HCID 977 | — |
| Reactant | 2-Methylbenzonitrile | HCID 10721 | — |
| Product | Phthalonitrile | HCID 7042 | — |
Reaction Steps
750 ml of a catalyst having a particle size of from 0.05 to 0.3 mm are introduced into a quartz reactor which has a diameter of 60 mm and a length of 1000 mm and is provided with an external heater and a quartz frit for uniformly distributing the reaction gas. The catalyst is composed of 5.0% by weight of V2O5, 5.9% by weight of Sb2O3 0.24% by weight of K2O, 0.56% by weight of BaO and 88.3% by weight of γ-Al2O3. The reactor is heated to 470° C. and a gas mixture consisting of 3.25% by volume of o-xylene, 13% by volume of oxygen and 83.75% by volume of ammonia is passed through. The hot reaction gases are cooled to 70° C. with ammonia water in two wash towers arranged in series. An aqueous suspension of crystals is formed, from which the o-phthalodinitrile is isolated by filtration. 2,687 parts of o-xylene give 2,581 parts of o-phthalodinitrile and 195 parts of o-tolunitrile. By reacting the 195 parts of o-tolunitrile again with ammonia and oxygen, a further 170 parts of o-phthalodinitrile are obtained. The total yield of o-phthalodinitrile is 84.8 mol %, based on converted o-xylene.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04814479 |
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| Source dataset | uspto-grants-1989_03 |
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| ORD ID | ord-541941d70fb243ae8055ed887a7d3cac |
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| Source note | uspto-grants-1989_03 |
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