Beteiligte Stoffe
| Rolle | Name | HCID | Einwaage |
|---|
| Edukt | 1,1-Dichloropropane | HCID 6573 | — |
| Edukt | Fenteracol | HCID 16462 | — |
| Edukt | Cornforth reagent | HCID 2724130 | — |
| Produkt | 1,1,2-Trichloropropane | HCID 11733 | — |
| Produkt | 1,1,1-Trichloropropane | HCID 24622 | — |
Reaktionsschritte
In the present process, dichloropropane is converted to a chlorinated alkene, e.g., TCPE, using a series of consecutive chlorination and dehydrochlorination steps. In one exemplary embodiment, PDC is fed to a liquid phase chlorination reactor, e.g., such as a batch or continuous stirred tank autoclave reactor with an internal cooling coil. A shell and multitube exchanger operating in plug flow, followed by vapor liquid disengagement tank or vessel can also be used. Suitable reaction conditions include, e.g., a temperature of from 30° C. to 150° C., a pressure of from 100 kPa to 2000 kPa. The reaction is carried out in the presence of one or more regioselective catalysts that provide a regioselectivity to, e.g., 1,1,2-trichloropropane of at least 5:1 over other trichloropropane isomers.
Herkunft & Nachweise
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patentnummer | US09334205B2 |
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| Quelldatensatz | uspto-grants-2016_05 |
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| ORD ID | ord-14b2e5b709964b72bcc0c865ee0479e2 |
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| Quellennotiz | uspto-grants-2016_05 |
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