Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Ethylene | HCID 6325 | — |
| Reactant | 2-Methyl-2-butene | HCID 10553 | — |
| Reactant | Pent-2-ene | HCID 12585 | — |
| Product | 1-Butene | HCID 7844 | — |
| Product | Propylene | HCID 8252 | — |
| Product | Isobutylene | HCID 8255 | — |
Reaction Steps
In a first reactor R1, 1-butene, 2-butene and isobutene are reacted in the presence of the metathesis catalyst of the present invention to give propene, 2-pentene and 2-methyl-2-butene. For this purpose, a raffinate I stream is fed to the reactor. The reactor is followed by a distillation column D1 at the top of which propene and ethene formed as by-product are removed. Unreacted raffinate I is taken off at the middle offtake. Some of it may: also be returned to the reactor R1 (not shown in FIG. 1). 2-Pentene, 2-methyl-2-butene and 3-hexene formed as by-product as well as high boilers are taken off at the bottom of D1. The bottoms are then fed together with added ethene to a reactor R2 which again contains a metathesis catalyst of the present invention. In this reactor R2, the reaction of 2-pentene and 2-methyl-2-butene with ethene to give 1-butene, isobutene and propene takes place. The reaction product from reactor R2 is fed to a distillation column D2 at the top of which propene and unreacted ethene are taken off. 1-Butene and isobutene formed are taken off at the middle offtake and at least sore is preferably returned to the reactor R1. Unreacted 2-pentene, 2-methyl-2-butene and also, as by-products, 3-hexene and high boilers are obtained at the bottom of D2. These are preferably returned to the reactor R2. The mixtures of propene and by-product ethene taken off at the top of D1 and D2 are fractionated in a further distillation column D3. Ethene is obtained at the top of D3 and this is preferably returned to the reactor R2 (not shown in FIG. 1), or discharged as co-cracker feed. The propene obtained at the bottom of D3 is the desired reaction product of the process of the present invention. D1 and D2 are designed such that a low-boiling phase, in particular a C2/3 phase comprising ethene and propene, is taken off at the top of the column. C4 streams, in particular butenes and butanes, are taken off as intermediate-boiling phase. As bottoms, C≧5-hydrocarbons are discharged.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US06646172B1 |
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| Source dataset | uspto-grants-2003_11 |
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| ORD ID | ord-4c2265e5cf5147ebabada4452e95c29d |
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| Source note | uspto-grants-2003_11 |
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