Beteiligte Stoffe
| Rolle | Name | HCID | Einwaage |
|---|
| Edukt | Lactic Acid | HCID 612 | — |
| Edukt | Itaconic acid | HCID 811 | — |
| Edukt | Pentaerythritol | HCID 8285 | — |
| Edukt | Stannous cation | HCID 104883 | — |
| Edukt | L-Lactic Acid | HCID 107689 | — |
| Produkt | Lactic acid itaconic acid | HCID 86597549 | — |
Reaktionsschritte
Into a 2 litre Rotavapor equipment used as the reactor was added 437.5 g L-lactic acid (88% water solution corresponding to 89 mole-%), 47.9 g itaconic acid (9 mol-%), 14.5 g pentaerythritol (2 mole-%) and 0.19 g tin(II) octoate. Dry nitrogen was led into the reactor and 500 mbar absolute pressure was established. The reactor vessel was partly immersed in an oil bath with a temperature of 90° C. The temperature of the oil bath was increased at a rate of 30° C./h to 120° C., and the reaction mixture was mixed by starting the rotation at a speed of 100 rpm. The temperature of the oil bath was evenly increased by 15° C./h until 180° C., where it was kept until the end of the polymerisation. The pressure was decreased every hour by the following steps: 500 (start)-500-450-400-350-290-190-140-90-60-50-40-30 mbar, at which pressure it was kept to the end of the polymerisation. Bubbling of nitrogen was continued throughout the polymerisation and the formed water was collected as it evolved. Total polymerisation time was 24 hours. During the polymerisation no lactide was formed on the reactor walls, condenser or receiver, although it typically forms in a condensation polymerisation of lactic acid.
Herkunft & Nachweise
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patentnummer | US07256250B2 |
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| Quelldatensatz | uspto-grants-2007_08 |
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| ORD ID | ord-0277ee7bc7eb45f5b6ed8ac6f6b00e24 |
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| Quellennotiz | uspto-grants-2007_08 |
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