Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Itaconic acid | HCID 811 | — |
| Reactant | Pentaerythritol | HCID 8285 | — |
| Reactant | Stannous cation | HCID 104883 | — |
| Reactant | L-Lactic Acid | HCID 107689 | — |
| Solvent | Water | HCID 962 | — |
| Product | Lactic acid itaconic acid | HCID 86597549 | — |
Reaction Steps
Into a 2 liter Rotavapor equipment, used as the reactor, 437.5 g of L-lactic acid was added (88% water solution corresponding to 89 mole-%), 47.9 g of itaconic acid (9 mole-%), 14.5 g of pentaerythritol (2 mole-%) and 0.19 g of tin(II) octoate. Dry nitrogen was led into the reactor and a 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.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|
| Patent number | US08563664B2 |
|---|
| Source dataset | uspto-grants-2013_10 |
|---|
| ORD ID | ord-18c60520748747cdb4b8e368fa21c1d6 |
|---|
| Source note | uspto-grants-2013_10 |
|---|