Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Malic Acid | HCID 525 | — |
| Reactant | Succinic Acid | HCID 1110 | — |
| Catalyst | Dioxogermane | HCID 14796 | — |
| Product | Malic Acid | HCID 525 | — |
| Product | Succinic Acid | HCID 1110 | — |
| Product | 1,4-Butanediol | HCID 8064 | — |
Reaction Steps
As a result of production of a polyester in the same manner as in Example 1-A except that 100.3 g (0.85 mol) of succinic acid, 80.4 g (0.89 mol) of 1,4-butanediol, 0.37 g (2.8×10−3 mol) of malic acid, and 1.34 g (2.8×10−3 mol, 0.64 mol % relative to succinic acid as a whole) of 27.7% by weight of an aqueous malic acid solution in which germanium dioxide as a catalyst had been dissolved in an amount of 4% by weight beforehand were added at the feed of the starting materials in Example 1-A, a polyester having a reduced viscosity (ηsp/C) of 2.8 was obtained. The polymerization reaction time under reduced pressure of 0.07×103 Pa was 1.5 hours. The amount of the terminal carboxyl group was 22 eq/ton, the amount of the terminal OH group was 60 eq/ton, and the contents of a carbonate bond, a urethane bond, an aliphatic monooxymonocarboxylic acid unit, and a phosphorus atom derived from a phosphorus-containing compound were each 0.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|
| Patent number | US07317069B2 |
|---|
| Source dataset | uspto-grants-2008_01 |
|---|
| ORD ID | ord-d768d99a52834af88b90072b3b41a849 |
|---|
| Source note | uspto-grants-2008_01 |
|---|