Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Propylene Oxide | HCID 6378 | — |
| Reactant | Tetrahydrofuran | HCID 8028 | — |
| Catalyst | HCID 131716952 | HCID 131716952 | — |
| Product | HCID 86744912 | HCID 86744912 | — |
Reaction Steps
The one-liter reactor previously described was charged with a 480 molecular weight poly(propylene oxide) triol (78.9 g), zinc hexacyanocobaltate/zinc chloride/glyme/water catalyst (0.575 g, 980 ppm), and tetrahydrofuran (60 mL). The load-cell reservoir was charged with propylene oxide (341 g). The reactor was purged several times with nitrogen, then pressurized to about 5 psi. The reactor contents were stirred and heated to 90° C. over a 1.5 hour period. An initial charge of 37 g of PO was added to the reactor. A pressure drop was observed about 1 hour after addition of the initial charge, indicating that initiation of the catalyst had occurred. The remaining PO was added over about a 10-hour period. The product was heated for an additional 8 hours at 90° C. following addition of the propylene oxide. ε-Caprolactone (165 g was charged to the load-cell reservoir, and was added to the reactor at 90° C. at a rate of about 40 g/hour. The product was heated for an additional 8 hours at 90° C. following addition of the ε-caprolactone. The product was cooled, drained from the reactor, and filtered through diatomaceous earth. Tetrahydrofuran was removed using a rotary evaporator. Residual ε-caprolactone was removed by passing the polymer product through a wiped-film evaporator under vacuum at 150° C. The ε-caprolactone-capped poly(PO) triol product had a hydroxyl number of 60.5 mg KOH/g and a GPC number average molecular weight of 2410.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|
| Patent number | US05032671 |
|---|
| Source dataset | uspto-grants-1991_07 |
|---|
| ORD ID | ord-3cc43190cb684abebb20d0cc8ff1113d |
|---|
| Source note | uspto-grants-1991_07 |
|---|