Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Ethylene | HCID 6325 | — |
| Reactant | Methyl Acrylate | HCID 7294 | — |
| Reactant | Maleic Anhydride | HCID 7923 | — |
| Reactant | Bis-sec-butyl peroxydicarbonate | HCID 89245 | — |
| Solvent | Methanol | HCID 887 | — |
| Product | HCID 86739097 | HCID 86739097 | — |
Reaction Steps
6.34 kg/h of ethylene plus 1.06 kg/h of liquid monomers containing by weight 97.2% methyl acrylate (MA), 2.7% maleic anhydride and 0.1% butylated hydroxy toluene (BHT) as well as 0.2-0.3 kg/h of methanol as telogen were fed continuously to a 720 ml adiabatic continuous stirred tank reactor. Reaction was initiated and maintained by the addition of di(sec-butyl)peroxydicarbonate (20% PDC/80% t-butylbenzene). Reaction conditions: Reactor temperature=160° C., Feed temp.=25° C. Pressure=186 MPa, Total monomer conversion=15±1%. Comonomers were introduced into the hot reactor at appropriate reactor pressures to avoid phase separation. Approximately 6.5 kg of E/MA/maleic anhydride polymer was made with a measured composition of 46.5/51/2.5 wt % and a melt flow rate (2160 grams weight, 190° C.) of 7-9.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04412043 |
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| Source dataset | uspto-grants-1983_10 |
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| ORD ID | ord-c155198ea0c24eafbff1fd330cfb4316 |
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| Source note | uspto-grants-1983_10 |
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