Participants
| Role | Name | HCID | Charge |
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| Reactant | Maleic Acid | HCID 444266 | — |
| Solvent | O-Xylene | HCID 7237 | — |
| Product | Phthalic Anhydride | HCID 6811 | — |
Reaction Steps
When conducting the concentration of aqueous solutions of maleic acid (maleic acid content: 28 wt%), which were obtained by absorbing in water gaseous reaction products, formed by catalytic oxidation of benzene or a spent gas from the production of phthalic anhydride formed by catalytic oxidation of o-xylene, at charge rates of 3.3 m3 /hr in a falling film evaporator at a temperature of 70° C. and further conducting the concentration and dehydration of the preconcentrated aqueous solutions in a rotary film evaporator at a temperature of 140°-150° C., 35 wt% aqueous solution of hydrogen peroxide was continuously added at a rate of 28 liter/hr to the aqueous solutions at ambient temperature. In these cases, even after seven days continuous operations, formation of resinous or gelatinous materials was not observed at all during the concentration and dehydration operations, and formation of only a trace amount of fumaric acid was observed.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04658042 |
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| Source dataset | uspto-grants-1987_04 |
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| ORD ID | ord-f4346bd4109d433f812daa63bad23570 |
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| Source note | uspto-grants-1987_04 |
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