Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Hexane | HCID 8058 | — |
| Reactant | Nickel octoate cyclohexene triethyl aluminum | HCID 131710492 | — |
| Reactant | HCID 178418361 | HCID 178418361 | — |
| Catalyst | Nickel | HCID 935 | — |
| Product | 2,3-Dibutyl-4-methylphenol | HCID 13783542 | — |
Reaction Conditions
| Temperature | 130 fahrenheit |
|---|
Reaction Steps
Five gallons of the block copolymer cement product from Example VI containing about 2500 gms. of polymer is charged to a hydrogenation reactor together with an additional 40 lbs. of dry hexane. The reactor is flushed 6 times by pressuring to 50 psig with hydrogen and then releasing the pressure to about 5 psig. Then the hydrogenation catalyst is added which comprises 25 millimoles of Ni in nickel octoate-cyclohexene-triethyl aluminum in proportions of 1/1/3 respectively. The temperature is raised to 130°F and hydrogen introduced to a pressure of 150 psig. Periodically the system is repressured to 150 psig and samples are removed three times at several hours intervals. The temperature is maintained at 130°-160°F over a period of about 7 hours after which the reaction mixture is cooled to 120°F and vented several times. The product is dropped into a 55 gallon drum containing methanol and a small amount of antioxidant (dibutyl-p-cresol) to provide about 0.5 gm. of A.O. per 100 gms. of polymer. The product is filtered and rinsed several times with hexane. The copolymer is found to be about 100% hydrogenated and to have a glass transition temperature of -59°C and a melting point of 97°C. This product shows excellent impact strength and is used in the tests of Example VIII.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US03985826 |
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| Source dataset | uspto-grants-1976_10 |
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| ORD ID | ord-e75a29b8a95e4e6e8f642dc0ec5d11cb |
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| Source note | uspto-grants-1976_10 |
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