US4151216A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Catalytic cracking of by-product polypropylene
Assignee: Himont Inc
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Filing: 1977-10-25
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Granted: 1979-04-24
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Expires: 1997-10-25
Abstract
Abstract By-product polypropylene may be converted by catalytic cracking into a fuel oil product having the viscosity necessary to permit it to be pumped and stored at the temperatures normally used for fuel oils. The cracking process is carried out at a temperature of, for example, 450° C. in a tubular reactor using a silica-on-alumina catalyst.
Inventors
- 👤 Vernon C. Smith
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 11:02
CPC Classifications
C; C10; C10G; C10G1/00
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
132 words
A process for converting by-product polypropylene to a fuel oil product having the viscosity necessary to permit it to be readily pumped and stored at the temperatures normally used for fuel oils, said process comprising the steps of heating the by-product polypropylene to a temperature in the range of from about 150° to about 350° C. to provide a molten feed material and then contacting said feed material with a silica-on-alumina catalyst containing from about 5 to about 20 percent by weight of silica in a tubular reactor at a temperature in the range of from about 425° to about 475° C. and for space times in the range of from about five to about 15 grams of the catalyst per gram of said by-product polypropylene fed to the reactor per minute.
Claim 2
Dependent Claim
132 words
A process for converting by-product polypropylene to a fuel oil product having the viscosity necessary to permit it to be readily pumped and stored at the temperatures normally used for fuel oils, said process comprising the steps of heating the by-product polypropylene to a temperature in the range of from about 150° to about 350° C. to provide a molten feed material and then contacting said feed material with a silica-on-alumina catalyst containing from about 5 to about 20 percent by weight of silica in a tubular reactor at a temperature in the range of from about 425° to about 475° C. and for space times in the range of from about five to about 15 grams of the catalyst per gram of said by-product polypropylene fed to the reactor per minute.
Claim 3
Dependent Claim
36 words
The process of claim 1 wherein the catalyst has a BET surface area of from about 10 to about 400 square meters per gram and a pore diameter of from about 35 to about 500 A.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-04-23 | 1982-10-23 | 1983-04-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-04-23 | 1986-10-23 | 1987-04-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-04-23 | 1990-10-23 | 1991-04-24 | $7700.00 | Window Closed / Lapsed |