Patent US2802890A successfully refreshed from Google Patents.
US2802890A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Polymerization of propylene
Assignee: Sunoco Inc
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Filing: 1954-09-15
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Granted: 1957-08-13
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Expires: 1974-09-15
Abstract
No abstract record available.
Inventors
- 👤 Charles H Brooks
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 21:51
CPC Classifications
C; C07; C07C; C07C2/00; C07C2/02; C07C2/04; C07C2/06; C07C2/08; C07C2/14; C07C2/18; C07C2527/00; C07C2527/14; C07C2527/16; C07C2527/167; C07C2527/173; Y; Y10; Y10S; Y10S585/00; Y10S585/949; Y10S585/951
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
335 words
METHOD OF CONDUCTING A POLYMERIZATION OPERATION WITH A PLURALITY OF POLYMERIZATION ZONES TO PRODUCE PROPYLENE TETRAMER AND LOWER BOILING PROPYLENE POLYMERS FROM A PROPYLENE CHARGE WHICH METHOD COMPRISES THE FOLLOWING SEQUENTIAL OPERATIONAL PHASES: (1) INTRODUCING 50-95 PARTS OF THE PROPYLENE CHARGE INTO A POLYMERIZATION ZONE A ANS THEREIN REACTING THE PROPYLENE AT A TEMPERATURE MAINTAINED SUBSTANTIALLY THROUGHOUT THE ZONE WITHIN THE RANGE OF 360-390*F. IN THE PRESENCE OF A PHOSPHORIC ACID CATALYST OF RELATIVELY LOW AVERAGE ACTIVITY AND WITHOUT SEPARATE ADDITION OF WATER TO THE REACTANT, INTRODUCING THE EFFUENT FROM ZONE A, TOGETHER WITH 5-50 ADDITIONAL PARTS OF PROPYLENE CHARGE AND WITH WATER ADDED IN AMOUNT OF AT LEAST ABOUT ONE LIQUID VOLUME PER 10,000 LIQUID VOLUMES OF TOTAL HYDROCARBON INTRODUCED, INTO A POLYMERIZATION ZONE B AND THEREIN REACTING THE MIXTURE AT A TEMPERATURE MAINTAINED SUBSTANTIALLY THROUGHOUT THE ZONE WITHIN THE RANGE OF 420-475* F. IN THE PRESENCE OF A PHOSPHORIC ACID CATALYST OF RELATIVELY HIGH AVERAGE ACTIVITY TO YIELD MAINLY PROPYLENE TETRAMER; (2) STOPPING THE OPERATION OF ZONE A AND REPLACING THE CATALYST THEREIN WITH CATALYST OF RELATIVELY HIGH AVERAGE ACTIVITY WHILE CONTINUING THE OPERATION OF ZONE B BY REACTING THEREIN PROPYLENE CHARGE, CONTAINING WATER ADDED IN AMOUNT OF AT LEAST ABOUT ONE LIQUID VOLUME PER 10,000 LIQUID VOLUMES OF TOTAL HYDROCARBON INTRODUCED, AT A TEMPERATURE MAINTAINED SUBSTANTIALLY THROUGHOUT THE ZONE WITHIN THE RANGE OF 390-475*F. TO YIELD MAINLY DIMER AND TRIMER PRODUCTS, THEN OPERATING ZONERS A AND B IN PARALLEL BY REACTING IN EACH PROPYLENE CHARGE UNDER THE CONDITIONS JUST SPECIFIED FOR ZONE B TO YIELD MAINLY DIMER AND TRIMER PRODUCTS; (3) THEN, WHEN THE CATALYST ACTIVITY IN ZONE B HAS BECOME RELATIVELY LOW, CONDUCTING THE OPERATION OF ZONES A AND B SO THAT EACH OPERATES IN THE MANNER OF, AND UNDER THE CONDITIONS SPECIFIED FOR, THE OTHER ZONE IN PHASE (1); AND (4) THEREAFTER CONDUCTING THE OPERATION SUCH THAT EACH OF ZONES A AND B OPERATES IN THE MANNER OF, AND UNDER THE CONDITIONS SPECIFIED FOR, THE OTHER ZONE IN PHASE (2).
Claim 2
Dependent Claim
335 words
METHOD OF CONDUCTING A POLYMERIZATION OPERATION WITH A PLURALITY OF POLYMERIZATION ZONES TO PRODUCE PROPYLENE TETRAMER AND LOWER BOILING PROPYLENE POLYMERS FROM A PROPYLENE CHARGE WHICH METHOD COMPRISES THE FOLLOWING SEQUENTIAL OPERATIONAL PHASES: (1) INTRODUCING 50-95 PARTS OF THE PROPYLENE CHARGE INTO A POLYMERIZATION ZONE A ANS THEREIN REACTING THE PROPYLENE AT A TEMPERATURE MAINTAINED SUBSTANTIALLY THROUGHOUT THE ZONE WITHIN THE RANGE OF 360-390*F. IN THE PRESENCE OF A PHOSPHORIC ACID CATALYST OF RELATIVELY LOW AVERAGE ACTIVITY AND WITHOUT SEPARATE ADDITION OF WATER TO THE REACTANT, INTRODUCING THE EFFUENT FROM ZONE A, TOGETHER WITH 5-50 ADDITIONAL PARTS OF PROPYLENE CHARGE AND WITH WATER ADDED IN AMOUNT OF AT LEAST ABOUT ONE LIQUID VOLUME PER 10,000 LIQUID VOLUMES OF TOTAL HYDROCARBON INTRODUCED, INTO A POLYMERIZATION ZONE B AND THEREIN REACTING THE MIXTURE AT A TEMPERATURE MAINTAINED SUBSTANTIALLY THROUGHOUT THE ZONE WITHIN THE RANGE OF 420-475* F. IN THE PRESENCE OF A PHOSPHORIC ACID CATALYST OF RELATIVELY HIGH AVERAGE ACTIVITY TO YIELD MAINLY PROPYLENE TETRAMER; (2) STOPPING THE OPERATION OF ZONE A AND REPLACING THE CATALYST THEREIN WITH CATALYST OF RELATIVELY HIGH AVERAGE ACTIVITY WHILE CONTINUING THE OPERATION OF ZONE B BY REACTING THEREIN PROPYLENE CHARGE, CONTAINING WATER ADDED IN AMOUNT OF AT LEAST ABOUT ONE LIQUID VOLUME PER 10,000 LIQUID VOLUMES OF TOTAL HYDROCARBON INTRODUCED, AT A TEMPERATURE MAINTAINED SUBSTANTIALLY THROUGHOUT THE ZONE WITHIN THE RANGE OF 390-475*F. TO YIELD MAINLY DIMER AND TRIMER PRODUCTS, THEN OPERATING ZONERS A AND B IN PARALLEL BY REACTING IN EACH PROPYLENE CHARGE UNDER THE CONDITIONS JUST SPECIFIED FOR ZONE B TO YIELD MAINLY DIMER AND TRIMER PRODUCTS; (3) THEN, WHEN THE CATALYST ACTIVITY IN ZONE B HAS BECOME RELATIVELY LOW, CONDUCTING THE OPERATION OF ZONES A AND B SO THAT EACH OPERATES IN THE MANNER OF, AND UNDER THE CONDITIONS SPECIFIED FOR, THE OTHER ZONE IN PHASE (1); AND (4) THEREAFTER CONDUCTING THE OPERATION SUCH THAT EACH OF ZONES A AND B OPERATES IN THE MANNER OF, AND UNDER THE CONDITIONS SPECIFIED FOR, THE OTHER ZONE IN PHASE (2).
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) | 1960-08-12 | 1961-02-11 | 1961-08-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1964-08-12 | 1965-02-11 | 1965-08-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1968-08-12 | 1969-02-11 | 1969-08-13 | $7700.00 | Window Closed / Lapsed |