US3927982A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Recirculating apparatus for continuous esterification reactions
Assignee: EIDP Inc
•
Filing: 1973-06-19
•
Granted: 1975-12-23
•
Expires: 1993-06-19
Abstract
Abstract Apparatus for continuous esterification in the presence of hot liquid esterification product which is circulated downward from the bottom of an esterification vessel, upward through an external heat exchanger and back to the vessel without mechanical pumping; including means for introducing reactant feed mixture directly into the lower fluid inlet of the heat exchanger and means for withdrawing esterification product directly from the vessel at a rate which maintains a constant liquid level. Esterification of terephthalic acid with ethylene glycol at 315*C. to form low molecular weight polyester product is illustrated.
Inventors
- 👤 Rodney M Chapman
- 👤 Kenneth A Temple
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 18:06
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/78; C08G63/785; B; B01; B01J; B01J19/00; B01J19/0006; B01J19/0013; B01J19/24; B01J19/2455; B01J19/2465; C07; C07C; C07C67/00; C07C67/08; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00074; B01J2219/00087; B01J2219/00103
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
208 words
A CHEMICAL PROCESS APPARATUS, WHICH IS SELF-STIRRING AND PROVIDES VIGOROUS AGITIOATION OF REACTING MATERIALS WITHOUT THE USE OF MECHANICAL STIRRRING OR PUMPING, COMPRISING AN ESTERIFICATION VESSEL FOR ESTERIFICATION LIQUID , A HEAT EXCHANGER FOR HEATING THE LIQUID TO A TEMPERATURE OF 250* TO 400*C. LOCATED EXTERNALLY OF SAID ESTERFICATION VESSEL, A CONDUIT LOOP FOR CONDUCTING LIQUID WITHOUT THE USE OF A PUMP DOWNWARD FROM THE BOTTOM OF THE VESSEL AND THEN UPWARD INTO THE HEAT EXCHANGER THROUGH A LOWER FLUID INLET, MEANS FOR INJECTING REACTANT FEED MIXTURE INTO THE LOWER FLUID INLET OF THE HEAT EXCHANGER AT A LEVEL AT LEAST 3 FEET ABOVE THE LOWEST POINT OF THE CONDUIT LOOP, MEANS FOR CONDUCTING HEATED FLUID FROM THE HEAT EXCHANGER THROUGH AN UPPER FLUID OUTLET AND INTO A VESSEL THROUGH AN INLET IN THE SIDE OF THE VESSEL, MEANS IN THE UPPER PART OF THE VESSEL FOR WITHDRAWING VAPORS, AND OVERFLOW MEANS IN THE VESSEL FOR WITHDRAWING ESTERIFICATION PRODUCT AT A RATE WHICH MAINTAINS A CONSTANT LIQUID LEVEL WITHIN THE VESSEL, SAID OVERFLOW MEANS BEING LOCATED WITHIN SAID VESSEL AT SUBSTANTIALLY THE SAME HEIGHT AS SAID INLET IN THE SIDE OF SAID VESSEL, THEREBY ENSURING SUFFICIENT LIQUID HEAD WITHIN SAID VESSEL TO MAINTAIN FLOW IN SAID CONDUIT LOOP.
Claim 2
Dependent Claim
208 words
A CHEMICAL PROCESS APPARATUS, WHICH IS SELF-STIRRING AND PROVIDES VIGOROUS AGITIOATION OF REACTING MATERIALS WITHOUT THE USE OF MECHANICAL STIRRRING OR PUMPING, COMPRISING AN ESTERIFICATION VESSEL FOR ESTERIFICATION LIQUID , A HEAT EXCHANGER FOR HEATING THE LIQUID TO A TEMPERATURE OF 250* TO 400*C. LOCATED EXTERNALLY OF SAID ESTERFICATION VESSEL, A CONDUIT LOOP FOR CONDUCTING LIQUID WITHOUT THE USE OF A PUMP DOWNWARD FROM THE BOTTOM OF THE VESSEL AND THEN UPWARD INTO THE HEAT EXCHANGER THROUGH A LOWER FLUID INLET, MEANS FOR INJECTING REACTANT FEED MIXTURE INTO THE LOWER FLUID INLET OF THE HEAT EXCHANGER AT A LEVEL AT LEAST 3 FEET ABOVE THE LOWEST POINT OF THE CONDUIT LOOP, MEANS FOR CONDUCTING HEATED FLUID FROM THE HEAT EXCHANGER THROUGH AN UPPER FLUID OUTLET AND INTO A VESSEL THROUGH AN INLET IN THE SIDE OF THE VESSEL, MEANS IN THE UPPER PART OF THE VESSEL FOR WITHDRAWING VAPORS, AND OVERFLOW MEANS IN THE VESSEL FOR WITHDRAWING ESTERIFICATION PRODUCT AT A RATE WHICH MAINTAINS A CONSTANT LIQUID LEVEL WITHIN THE VESSEL, SAID OVERFLOW MEANS BEING LOCATED WITHIN SAID VESSEL AT SUBSTANTIALLY THE SAME HEIGHT AS SAID INLET IN THE SIDE OF SAID VESSEL, THEREBY ENSURING SUFFICIENT LIQUID HEAD WITHIN SAID VESSEL TO MAINTAIN FLOW IN SAID CONDUIT LOOP.
References Cited (Backward Citations)
US2820815A
Cited
US2925450A
Cited
US3227743A
Cited
US3458467A
Cited
US3497473A
Cited
US3544269A
Cited
US3527820A
Cited
US3600137A
Cited
US3676485A
Cited
US3697579A
Cited
US3644096A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1978-12-22 | 1979-06-23 | 1979-12-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-12-22 | 1983-06-23 | 1983-12-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-12-22 | 1987-06-23 | 1987-12-23 | $7700.00 | Window Closed / Lapsed |