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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
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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
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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

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