US4233267A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Combined batch reactor system and continuous distillation apparatus
Assignee: AOC LLC
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Filing: 1978-01-18
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Granted: 1980-11-11
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Expires: 1998-01-18
Abstract
Abstract Volatile reactants are heated under reflux in a reactor and form volatile reaction by-products which are continuously removed in a vapor effluent from a reflux column and partial condenser. The effluent, which entrains some of the reactants, is condensed in a first total condenser and is fed to a distillation apparatus for separation of the volatile reactants and by-products and return of the separated reactants to the reactor. Before the condensate reaches the distillation apparatus, it is temporarily stored in a receiver from which it is controllably fed to a pre-heater where it is evaporated and then fed as a vapor to the distillation column of the distillation apparatus for separation. The distillation column includes at one end a reboiler which retains the reactants. The other end of the distillation column is coupled to a second total condenser in which the volatile by-products are condensed and withdrawn through a cooler for disposal. The reactants are controllably fed from the reboiler back to the reactor, thereby providing control of the system, which has improved efficiency since the distillation apparatus operates independently of the temperature and pressure conditions in the reactor and of the rate and composition of effluent from the reflux column.
Inventors
- 👤 Robert J. Coker
- 👤 Gary W. Bate
- 👤 Henk J. Deuzeman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 12:45
CPC Classifications
B; B01; B01J; B01J14/00; B01D; B01D3/00; B01D3/14; B01D3/143; B01D3/146; Y; Y10; Y10S; Y10S203/00; Y10S203/06; Y10S203/17; Y10S203/23
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
222 words
An apparatus comprising a batch reactor system having a condensate output and a distillation apparatus in fluid communication with the condensate output; the batch reactor system comprising a batch reactor, a reflux column in communication with the batch reactor and a first total condenser for receiving and condensing a vapour effluent containing volatile by-products and reactants from the reflux column; the distillation apparatus comprising: condensate receiving means including a condensate inlet coupled to said condensate output for receiving and temporarily storing condensate from the first condenser so that the distillation apparatus has operating parameters which are substantially independent of the operating parameters of the batch reactor system; distillation column means for separating said by-products and reactants, the distillation column means including a reboiler disposed at a low end thereof and a vapour effluent oiutlet at the opposite end; and feed preheater means having an inlet in fluid communication with an outlet of said receiver means, evaporator means to vaporize condensate input thereto and an outlet feed in fluid communication with a vapour inlet of the distillation column means, whereby vaporized condensate is continuously separated into volatile by-products at the vapour effluent outlet and volatile reactants in the distillation column means independent of the temperature and pressure conditions in the batch reactor and the rate and composition of effluent from the reflux column.
Claim 2
Independent Claim
222 words
An apparatus comprising a batch reactor system having a condensate output and a distillation apparatus in fluid communication with the condensate output; the batch reactor system comprising a batch reactor, a reflux column in communication with the batch reactor and a first total condenser for receiving and condensing a vapour effluent containing volatile by-products and reactants from the reflux column; the distillation apparatus comprising: condensate receiving means including a condensate inlet coupled to said condensate output for receiving and temporarily storing condensate from the first condenser so that the distillation apparatus has operating parameters which are substantially independent of the operating parameters of the batch reactor system; distillation column means for separating said by-products and reactants, the distillation column means including a reboiler disposed at a low end thereof and a vapour effluent oiutlet at the opposite end; and feed preheater means having an inlet in fluid communication with an outlet of said receiver means, evaporator means to vaporize condensate input thereto and an outlet feed in fluid communication with a vapour inlet of the distillation column means, whereby vaporized condensate is continuously separated into volatile by-products at the vapour effluent outlet and volatile reactants in the distillation column means independent of the temperature and pressure conditions in the batch reactor and the rate and composition of effluent from the reflux column.
Claim 3
Dependent Claim
37 words
The apparatus of claim 1 wherein the distillation apparatus further comprises pump means disposed intermediate to the outlet of said condensate receiving means and the inlet of said feed pre-heater means for controllably feeding the condensate thereto.
Claim 4
Dependent Claim
32 words
The apparatus of claim 2 further comprising a second total condenser in serial fluid communication with the vapour effluent outlet of said distillation column means for receiving and condensing vaporized volatile by-products.
Claim 5
Dependent Claim
35 words
The apparatus of claim 3 wherein said distillatiin column means further includes an overflow conduit, and waste disposal means whereby a liquid seal is formed between the distillation column means and the waste disposal means.
Claim 6
Dependent Claim
36 words
The apparatus of claim 4 further comprising: a return conduit communicating the reboiler with the reactor; and a pump serially disposed with the return conduit to controllably feed the content of the reboiler to the reactor.
Claim 7
Dependent Claim
25 words
The apparatus of claim 5 wherein said distillation column means includes a distillation column partially packed with Pall rings fabricated of type 316 stainless steel.
Claim 8
Dependent Claim
35 words
The apparatus of claim 6 further comprising vacuum pump means coupled to a vent outlet of the second total condenser for reducing the pressure therein and in the distillation column to a predetermined sub-atmospheric pressure.
Claim 9
Dependent Claim
23 words
Apparatus as claimed in claim 7 further comprising a product cooler in serial communication with a condensate outlet of the second total condenser.
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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) | 1983-11-11 | 1984-05-12 | 1984-11-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-11-11 | 1988-05-12 | 1988-11-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-11-11 | 1992-05-12 | 1992-11-11 | $7700.00 | Window Closed / Lapsed |