US4415443A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Distillation process
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1981-07-10
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Granted: 1983-11-15
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Expires: 2001-07-10
Abstract
Abstract A method for improving the separation of a feed into a distillate and a bottoms product is disclosed. The subject invention includes a first distillation zone and a second distillation zone, each having rectification and stripping zones. Bottoms from the first stripping zone are passed into the second distillation zone. Distillate from the second rectification zone is removed utilizing a fluid evacuation means and returned to the first stripping zone.
Inventors
- 👤 Martin A. Murphy
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 18:28
CPC Classifications
C; C10; C10G; C10G7/00
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
158 words
A method for separating a feed into a distillate relatively rich in lower boiling components and a bottoms relatively rich in higher boiling components comprising: (a) passing the feed into a first distillation zone having a first stripping zone and a first rectification zone, wherein the feed is separated into a first distillate removed from the rectification zone and a first bottoms removed from the stripping zone; and (b) passing the first bottoms into a second distillation zone having a second rectification zone and a second stripping zone wherein the second distillation zone operates at a lower absolute pressure than the first distillation zone and wherein the bottoms from the first stripping zone are separated into a second distillate and a second bottoms, the rectification zone of the second column communicating with a fluid ejection means, whereby second distillate from the second rectification zone is transferred by the fluid ejection means into the first stripping zone without condensation.
Claim 2
Independent Claim
158 words
A method for separating a feed into a distillate relatively rich in lower boiling components and a bottoms relatively rich in higher boiling components comprising: (a) passing the feed into a first distillation zone having a first stripping zone and a first rectification zone, wherein the feed is separated into a first distillate removed from the rectification zone and a first bottoms removed from the stripping zone; and (b) passing the first bottoms into a second distillation zone having a second rectification zone and a second stripping zone wherein the second distillation zone operates at a lower absolute pressure than the first distillation zone and wherein the bottoms from the first stripping zone are separated into a second distillate and a second bottoms, the rectification zone of the second column communicating with a fluid ejection means, whereby second distillate from the second rectification zone is transferred by the fluid ejection means into the first stripping zone without condensation.
Claim 3
Dependent Claim
34 words
The method of claim 1 wherein the fluid ejection means is a steam jet ejector whereby steam passing through the ejector entrains second distillate and conveys the second distillate to the first stripping zone.
Claim 4
Dependent Claim
13 words
The method of claim 2 wherein the second distillation zone operates under vacuum.
Claim 5
Dependent Claim
14 words
The method of claim 3 wherein the first distillation zone is operated under vacuum.
Claim 6
Dependent Claim
41 words
The method of claim 4 further comprising an intermediate feed stream communicating between the first and second distillation zones whereby fluid from an intermediate point in the first distillation zone passes into an intermediate feed point in the second distillation zone.
Claim 7
Dependent Claim
17 words
The method of claim 5 wherein a product side stream is removed from the first rectification zone.
Claim 8
Dependent Claim
17 words
The method of claim 5 wherein a product side stream is removed from the second rectification zone.
Claim 9
Dependent Claim
154 words
In a distillation process wherein the feed stream is passed into a first distillation zone having a first rectification zone and a first stripping zone wherein the feed is separated into a first distillate relatively rich in lower boiling compounds exiting from the first rectification zone and a first bottoms relatively rich in higher boiling compounds exiting from the first stripping zone, the improvement which comprises: (a) passing the first bottoms into a second distillation zone at a lower absolute pressure than the first distillation zone, the second distillation zone having a second rectification zone and second stripping zone wherein the first bottoms are separated into a second distillate exiting from the second rectification zone and a second bottoms exiting from the second stripping zone; and (b) passing the second distillate through a steam jet ejector communicating with the second rectification zone and returning the second distillate without condensation to the first stripping zone.
Claim 10
Dependent Claim
154 words
In a distillation process wherein the feed stream is passed into a first distillation zone having a first rectification zone and a first stripping zone wherein the feed is separated into a first distillate relatively rich in lower boiling compounds exiting from the first rectification zone and a first bottoms relatively rich in higher boiling compounds exiting from the first stripping zone, the improvement which comprises: (a) passing the first bottoms into a second distillation zone at a lower absolute pressure than the first distillation zone, the second distillation zone having a second rectification zone and second stripping zone wherein the first bottoms are separated into a second distillate exiting from the second rectification zone and a second bottoms exiting from the second stripping zone; and (b) passing the second distillate through a steam jet ejector communicating with the second rectification zone and returning the second distillate without condensation to the first stripping zone.
Claim 11
Dependent Claim
14 words
The method of claim 8 wherein the feed is residuum from an atmospheric distillation.
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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) | 1986-11-14 | 1987-05-16 | 1987-11-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-11-14 | 1991-05-16 | 1991-11-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-11-14 | 1995-05-16 | 1995-11-15 | $7700.00 | Window Closed / Lapsed |