US4714542A
Expired / Lapsed
US
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Distillation vapor and feed mixing process
Assignee: ENCON ASSOCIATED Inc
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Filing: 1986-01-06
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Granted: 1987-12-22
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Expires: 2006-01-06
Abstract
Abstract The present invention is a distillation vapor and feed mixing and subsequent separation process and apparatus involving the introduction of a vaporizing liquid feed into a flash zone via a tangential nozzle into a mixing and separation chamber which directs the feed into a circumferential path to enhance mixing, and the redirection of rising vapors from the distillation below the flash zone by baffling these vapors into the chamber inlet. The rising vapors are inspirated by the high velocity feed at the inlet side of the chamber and intimate contact and mixing of the rising vapors with the vaporizing feed are enhanced by creating a spinning action. Preferably, the chamber runs peripherally and slightly downward along the inside wall of the distillation column along an arc no greater than 360°. Alternatively, the mixing section of the mixing and separation chamber may be located outside of the distillation tower and the feed, passing through a jet ejector would inspirate the rising vapors. Increasing contacting and mixing efficiency in a distillation flash zone increases the yield of more valuable overhead product for the same energy input or permits lower energy input for constant separation between overheads and bottoms in the flash zone.
Inventors
- 👤 William Lockett, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 05:37
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/14; B01D3/30
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
348 words
In a distillation process wherein vaporizing liquid feed is being fed into a flash zone located within a column and contacted with rising vapors from the stripping section therein an improvement, for more complete mixing of the vaporizing liquid feed with the rising vapors from the stripping section in order to achieve a lower partial pressure effect on the feed to improve overall fractionation-energy efficiency, to minimize entrainment of heavy liquid dropleets in vapors leaving the flash zone, and, to improve the flow of liquid on the top stripping tray, which improvement comprises: (a) introducing the vaporizing liquid into the flash zone located within the column at an angle approximately tangential to the column via a nozzle and through a mixing and separation chamber having a port at its upstream end at the nozzle and an open downstream end at the flash zone, said chamber being constructed to approximately conform to the inside cross-sectional configuration of the column at the flash zone, and having side walls, a bottom and a top and having a rising vapors inlet port near the upstream end, said chamber having a length which is less than the full perimeter of the column at the flash zone; (b) enhancing the efficiency of the contacting and mixing of all of the rising vapors with the vaporizing liquid feed by redirecting all of the rising vapors from the column into said chamber near its upstream end by physically partitioning at least a part of the column with a partition baffle located in the flash zone to direct the rising vapors to the rising vapors inlet of said chamber; and, (c) further enhancing the efficiency of the contacting and mixing of all of the rising vapors with the vaporizing liquid feed by creating a spinning action with a deflector baffle located at said rising vapors inlet whereby high velocity feed inspirates all of the rising vapors so as to create the spinning action in said chamber and so as to thereby effect intimate mixing of all rising vapors from the stripping section with the vaporizing liquid feed.
Claim 2
Dependent Claim
348 words
In a distillation process wherein vaporizing liquid feed is being fed into a flash zone located within a column and contacted with rising vapors from the stripping section therein an improvement, for more complete mixing of the vaporizing liquid feed with the rising vapors from the stripping section in order to achieve a lower partial pressure effect on the feed to improve overall fractionation-energy efficiency, to minimize entrainment of heavy liquid dropleets in vapors leaving the flash zone, and, to improve the flow of liquid on the top stripping tray, which improvement comprises: (a) introducing the vaporizing liquid into the flash zone located within the column at an angle approximately tangential to the column via a nozzle and through a mixing and separation chamber having a port at its upstream end at the nozzle and an open downstream end at the flash zone, said chamber being constructed to approximately conform to the inside cross-sectional configuration of the column at the flash zone, and having side walls, a bottom and a top and having a rising vapors inlet port near the upstream end, said chamber having a length which is less than the full perimeter of the column at the flash zone; (b) enhancing the efficiency of the contacting and mixing of all of the rising vapors with the vaporizing liquid feed by redirecting all of the rising vapors from the column into said chamber near its upstream end by physically partitioning at least a part of the column with a partition baffle located in the flash zone to direct the rising vapors to the rising vapors inlet of said chamber; and, (c) further enhancing the efficiency of the contacting and mixing of all of the rising vapors with the vaporizing liquid feed by creating a spinning action with a deflector baffle located at said rising vapors inlet whereby high velocity feed inspirates all of the rising vapors so as to create the spinning action in said chamber and so as to thereby effect intimate mixing of all rising vapors from the stripping section with the vaporizing liquid feed.
Claim 3
Dependent Claim
44 words
The process of claim 1 wherein the column is circular in its cross-sectional configuration at the flash zone and said chamber is arcuated and makes an arc of less than 360° and is oriented slightly downward from its upstream end to its downstream end.
Claim 4
Dependent Claim
16 words
The process of claim 2 wherein said chamber makes an arc of between 60° and 270°.
Claim 5
Dependent Claim
19 words
The process of claim 3 wherein the bottom of said chamber makes an arc of between 40° and 200°.
Claim 6
Dependent Claim
15 words
The process of claim 1 wherein the distillation process is a primary atmospheric distillation process.
Claim 7
Dependent Claim
15 words
The process of claim 1 wherein the distillation process is a secondary vacuum distillation process.
Claim 8
Dependent Claim
28 words
The process of claim 1 wherein the distillation is crude oil distillation, the vaporizing liquid feed is crude oil and the rising vapors are steam-rich bottoms hydrocarbon vapors.
Claim 9
Dependent Claim
31 words
The process of claim 7 wherein the column is circular in its cross-sectional configuration at the flash zone and said chamber is arcuated and makes an arc of less than 360°.
Claim 10
Dependent Claim
29 words
The process of claim 8 wherein said chamber makes an arc of between 60° and 270° and is oriented slightly downward from its upstream end to its downstream end.
Claim 11
Dependent Claim
19 words
The process of claim 9 wherein the bottom of said chamber makes an arc of between 40° and 200°.
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) | 1990-12-21 | 1991-06-22 | 1991-12-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-12-21 | 1995-06-22 | 1995-12-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-12-21 | 1999-06-22 | 1999-12-22 | $7700.00 | Window Closed / Lapsed |