US4008289A
Expired / Lapsed
US
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Adsorbent treating method
Assignee: Universal Oil Products Co
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Filing: 1975-07-07
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Granted: 1977-02-15
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Expires: 1995-07-07
Abstract
Abstract A more economical method of removing materials adsorbed on solid adsorbents used to treat hydrocarbon streams is presented. The method comprises removing a liquid hydrocarbon stream from a distillation column, vaporizing the liquid stream and superheating the vapors which are formed, passing the superheated vapor through the adsorbent and effecting the removal of the adsorbed material, and then returning the vapor to the fractionation column and utilizing the vapor as stripping media within the column. In the preferred embodiment, water is removed from alumina.
Inventors
- 👤 Dennis J. Ward
- 👤 George R. Winter, III
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 20:52
CPC Classifications
C; C07; C07C; C07C15/00; C07C15/02; B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01J; B01J20/00; B01J20/02; B01J20/06; B01J20/08; B01J20/10; B01J20/103; B01J20/30; B01J20/34; B01J20/3433; B01J20/345; B01J20/3458; B01J20/3483; C07C2/00; C07C2/54; C07C2/64; C07C2/66; C07C2/68; C07C7/00; C07C7/04; C07C7/12; B01D2253/00; B01D2253/10; B01D2253/104; B01D2253/106; B01D2256/00; B01D2256/24; B01D2257/00; B01D2257/70; B01D2257/702; B01D2257/80; B01D2259/00; B01D2259/40; B01D2259/40083; B01D2259/40084; C07C2527/00; C07C2527/06; C07C2527/08; Y; Y10; Y10S; Y10S203/00; Y10S203/11
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
107 words
A method of removing adsorbed material from a solid adsorbent in a process employing a fractionation column, which comprises the steps of: a. removing a liquid hydrocarbon bottoms stream from the lower portion of said column and reboiling the same to form vapors; b. returning a portion of said vapors to the lower portion of the column; c. superheating another portion of said vapors to a temperature sufficient to vaporize the adsorbed material from said adsorbent; d. contacting the superheated vapors with the adsorbent and thereby removing adsorbed material from the adsorbent; and e. supplying the resultant vapor stream to the lower portion of said fractionation column.
Claim 2
Independent Claim
107 words
A method of removing adsorbed material from a solid adsorbent in a process employing a fractionation column, which comprises the steps of: a. removing a liquid hydrocarbon bottoms stream from the lower portion of said column and reboiling the same to form vapors; b. returning a portion of said vapors to the lower portion of the column; c. superheating another portion of said vapors to a temperature sufficient to vaporize the adsorbed material from said adsorbent; d. contacting the superheated vapors with the adsorbent and thereby removing adsorbed material from the adsorbent; and e. supplying the resultant vapor stream to the lower portion of said fractionation column.
Claim 3
Dependent Claim
15 words
The method of claim 1 further characterized in that said adsorbed material comprises a hydrocarbon.
Claim 4
Dependent Claim
19 words
The method of claim 1 further characterized in that the adsorbent is alumina and the adsorbed material is water.
Claim 5
Dependent Claim
16 words
The method of claim 1 further characterized in that the liquid hydrocarbon bottoms stream comprises benzene.
Claim 6
Dependent Claim
28 words
The method of claim 1 further characterized in that the adsorbent is silica gel, the liquid hydrocarbon bottoms stream is benzene and the adsorbed material is N-methyl pyrolidone.
Claim 7
Dependent Claim
197 words
In a process for the alkylation of benzene wherein: a. benzene is passed into a benzene drying column to form a dry benzene feed stream; b. the dry benzene feed stream is reacted with an olefin in an alkylation zone containing a boron halide promoted catalyst, and an alkylation zone effluent comprising benzene, an alkylaromatic hydrocarbon and boron oxide hydrates is removed from the alkylation zone and passed into a fractionation zone; c. the formation of a volatile complex containing the boron oxide hydrate is effected by admixing the boron oxide hydrates with a boron halide within the fractionation zone, and the complex is removed from the fractionation zone dissolved in a distillate stream comprising benzene; and, d. the distillate stream is passed through a bed of a solid adsorbent which is periodically replaced and which removes the complex from the distillate stream, the improvement in the method of replacing the solid adsorbent which comprises drying the solid adsorbent with a vapor stream formed by vaporizing and superheating liquid removed from the bottom of the benzene drying column, and then returning the vapor stream to the benzene drying column and using the vapor stream as stripping vapor.
Claim 8
Dependent Claim
197 words
In a process for the alkylation of benzene wherein: a. benzene is passed into a benzene drying column to form a dry benzene feed stream; b. the dry benzene feed stream is reacted with an olefin in an alkylation zone containing a boron halide promoted catalyst, and an alkylation zone effluent comprising benzene, an alkylaromatic hydrocarbon and boron oxide hydrates is removed from the alkylation zone and passed into a fractionation zone; c. the formation of a volatile complex containing the boron oxide hydrate is effected by admixing the boron oxide hydrates with a boron halide within the fractionation zone, and the complex is removed from the fractionation zone dissolved in a distillate stream comprising benzene; and, d. the distillate stream is passed through a bed of a solid adsorbent which is periodically replaced and which removes the complex from the distillate stream, the improvement in the method of replacing the solid adsorbent which comprises drying the solid adsorbent with a vapor stream formed by vaporizing and superheating liquid removed from the bottom of the benzene drying column, and then returning the vapor stream to the benzene drying column and using the vapor stream as stripping vapor.
Claim 9
Independent Claim
166 words
A method of drying a solid adsorbent used to treat a recycle benzene stream in a process for the alkylation of benzene wherein an alkylation zone effluent is formed by reacting benzene with ethylene in the presence of a boron halide promoted catalyst and the recycle benzene stream is formed by fractionating the alkylation zone effluent in a first fractionation column, which method comprises the steps of: a. withdrawing a hydrocarbon stream comprising monoalkylated and polyalkylated benzenes from the first fractionation column and passing the hydrocarbon stream into a second fractionation column; b. withdrawing a liquid stream comprising a polyalkylated benzene from the second fractionation column, and effecting the formation of a vapor stream by vaporizing the liquid stream; c. superheating the vapor stream; d. contacting the solid adsorbent with the vapor stream and effecting the drying of the solid adsorbent; and, e. injecting the vapor stream into the second fractionation column at a point above the lowest distillation tray contained within the second fractionation column.
Claim 10
Independent Claim
166 words
A method of drying a solid adsorbent used to treat a recycle benzene stream in a process for the alkylation of benzene wherein an alkylation zone effluent is formed by reacting benzene with ethylene in the presence of a boron halide promoted catalyst and the recycle benzene stream is formed by fractionating the alkylation zone effluent in a first fractionation column, which method comprises the steps of: a. withdrawing a hydrocarbon stream comprising monoalkylated and polyalkylated benzenes from the first fractionation column and passing the hydrocarbon stream into a second fractionation column; b. withdrawing a liquid stream comprising a polyalkylated benzene from the second fractionation column, and effecting the formation of a vapor stream by vaporizing the liquid stream; c. superheating the vapor stream; d. contacting the solid adsorbent with the vapor stream and effecting the drying of the solid adsorbent; and, e. injecting the vapor stream into the second fractionation column at a point above the lowest distillation tray contained within the second fractionation column.
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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) | 1980-02-15 | 1980-08-16 | 1981-02-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-02-15 | 1984-08-16 | 1985-02-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-02-15 | 1988-08-16 | 1989-02-15 | $7700.00 | Window Closed / Lapsed |