US4189616A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Maximum utilization of energy in isoparaffin recycle in alkylation
Assignee: Phillips Petroleum Co
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Filing: 1978-02-02
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Granted: 1980-02-19
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Expires: 1998-02-02
Abstract
Abstract In a fractionation system wherein a stream of heat-containing fluid is taken from a zone effecting at least a partial control of at least one operating condition in said zone by withdrawing said fluid at a rate responsive to and correlated with a change in said condition and utilizing the heat in said withdrawn fluid. In one application, in operation of an HF alkylation of isoparaffin with olefin, in which a mixed paraffins feed is fractionated in a first fractionator to obtain isoparaffin therefrom, an alkylate product is fractionated in a second fractionator to recover isoparaffin as a side draw from the second fractionator the temperature in the upper section of the second fractionator is controlled by removing more or less isoparaffin vapor therefrom, determining the change in amount of isoparaffin being removed and applying this measurement to adjust the amount of isoparaffin fed to the mixed paraffins feed fractionator reboiler section, increasing isoparaffin to said section when the preselected temperature in the overhead outlet of the alkylate product fractionator attempts to increase (and vice versa) and causing adjustment in the amount of steam needed to supply the remainder of heat required to reboil the mixed paraffins fractionation zone. In one embodiment the isoparaffin vapor removed from the alkylate product fractionator is passed through a cooling zone, condensed therein, and the flow of the produced condensate, while being passed to the alkylation, is detected and is representative of the attempted temperature change in the alkylate product fractionator and is employed to adjust flow of the isoparaffin vapor to the isoparaffin vapor-heated reboiler in the mixed paraffin fractionation zone; the operation providing for suitable adjustment of steam to the steam reboiler to said mixed paraffins fractionation zone. In another modification, the amount of steam is further controlled with respect to the amount of total heat needed in the reboiled section of the mixed paraffins fractionation zone in manner correlated with the composition of paraffins removed in a side draw from said mixed paraffins fractionation zone.
Inventors
- 👤 Timothy C. Liebert
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 12:24
CPC Classifications
C; C07; C07C; C07C9/00; C07C9/14; C07C9/16; C07C2/00; C07C2/54; C07C2/56; C07C2/58; C07C2/62; C07C7/00; C07C7/04; C07C2527/00; C07C2527/06; C07C2527/08; C07C2527/12; C07C2527/1206; Y; Y10; Y10S; Y10S208/00; Y10S208/01
Claims Analysis
Total Claims: 20
Claim 1
Independent Claim
146 words
In an operating unit in which there is a first fractionator being reboiled with a steam reboiler and with a stream of heat-containing fluid taken from a second fractionator and passed into and through a second reboiler in said first fractionator, wherein said second reboiler is being supplied with said fluid separated from said second fractionator having a locus in a top portion thereof and wherein a maximum use of said fluid to said second reboiler and a minimum use of steam to said steam reboiler are to be provided, the invention which comprises: detecting a change in a controlled variable at said locus in said top portion of said second fractionator and adjusting the rate of flow of said fluid from said second fractionator to said second reboiler to return said controlled variable to the condition desired in said top portion of said second fractionator.
Claim 2
Dependent Claim
146 words
In an operating unit in which there is a first fractionator being reboiled with a steam reboiler and with a stream of heat-containing fluid taken from a second fractionator and passed into and through a second reboiler in said first fractionator, wherein said second reboiler is being supplied with said fluid separated from said second fractionator having a locus in a top portion thereof and wherein a maximum use of said fluid to said second reboiler and a minimum use of steam to said steam reboiler are to be provided, the invention which comprises: detecting a change in a controlled variable at said locus in said top portion of said second fractionator and adjusting the rate of flow of said fluid from said second fractionator to said second reboiler to return said controlled variable to the condition desired in said top portion of said second fractionator.
Claim 3
Dependent Claim
12 words
An operation according to claim 1 wherein said fluid is a vapor.
Claim 4
Dependent Claim
12 words
An operation according to claim 1 wherein said fluid is a liquid.
Claim 5
Dependent Claim
15 words
The operation of claim 1 wherein the condition desired for a said locus is temperature.
Claim 6
Dependent Claim
15 words
The operation of claim 1 wherein the condition desired for a said locus is pressure.
Claim 7
Dependent Claim
15 words
The operation according to claim 1 wherein the condition desired for said locus is composition.
Claim 8
Dependent Claim
21 words
The operation of claim 1 wherein the condition desired for said locus is at least one of temperature, pressure and composition.
Claim 9
Dependent Claim
144 words
In an operating unit in which there is a mixed butane feed fractionater being separately reboiled with a steam reboiler and a hot isobutane vapor reboiler wherein said hot isobutane vapor reboiler is being supplied with hot isobutane vapor separated from an alkylate product fractionator having a locus in a top portion thereof and wherein a maximum use of said hot isobutane vapor to said hot isobutane vapor reboiler and a minimum use of steam to said steam reboiler are to be provided, the invention which comprises: detecting a change in a controlled variable at said locus in said top portion of said alkylate product fractionator and adjusting the rate of flow of hot isobutane vapor from said alkylate product fractionator to said hot isobutane reboiler to return said controlled variable to the condition desired in said top portion of said alkylate product fractionator.
Claim 10
Dependent Claim
144 words
In an operating unit in which there is a mixed butane feed fractionater being separately reboiled with a steam reboiler and a hot isobutane vapor reboiler wherein said hot isobutane vapor reboiler is being supplied with hot isobutane vapor separated from an alkylate product fractionator having a locus in a top portion thereof and wherein a maximum use of said hot isobutane vapor to said hot isobutane vapor reboiler and a minimum use of steam to said steam reboiler are to be provided, the invention which comprises: detecting a change in a controlled variable at said locus in said top portion of said alkylate product fractionator and adjusting the rate of flow of hot isobutane vapor from said alkylate product fractionator to said hot isobutane reboiler to return said controlled variable to the condition desired in said top portion of said alkylate product fractionator.
Claim 11
Dependent Claim
45 words
An operation according to claim 8 wherein the effect of the variation in the flow rate of hot isobutane vapor passed through said reboiler is detected and the amount of any steam necessary to maintain desired conditions in the mixed butane fractionator is adjusted accordingly.
Claim 12
Dependent Claim
55 words
The operation of claim 8 wherein the heat requirement for the mixed butanes feed fractionator is supplied by the flow of hot isobutane to its hot isobutane reboiler and the amount of steam added to its steam reboiler is adjusted to supply the balance of the total heat requirement to the mixed butane feed fractionator.
Claim 13
Dependent Claim
50 words
The operation of claim 10 wherein a first condition in a locus of the mixed butane feed fractionator is determined, said first condition is compared with a second condition desired for said locus of said mixed butane feed fractionator and addition of steam to said steam reboiler is adjusted accordingly.
Claim 14
Dependent Claim
14 words
The operation of claim 10 wherein the condition desired for said locus is temperature.
Claim 15
Dependent Claim
14 words
The operation of claim 10 wherein the condition desired for said locus is pressure.
Claim 16
Dependent Claim
15 words
The operation according to claim 10 wherein the condition desired for said locus is composition.
Claim 17
Dependent Claim
21 words
The operation of claim 10 wherein the condition desired for said locus is at least one of temperature, pressure and composition.
Claim 18
Dependent Claim
144 words
In an operating unit in which there is a mixed paraffin feed fractionator being separately reboiled with a steam reboiler and a hot isoparaffin vapor reboiler wherein said hot isoparaffin vapor reboiler is being supplied with hot isoparaffin vapor separated from an alkylate product fractionator having a locus in a top portion thereof and wherein a maximum use of said hot isoparaffin vapor to said hot isoparaffin vapor reboiler and a minimum use of steam to said steam reboiler are to be provided, the invention which comprises: detecting a change in a controlled variable at said locus in said top portion of said alkylate product fractionator and adjusting the rate of flow of hot isoparaffin vapor from said alkylate product fractionator to said hot isoparaffin reboiler to return said controlled variable to the condition desired in said top portion of said alkylate product fractionator.
Claim 19
Dependent Claim
144 words
In an operating unit in which there is a mixed paraffin feed fractionator being separately reboiled with a steam reboiler and a hot isoparaffin vapor reboiler wherein said hot isoparaffin vapor reboiler is being supplied with hot isoparaffin vapor separated from an alkylate product fractionator having a locus in a top portion thereof and wherein a maximum use of said hot isoparaffin vapor to said hot isoparaffin vapor reboiler and a minimum use of steam to said steam reboiler are to be provided, the invention which comprises: detecting a change in a controlled variable at said locus in said top portion of said alkylate product fractionator and adjusting the rate of flow of hot isoparaffin vapor from said alkylate product fractionator to said hot isoparaffin reboiler to return said controlled variable to the condition desired in said top portion of said alkylate product fractionator.
Claim 20
Dependent Claim
50 words
The operation of claim 16 wherein a first condition in a locus of the mixed paraffin feed fractionator is determined, said first condition is compared with a second condition desired for said locus of said mixed butane feed fractionator and addition of steam to said steam reboiler is adjusted accordingly.
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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) | 1983-02-18 | 1983-08-20 | 1984-02-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-02-18 | 1987-08-20 | 1988-02-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-02-18 | 1991-08-20 | 1992-02-19 | $7700.00 | Window Closed / Lapsed |