US4624746A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for controlling distillation column
Assignee: Zeon Corp
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Filing: 1984-08-09
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Granted: 1986-11-25
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Expires: 2004-08-09
Abstract
Abstract A process for controlling a distillation column in which a feedstock is distilled for separation into a product from the top of the column having a first predetermined content of an intended component with a high boiling point and a product from the bottom of the column having a second predetermined content of an intended component with a low boiling point. The process includes the steps of computing a desired value of the flow rate of the product from the bottom of the column in accordance with a material balance and controlling the flow rate of the bottom product in accordance with a corrected desired value which is derived from one of deviations between the actual and desired compositions of the top or bottom products or limit values depending upon the magnitude and direction of the deviations. Reflux of part of the top product to the column is also controlled in accordance with the direction of the deviations and their magnitudes or limiting values.
Inventors
- 👤 Teruaki Hiramatsu
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 02:39
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/42; B01D3/4211; B01D3/425; Y; Y10; Y10S; Y10S203/00; Y10S203/19
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
368 words
A process for controlling a distillation column in which feedstock is distilled for separation into a product from the top of the column having a first predetermined content of an intended component with a high boiling point and a product from the bottom of the column having a second predetermined content of an intended component with a low boiling point by controlling the flow rate of either one of the products and a part of said product from the top of the column is refluxed to the column comprising the steps of: (a) computing a desired value of the flow rate of said product from the bottom of the column in accordance with a material balance; (b) controlling the flow rate of said product from the bottom of the column in accordance with a first corrected desired value which is obtained by correcting the desired value of the flow rate of said product from the bottom of the column in response to the larger one of a first deviation between the first content of the intended component with a high boiling point and its desired value and a second deviation between the second content of the intended component with a low boiling point and its desired value when the control directions of the flow rate of said product from the bottom of the column determined by the polarities of the first and second deviations are the same; (c) controlling the flow rate of said product from the bottom of the column in accordance with a second corrected desired value which is obtained by correcting the desired value in response to the second deviation when the control directions of the flow rate of said product from the bottom of the column determined by the polarities of the first and second deviations are different and controlling the reflux rate in response to the larger one of the first and second deviations; and (d) controlling the flow rate of said product from the bottom of the column in accordance with the limit values for a given range when the first and second desired values do not fall in said range and controlling the reflux rate in accordance with said limit values.
Claim 2
Dependent Claim
368 words
A process for controlling a distillation column in which feedstock is distilled for separation into a product from the top of the column having a first predetermined content of an intended component with a high boiling point and a product from the bottom of the column having a second predetermined content of an intended component with a low boiling point by controlling the flow rate of either one of the products and a part of said product from the top of the column is refluxed to the column comprising the steps of: (a) computing a desired value of the flow rate of said product from the bottom of the column in accordance with a material balance; (b) controlling the flow rate of said product from the bottom of the column in accordance with a first corrected desired value which is obtained by correcting the desired value of the flow rate of said product from the bottom of the column in response to the larger one of a first deviation between the first content of the intended component with a high boiling point and its desired value and a second deviation between the second content of the intended component with a low boiling point and its desired value when the control directions of the flow rate of said product from the bottom of the column determined by the polarities of the first and second deviations are the same; (c) controlling the flow rate of said product from the bottom of the column in accordance with a second corrected desired value which is obtained by correcting the desired value in response to the second deviation when the control directions of the flow rate of said product from the bottom of the column determined by the polarities of the first and second deviations are different and controlling the reflux rate in response to the larger one of the first and second deviations; and (d) controlling the flow rate of said product from the bottom of the column in accordance with the limit values for a given range when the first and second desired values do not fall in said range and controlling the reflux rate in accordance with said limit values.
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) | 1989-11-24 | 1990-05-26 | 1990-11-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-11-24 | 1994-05-26 | 1994-11-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-11-24 | 1998-05-26 | 1998-11-25 | $7700.00 | Window Closed / Lapsed |