US3881994A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Distillation column reboiler control system
Assignee: Honeywell UOP LLC
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Filing: 1974-04-11
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Granted: 1975-05-06
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Expires: 1994-04-11
Abstract
Abstract A control system for regulating the heat input to the reboiler section of a distillation (fractionation) column. Flow-measuring means, for determining the quantity of vapor, passing upwardly from the reboiler section into the fractionation section (stripping and rectification), and internally disposed within the reboiler section, provides a signal which is transmitted to the reboiler heater, thereby adjusting the fuel input thereto in order to regulate the degree of vaporization being effected therein.
Inventors
- 👤 R Gene Fickel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 03:53
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/14; B01D3/141; B01D3/32; B01D3/322; B01D3/42; B01D3/4211; B01D3/4283; Y; Y02; Y02P; Y02P70/00; Y02P70/10
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
321 words
A control system for regulating the heat input to the reboiler section of a distillation column which comprises, in cooperative combination: a. a chamber in said reboiler section for receiving liquid bottoms material from the fractionation section of said column; b. a reboiler heater having feed input means thereto connected to said chamber, flow regulating means for controlling the flow of said liquid bottoms from said chamber to said reboiler heater in accordance with the liquid level in said chamber; c. conduit means in interconnection with said reboiler heater for passing heated, mixed-phase bottoms material from said heater into a paRtitioned and segregated portion of said chamber in said reboiler section; d. fuel-varying means in a fuel input means in interconnection with said heater for adjusting the fuel input to said heater; e. vapor flow-measuring means in said reboiler section responsive to the total quantity of upward flowing vapor from said mixed-phase bottoms material passing from said segregated portion of said reboiler section upwardly into the fractionation section of said distillation column, said flow measuring means being internally disposed within said segregated portion of said reboiler section; and f. signal-generating means in said segregated portion of said reboiler section for establishing a signal representative of the volumetric flow rate of vapor from said segregated portion passing into said fractionation section, and signal transmitting means for modifying and transmitting the resulting signal to said fuel varying means, whereby fuel input through said fuel input means to said heater is decreased in response to increasing flow rates of said vapor and increased in response to decreasing flow rates of said vapor; said control system being further characterized in that said reboiler section is partitioned to provide two inventory chambers of said liquid bottoms material, the first of which is said segregated portion which has said vapor flow measuring means disposed therein and the second of which is connected to said freed input means.
Claim 2
Dependent Claim
321 words
A control system for regulating the heat input to the reboiler section of a distillation column which comprises, in cooperative combination: a. a chamber in said reboiler section for receiving liquid bottoms material from the fractionation section of said column; b. a reboiler heater having feed input means thereto connected to said chamber, flow regulating means for controlling the flow of said liquid bottoms from said chamber to said reboiler heater in accordance with the liquid level in said chamber; c. conduit means in interconnection with said reboiler heater for passing heated, mixed-phase bottoms material from said heater into a paRtitioned and segregated portion of said chamber in said reboiler section; d. fuel-varying means in a fuel input means in interconnection with said heater for adjusting the fuel input to said heater; e. vapor flow-measuring means in said reboiler section responsive to the total quantity of upward flowing vapor from said mixed-phase bottoms material passing from said segregated portion of said reboiler section upwardly into the fractionation section of said distillation column, said flow measuring means being internally disposed within said segregated portion of said reboiler section; and f. signal-generating means in said segregated portion of said reboiler section for establishing a signal representative of the volumetric flow rate of vapor from said segregated portion passing into said fractionation section, and signal transmitting means for modifying and transmitting the resulting signal to said fuel varying means, whereby fuel input through said fuel input means to said heater is decreased in response to increasing flow rates of said vapor and increased in response to decreasing flow rates of said vapor; said control system being further characterized in that said reboiler section is partitioned to provide two inventory chambers of said liquid bottoms material, the first of which is said segregated portion which has said vapor flow measuring means disposed therein and the second of which is connected to said freed input means.
Claim 3
Dependent Claim
32 words
The control system of claim 1 further characterized in that a second flow-regulating means effects withdrawal of bottoms material from the first of said inventory chambers and out of said distillation column.
Claim 4
Dependent Claim
36 words
The control system of claim 2 further characterized in that said second flow-regulating means, includes means to maintain the level of the liquid bottoms in said first inventory chamber out of contact with said flow-measuring means.
Claim 5
Independent Claim
201 words
A method for controlling the heat input to the reboiler section of a distillation column, in response to variations in the steady-state operation of said column, which method comprises the steps of: a. regulating the quantity of liquid bottoms material withdrawn from one side of a partitioned reboiler section in response to the liquid level in said one side and introducing same into a reboiler heater; b. passing heated, mixed-phase bottoms material from said heater into the second side of said partitioned reboiler section; c. measuring within said second side of said reboiler section the quantity of vapor in said heated, mixed-phase bottoms, which passes from said second side of said reboiler section into the fractionation section of said distillation column; d. regulating the fuel input to said reboiler heater in response to a signal representative of the said measured quantity of vapor flowing into said fractionation section, said regulation comprising reducing the fuel input with reduced vapor flow and vice versa; and, e. withdrawing excess liquid bottoms material out of said distillation column from the second side of said partitioned reboiler section in response to the liquid level in said second side maintained below the point of measuring vapor flow.
Claim 6
Independent Claim
201 words
A method for controlling the heat input to the reboiler section of a distillation column, in response to variations in the steady-state operation of said column, which method comprises the steps of: a. regulating the quantity of liquid bottoms material withdrawn from one side of a partitioned reboiler section in response to the liquid level in said one side and introducing same into a reboiler heater; b. passing heated, mixed-phase bottoms material from said heater into the second side of said partitioned reboiler section; c. measuring within said second side of said reboiler section the quantity of vapor in said heated, mixed-phase bottoms, which passes from said second side of said reboiler section into the fractionation section of said distillation column; d. regulating the fuel input to said reboiler heater in response to a signal representative of the said measured quantity of vapor flowing into said fractionation section, said regulation comprising reducing the fuel input with reduced vapor flow and vice versa; and, e. withdrawing excess liquid bottoms material out of said distillation column from the second side of said partitioned reboiler section in response to the liquid level in said second side maintained below the point of measuring vapor flow.
Claim 7
Dependent Claim
39 words
The method of claim 4 further characterized in that the quantity of vapor, in the heated, mixed-phase bottoms material from said heater, which passes into said fractionation section, is measured within said reboiler section in a substantially liquid-free atmosphere.
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) | 1978-05-05 | 1978-11-04 | 1979-05-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-05-05 | 1982-11-04 | 1983-05-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-05-05 | 1986-11-04 | 1987-05-06 | $7700.00 | Window Closed / Lapsed |