Patent US4132530A successfully refreshed from Google Patents.
US4132530A
Expired / Lapsed
US
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Temperature control in exothermic/endothermic reaction systems
Assignee: Honeywell UOP LLC
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Filing: 1977-11-16
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Granted: 1979-01-02
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Expires: 1997-11-16
Abstract
Abstract Control of temperature increases (delta-T) through a reaction zone, in which both exothermic and endothermic reactions are effected, is achieved by sensing the inlet temperature of the charge stock, a highest temperature from a plurality of intermediate loci within the reaction zone and the outlet temperature of the effluent from the reaction zone. The inlet temperature sensor co-acts with a Temperature Recorder Controller (TRC), having an adjustable set point (control point), to produce a representative signal which is transmitted to flow-regulating means which adjusts the quantity of charge stock bypassing the feed heater. The difference between the inlet and intermediate temperatures, and that between the intermediate and outlet temperatures are determined to produce two delta-T signals which are transmitted to a Double differential Temperature Recorder Controller (DdTRC) which develops a signal representing the difference between the two delta-T signals compared to a preset difference. The signal is transmitted to the inlet Temperature Recorder Controller to adjust the set point thereof, and the quantity of charge stock bypassing the feed heater is further regulated responsive thereto. Enhanced control is afforded by selecting the higher of the outlet and highest intermediate temperatures, developing another representative signal and adjusting, or overriding the signal being transmitted to the charge stock bypass regulating means.
Inventors
- 👤 Michael F. Schwimmer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 13:23
CPC Classifications
B; B01; B01J; B01J19/00; B01J19/0006; B01J19/0013; B01J8/00; B01J8/001; C; C10; C10G; C10G49/00; C10G49/26; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00054; B01J2219/00056; B01J2219/00058; B01J2219/00063; B01J2219/00164; B01J2219/00191; B01J2219/00193; B01J2219/00195; B01J2219/00198; B01J2219/002; B01J2219/00211; B01J2219/0022; B01J2219/00222; B01J2219/00227; B01J2219/00229; B01J2219/00231; Y; Y10; Y10S; Y10S208/00; Y10S208/01; Y10S585/00; Y10S585/949; Y10S585/956; Y10T; Y10T137/00; Y10T137/0318; Y10T137/0324; Y10T137/2496; Y10T137/2559; Y10T137/2562; Y10T436/00; Y10T436/12
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
296 words
In a hydrocarbon conversion method wherein (1) a hydrocarbonaceous charge stock is introduced into heating means in which the temperature thereof is increased prior to passing into an elongated reaction zone and, (2) the reactions effected in said elongated reaction zone are both exothermic and endothermic in nature, the method of controlling the temperature rise through said reaction zone which comprises the steps of: (a) sensing (i) the temperature of said charge stock at the inlet to said reaction zone and developing a first signal representative thereof; (ii) the temperatures at a plurality of intermediate loci within said reaction zone, developing a plurality of signals, each being representative of and having associated therewith one of said temperatures, and selecting the signal representing the highest of said plurality of temperatures as a second signal; and (iii) the temperature of the effluent from said reaction zone and developing a third signal representative thereof; (b) comparing said inlet charge stock temperature with that temperature specified by the adjustable set point of a temperature controller, developing a fourth signal representative of said comparison and regulating the quantity of said charge stock which is caused to bypass said heating means in response to said fourth signal; (c) measuring the difference between said first and second signals and developing a fifth signal representative of said difference; (d) measuring the difference between said second and third signals and developing a sixth signal representative of said difference; (e) comparing said fifth and sixth signals, developing a seventh signal representative of said comparison and adjusting the set point of said temperature controller in response to said seventh signal; and, (f) further regulating the quantity of said charge stock which is caused to bypass said heating means in response to the adjustment of said set point.
Claim 2
Dependent Claim
296 words
In a hydrocarbon conversion method wherein (1) a hydrocarbonaceous charge stock is introduced into heating means in which the temperature thereof is increased prior to passing into an elongated reaction zone and, (2) the reactions effected in said elongated reaction zone are both exothermic and endothermic in nature, the method of controlling the temperature rise through said reaction zone which comprises the steps of: (a) sensing (i) the temperature of said charge stock at the inlet to said reaction zone and developing a first signal representative thereof; (ii) the temperatures at a plurality of intermediate loci within said reaction zone, developing a plurality of signals, each being representative of and having associated therewith one of said temperatures, and selecting the signal representing the highest of said plurality of temperatures as a second signal; and (iii) the temperature of the effluent from said reaction zone and developing a third signal representative thereof; (b) comparing said inlet charge stock temperature with that temperature specified by the adjustable set point of a temperature controller, developing a fourth signal representative of said comparison and regulating the quantity of said charge stock which is caused to bypass said heating means in response to said fourth signal; (c) measuring the difference between said first and second signals and developing a fifth signal representative of said difference; (d) measuring the difference between said second and third signals and developing a sixth signal representative of said difference; (e) comparing said fifth and sixth signals, developing a seventh signal representative of said comparison and adjusting the set point of said temperature controller in response to said seventh signal; and, (f) further regulating the quantity of said charge stock which is caused to bypass said heating means in response to the adjustment of said set point.
Claim 3
Dependent Claim
48 words
The method of claim 1 further characterized in that a selection is made of the higher of said second and third signals and said fourth signal is adjusted in response to said selected higher signal to regulate the quantity of charge stock caused to bypass said heating means.
Claim 4
Dependent Claim
21 words
The method of claim 1 further characterized in that said seventh signal represents the difference between said fifth and sixth signals.
Claim 5
Dependent Claim
38 words
The method of claim 1 further characterized in that said fourth signal is transmitted to flow control means, from the resulting adjustment of which the quantity of said charge stock caused to bypass said heating means is regulated.
Claim 6
Dependent Claim
24 words
The method of claim 1 further characterized in that the total amount of said charge stock introduced into said reaction zone remains substantially unchanged.
Claim 7
Dependent Claim
291 words
In a hydrocarbon conversion apparatus wherein (1) a hydrocarbon charge stock is passed into heating means in which its temperature is increased prior to the introduction thereof into an elongated reaction zone and (2) the reactions effected in said zone are both exothermic and endothermic in nature, a control system for controlling the temperature rise through said elongated reaction zone which comprises, in cooperative relationship: (a) first temperature-sensing means, sensing the temperature of said charge stock at the inlet to said reaction zone and developing a first signal representative thereof; (b) a plurality of second temperature-sensing means sensing the temperatures at a plurality of intermediate loci within said reaction zone; (c) high temperature selecting means, co-acting with said plurality of temperature-sensing means, selecting the highest of said temperatures and developing a second signal representative thereof; (d) third temperature-sensing means, sensing the temperature of the effluent from said reaction zone and developing a third signal representative thereof; (e) set point-adjustable temperature control means co-acting with said first signal and developing a fourth signal representative of a comparison between said first signal and said set point; (f) flow regulating means co-acting with said fourth signal whereby the quantity of said charge stock bypassing said heating means is adjusted in response thereto; (g) first differential temperature means measuring the difference between said first and second signals and developing a fifth signal representing said difference; (h) second differential temperature means measuring the difference between said second and third signals and developing a sixth signal representing said difference; (i) means for comparing said fifth and sixth signals, and developing a seventh signal representing the comparison; and, (j) means for adjusting the set point of said set point-adjustable temperature control means in response to said seventh signal.
Claim 8
Dependent Claim
291 words
In a hydrocarbon conversion apparatus wherein (1) a hydrocarbon charge stock is passed into heating means in which its temperature is increased prior to the introduction thereof into an elongated reaction zone and (2) the reactions effected in said zone are both exothermic and endothermic in nature, a control system for controlling the temperature rise through said elongated reaction zone which comprises, in cooperative relationship: (a) first temperature-sensing means, sensing the temperature of said charge stock at the inlet to said reaction zone and developing a first signal representative thereof; (b) a plurality of second temperature-sensing means sensing the temperatures at a plurality of intermediate loci within said reaction zone; (c) high temperature selecting means, co-acting with said plurality of temperature-sensing means, selecting the highest of said temperatures and developing a second signal representative thereof; (d) third temperature-sensing means, sensing the temperature of the effluent from said reaction zone and developing a third signal representative thereof; (e) set point-adjustable temperature control means co-acting with said first signal and developing a fourth signal representative of a comparison between said first signal and said set point; (f) flow regulating means co-acting with said fourth signal whereby the quantity of said charge stock bypassing said heating means is adjusted in response thereto; (g) first differential temperature means measuring the difference between said first and second signals and developing a fifth signal representing said difference; (h) second differential temperature means measuring the difference between said second and third signals and developing a sixth signal representing said difference; (i) means for comparing said fifth and sixth signals, and developing a seventh signal representing the comparison; and, (j) means for adjusting the set point of said set point-adjustable temperature control means in response to said seventh signal.
Claim 9
Dependent Claim
26 words
The apparatus of claim 6 further characterized in having high-signal selecting means adjusting said fourth signal responsive to the higher of said second and third signals.
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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) | 1982-01-01 | 1982-07-03 | 1983-01-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-01-01 | 1986-07-03 | 1987-01-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-01-01 | 1990-07-03 | 1991-01-02 | $7700.00 | Window Closed / Lapsed |