US4290110A
Expired / Lapsed
US
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Temperature control for a reactor
Assignee: Phillips Petroleum Co
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Filing: 1979-11-08
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Granted: 1981-09-15
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Expires: 1999-11-08
Abstract
Abstract Control of the temperature rise across a reactor where a portion of the product stream flowing from the reactor is recycled and mixed with the feed flowing to the reactor is accomplished by controlling the flow rate of the recycle stream to thus control the concentration of the reactants flowing to the reactor in such a manner that a desired temperature differential across the reactor is obtained. The inlet temperature to the reactor is controlled by manipulating the temperature of the recycle stream to thus maintain the inlet temperature to the reactor at some desired temperature. Ratio control is utilized to maintain a desired ratio of reactants flowing to the reactor if more than one reactant is flowing to the reactor.
Inventors
- 👤 Donald J. Makovec
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 23:57
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; B; B01; B01J; B01J8/00; B01J8/001; Y; Y10; Y10T; Y10T436/00; Y10T436/12
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
169 words
Apparatus comprising: a reactor; means for supplying a first feed stream containing a first reactant to the feed inlet of said reactor; means for withdrawing the reaction product from said reactor; means for passing a portion of said reaction product as a recycle stream to the feed inlet of said reactor; means for establishing a first signal representative of the flow rate of said first feed stream; means, responsive to said first signal, for establishing a second signal representative of the flow rate of the recycle stream required to substantially maintain a desired temperature differential across said reactor; means for establishing a third signal representative of the actual flow rate of said recycle stream; means for comparing said second signal and said third signal and for establishing a fourth signal responsive to the difference between said second signal and said third signal; and means for manipulating the flow rate of said recycle stream in response to said fourth signal to thereby maintain a desired temperature differential across said reactor.
Claim 2
Dependent Claim
169 words
Apparatus comprising: a reactor; means for supplying a first feed stream containing a first reactant to the feed inlet of said reactor; means for withdrawing the reaction product from said reactor; means for passing a portion of said reaction product as a recycle stream to the feed inlet of said reactor; means for establishing a first signal representative of the flow rate of said first feed stream; means, responsive to said first signal, for establishing a second signal representative of the flow rate of the recycle stream required to substantially maintain a desired temperature differential across said reactor; means for establishing a third signal representative of the actual flow rate of said recycle stream; means for comparing said second signal and said third signal and for establishing a fourth signal responsive to the difference between said second signal and said third signal; and means for manipulating the flow rate of said recycle stream in response to said fourth signal to thereby maintain a desired temperature differential across said reactor.
Claim 3
Dependent Claim
18 words
Apparatus in accordance with claim 1 wherein said means for establishing said second signal comprises a ratio transducer.
Claim 4
Dependent Claim
95 words
Apparatus in accordance with claim 1 additionally comprising: means for establishing a fifth signal representative of the actual feed inlet temperature of said reactor; means for establishing a sixth signal representative of the desired feed inlet temperature of said reactor; means for comparing said fifth signal and said sixth signal and for establishing a seventh signal responsive to the difference between said fifth signal and said sixth signal; and means for manipulating the temperature of said recycle stream in response to said seventh signal to thereby maintain a desired feed inlet temperature for said reactor.
Claim 5
Dependent Claim
227 words
Apparatus in accordance with claim 3 additionally comprising: means for supplying a second feed stream containing a second reactant to the feed inlet of said reactor; means for establishing an eighth signal representative of the desired flow rate of said first feed stream; means for comparing said first signal and said eighth signal and for establishing a ninth signal responsive to the difference between said first signal and said eighth signal; means for manipulating the flow rate of said first feed stream in response to said ninth signal to thereby maintain the flow rate of said first feed stream substantially equal to the desired flow rate represented by said eighth signal; means for establishing a tenth signal representative of the flow rate of said second feed stream required to maintain a desired ratio of said second reactant to said first reactant in response to said first signal; means for establishing an eleventh signal representative of the actual flow rate of said second feed stream; means for comparing said tenth signal and said eleventh signal and for establishing a twelfth signal responsive to the difference between said tenth signal and said eleventh signal; and means for manipulating the flow rate of said second feed stream in response to said twelfth signal to thereby maintain a desired ratio of said second reactant to said first reactant in said reactor.
Claim 6
Independent Claim
183 words
A method for controlling the temperature differential across a reaction zone, where a portion of the product stream flowing from said reaction zone is passed as a recycle stream and mixed with the feed stream flowing to said reaction zone before said feed stream is introduced into said reaction zone, wherein said feed stream contains a first reactant, said method comprising the steps of: establishing a first signal representative of the flow rate of said feed stream before said feed stream is mixed with said recycle stream; establishing a second signal representative of the flow rate of said recycle stream required to substantially maintain a desired temperature differential across said reaction zone in response to said first signal; establishing a third signal representative of the actual flow rate of said recycle stream; comparing said second signal and said third signal and establishing a fourth signal responsive to the difference between said second signal and said third signal; and manipulating the flow rate of said recycle stream in response to said fourth signal to thereby maintain a desired temperature differential across said reaction zone.
Claim 7
Independent Claim
183 words
A method for controlling the temperature differential across a reaction zone, where a portion of the product stream flowing from said reaction zone is passed as a recycle stream and mixed with the feed stream flowing to said reaction zone before said feed stream is introduced into said reaction zone, wherein said feed stream contains a first reactant, said method comprising the steps of: establishing a first signal representative of the flow rate of said feed stream before said feed stream is mixed with said recycle stream; establishing a second signal representative of the flow rate of said recycle stream required to substantially maintain a desired temperature differential across said reaction zone in response to said first signal; establishing a third signal representative of the actual flow rate of said recycle stream; comparing said second signal and said third signal and establishing a fourth signal responsive to the difference between said second signal and said third signal; and manipulating the flow rate of said recycle stream in response to said fourth signal to thereby maintain a desired temperature differential across said reaction zone.
Claim 8
Dependent Claim
91 words
A method in accordance with claim 5 additionally comprising the steps of: establishing a fifth signal representative of the actual inlet temperature of said reaction zone; establishing a sixth signal representative of the desired inlet temperature of said reaction zone; comparing said fifth signal and said sixth signal and establishing a seventh signal responsive to the difference between said fifth signal and said sixth signal; and manipulating the temperature of said recycle stream in response to said seventh signal to thereby maintain a desired feed inlet temperature for said reaction zone.
Claim 9
Independent Claim
188 words
A method for controlling the temperature differential across a reaction zone where a portion of the product stream flowing from said reaction zone is passed as a recycle stream and mixed with the reaction zone feed stream, which is formed from at least a first feed stream containing a first reactant and a second feed stream containing a second reactant, before said reaction zone feed stream is introduced into said reaction zone, said method comprising the steps of: establishing a first signal representative of the flow rate of said first feed stream; establishing a second signal representative of the flow rate of said recycle stream required to substantially maintain a desired temperature differential across said reaction zone in response to said first signal; establishing a third signal representative of the actual flow rate of said recycle stream; comparing said second signal and said third signal and establishing a fourth signal responsive to the difference between said second signal and said third signal; and manipulating the flow rate of said recycle stream in response to said fourth signal to thereby maintain a desired temperature differential across said reaction zone.
Claim 10
Independent Claim
188 words
A method for controlling the temperature differential across a reaction zone where a portion of the product stream flowing from said reaction zone is passed as a recycle stream and mixed with the reaction zone feed stream, which is formed from at least a first feed stream containing a first reactant and a second feed stream containing a second reactant, before said reaction zone feed stream is introduced into said reaction zone, said method comprising the steps of: establishing a first signal representative of the flow rate of said first feed stream; establishing a second signal representative of the flow rate of said recycle stream required to substantially maintain a desired temperature differential across said reaction zone in response to said first signal; establishing a third signal representative of the actual flow rate of said recycle stream; comparing said second signal and said third signal and establishing a fourth signal responsive to the difference between said second signal and said third signal; and manipulating the flow rate of said recycle stream in response to said fourth signal to thereby maintain a desired temperature differential across said reaction zone.
Claim 11
Dependent Claim
93 words
A method in accordance with claim 7 additionally comprising the steps of: establishing a fifth signal representative of the actual feed inlet temperature of said reaction zone; establishing a sixth signal representative of the desired feed inlet temperature of said reaction zone; comparing said fifth signal and said sixth signal and establishing a seventh signal responsive to the difference between said fifth signal and said sixth signal; and manipulating the temperature of said recycle stream in response to said seventh signal to thereby maintain a desired feed inlet temperature for said reaction zone.
Claim 12
Dependent Claim
198 words
A method in accordance with claim 8 additionally comprising the steps of: establishing an eighth signal representative of the desired flow rate of said first feed stream; comparing said first signal and said eighth signal and establishing a ninth signal responsive to the difference between said first signal and said eighth signal; manipulating the flow rate of said first feed stream in response to said ninth signal to thereby maintain the flow rate of said first feed stream substantially equal to the desired flow rate represented by said eighth signal; establishing a tenth signal representative of the flow rate of said second feed stream required to maintain a desired ratio of said second reactant to said first reactant in response to said first signal; establishing an eleventh signal representative of the actual flow rate of said second feed stream; comparing said tenth signal and said eleventh signal and establishing a twelfth signal responsive to the difference between said tenth signal and said eleventh signal; and manipulating the flow rate of said second feed stream in response to said twelfth signal to thereby maintain a desired ratio of said second reactant to said first reactant in said reaction zone.
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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) | 1984-09-14 | 1985-03-16 | 1985-09-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-09-14 | 1989-03-16 | 1989-09-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-09-14 | 1993-03-16 | 1993-09-15 | $7700.00 | Window Closed / Lapsed |