Patent US4477413A successfully refreshed from Google Patents.
US4477413A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Utility conservation in hydrogen recycle processes
Assignee: Honeywell UOP LLC
•
Filing: 1982-05-04
•
Granted: 1984-10-16
•
Expires: 2002-05-04
Abstract
Abstract A control system is disclosed for modifying the flow of hydrogen in a hydrocarbonaceous apparatus wherein a charge stock and a vaporous hydrocarbon-hydrogen recycle are charged to a reaction zone to convert the hydrocarbons and produce a reaction zone effluent conduit which is cooled to provide, via a gas-liquid separation zone, a liquid hydrocarbon product stream and the vaporous hydrocarbon-hydrogen recycle stream, the latter being returned to charge stock admixture by a compressor. The control system senses the partial pressure of hydrogen, compares that value to a previously determined value and develops a signal correlative thereto, which is transmitted to a regulater that controls the quantity of vaporous hydrocarbon-hydrogen stream recycled to admixture with the charge stock. In a hydrogen consuming process, the hydrogen partial pressure is sensed downstream of the reactor while in the hydrogen producing process, the hydrogen partial pressure is sensed in the inlet to the reaction zone.
Inventors
- 👤 Don B. Carson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 19:49
CPC Classifications
C; C10; C10G; C10G49/00; C10G49/26; Y; Y10; Y10S; Y10S208/00; Y10S208/01; Y10T; Y10T436/00; Y10T436/12; Y10T436/22
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
249 words
A control system for modifying the flow of hydrogen in a hydrocarbonaceous conversion apparatus, which apparatus comprises: (a) a charge stock stream inlet conduit in interconnection with a vaporous hydrocarbon-hydrogen recycle stream conduit; (b) a reaction zone for reacting hydrocarbonaceous materials contained within said charge stock stream to a converted hydrocarbon product stream; (c) a reaction zone effluent conduit having a hydrogen partial pressure sensor therein; (d) a cooling zone for cooling said effluent stream to provide via condensing in liquid hydrocarbon product stream and at least a portion of said vaporous hydrocarbon-hydrogen recycle stream; (e) a cooling zone effluent conduit in communication with a gas-liquid separation zone, said gas-liquid separation zone effective to exorcise said liquid hydrocarbon product stream from said vaporous hydrocarbon-hydrogen recycle stream; and (f) a compressor means having variable output capability in communication with said separation zone and said recycle stream conduit of step (a); said control system consisting of: (i) means for sensing the partial pressure of hydrogen at a point downstream of said reaction zone of step (b) in said reaction zone effluent conduit; (ii) comparison means for comparing said partial pressure of hydrogen to a previously determined value and developing a signal correlating thereto; (iii) transmission means for transmitting said signal of step (ii) to said variable output compressor; and (iv) regulation means for controlling the quantity of varporous hydrocarbon and hydrogen recycled to said reaction zone via said recycle stream conduit based on the partial pressure sensed in said step (i).
Claim 2
Dependent Claim
249 words
A control system for modifying the flow of hydrogen in a hydrocarbonaceous conversion apparatus, which apparatus comprises: (a) a charge stock stream inlet conduit in interconnection with a vaporous hydrocarbon-hydrogen recycle stream conduit; (b) a reaction zone for reacting hydrocarbonaceous materials contained within said charge stock stream to a converted hydrocarbon product stream; (c) a reaction zone effluent conduit having a hydrogen partial pressure sensor therein; (d) a cooling zone for cooling said effluent stream to provide via condensing in liquid hydrocarbon product stream and at least a portion of said vaporous hydrocarbon-hydrogen recycle stream; (e) a cooling zone effluent conduit in communication with a gas-liquid separation zone, said gas-liquid separation zone effective to exorcise said liquid hydrocarbon product stream from said vaporous hydrocarbon-hydrogen recycle stream; and (f) a compressor means having variable output capability in communication with said separation zone and said recycle stream conduit of step (a); said control system consisting of: (i) means for sensing the partial pressure of hydrogen at a point downstream of said reaction zone of step (b) in said reaction zone effluent conduit; (ii) comparison means for comparing said partial pressure of hydrogen to a previously determined value and developing a signal correlating thereto; (iii) transmission means for transmitting said signal of step (ii) to said variable output compressor; and (iv) regulation means for controlling the quantity of varporous hydrocarbon and hydrogen recycled to said reaction zone via said recycle stream conduit based on the partial pressure sensed in said step (i).
Claim 3
Dependent Claim
18 words
The control system of claim 1 further characterized in that said hydrocarbon reaction zone is a hydrogenation unit.
Claim 4
Dependent Claim
18 words
The control system of claim 1 further characterized in that said hydrocarbon reaction zone is a hydrodealkylation zone.
Claim 5
Dependent Claim
18 words
The control system of claim 1 further characterized in that said hydrocarbon reaction zone is a hydrodesulfurization unit.
Claim 6
Dependent Claim
18 words
The control system of claim 1 further characterized in that said hydrocarbon reaction zone is a hydrocracking unit.
Claim 7
Dependent Claim
18 words
The control system of claim 1 further characterized in that said hydrocarbon reaction zone is an isomerization unit.
Claim 8
Dependent Claim
280 words
A control system for modifying the flow of hydrogen in a hydrocarbonaceous conversion apparatus, said apparatus which comprises: (a) a charge stock inlet conduit in interconnection with a vaporous hydrocarbon-hydrogen recycle stream conduit; (b) a reaction zone inlet stream conduit in communication with said charge stock inlet conduit and a reaction zone, said inlet stream conduit having a means to sense the partial pressure of hydrogen contained therein; (c) a reaction zone for reacting hydrocarbonaceous materials contained within said charge stream to produce a converted hydrocarbon product stream; (d) a cooling zone in communication with said reaction zone via a reaction zone effluent conduit to cool and condense said effluent from said reaction zone to a liquid hydrocarbon product stream and at least a portion of said vaporous hydrocarbon-hydrogen recycle stream; (e) a gas-liquid separation zone in communication with said cooling zone via a cooling zone effluent conduit to exorcise said liquid hydrocarbon product stream from said vaporous hydrocarbon-hydrogen recycle stream; and (f) a compressor means having a variable output capability and in communication with said separation zone and said charge stock inlet of element (a); said control system consisting of: (i) means for sensing the partial pressure of hydrogen at a point within the reaction inlet stream conduit of step (b); (ii) comparison means for comparing said partial pressure of hydrogen to a previously determined value and developing a signal correlating thereto; (iii) transmission means for transmitting said signal of step (ii) to said variable output compressor; and (iv) regulating means for controlling the quantity of flow of vaporous hydrocarbon and hydrogen recycle to said reaction zone based on the partial pressure sensed in said reaction inlet stream conduit.
Claim 9
Dependent Claim
280 words
A control system for modifying the flow of hydrogen in a hydrocarbonaceous conversion apparatus, said apparatus which comprises: (a) a charge stock inlet conduit in interconnection with a vaporous hydrocarbon-hydrogen recycle stream conduit; (b) a reaction zone inlet stream conduit in communication with said charge stock inlet conduit and a reaction zone, said inlet stream conduit having a means to sense the partial pressure of hydrogen contained therein; (c) a reaction zone for reacting hydrocarbonaceous materials contained within said charge stream to produce a converted hydrocarbon product stream; (d) a cooling zone in communication with said reaction zone via a reaction zone effluent conduit to cool and condense said effluent from said reaction zone to a liquid hydrocarbon product stream and at least a portion of said vaporous hydrocarbon-hydrogen recycle stream; (e) a gas-liquid separation zone in communication with said cooling zone via a cooling zone effluent conduit to exorcise said liquid hydrocarbon product stream from said vaporous hydrocarbon-hydrogen recycle stream; and (f) a compressor means having a variable output capability and in communication with said separation zone and said charge stock inlet of element (a); said control system consisting of: (i) means for sensing the partial pressure of hydrogen at a point within the reaction inlet stream conduit of step (b); (ii) comparison means for comparing said partial pressure of hydrogen to a previously determined value and developing a signal correlating thereto; (iii) transmission means for transmitting said signal of step (ii) to said variable output compressor; and (iv) regulating means for controlling the quantity of flow of vaporous hydrocarbon and hydrogen recycle to said reaction zone based on the partial pressure sensed in said reaction inlet stream conduit.
Claim 10
Dependent Claim
18 words
The control system of claim 7 further characterized in that said reaction zone is a catalytic reforming unit.
Claim 11
Dependent Claim
17 words
The control system of claim 7 further characterized in that said reaction zone is a dehydrogenation unit.
References Cited (Backward Citations)
US3497449A
Cited
US3649202A
Cited
US3607091A
Cited
US3656911A
Cited
US3972804A
Cited
US3974064A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-10-16 | 1988-04-16 | 1988-10-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-10-16 | 1992-04-16 | 1992-10-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-10-16 | 1996-04-16 | 1996-10-16 | $7700.00 | Window Closed / Lapsed |