US4479189A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Utility and hydrogen conservation in hydrogen recycle processes
Assignee: Honeywell UOP LLC
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Filing: 1984-10-23
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Granted: 1984-10-23
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Expires: 2004-10-23
Abstract
Abstract There is disclosed a system for measuring and controlling the concentration of hydrogen in hydrogen-consuming hydrogen recycle processes used in oil refineries and petrochemical plants. The system is intended to reduce utilities and hydrogen usage by means of adjusting vent gas flow and the quantity of hydrogen and hydrocarbon vapor circulating to obtain the operating parameters which yield minimum cost. Specifically there can be a savings of compressor power, fuel required for heating, and hydrogen. The system is dependent on the recognition that a decrease in cooling medium temperature results in an increase in hydrogen flow, which can be decreased to the minimum permissible without endangering catalyst activity and stability and product yield if hydrogen concentration is monitored, that partial pressure is the key parameter, and that it is advantageous to optimize.
Inventors
- 👤 Don B. Carson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 06:06
CPC Classifications
C; C10; C10G; C10G49/00; C10G49/26; G; G06; G06Q; G06Q50/00; G06Q50/06; Y; Y10; Y10S; Y10S208/00; Y10S208/01
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
351 words
In a hydrocarbon processing unit controlled by computer means and means for monitoring process variables, said unit comprising heater means, reactor means, cooler means, gas-liquid separator means, and compressor means, wherein a charge stock stream comprising hydrocarbons is combined with a recycle stream comprising hydrogen and hydrocarbon vapors to form a feed stream which is heated in said heater means and then charged to said reactor means, wherein an effluent stream from said reactor means is cooled in said cooler means so that it is separated into a liquid product stream and a hydrogen and hydrocarbon vapor stream in said gas-liquid separator means, wherein at least a portion of said hydrogen and hydrocarbon vapor stream is recycled through said compressor means to said heater means and reactor means to serve as a portion of said feed stream, wherein a vent gas stream consisting of a portion of said hydrogen and hydrocarbon vapor stream is removed from said hydrocarbon processing unit, wherein it is desirable to maintain the hydrogen concentration in said reactor means at or above a certain minimum value, a method of using lesser quantities of utilities and hydrogen, which method comprises the following steps: (a) providing the concentration of hydrogen in said hydrocarbon processing unit to said computer means; (b) comparing, in said computer means, said concentration of hydrogen to a previously established value; (c) providing monitored process variables from said processing unit to said computer means; (d) calculating in said computer means the values of compressor output and vent gas flow which satisfy the conditions that said hydrogen concentration is equal to said previously established value and that said unit is operating at a minimum cost, said cost being based on: (i) fuel supplied to said heater means, (ii) power supplied to said compressor means, (iii) the quantity of hydrogen supplied to said processing unit minus a credit for hydrogen removed from said processing unit in said vent gas stream; (e) adjusting compressor output and vent gas flow to the calculated values; and, (f) continuously repeating steps (a) through (e) as process measurements used in said calculation vary.
Claim 2
Dependent Claim
351 words
In a hydrocarbon processing unit controlled by computer means and means for monitoring process variables, said unit comprising heater means, reactor means, cooler means, gas-liquid separator means, and compressor means, wherein a charge stock stream comprising hydrocarbons is combined with a recycle stream comprising hydrogen and hydrocarbon vapors to form a feed stream which is heated in said heater means and then charged to said reactor means, wherein an effluent stream from said reactor means is cooled in said cooler means so that it is separated into a liquid product stream and a hydrogen and hydrocarbon vapor stream in said gas-liquid separator means, wherein at least a portion of said hydrogen and hydrocarbon vapor stream is recycled through said compressor means to said heater means and reactor means to serve as a portion of said feed stream, wherein a vent gas stream consisting of a portion of said hydrogen and hydrocarbon vapor stream is removed from said hydrocarbon processing unit, wherein it is desirable to maintain the hydrogen concentration in said reactor means at or above a certain minimum value, a method of using lesser quantities of utilities and hydrogen, which method comprises the following steps: (a) providing the concentration of hydrogen in said hydrocarbon processing unit to said computer means; (b) comparing, in said computer means, said concentration of hydrogen to a previously established value; (c) providing monitored process variables from said processing unit to said computer means; (d) calculating in said computer means the values of compressor output and vent gas flow which satisfy the conditions that said hydrogen concentration is equal to said previously established value and that said unit is operating at a minimum cost, said cost being based on: (i) fuel supplied to said heater means, (ii) power supplied to said compressor means, (iii) the quantity of hydrogen supplied to said processing unit minus a credit for hydrogen removed from said processing unit in said vent gas stream; (e) adjusting compressor output and vent gas flow to the calculated values; and, (f) continuously repeating steps (a) through (e) as process measurements used in said calculation vary.
Claim 3
Dependent Claim
29 words
The method of claim 1 further characterized with respect to step (a) in that the concentration of hydrogen in said processing unit is expressed in terms of partial pressure.
Claim 4
Dependent Claim
35 words
The method of claim 1 further characterized with respect to step (a) in that the concentration of hydrogen in said hydrocarbon processing unit is obtained by means of an apparatus which directly measures partial pressure.
Claim 5
Dependent Claim
58 words
The method of claim 1 further characterized with respect to step (a) in that the concentration of hydrogen in said hydrocarbon processing unit is obtained by means of measuring the total pressure of said feed stream, measuring the mole fraction of hydrogen in said feed stream, then multiplying mole fraction times total pressure, the product being partial pressure.
Claim 6
Dependent Claim
17 words
The method of claim 1 further characterized in that said hydrocarbon processing unit is a hydrogenation unit.
Claim 7
Dependent Claim
17 words
The method of claim 1 further characterized in that said hydrocarbon processing unit is a hydrodealkylation unit.
Claim 8
Dependent Claim
17 words
The method of claim 1 further characterized in that said hydrocarbon processing unit is a hydrodesulfurization unit.
Claim 9
Dependent Claim
17 words
The method of claim 1 further characterized in that said hydrocarbon processing unit is a hydrocracking unit.
Claim 10
Dependent Claim
17 words
The method of claim 1 further characterized in that said hydrocarbon processing unit is an isomerization unit.
Claim 11
Dependent Claim
312 words
In a hydrocarbon processing unit comprising computer means, heater means, reactor means, cooler means, gas-liquid separator means, and compressor means, wherein a charge stock stream comprising hydrocarbons is combined with a recycle stream comprising hydrogen and hydrocarbon vapors to form a feed stream which is heated in said heater means and then charged to said reactor means, wherein an effluent stream from said reactor means is cooled in said cooler means so that it is separated into a liquid product stream and a hydrogen and hydrocarbon vapor stream in said gas-liquid separator means, wherein at least a portion of said hydrogen and hydrocarbon vapor stream is recycled through said compressor means to said heater means and reactor means to serve as a portion of said feed stream, wherein a vent gas stream consisting of a portion of said hydrogen and hydrocarbon vapor stream is removed from said hydrocarbon processing unit, wherein it is desirable to maintain the hydrogen concentration in said reactor means at or above a certain minimum value, a control system for using lesser quantities of utilities and hydrogen in the operation of said hydrocarbon processing unit comprising, in cooperative combination: (a) means for monitoring process variables in said hydrocarbon processing unit and providing signals representative of said variables to said computer means; (b) said computer means for continuously calculating the values of compressor output and vent gas flow which satisfy conditions that said hydrogen concentration is equal to a previously established variable and that said unit is operating at minimum cost, said cost being based upon: (i) fuel supplied to said heater means, (ii) power supplied to said compressor means, (iii) the quantity of hydrogen supplied to said processing unit minus a credit for hydrogen removed from said processing unit in said vent gas stream; (c) means for adjusting compressor output and vent gas flow to the calculated values.
Claim 12
Dependent Claim
312 words
In a hydrocarbon processing unit comprising computer means, heater means, reactor means, cooler means, gas-liquid separator means, and compressor means, wherein a charge stock stream comprising hydrocarbons is combined with a recycle stream comprising hydrogen and hydrocarbon vapors to form a feed stream which is heated in said heater means and then charged to said reactor means, wherein an effluent stream from said reactor means is cooled in said cooler means so that it is separated into a liquid product stream and a hydrogen and hydrocarbon vapor stream in said gas-liquid separator means, wherein at least a portion of said hydrogen and hydrocarbon vapor stream is recycled through said compressor means to said heater means and reactor means to serve as a portion of said feed stream, wherein a vent gas stream consisting of a portion of said hydrogen and hydrocarbon vapor stream is removed from said hydrocarbon processing unit, wherein it is desirable to maintain the hydrogen concentration in said reactor means at or above a certain minimum value, a control system for using lesser quantities of utilities and hydrogen in the operation of said hydrocarbon processing unit comprising, in cooperative combination: (a) means for monitoring process variables in said hydrocarbon processing unit and providing signals representative of said variables to said computer means; (b) said computer means for continuously calculating the values of compressor output and vent gas flow which satisfy conditions that said hydrogen concentration is equal to a previously established variable and that said unit is operating at minimum cost, said cost being based upon: (i) fuel supplied to said heater means, (ii) power supplied to said compressor means, (iii) the quantity of hydrogen supplied to said processing unit minus a credit for hydrogen removed from said processing unit in said vent gas stream; (c) means for adjusting compressor output and vent gas flow to the calculated 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) | 1987-10-23 | 1988-04-23 | 1988-10-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-10-23 | 1992-04-23 | 1992-10-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-10-23 | 1996-04-23 | 1996-10-23 | $7700.00 | Window Closed / Lapsed |