US5224336A
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US
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Process and system for controlling a cryogenic air separation unit during rapid changes in production
Assignee: Air Products and Chemicals Inc
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Filing: 1991-06-20
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Granted: 1993-07-06
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Expires: 2011-06-20
Abstract
Abstract A process and system for controlling a cryogenic air separation unit during rapid changes in production. During operation of an air separation unit, demands for oxygen will vary and the pressure of the feed air will fluctuate. The changes in oxygen demand and feed air pressure translate into a ramping, either up or down, of the distillation system pressure in the air separation unit. Because the product streams have tight purity requirements, the ramping system pressure (which could adversely affect product purity) is compensated for. This compensation is by way of a net transfer of refrigeration, in the form of liquid nitrogen, into and out of the distillation system. This transfer of refrigeration is implemented using a storage vessel of liquid nitrogen connected to the reflux path of the distillation system. Liquid nitrogen via the reflux path is removed and stored or added to the distillation system to decrease or increase the refrigeration, respectively.
Inventors
- 👤 Rakesh Agrawal
- 👤 David M. Espie
- 👤 Declan P. O'Connor
- 👤 Jorge A. Mandler
- 👤 Arthur R. Smith
- 👤 Donald W. Woodward
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 12:52
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04521; F25J3/04593; F25J3/046; F25J3/04248; F25J3/04333; F25J3/04351; F25J3/04406; F25J3/04412; F25J3/04472; F25J3/04478; F25J3/0449; F25J3/04527; F25J3/04539; F25J3/04545; F25J3/04563; F25J3/04763; F25J3/04769; F25J3/04848; F25J2245/00; F25J2245/42; F25J2290/00; F25J2290/10; F25J2290/62
Claims Analysis
Total Claims: 26
Claim 1
Independent Claim
100 words
In a process for the separation of feed air in a cryogenic distillation system having at least one distillation column wherein feed air is separated into at least oxygen-rich and nitrogen-rich products, the improvement for substantially maintaining purity requirements during variations in product demand and feed air pressure comprising the steps of: a) removing and storing refrigeration in the form of nitrogen-rich fluid from the distillation system as the feed air pressure substantially increases; and b) adding refrigeration in the form of nitrogen-rich fluid to the distillation system from the stored nitrogen-rich fluid as the feed air pressure substantially decreases.
Claim 2
Dependent Claim
100 words
In a process for the separation of feed air in a cryogenic distillation system having at least one distillation column wherein feed air is separated into at least oxygen-rich and nitrogen-rich products, the improvement for substantially maintaining purity requirements during variations in product demand and feed air pressure comprising the steps of: a) removing and storing refrigeration in the form of nitrogen-rich fluid from the distillation system as the feed air pressure substantially increases; and b) adding refrigeration in the form of nitrogen-rich fluid to the distillation system from the stored nitrogen-rich fluid as the feed air pressure substantially decreases.
Claim 3
Dependent Claim
36 words
The process of claim 1, in which steps a) and b) further include the step of providing for removing, storing, and adding refrigeration by way of a reflux flow of nitrogen-rich fluid in the distillation system.
Claim 4
Dependent Claim
44 words
The process of claim 2, in which the step of storing refrigeration further includes storing the refrigeration in a storage vessel, and there is provided the further steps of controlling the reflux flow upstream and controlling the reflux flow downstream of the storage vessel.
Claim 5
Dependent Claim
21 words
The process of claim 1, in which the step of storing refrigeration further includes storing the refrigeration in a storage vessel.
Claim 6
Dependent Claim
40 words
The process of claim 1, wherein said distillation system is a double column system including a high pressure distillation column, a low pressure distillation column, and a reflux path flowing from the high pressure column to the low pressure column.
Claim 7
Dependent Claim
37 words
The process of claim 5, in which step a) further includes the step of decreasing the flow of nitrogen-rich product from the low pressure distillation column proportional to feed air flow as the feed air pressure increases.
Claim 8
Dependent Claim
37 words
The process of claim 5, in which step b) further includes the step of increasing the flow of nitrogen-rich product from the low pressure distillation column proportional to feed air flow as the feed air pressure decreases.
Claim 9
Dependent Claim
14 words
The process of claim 1, wherein said nitrogen-rich fluid is at least 90% nitrogen.
Claim 10
Dependent Claim
127 words
In a process for the separation of air in a cryogenic distillation system having at least one distillation column where air is separated into at least oxygen-rich and nitrogen-rich products, the improvement for substantially maintaining purity requirements upon (1) increase in product demand and increase in feed air pressure and (2) decrease in product demand and decrease in feed air pressure comprising the steps of: (a) providing a reflux flow of nitrogen-rich fluid in the distillation system; (b) removing and storing a portion of the nitrogen-rich reflux flow fluid as the product demand increases and the feed air pressure substantially increases, and (c) adding to the reflux flow a portion of the stored nitrogen-rich fluid as the product demand decreases and the feed air pressure substantially decreases.
Claim 11
Dependent Claim
127 words
In a process for the separation of air in a cryogenic distillation system having at least one distillation column where air is separated into at least oxygen-rich and nitrogen-rich products, the improvement for substantially maintaining purity requirements upon (1) increase in product demand and increase in feed air pressure and (2) decrease in product demand and decrease in feed air pressure comprising the steps of: (a) providing a reflux flow of nitrogen-rich fluid in the distillation system; (b) removing and storing a portion of the nitrogen-rich reflux flow fluid as the product demand increases and the feed air pressure substantially increases, and (c) adding to the reflux flow a portion of the stored nitrogen-rich fluid as the product demand decreases and the feed air pressure substantially decreases.
Claim 12
Dependent Claim
40 words
The process of claim 9, wherein said distillation system is a double column system including a high pressure distillation column, a low pressure distillation column, and a reflux path flowing from the high pressure column to the low pressure column.
Claim 13
Dependent Claim
37 words
The process of claim 10, in which step (b) further includes the step of decreasing the flow of nitrogen-rich product from the low pressure distillation column proportional to feed air flow as the feed air pressure increases.
Claim 14
Dependent Claim
37 words
The process of claim 10, in which step (c) further includes the step of increasing the flow of nitrogen-rich product from the low pressure distillation column proportional to feed air flow as the feed air pressure decreases.
Claim 15
Dependent Claim
54 words
The process of claim 9, wherein said distillation system is a double column system including a high pressure distillation column and a low pressure distillation column, in which there is provided the further step of recycling a portion of the nitrogen-rich product from the low pressure distillation column to the high pressure distillation column.
Claim 16
Dependent Claim
37 words
The process of claim 13, in which there is provided the further step of controlling the recycling of the portion of nitrogen-rich product for maintaining the purity of the nitrogen-rich product from the low pressure distillation column.
Claim 17
Dependent Claim
141 words
A cryogenic distillation system having at least one distillation column for separating air into at least oxygen-rich and nitrogen-rich products for an integrated gasifier combined cycle power plant (IGCC) in which purity requirements are maintained during variations in product demand by the IGCC and during variations of feed air pressure comprising: reflux flow means for said distillation system for providing reflux flow of nitrogen-rich fluid; storage means coupled to said reflux flow means for storing nitrogen-rich fluid; and means for controlling the reflux flow (1) for removing nitrogen-rich fluid from the reflux flow means and storing said removed nitrogen-rich fluid in said storage means as the product demand and the feed air pressure substantially increases and (2) for adding nitrogen-rich fluid from the storage means to the reflux flow means as the product demand and the feed air pressure substantially decreases.
Claim 18
Dependent Claim
141 words
A cryogenic distillation system having at least one distillation column for separating air into at least oxygen-rich and nitrogen-rich products for an integrated gasifier combined cycle power plant (IGCC) in which purity requirements are maintained during variations in product demand by the IGCC and during variations of feed air pressure comprising: reflux flow means for said distillation system for providing reflux flow of nitrogen-rich fluid; storage means coupled to said reflux flow means for storing nitrogen-rich fluid; and means for controlling the reflux flow (1) for removing nitrogen-rich fluid from the reflux flow means and storing said removed nitrogen-rich fluid in said storage means as the product demand and the feed air pressure substantially increases and (2) for adding nitrogen-rich fluid from the storage means to the reflux flow means as the product demand and the feed air pressure substantially decreases.
Claim 19
Dependent Claim
31 words
The system of claim 15, in which said storage means comprises a storage vessel and which further comprises means for controlling the reflux flow upstream and downstream of the storage vessel.
Claim 20
Dependent Claim
182 words
In a process for the separation of air in a double column cryogenic distillation system having a low pressure column, a high pressure column, and reflux flows from the high pressure column to the low pressure column wherein air is separated into at least oxygen-rich and nitrogen-rich products, the improvement for substantially maintaining purity requirements during variations in product demand and feed air pressure comprising the steps of: (a) upon an increase in oxygen product demand, increasing feed air pressure and decreasing flow of nitrogen-rich product from the low pressure column, thereby increasing the pressure in the low pressure column; (b) upon a decrease in oxygen product demand, decreasing feed air pressure and increasing flow of nitrogen-rich product from the low pressure column, thereby decreasing the pressure in the low pressure column; (c) removing and storing a portion of the nitrogen-rich reflux flow fluid as the product demand increases and the feed air pressure substantially increases; and (d) adding to the reflux flow a portion of the stored nitrogen-rich fluid as the product demand decreases and the feed air pressure substantially decreases.
Claim 21
Dependent Claim
182 words
In a process for the separation of air in a double column cryogenic distillation system having a low pressure column, a high pressure column, and reflux flows from the high pressure column to the low pressure column wherein air is separated into at least oxygen-rich and nitrogen-rich products, the improvement for substantially maintaining purity requirements during variations in product demand and feed air pressure comprising the steps of: (a) upon an increase in oxygen product demand, increasing feed air pressure and decreasing flow of nitrogen-rich product from the low pressure column, thereby increasing the pressure in the low pressure column; (b) upon a decrease in oxygen product demand, decreasing feed air pressure and increasing flow of nitrogen-rich product from the low pressure column, thereby decreasing the pressure in the low pressure column; (c) removing and storing a portion of the nitrogen-rich reflux flow fluid as the product demand increases and the feed air pressure substantially increases; and (d) adding to the reflux flow a portion of the stored nitrogen-rich fluid as the product demand decreases and the feed air pressure substantially decreases.
Claim 22
Dependent Claim
41 words
The process of claim 17, in which there is provided the further step of measuring the purity of the oxygen-rich product from the low pressure column and controlling the feed air pressure as a function of the oxygen product purity measurement.
Claim 23
Dependent Claim
46 words
The process of claim 17, in which there is provided the further step of measuring the purity of the nitrogen-rich product from the low pressure column and controlling a portion of the nitrogen-rich product from the low pressure column as a function of the purity measurement.
Claim 24
Dependent Claim
33 words
The process of claim 17, in which there is provided the further step of measuring the purity of the reflux flow and controlling the reflux flow as a function of the purity measurement.
Claim 25
Dependent Claim
35 words
The process of claim 1 wherein step a) includes removing and storing refrigeration in the form of nitrogen-rich liquid from the distillation system as the feed air pressure increases by at least 3% per minute.
Claim 26
Dependent Claim
33 words
The process of claim 21 wherein step b) includes adding refrigeration in the form of nitrogen-rich liquid to the distillation system as the feed air pressure decreases by at least 3% per minute.
References Cited (Backward Citations)
US3208230A
Cited
US3731495A
Cited
US3912476A
Cited
US4251248A
Cited
US4224045A
Cited
US4529425A
Cited
US4617040A
Cited
US4732595A
Cited
US5084081A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1996-07-05 | 1997-01-04 | 1997-07-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2000-07-05 | 2001-01-04 | 2001-07-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2004-07-05 | 2005-01-04 | 2005-07-06 | $7700.00 | Window Closed / Lapsed |