US4653572A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Dual-zone boiling process
Assignee: Air Products and Chemicals Inc
•
Filing: 1986-03-11
•
Granted: 1987-03-31
•
Expires: 2006-03-11
Abstract
Abstract The invention relates to a process and apparatus for boiling flowing liquid such as liquefied gases in a heat exchanger in which a circulating flow is occuring, such as in reboiler-condensers in air separation and similar cryogenic plants or other applications where a high efficiency for boiling heat transfer is beneficial. The important feature of the process and apparatus is the use of two sequential heat transfer zones having different pressure drop and heat transfer characteristics in the same boiling channel, the first zone having a higher pressure drop and high convective heat transfer characteristic and the second zone having a lower pressure drop and an enhanced nucleate boiling heat transfer characteristic.
Inventors
- 👤 Douglas L. Bennett
- 👤 Alexander Schwarz
- 👤 Robert M. Thorogood
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 21:46
CPC Classifications
F; F25; F25J; F25J5/00; F28; F28F; F28F13/00; F28F13/18; F28F13/185; F28F13/187; F25J3/00; F25J3/02; F25J3/04; F25J3/04406; F25J3/04412; F25J5/002; F25J5/005; F28F13/14; F25J2250/00; F25J2250/02; F25J2290/00; F25J2290/44; Y; Y10; Y10S; Y10S165/00; Y10S165/911
Claims Analysis
Total Claims: 25
Claim 1
Independent Claim
104 words
In a process for boiling flowing liquids in a heat exchanger wherein said flowing liquid is heated in a single heat exchanger to vaporize said liquid, the improvement of which comprises: (a) passing said boiling flowing liquid through a first heat transfer zone of said heat exchanger comprising a surface with a high-convective-heat-transfer characteristic and a higher pressure drop characteristic; and then (b) passing said boiling flowing liquid through a second heat transfer zone of said heat exchanger comprising an essentially open channel with only minor obstructions by secondary surfaces, with an enhanced nucleate boiling heat transfer surface and a lower pressure drop characteristic.
Claim 2
Dependent Claim
104 words
In a process for boiling flowing liquids in a heat exchanger wherein said flowing liquid is heated in a single heat exchanger to vaporize said liquid, the improvement of which comprises: (a) passing said boiling flowing liquid through a first heat transfer zone of said heat exchanger comprising a surface with a high-convective-heat-transfer characteristic and a higher pressure drop characteristic; and then (b) passing said boiling flowing liquid through a second heat transfer zone of said heat exchanger comprising an essentially open channel with only minor obstructions by secondary surfaces, with an enhanced nucleate boiling heat transfer surface and a lower pressure drop characteristic.
Claim 3
Dependent Claim
14 words
The process of claim 1 wherein said heat exchanger is a thermosyphon heat exchanger.
Claim 4
Dependent Claim
16 words
The process of claim 1 wherein said heat exchanger is a shell and tube heat exchanger.
Claim 5
Dependent Claim
15 words
The process of claim 1 wherein said heat exchanger is a plate-fin brazed heat exchanger.
Claim 6
Dependent Claim
31 words
The process of claim 1 wherein the length of said first heat transfer zone is in the range of 10 percent to 60 percent of total length of said heat exchanger.
Claim 7
Dependent Claim
31 words
The process of claim 1 wherein the length of said first heat transfer zone is in the range of 20 percent to 40 percent of total length of said heat exchanger.
Claim 8
Dependent Claim
19 words
The process of claim 1 wherein said enhanced nucleate boiling heat transfer surface is a bonded high-porosity porous metal.
Claim 9
Dependent Claim
18 words
The process of claim 1 wherein said enhanced nucleate boiling heat transfer surface is a mechanically formed surface.
Claim 10
Dependent Claim
32 words
The process of claim 1 wherein said enhanced nucleate boiling heat transfer surface has a heat transfer coefficient greater than or equal to three times greater than for a corresponding flat plate.
Claim 11
Dependent Claim
27 words
The process of claim 1 wherein the length of said first heat transfer zone is that required to completely preheat a boiling liquid to its saturation temperature.
Claim 12
Dependent Claim
83 words
A heat exchanger for boiling flowing liquids, the improvement of which comprises the incorporation of two sequential heat transfer zones of different characteristics in a single exchanger, said heat exchanger comprising: (a) a first heat transfer zone comprising a surface with a high-convective-heat-transfer characteristic and a higher pressure drop characteristic; and (b) a second heat transfer zone comprising an essentially open channel with only minor obstructions by secondary surfaces, with an enhanced nucleate boiling heat transfer surface and a lower pressure drop characteristic.
Claim 13
Dependent Claim
83 words
A heat exchanger for boiling flowing liquids, the improvement of which comprises the incorporation of two sequential heat transfer zones of different characteristics in a single exchanger, said heat exchanger comprising: (a) a first heat transfer zone comprising a surface with a high-convective-heat-transfer characteristic and a higher pressure drop characteristic; and (b) a second heat transfer zone comprising an essentially open channel with only minor obstructions by secondary surfaces, with an enhanced nucleate boiling heat transfer surface and a lower pressure drop characteristic.
Claim 14
Dependent Claim
15 words
The heat exchanger of claim 11 wherein said heat exchanger is a thermosyphon heat exchanger.
Claim 15
Dependent Claim
17 words
The heat exchanger of claim 11 wherein said heat exchanger is a shell and tube heat exchanger.
Claim 16
Dependent Claim
16 words
The heat exchanger of claim 11 wherein said heat exchanger is a plate-fin brazed heat exchanger.
Claim 17
Dependent Claim
32 words
The heat exchanger of claim 11 wherein the length of said first heat transfer zone is in the range of 10 percent to 60 percent of total length of said heat exchanger.
Claim 18
Dependent Claim
32 words
The heat exchanger of claim 11 wherein the length of said first heat transfer zone is in the range of 20 percent to 40 percent of total length of said heat exchanger.
Claim 19
Dependent Claim
20 words
The heat exchanger of claim 11 wherein said enhanced nucleate boiling heat transfer surface is a bonded high-porosity porous metal.
Claim 20
Dependent Claim
19 words
The heat exchanger of claim 11 wherein said enhanced nucleate boiling heat transfer surface is a mechanically formed surface.
Claim 21
Dependent Claim
33 words
The heat exchanger of claim 11 wherein said enhanced nucleate boiling heat transfer surface has a heat transfer coefficient greater than or equal to three times greater than for a corresponding flat plate.
Claim 22
Dependent Claim
28 words
The heat exchanger of claim 11 wherein the length of said first heat transfer zone is that required to completely preheat a boiling liquid to its saturation temperature.
Claim 23
Dependent Claim
121 words
In a process for the separation of air into its constituent oxygen and nitrogen components, wherein a single heat exchanger is utilized to heat a nitrogen-rich liquid or an oxygen-rich liquid so as to vaporize said nitrogen-rich liquid or oxygen-rich liquid, the improvement comprising: (a) passing said nitrogen-rich liquid or oxygen-rich liquid through a first heat transfer zone of said heat exchanger comprising a surface with a high-convective-heat-tranfer characteristic and a higher pressure drop characteristic; and then (b) passing said nitrogen-rich liquid or oxygen-rich liquid through a second heat transfer zone of said heat exchanger comprising an essentially open channel with only minor obstruction by secondary surfaces, with an enhanced nucleate boiling heat transfer surface and a lower pressure drop characteristic.
Claim 24
Dependent Claim
121 words
In a process for the separation of air into its constituent oxygen and nitrogen components, wherein a single heat exchanger is utilized to heat a nitrogen-rich liquid or an oxygen-rich liquid so as to vaporize said nitrogen-rich liquid or oxygen-rich liquid, the improvement comprising: (a) passing said nitrogen-rich liquid or oxygen-rich liquid through a first heat transfer zone of said heat exchanger comprising a surface with a high-convective-heat-tranfer characteristic and a higher pressure drop characteristic; and then (b) passing said nitrogen-rich liquid or oxygen-rich liquid through a second heat transfer zone of said heat exchanger comprising an essentially open channel with only minor obstruction by secondary surfaces, with an enhanced nucleate boiling heat transfer surface and a lower pressure drop characteristic.
Claim 25
Dependent Claim
14 words
The process of claim 21 wherein said heat exchanger is a thermosyphon heat exchanger.
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) | 1990-03-30 | 1990-09-29 | 1991-03-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-03-30 | 1994-09-29 | 1995-03-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-03-30 | 1998-09-29 | 1999-03-31 | $7700.00 | Window Closed / Lapsed |