US20050092472A1 - Heat exchange system - Google Patents
Heat exchange system Download PDFInfo
- Publication number
- US20050092472A1 US20050092472A1 US10/700,805 US70080503A US2005092472A1 US 20050092472 A1 US20050092472 A1 US 20050092472A1 US 70080503 A US70080503 A US 70080503A US 2005092472 A1 US2005092472 A1 US 2005092472A1
- Authority
- US
- United States
- Prior art keywords
- working fluid
- tube
- heat
- finned
- exchanger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 238000000034 method Methods 0.000 claims abstract description 20
- 239000012530 fluid Substances 0.000 claims description 82
- 238000011084 recovery Methods 0.000 claims description 11
- 238000001816 cooling Methods 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 5
- 230000037361 pathway Effects 0.000 claims description 4
- 238000010276 construction Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000003345 natural gas Substances 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000010960 commercial process Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/0408—Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids
- F28D1/0426—Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids with units having particular arrangement relative to the large body of fluid, e.g. with interleaved units or with adjacent heat exchange units in common air flow or with units extending at an angle to each other or with units arranged around a central element
- F28D1/0435—Combination of units extending one behind the other
Definitions
- This invention pertains to the field of heat exchange and specifically to a more efficient design of heat exchangers.
- Plate fin and tube heat exchangers or externally finned tube exchangers have long been employed to recover process heat. These exchangers are most often employed to heat or cool a low density gas stream located on the finned side against a denser fluid with higher heat transfer coefficient within the tubes.
- the extended surface on the finned exterior pass allows greater heat transfer surface than a bare tube and provides greater heat transfer at a low-pressure drop.
- a method for operating a heat exchanger of the plate fin and tube or finned tube type that can be used in heat transfer system that comprises:
- the invention may be described as a method of recovering energy that comprises:
- Fluids of the same or different composition may be used.
- An alternative embodiment is a method of construction of a heat exchanger that comprises providing a plurality of circulation paths in a plate fin and tube or finned tube exchanger utilizing a plurality of tube side circuits that are interlaced to accomplish more effective heat transfer than would be possible with a plurality of tube side fluid streams arranged in series without interlacing the circuitry.
- first working fluid and the second working fluid have the same composition or the working fluids may be of different composition.
- the invention may also be described as an energy recovery apparatus specially designed to practice the methods described above that comprises:
- the inventive concept may also be embodied as a method for an energy recovery system for increasing the efficiency of a gas turbine exhaust heat recovery by providing an integrated tube side heating circuitry to heat a plurality of working fluid circuits while cooling the exhaust stream of the gas turbine.
- the invention provides a system for more efficient heat transfer in a plate fin and tube or finned tube exchanger by providing a plurality of separate working fluids in a plurality of working fluid circulation paths.
- FIG. 1 is a sketch of a typical integrated coil having two working fluids in separate circuits.
- FIG. 2 is a sketch of an integrated coil having 4 working fluids with interwoven circuitry.
- the invention provides a method of interweaving streams with various working fluids in a common plate fin and tube or finned tube exchanger to accomplish more efficient heat transfer.
- the invention may be employed to increase the hear recovery efficiency of any gas turbine or other device that produces a waste heat exhaust or is a source of process heat.
- the arrangement may produce more efficient refrigeration at locations requiring refrigeration or cooling.
- FIG. 1 a simple two fluid system is shown.
- the principals illustrated in the more complex system also apply to the two fluid system of FIG. 1 .
- a first working fluid consisting of 88.67 mol % N2 and 11.32 mol % H2O enters the heat exchanger at 263.2F, 366.5 psia, 18,946 moles/hr and leaves the exchanger at 101.9 F, 363.3 psia. It exchanges heat with a 2 nd working fluid, natural gas in this illustration, entering at 45.6 F, 512 psia, 4460 moles/hr and leaving at 241.5 F, 501 psia.
- the first working fluid also exchanges heat with a 3 rd working fluid, water, entering at 74.4 F, 61 psia, 17660 moles/hr and leaving at 209.5 F, 42.8 psia.
- the first working fluid also exchanges heat with a 4 th working fluid, water, entering at 92 F, 54.7 psia, 20,900 moles/hr and leaving at 107 F, 44.7 psia.
- the exchanger is modeled with fluid separation and removal after each heat exchange zone as can be accomplished with the invention device. Under the invention integrated heat exchange design, the total UA required is 934,180 BTU/F-hr.
- the total UA required to accomplish the same leaving working fluid 1 temperature is 1,127900 BTU/F-hr.
- the flow-rate of the 4 th working fluid is increased from 20,900 moles/hr to 25,760 moles/hr. Since UA is the heat transfer coefficient times the required heat transfer area, one can assume the heat transfer coefficient is essentially the same. Therefore the invention integrated heat exchanger design using the interwoven heat transfer zones can achieve the same desired working fluid 1 exit temperature with 20.7% less heat transfer area.
- the working fluids may be any available fluid that can be circulated at pressures within the design limits of the selected exchanger and will be selected depending on available fluids at the site. They may include multiple streams of the same fluid at different temperatures and pressures (such as water in example 1) or the fluids may be different (such as natural gas, working fluid 2 in the example).
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention provides a method and apparatus for integrating the heat transfer zones of plate fin and tube and finned tube exchangers by providing a plurality of heat exchange circulation paths within a single heat exchange zone of a heat exchanger.
Description
- This invention pertains to the field of heat exchange and specifically to a more efficient design of heat exchangers.
- Plate fin and tube heat exchangers or externally finned tube exchangers have long been employed to recover process heat. These exchangers are most often employed to heat or cool a low density gas stream located on the finned side against a denser fluid with higher heat transfer coefficient within the tubes. The extended surface on the finned exterior pass allows greater heat transfer surface than a bare tube and provides greater heat transfer at a low-pressure drop.
- The art has not heretofore recognized the unexpected advantage of using multiple process streams on the tube side of one or more heat exchangers and interlacing the heat transfer zones to allow more effective heat transfer was not recognized in the art. Kohlenberger U.S. Pat. Nos. 5,790,972 and 5,444,971 disclose inlet cooling of a gas turbine using zones in series, but do not suggest the advantages of integrating the fluid circuits into one heat exchange zone.
- The invention may be described in several ways as alternate embodiments of the same novel discovery.
- A method for operating a heat exchanger of the plate fin and tube or finned tube type that can be used in heat transfer system that comprises:
-
- a. providing a first working fluid on the finned exterior side of the heat transfer device,
- b. providing two or more working fluids flowing in separate circuits within the tube circuits of the heat transfer device,
- c. feeding the first working fluid to the exterior finned side of a heat transfer zone or zones to transfer heat to or from the first working fluid thereby heating or cooling the first working fluid to a higher or lower temperature,
- d. feeding the second working fluid into a tube or group of tubes to be heated or cooled by the first working fluid,
- e. feeding a third or more working fluid(s) into a tube or group of tubes to be heated or cooled by the first or second working fluid.
- f. the multiple tube circuits being interwoven to more effectively approach the cooling curve of the finned external side fluid.
- In a preferred embodiment the invention provides:
-
- g. a heat exchange device having one or more finned exterior side working fluid streams against multiple tube side circuits,
- h. the multiple tube circuits being interlaced to more effectively approach the cooling curve of the finned exterior side working fluid.
- In a more preferred embodiment the invention further provides:
-
- i. A method of circuitry of a plate fin and tube or finned tube exchanger that allows for more effective heat transfer by adjusting the cooling curve, by providing multiple working fluids in separate but integrated circulation paths.
- j. A method of construction and design allowing complex circuitry of a plate finned and tube or finned tube exchanger utilizing multiple tube side circuits that are interlaced to accomplish more effective heat transfer than would be possible with multiple tube side fluid streams arranged in series without interlacing the circuitry.
- The invention may be described as a method of recovering energy that comprises:
-
- providing a multiple zone integrated plate fin and tube or finned tube exchanger that can be used in heat transfer system that comprises the steps of:
- a. providing a first working fluid circulation path on a finned exterior side of a heat transfer device,
- b. feeding the first working fluid to the circulation path on the exterior finned side of a heat transfer zone to transfer heat to or from the first working fluid thereby heating or cooling the first working fluid to a higher or lower temperature,
- c. feeding a second working fluid into a second circulation path within the heat exchanger to be heated or cooled by the first working fluid.
- d. And feeding a third fluid into a circulation path to be heated or cooled by the first working fluid or the second working fluid.
- Fluids of the same or different composition may be used.
- An alternative embodiment is a method of construction of a heat exchanger that comprises providing a plurality of circulation paths in a plate fin and tube or finned tube exchanger utilizing a plurality of tube side circuits that are interlaced to accomplish more effective heat transfer than would be possible with a plurality of tube side fluid streams arranged in series without interlacing the circuitry.
- As noted above first working fluid and the second working fluid have the same composition or the working fluids may be of different composition.
- The invention may also be described as an energy recovery apparatus specially designed to practice the methods described above that comprises:
-
- a. A finned surface heat exchanger comprising a plurality of circulation pathways for a plurality of working fluids, and
- b. circulation means to pass a plurality of working fluids into at least one heat exchange zone. For example the apparatus may comprise a plurality of working fluid streams on the tubing interior side of a plate fin and tube or finned tube exchanger. In a preferred embodiment the apparatus further comprises multiple heat recovery stages to provide additional heat recovery.
- The inventive concept may also be embodied as a method for an energy recovery system for increasing the efficiency of a gas turbine exhaust heat recovery by providing an integrated tube side heating circuitry to heat a plurality of working fluid circuits while cooling the exhaust stream of the gas turbine.
- In summary, the invention provides a system for more efficient heat transfer in a plate fin and tube or finned tube exchanger by providing a plurality of separate working fluids in a plurality of working fluid circulation paths.
- The invention is illustrated by the specific example set out below.
-
FIG. 1 is a sketch of a typical integrated coil having two working fluids in separate circuits. -
FIG. 2 is a sketch of an integrated coil having 4 working fluids with interwoven circuitry. - The invention provides a method of interweaving streams with various working fluids in a common plate fin and tube or finned tube exchanger to accomplish more efficient heat transfer.
- The invention may be employed to increase the hear recovery efficiency of any gas turbine or other device that produces a waste heat exhaust or is a source of process heat. Alternatively the arrangement may produce more efficient refrigeration at locations requiring refrigeration or cooling.
- These examples are provided to illustrate the invention and not to limit the concepts embodied therein. The invention is defined and limited by the claims set out below. The examples below were modeled using a commercial process simulator.
- In
FIG. 1 a simple two fluid system is shown. The principals illustrated in the more complex system also apply to the two fluid system ofFIG. 1 . Turning toFIG. 2 , a first working fluid consisting of 88.67 mol % N2 and 11.32 mol % H2O enters the heat exchanger at 263.2F, 366.5 psia, 18,946 moles/hr and leaves the exchanger at 101.9 F, 363.3 psia. It exchanges heat with a 2nd working fluid, natural gas in this illustration, entering at 45.6 F, 512 psia, 4460 moles/hr and leaving at 241.5 F, 501 psia. The first working fluid also exchanges heat with a 3rd working fluid, water, entering at 74.4 F, 61 psia, 17660 moles/hr and leaving at 209.5 F, 42.8 psia. The first working fluid also exchanges heat with a 4th working fluid, water, entering at 92 F, 54.7 psia, 20,900 moles/hr and leaving at 107 F, 44.7 psia. The exchanger is modeled with fluid separation and removal after each heat exchange zone as can be accomplished with the invention device. Under the invention integrated heat exchange design, the total UA required is 934,180 BTU/F-hr. If working fluid streams 2, 3 and 4 are arranged in series without integrated heat exchange and with fluid separation and removal after each heat exchange zone, the total UA required to accomplish the sameleaving working fluid 1 temperature is 1,127900 BTU/F-hr. In this example the flow-rate of the 4th working fluid is increased from 20,900 moles/hr to 25,760 moles/hr. Since UA is the heat transfer coefficient times the required heat transfer area, one can assume the heat transfer coefficient is essentially the same. Therefore the invention integrated heat exchanger design using the interwoven heat transfer zones can achieve the same desired workingfluid 1 exit temperature with 20.7% less heat transfer area. - The working fluids may be any available fluid that can be circulated at pressures within the design limits of the selected exchanger and will be selected depending on available fluids at the site. They may include multiple streams of the same fluid at different temperatures and pressures (such as water in example 1) or the fluids may be different (such as natural gas, working fluid 2 in the example).
Claims (11)
1. A method of recovering energy that comprises:
Providing a multiple circulation path integrated plate fin and tube or finned tube heat exchanger that can be used in heat transfer system that comprises the steps of:
a. providing a first working fluid circulation path on a finned exterior side of a heat transfer device,
b. feeding the first working fluid to the circulation path on the exterior finned side of a heat transfer zone to transfer heat to or from the first working fluid thereby heating or cooling the first working fluid to a higher or lower temperature, and feeding a second working fluid into a second interior (tube side) circulation path within a heat exchanger to be heated or cooled by the first working fluid and
c. providing a third fluid circulation path in the heat exchanger and feeding a third working fluid into the third interior (tube side) circulation path to be heated or cooled by the first working fluid.
d. interweaving the second and third fluid flow paths of the exchanger to achieve more efficient heat transfer characteristics than can be achieved with the same streams arranged in series.
2. The method of claim 1 wherein the first working fluid and the second working fluid have the same composition.
3. The method of claim 1 where the first working fluid and the second working fluid are of different composition.
4. The method of claim 1 wherein more than two working fluid circulation pathways are provided in the interior (tube side) of the exchanger.
5. A method of construction of a heat exchanger that comprises providing a plurality of circulation paths in a plate finned and tube or finned tube exchanger utilizing a plurality of tube side circuits that are interlaced to accomplish more effective heat transfer than would be possible with a plurality of tube side fluid streams arranged in series without interlacing the circuitry.
6. The method of claim 4 wherein the first working fluid and the second working fluid have the same composition.
7. The method of claim 4 where the tube working fluids are of different composition.
8. An energy recovery apparatus that comprises: a finned surface heat exchanger comprising a plurality of circulation pathways for a plurality of working fluids, and circulation means to pass a plurality of working fluids into at least one heat exchange zone.
9. The apparatus of claim 8 wherein the apparatus comprises a plurality working fluid streams in circulation pathways of a plate fin and tube or finned tube exchanger.
10. The apparatus of claim 9 further comprising multiple heat recovery stages to provide additional heat recovery.
11. A method for designing an energy recovery system for increasing the efficiency of a gas turbine exhaust heat recovery by providing an integrated tube side heating circuitry to heat a plurality of working fluid circuits while cooling the exhaust stream of the gas turbine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10/700,805 US20050092472A1 (en) | 2003-11-03 | 2003-11-03 | Heat exchange system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10/700,805 US20050092472A1 (en) | 2003-11-03 | 2003-11-03 | Heat exchange system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20050092472A1 true US20050092472A1 (en) | 2005-05-05 |
Family
ID=34551289
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US10/700,805 Abandoned US20050092472A1 (en) | 2003-11-03 | 2003-11-03 | Heat exchange system |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US20050092472A1 (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050263262A1 (en) * | 2004-05-26 | 2005-12-01 | Larry Lewis | Heat exchange system for plume abatement |
| EP1813572A3 (en) * | 2006-01-31 | 2011-01-26 | Linde BOC Process Plants LLC | Process and apparatus for synthesis gas |
| US8057747B2 (en) | 2004-11-19 | 2011-11-15 | Sme Products, Lp | Heat exchange system |
| US20130264027A1 (en) * | 2012-04-10 | 2013-10-10 | International Business Machines Corporation | Process for optimizing a heat exchanger configuration |
| US8828107B2 (en) | 2006-01-31 | 2014-09-09 | Linde Process Plants, Inc. | Process and apparatus for synthesis gas heat exchange system |
| US20160313026A1 (en) * | 2013-12-13 | 2016-10-27 | Intergas Heating Assets B.V. | Heat Exchanger, Heating Device, Heating System and Method for Heating Water |
| KR20200081676A (en) * | 2018-12-28 | 2020-07-08 | 주식회사 경동나비엔 | Boiler and the Method for Controlling Combustion of the Boiler |
| CN112771265A (en) * | 2018-07-31 | 2021-05-07 | 赛峰飞机发动机公司 | Heat exchanger for a turbomachine and production thereof |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2633338A (en) * | 1947-02-19 | 1953-03-31 | Continental Aviat & Engineerin | Heat exchanger |
| US2735660A (en) * | 1956-02-21 | Craig | ||
| US3277958A (en) * | 1962-11-27 | 1966-10-11 | Babcock & Wilcox Ltd | Heat exchangers |
| US3294161A (en) * | 1961-07-03 | 1966-12-27 | Continental Aviat & Eng Corp | Heat exchangers |
| US4158438A (en) * | 1976-06-03 | 1979-06-19 | Raytheon Company | Self-pumping water boiler system |
| US4344482A (en) * | 1979-12-29 | 1982-08-17 | Suddeutsche Kuhlerfabrik Julius Fr. Behr Gmbh & Co. Kg | Multiple flow condenser for air conditioning units of motor vehicles |
| US4546818A (en) * | 1982-10-28 | 1985-10-15 | Halstead Industries, Inc. | Multiple source energy recovery system |
| US4781241A (en) * | 1987-08-27 | 1988-11-01 | International Fuel Cells Corporation | Heat exchanger for fuel cell power plant reformer |
| US5419392A (en) * | 1993-02-10 | 1995-05-30 | Maruyama; Noboru | Heat exchanging apparatus |
-
2003
- 2003-11-03 US US10/700,805 patent/US20050092472A1/en not_active Abandoned
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2735660A (en) * | 1956-02-21 | Craig | ||
| US2633338A (en) * | 1947-02-19 | 1953-03-31 | Continental Aviat & Engineerin | Heat exchanger |
| US3294161A (en) * | 1961-07-03 | 1966-12-27 | Continental Aviat & Eng Corp | Heat exchangers |
| US3277958A (en) * | 1962-11-27 | 1966-10-11 | Babcock & Wilcox Ltd | Heat exchangers |
| US4158438A (en) * | 1976-06-03 | 1979-06-19 | Raytheon Company | Self-pumping water boiler system |
| US4344482A (en) * | 1979-12-29 | 1982-08-17 | Suddeutsche Kuhlerfabrik Julius Fr. Behr Gmbh & Co. Kg | Multiple flow condenser for air conditioning units of motor vehicles |
| US4546818A (en) * | 1982-10-28 | 1985-10-15 | Halstead Industries, Inc. | Multiple source energy recovery system |
| US4781241A (en) * | 1987-08-27 | 1988-11-01 | International Fuel Cells Corporation | Heat exchanger for fuel cell power plant reformer |
| US5419392A (en) * | 1993-02-10 | 1995-05-30 | Maruyama; Noboru | Heat exchanging apparatus |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050263262A1 (en) * | 2004-05-26 | 2005-12-01 | Larry Lewis | Heat exchange system for plume abatement |
| US8066056B2 (en) | 2004-05-26 | 2011-11-29 | Sme Products, Lp | Heat exchange system for plume abatement |
| US8057747B2 (en) | 2004-11-19 | 2011-11-15 | Sme Products, Lp | Heat exchange system |
| EP1813572A3 (en) * | 2006-01-31 | 2011-01-26 | Linde BOC Process Plants LLC | Process and apparatus for synthesis gas |
| US8828107B2 (en) | 2006-01-31 | 2014-09-09 | Linde Process Plants, Inc. | Process and apparatus for synthesis gas heat exchange system |
| US20130264027A1 (en) * | 2012-04-10 | 2013-10-10 | International Business Machines Corporation | Process for optimizing a heat exchanger configuration |
| US9631880B2 (en) * | 2012-04-10 | 2017-04-25 | Lenovo Enterprise Solutions (Singapore) Pte. Ltd. | Process for optimizing a heat exchanger configuration |
| US20160313026A1 (en) * | 2013-12-13 | 2016-10-27 | Intergas Heating Assets B.V. | Heat Exchanger, Heating Device, Heating System and Method for Heating Water |
| CN112771265A (en) * | 2018-07-31 | 2021-05-07 | 赛峰飞机发动机公司 | Heat exchanger for a turbomachine and production thereof |
| KR20200081676A (en) * | 2018-12-28 | 2020-07-08 | 주식회사 경동나비엔 | Boiler and the Method for Controlling Combustion of the Boiler |
| KR102260500B1 (en) | 2018-12-28 | 2021-06-03 | 주식회사 경동나비엔 | Boiler and the Method for Controlling Combustion of the Boiler |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |