US20170336096A1 - Heat exchanger refrigerant drain - Google Patents
Heat exchanger refrigerant drain Download PDFInfo
- Publication number
- US20170336096A1 US20170336096A1 US15/522,886 US201515522886A US2017336096A1 US 20170336096 A1 US20170336096 A1 US 20170336096A1 US 201515522886 A US201515522886 A US 201515522886A US 2017336096 A1 US2017336096 A1 US 2017336096A1
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- United States
- Prior art keywords
- shell
- refrigerant
- heat exchanger
- displacement
- drain device
- 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
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/30—Arrangement or mounting of heat-exchangers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/04—Condensers
-
- 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
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/163—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F17/00—Removing ice or water from heat-exchange apparatus
- F28F17/005—Means for draining condensates from heat exchangers, e.g. from evaporators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
- F25B2339/046—Condensers with refrigerant heat exchange tubes positioned inside or around a vessel containing water or pcm to cool the refrigerant gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
- F28F2265/06—Safety or protection arrangements; Arrangements for preventing malfunction by using means for draining heat exchange media from heat exchangers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
- F28F2265/22—Safety or protection arrangements; Arrangements for preventing malfunction for draining
Definitions
- This disclosure relates generally to a heat exchanger refrigerant drain, such as in gravity draining of refrigerant in a heat exchanger.
- the heat exchanger drain can be in a shell and tube heat exchanger, for example a condenser, which may be used in a chiller unit of a heating, ventilation, and air conditioning (HVAC) system or refrigeration system.
- HVAC heating, ventilation, and air conditioning
- apparatuses, systems, and methods are directed a refrigerant drain channel which displaces available volume in a shell of the heat exchanger, e.g. the condenser, to efficiently use and/or even reduce amount of refrigerant used in a chiller unit.
- Refrigerants are used in HVAC systems such as, for example, in a chiller unit.
- Some heat exchangers in chiller units employ gravity drain type systems for the refrigerant circulating into and out of the heat exchanger.
- refrigerants such as, for example, hydrochlorofluorocarbons (HCFCs) and hydrofluorocarbons (HFCs) are being or have been phased out due to increasing standards to reduce ozone depletion.
- HCFCs hydrochlorofluorocarbons
- HFCs hydrofluorocarbons
- the use of relatively expensive refrigerants are being looked at as alternatives to meet such changing standards.
- Use of such relatively expensive refrigerants may be a concern when considering factors as larger capacity cooling systems, e.g., chiller units of an HVAC system, are being designed to meet for example growing comfort cooling or air-conditioning demands. Reducing refrigerant charge in such systems would be advantageous while still meeting such environmental standards and market demands on higher capacity units.
- condenser heat exchanger in a shell and tube design used in a chiller unit.
- the condenser is the heat exchanger wherein the heat is rejected by the chiller to a second fluid system.
- the refrigerant within the condenser undergoes a phase change from vapor to liquid.
- the condensed liquid refrigerant can cascade from the tubes to the bottom of the shell, such as in a falling film or a gravity drain configuration.
- one method of extracting the liquid refrigerant is using a gravity drain design where liquid accumulates until, for example, a sufficient liquid head is equivalent to the velocity head and head losses to induce flow toward a drain connection located axially along the shell length.
- a significant amount of liquid refrigerant charge can accumulate on the bottom of the condenser, e.g., the shell of the condenser.
- Improvements may be made to such shell and tube heat exchangers, for example condensers.
- Embodiments illustrated and described herein are directed to a combination refrigeration displacement and drain device that can be mounted within a heat exchanger, such as a shell and tube heat exchanger, which may be used, for example, as a heat exchanger in a chiller unit, which may be used in an HVAC or refrigeration system.
- a heat exchanger such as a shell and tube heat exchanger
- a condenser employing a gravity drain, e.g., falling film type heat exchanger in a shell and tube construction.
- combination refrigeration displacement and drain device can be implemented in various types of chillers using various types of compressors, such as, for example, a centrifugal compressor, and can be applied in various types of heat exchangers of various sized lengths and/or diameters of the shell, and where refrigerant charge may be accumulating.
- compressors such as, for example, a centrifugal compressor
- heat exchangers of various sized lengths and/or diameters of the shell, and where refrigerant charge may be accumulating.
- the combination refrigeration displacement and drain device herein can provide a refrigerant charge reduction, for example, that is used in the chiller unit, while facilitating drainage out of the heat exchanger.
- the combination refrigeration displacement and drain device can alleviate the liquid refrigerant accumulation that may normally be necessary to induce flow in a gravity drain design.
- the combination refrigeration displacement and drain device generally has one or more slants and one or more channels that are inclined and decline in the direction of a drain outlet or connection of the heat exchanger. It will be appreciated that the combination refrigeration displacement and drain device can be configured, designed, and/or optimized to account for relative velocity profiles across any section of the shell and locations at which the combination refrigeration displacement and drain device may reside.
- Energy equations such as Bernoulli equations, derivatives and variants thereof, which are known, can be used to analyze and determine flow profiles that may be desired and/or necessary, while considering factors such as liquid head, velocity head, head losses, hydrostatic head, and specific structure of the slant(s) and channel(s) (e.g., friction slope(s)) of the combination refrigeration displacement and drain device.
- a heat exchanger in one embodiment, includes a shell with a volume therein.
- the shell includes an inlet for a heat exchange fluid, such as for example a vapor inlet for refrigerant vapor to enter the shell, and includes an outlet which can have a drain connection.
- the outlet is for fluids containing predominantly liquid (e.g., liquid refrigerant that has undergone a heat exchange with the fluid on the tube side (e.g., water running through the tubes)) to drain from the shell.
- Heat exchange tubes that may be configured to carry a process fluid, such as, for example, water, along substantially the length of the shell. The tubes reside in the volume of the shell at around a relatively middle height and upward toward the top at about relatively higher height.
- a combination refrigeration displacement and drain device resides within the shell, and is located and/or positioned toward relatively a lower height of the shell.
- the combination refrigeration displacement and drain device has a structure, arrangement, and/or configuration to displace or prevent refrigerant from collecting at portions on the bottom of the shell, and to induce flow toward the outlet.
- the combination refrigeration displacement and drain device has one or more slanted portions.
- the slanted portions extend along the length of the shell and decline from the shell wall toward a bottom of the shell. In some embodiments, the slanted portions decline from an end of the shell along one or more portions of the length of the shell.
- the slanted portions provide displacement which displaces, blocks, and/or does not allow the heat exchange fluid, e.g. refrigerant, to collect or otherwise accumulate on wall(s) at the bottom of the shell.
- the heat exchange fluid e.g. refrigerant
- the heat exchanger is a condenser.
- the heat exchanger can be used in a chiller unit.
- the chiller unit is used in an HVAC system.
- liquid head required to induce flow in a gravity type drain which may otherwise be needed without the use of the combination refrigeration displacement and drain device, can be displaced by the use of the combination refrigeration displacement and drain device to facilitate flow.
- a full load operating condition which is the same condition where optimal charge may be determined.
- the combination refrigeration displacement and drain device can be configured, designed, and/or optimized, such that displaced refrigerant volume can be closely and/or directly correlated to a reduction in refrigerant charge such as in a chiller unit.
- the combination refrigeration displacement and drain device may reduce as much as 50% to 75% of the liquid refrigerant charge, as compared to some designs primarily or only relying on gravity drain, e.g., velocity head of the liquid, within the shell.
- FIG. 1 is side schematic view of one embodiment of a heat exchanger with a combination refrigerant displacement and drain device within the shell of the heat exchanger.
- FIG. 2 is a sectional or end view of the heat exchanger of FIG. 1 .
- FIG. 3 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device.
- FIG. 4 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device.
- FIG. 5 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device.
- FIG. 6 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device.
- FIG. 7 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device.
- FIG. 8 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device.
- FIG. 9 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device.
- FIG. 10 is a partial sectional view showing the combination refrigerant displacement and drain device of FIG. 9 .
- FIG. 11 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device.
- FIG. 12 is a partial sectional view showing the combination refrigerant displacement and drain device of FIG. 9 .
- FIG. 13 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device.
- FIG. 14 is a partial end view showing the combination refrigerant displacement and drain device of FIG. 13 .
- Embodiments disclosed herein relate generally to a heat exchanger refrigerant drain, such as in gravity draining of refrigerant in a heat exchanger.
- the heat exchanger drain can be in a shell and tube heat exchanger, for example a condenser, which may be used in a chiller unit of a heating, ventilation, and air conditioning (HVAC) system or refrigeration system.
- HVAC heating, ventilation, and air conditioning
- apparatuses, systems, and methods are directed a refrigerant drain channel which displaces available volume in a shell of the heat exchanger, e.g. the condenser, to efficiently use and/or even reduce amount of refrigerant used in a chiller unit.
- the combination refrigeration displacement and drain device generally has one or more slants (e.g., ramps, ramp portions) and one or more channels that are inclined and decline in the direction of a drain outlet or connection of the heat exchanger. It will be appreciated that the combination refrigeration displacement and drain device can be configured, designed, and/or optimized to account for relative velocity profiles across any section of the shell and locations at which the combination refrigeration displacement and drain device may reside. Such configuration, design, and/or optimization, whether such velocity profiles are uniform or not uniform within the shell, can be determined.
- Energy equations such as Bernoulli equations, derivatives and variants thereof, which are known, can be used to analyze and determine flow profiles that may be desired and/or necessary, while considering factors such as liquid head, velocity head, head losses, hydrostatic head, and specific structure of the slant(s) and channel(s) (e.g., friction slope(s)) of the combination refrigeration displacement and drain device.
- FIG. 1 is side schematic view of one embodiment of a heat exchanger 10 with a combination refrigerant displacement and drain device 30 within a shell 16 of the heat exchanger 10 , according to an embodiment.
- the heat exchanger 10 has an inlet 12 and an outlet 14 .
- Heat exchange tubes 22 run substantially the length L of the shell 16 and between the tubesheets 20 .
- the combination refrigerant displacement and drain device 30 has one or more slanted portions 32 or slants that direct and/or induce fluid flow, e.g., liquid flow, to the outlet 14 .
- the combination refrigerant displacement and drain device 30 separates the volume inside the shell 16 which displaces portions of the volume inside the shell 16 and proximate or toward a bottom 18 of the shell 16 .
- FIG. 2 is a sectional or end view of the heat exchanger 10 of FIG. 1 , according to an embodiment.
- FIG. 2 shows the combination refrigerant displacement and drain device 30 slanting downward relative to the drawing view.
- FIGS. 3 to 14 show additional embodiments for a combination refrigerant displacement and drain device, e.g., the combination refrigerant displacement and drain device 30 of FIGS. 1-2 , and which are specifically described below. While bottom quarter perspective views are shown for the embodiments of FIGS. 3 to 14 , it will be appreciated that structures based on the mirror images of what is shown can be achieved at any of the other bottom three quarters of the heat exchange shell to complete the view.
- FIG. 3 is a perspective view showing a part of a shell and tube heat exchanger showing part of a shell 306 and outlet 304 , and part of an embodiment of a combination refrigerant displacement and drain device 300 .
- the combination refrigerant displacement and drain device 300 has slants 302 which slant down toward a bottom of the shell 306 and also slant from an end toward the outlet 304 .
- the slants 302 converge forming a channel(s) 308 .
- FIG. 4 is a perspective view showing a part of a shell and tube heat exchanger showing part of a shell 406 and outlet 404 and part of an embodiment of a combination refrigerant displacement and drain device 400 .
- the combination refrigerant displacement and drain device 400 has slants 402 which slant down toward a bottom of the shell 406 and also slant from an end toward the outlet 404 .
- the slants 402 converge forming a channel(s) 408 which meets up with the outlet 404 .
- FIG. 5 is a perspective view showing a part of a shell and tube heat exchanger showing part of a shell 506 and outlet 504 and part of an embodiment of a combination refrigerant displacement and drain device 500 .
- the combination refrigerant displacement and drain device 500 has slants 502 which slant down toward a bottom of the shell 506 and also slant from an end toward the outlet 504 .
- the slants 502 converge forming a channel(s) 508 .
- the device 500 can also include a modified sump area 510 , which is in fluid communication with the channel 510 and the outlet 504 , where the sump 510 forms a step or intermediate region to induce fluid flow.
- FIG. 6 is a perspective view showing a part of a shell and tube heat exchanger showing part of a shell 606 and outlet 604 and part of an embodiment of a combination refrigerant displacement and drain device 600 .
- the combination refrigerant displacement and drain device 600 has slants 602 which slant down toward a bottom of the shell 606 and also slant from an end toward the outlet 604 .
- the slants 602 converge forming a channel(s) 608 , which can meet with the outlet 604 .
- the channel 608 at a portion proximate the outlet can be “clipped” or shaped to provide a slanted edge to help induce flow.
- FIG. 7 is a perspective view showing a part of a shell and tube heat exchanger showing part of a shell 706 and an outlet 704 and part of an embodiment of a combination refrigerant displacement and drain device 700 .
- the combination refrigerant displacement and drain device 700 has slants 702 which slant down toward a bottom of the shell 706 and also slant from an end toward the outlet 704 . As shown there are multiple discreet or separate slants 702 which may have tapered edge to form separate channels 708 .
- FIG. 8 is a perspective view showing a part of a shell and tube heat exchanger showing part of a shell 806 and outlet 804 and part of an embodiment of a combination refrigerant displacement and drain device 800 .
- the combination refrigerant displacement and drain device 800 has slants 802 which slant down toward a bottom of the shell 806 and also slant from an end toward the outlet 804 . As shown there are multiple discreet or separate slants 802 which may have tapered edge to form separate channels 808 and which may taper toward the center to form additional channels.
- FIG. 9 is a perspective view showing a part of a shell and tube heat exchanger showing part of a shell 906 and an outlet 904 and part of an embodiment of a combination refrigerant displacement and drain device 900 .
- the combination refrigerant displacement and drain device 900 has a slant 902 which slant which may also include a curvature portion down toward a bottom of the shell 906 and also slant from an end toward the outlet 904 .
- the slant 902 can converge forming a channel(s) 908 .
- the slant 902 also can include a displacer wall.
- FIG. 10 is a partial sectional view showing the combination refrigerant displacement and drain device 900 of FIG. 9 .
- FIG. 11 is a perspective view showing a part of a shell and tube heat exchanger showing part of a shell 1106 and an outlet 1104 and part of an embodiment of a combination refrigerant displacement and drain device 1100 .
- the combination refrigerant displacement and drain device 1100 has a slant 1102 which slants down toward a bottom of the shell 1106 and also slants from an end toward the outlet 1104 .
- the slant 1102 can converges forming a channel(s) 1108 .
- the slant 1102 also can include be a displacer wall.
- FIG. 12 is a partial sectional view showing the combination refrigerant displacement and drain device 1100 of FIG. 9 .
- FIG. 13 is a perspective view showing a part of a shell and tube heat exchanger showing part of a shell 1306 and the outlet 1304 and part of an embodiment of a combination refrigerant displacement and drain device 1300 .
- the combination refrigerant displacement and drain device 1300 has slants 1302 which slant down toward a bottom of the shell 1306 and also slant from an end toward the outlet 1304 .
- the slants 1302 converge forming a channel(s) 1308 .
- the channel 1308 can include a trough section, such as a central trough, which can help induce flow.
- FIG. 14 is a partial end view showing the combination refrigerant displacement and drain device 1300 of FIG. 13 .
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Abstract
Description
- This disclosure relates generally to a heat exchanger refrigerant drain, such as in gravity draining of refrigerant in a heat exchanger. In particular, the heat exchanger drain can be in a shell and tube heat exchanger, for example a condenser, which may be used in a chiller unit of a heating, ventilation, and air conditioning (HVAC) system or refrigeration system. In particular, apparatuses, systems, and methods are directed a refrigerant drain channel which displaces available volume in a shell of the heat exchanger, e.g. the condenser, to efficiently use and/or even reduce amount of refrigerant used in a chiller unit.
- Refrigerants are used in HVAC systems such as, for example, in a chiller unit. Some heat exchangers in chiller units employ gravity drain type systems for the refrigerant circulating into and out of the heat exchanger.
- Certain refrigerants, such as, for example, hydrochlorofluorocarbons (HCFCs) and hydrofluorocarbons (HFCs), are being or have been phased out due to increasing standards to reduce ozone depletion. The use of relatively expensive refrigerants are being looked at as alternatives to meet such changing standards. Use of such relatively expensive refrigerants may be a concern when considering factors as larger capacity cooling systems, e.g., chiller units of an HVAC system, are being designed to meet for example growing comfort cooling or air-conditioning demands. Reducing refrigerant charge in such systems would be advantageous while still meeting such environmental standards and market demands on higher capacity units.
- One example where such charge minimization may be available is in a condenser heat exchanger in a shell and tube design used in a chiller unit. In HVAC chillers, as one example, the condenser is the heat exchanger wherein the heat is rejected by the chiller to a second fluid system. The refrigerant within the condenser undergoes a phase change from vapor to liquid. In shell and tube condensers, the condensed liquid refrigerant can cascade from the tubes to the bottom of the shell, such as in a falling film or a gravity drain configuration. For example, one method of extracting the liquid refrigerant is using a gravity drain design where liquid accumulates until, for example, a sufficient liquid head is equivalent to the velocity head and head losses to induce flow toward a drain connection located axially along the shell length. However, in previous designs, a significant amount of liquid refrigerant charge can accumulate on the bottom of the condenser, e.g., the shell of the condenser.
- Improvements may be made to such shell and tube heat exchangers, for example condensers.
- Embodiments illustrated and described herein are directed to a combination refrigeration displacement and drain device that can be mounted within a heat exchanger, such as a shell and tube heat exchanger, which may be used, for example, as a heat exchanger in a chiller unit, which may be used in an HVAC or refrigeration system. One example of such components can include heat exchangers, such as, for example, a condenser employing a gravity drain, e.g., falling film type heat exchanger in a shell and tube construction. It will be appreciated that the combination refrigeration displacement and drain device herein can be implemented in various types of chillers using various types of compressors, such as, for example, a centrifugal compressor, and can be applied in various types of heat exchangers of various sized lengths and/or diameters of the shell, and where refrigerant charge may be accumulating.
- Advantageously, the combination refrigeration displacement and drain device herein can provide a refrigerant charge reduction, for example, that is used in the chiller unit, while facilitating drainage out of the heat exchanger. The combination refrigeration displacement and drain device can alleviate the liquid refrigerant accumulation that may normally be necessary to induce flow in a gravity drain design. The combination refrigeration displacement and drain device generally has one or more slants and one or more channels that are inclined and decline in the direction of a drain outlet or connection of the heat exchanger. It will be appreciated that the combination refrigeration displacement and drain device can be configured, designed, and/or optimized to account for relative velocity profiles across any section of the shell and locations at which the combination refrigeration displacement and drain device may reside. Such configuration, design, and/or optimization, whether such velocity profiles are uniform or not uniform within the shell, can be determined. Energy equations such as Bernoulli equations, derivatives and variants thereof, which are known, can be used to analyze and determine flow profiles that may be desired and/or necessary, while considering factors such as liquid head, velocity head, head losses, hydrostatic head, and specific structure of the slant(s) and channel(s) (e.g., friction slope(s)) of the combination refrigeration displacement and drain device.
- In one embodiment, a heat exchanger includes a shell with a volume therein. The shell includes an inlet for a heat exchange fluid, such as for example a vapor inlet for refrigerant vapor to enter the shell, and includes an outlet which can have a drain connection. The outlet is for fluids containing predominantly liquid (e.g., liquid refrigerant that has undergone a heat exchange with the fluid on the tube side (e.g., water running through the tubes)) to drain from the shell. Heat exchange tubes that may be configured to carry a process fluid, such as, for example, water, along substantially the length of the shell. The tubes reside in the volume of the shell at around a relatively middle height and upward toward the top at about relatively higher height. A combination refrigeration displacement and drain device resides within the shell, and is located and/or positioned toward relatively a lower height of the shell. The combination refrigeration displacement and drain device has a structure, arrangement, and/or configuration to displace or prevent refrigerant from collecting at portions on the bottom of the shell, and to induce flow toward the outlet.
- In some embodiments, the combination refrigeration displacement and drain device has one or more slanted portions. In some embodiments, the slanted portions extend along the length of the shell and decline from the shell wall toward a bottom of the shell. In some embodiments, the slanted portions decline from an end of the shell along one or more portions of the length of the shell.
- In some embodiments, the slanted portions provide displacement which displaces, blocks, and/or does not allow the heat exchange fluid, e.g. refrigerant, to collect or otherwise accumulate on wall(s) at the bottom of the shell.
- In some embodiments, the heat exchanger is a condenser.
- In some embodiments, the heat exchanger can be used in a chiller unit.
- In some embodiments, the chiller unit is used in an HVAC system.
- Advantageously, liquid head required to induce flow in a gravity type drain, which may otherwise be needed without the use of the combination refrigeration displacement and drain device, can be displaced by the use of the combination refrigeration displacement and drain device to facilitate flow. For example, in a full load operating condition, which is the same condition where optimal charge may be determined. The combination refrigeration displacement and drain device can be configured, designed, and/or optimized, such that displaced refrigerant volume can be closely and/or directly correlated to a reduction in refrigerant charge such as in a chiller unit. Dependent, for example, on spatial constraints of the chiller unit or the heat exchanger, the combination refrigeration displacement and drain device may reduce as much as 50% to 75% of the liquid refrigerant charge, as compared to some designs primarily or only relying on gravity drain, e.g., velocity head of the liquid, within the shell.
- These and other features, aspects, and advantages of the will become better understood when the following detailed description is read with reference to the accompanying drawings, wherein:
-
FIG. 1 is side schematic view of one embodiment of a heat exchanger with a combination refrigerant displacement and drain device within the shell of the heat exchanger. -
FIG. 2 is a sectional or end view of the heat exchanger ofFIG. 1 . -
FIG. 3 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device. -
FIG. 4 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device. -
FIG. 5 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device. -
FIG. 6 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device. -
FIG. 7 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device. -
FIG. 8 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device. -
FIG. 9 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device. -
FIG. 10 is a partial sectional view showing the combination refrigerant displacement and drain device ofFIG. 9 . -
FIG. 11 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device. -
FIG. 12 is a partial sectional view showing the combination refrigerant displacement and drain device ofFIG. 9 . -
FIG. 13 is a perspective view showing a part of a shell and tube heat exchanger showing part of the shell and part of an embodiment of a combination refrigerant displacement and drain device. -
FIG. 14 is a partial end view showing the combination refrigerant displacement and drain device ofFIG. 13 . - While the above-identified figures set forth particular embodiments of the combination refrigerant displacement and drain device in a shell and tube heat exchanger, other embodiments are also contemplated, as noted in the descriptions herein. In all cases, this disclosure presents illustrated embodiments of the combination refrigerant displacement and drain device by way of representation but not limitation. Numerous other modifications and embodiments can be devised by those skilled in the art which fall within the scope and spirit of the principles of the combination refrigerant displacement and drain device described and illustrated herein.
- Embodiments disclosed herein relate generally to a heat exchanger refrigerant drain, such as in gravity draining of refrigerant in a heat exchanger. In particular, the heat exchanger drain can be in a shell and tube heat exchanger, for example a condenser, which may be used in a chiller unit of a heating, ventilation, and air conditioning (HVAC) system or refrigeration system. In particular, apparatuses, systems, and methods are directed a refrigerant drain channel which displaces available volume in a shell of the heat exchanger, e.g. the condenser, to efficiently use and/or even reduce amount of refrigerant used in a chiller unit.
- The combination refrigeration displacement and drain device generally has one or more slants (e.g., ramps, ramp portions) and one or more channels that are inclined and decline in the direction of a drain outlet or connection of the heat exchanger. It will be appreciated that the combination refrigeration displacement and drain device can be configured, designed, and/or optimized to account for relative velocity profiles across any section of the shell and locations at which the combination refrigeration displacement and drain device may reside. Such configuration, design, and/or optimization, whether such velocity profiles are uniform or not uniform within the shell, can be determined. Energy equations such as Bernoulli equations, derivatives and variants thereof, which are known, can be used to analyze and determine flow profiles that may be desired and/or necessary, while considering factors such as liquid head, velocity head, head losses, hydrostatic head, and specific structure of the slant(s) and channel(s) (e.g., friction slope(s)) of the combination refrigeration displacement and drain device.
-
FIG. 1 is side schematic view of one embodiment of aheat exchanger 10 with a combination refrigerant displacement anddrain device 30 within ashell 16 of theheat exchanger 10, according to an embodiment. Theheat exchanger 10 has aninlet 12 and anoutlet 14.Heat exchange tubes 22 run substantially the length L of theshell 16 and between thetubesheets 20. The combination refrigerant displacement anddrain device 30 has one or moreslanted portions 32 or slants that direct and/or induce fluid flow, e.g., liquid flow, to theoutlet 14. The combination refrigerant displacement anddrain device 30 separates the volume inside theshell 16 which displaces portions of the volume inside theshell 16 and proximate or toward a bottom 18 of theshell 16. -
FIG. 2 is a sectional or end view of theheat exchanger 10 ofFIG. 1 , according to an embodiment.FIG. 2 shows the combination refrigerant displacement anddrain device 30 slanting downward relative to the drawing view. -
FIGS. 3 to 14 show additional embodiments for a combination refrigerant displacement and drain device, e.g., the combination refrigerant displacement anddrain device 30 ofFIGS. 1-2 , and which are specifically described below. While bottom quarter perspective views are shown for the embodiments ofFIGS. 3 to 14 , it will be appreciated that structures based on the mirror images of what is shown can be achieved at any of the other bottom three quarters of the heat exchange shell to complete the view. -
FIG. 3 is a perspective view showing a part of a shell and tube heat exchanger showing part of ashell 306 andoutlet 304, and part of an embodiment of a combination refrigerant displacement anddrain device 300. The combination refrigerant displacement anddrain device 300 hasslants 302 which slant down toward a bottom of theshell 306 and also slant from an end toward theoutlet 304. Theslants 302 converge forming a channel(s) 308. -
FIG. 4 is a perspective view showing a part of a shell and tube heat exchanger showing part of ashell 406 andoutlet 404 and part of an embodiment of a combination refrigerant displacement anddrain device 400. The combination refrigerant displacement anddrain device 400 hasslants 402 which slant down toward a bottom of theshell 406 and also slant from an end toward theoutlet 404. Theslants 402 converge forming a channel(s) 408 which meets up with theoutlet 404. -
FIG. 5 is a perspective view showing a part of a shell and tube heat exchanger showing part of ashell 506 andoutlet 504 and part of an embodiment of a combination refrigerant displacement and drain device 500. The combination refrigerant displacement and drain device 500 hasslants 502 which slant down toward a bottom of theshell 506 and also slant from an end toward theoutlet 504. Theslants 502 converge forming a channel(s) 508. The device 500 can also include a modifiedsump area 510, which is in fluid communication with thechannel 510 and theoutlet 504, where thesump 510 forms a step or intermediate region to induce fluid flow. -
FIG. 6 is a perspective view showing a part of a shell and tube heat exchanger showing part of ashell 606 andoutlet 604 and part of an embodiment of a combination refrigerant displacement anddrain device 600. The combination refrigerant displacement anddrain device 600 hasslants 602 which slant down toward a bottom of theshell 606 and also slant from an end toward theoutlet 604. Theslants 602 converge forming a channel(s) 608, which can meet with theoutlet 604. Thechannel 608 at a portion proximate the outlet can be “clipped” or shaped to provide a slanted edge to help induce flow. -
FIG. 7 is a perspective view showing a part of a shell and tube heat exchanger showing part of ashell 706 and anoutlet 704 and part of an embodiment of a combination refrigerant displacement anddrain device 700. The combination refrigerant displacement anddrain device 700 hasslants 702 which slant down toward a bottom of theshell 706 and also slant from an end toward theoutlet 704. As shown there are multiple discreet orseparate slants 702 which may have tapered edge to formseparate channels 708. -
FIG. 8 is a perspective view showing a part of a shell and tube heat exchanger showing part of ashell 806 andoutlet 804 and part of an embodiment of a combination refrigerant displacement anddrain device 800. The combination refrigerant displacement anddrain device 800 hasslants 802 which slant down toward a bottom of theshell 806 and also slant from an end toward theoutlet 804. As shown there are multiple discreet orseparate slants 802 which may have tapered edge to formseparate channels 808 and which may taper toward the center to form additional channels. -
FIG. 9 is a perspective view showing a part of a shell and tube heat exchanger showing part of ashell 906 and anoutlet 904 and part of an embodiment of a combination refrigerant displacement anddrain device 900. The combination refrigerant displacement anddrain device 900 has aslant 902 which slant which may also include a curvature portion down toward a bottom of theshell 906 and also slant from an end toward theoutlet 904. Theslant 902 can converge forming a channel(s) 908. Theslant 902 also can include a displacer wall.FIG. 10 is a partial sectional view showing the combination refrigerant displacement anddrain device 900 ofFIG. 9 . -
FIG. 11 is a perspective view showing a part of a shell and tube heat exchanger showing part of ashell 1106 and anoutlet 1104 and part of an embodiment of a combination refrigerant displacement anddrain device 1100. The combination refrigerant displacement anddrain device 1100 has aslant 1102 which slants down toward a bottom of theshell 1106 and also slants from an end toward theoutlet 1104. Theslant 1102 can converges forming a channel(s) 1108. Theslant 1102 also can include be a displacer wall.FIG. 12 is a partial sectional view showing the combination refrigerant displacement anddrain device 1100 ofFIG. 9 . -
FIG. 13 is a perspective view showing a part of a shell and tube heat exchanger showing part of ashell 1306 and theoutlet 1304 and part of an embodiment of a combination refrigerant displacement anddrain device 1300. The combination refrigerant displacement anddrain device 1300 hasslants 1302 which slant down toward a bottom of theshell 1306 and also slant from an end toward theoutlet 1304. Theslants 1302 converge forming a channel(s) 1308. Thechannel 1308 can include a trough section, such as a central trough, which can help induce flow.FIG. 14 is a partial end view showing the combination refrigerant displacement anddrain device 1300 ofFIG. 13 . - With regard to the forgoing description, it is to be understood that changes may be made in detail, without departing from the scope of the present invention. It is intended that the specification and depicted embodiments are to be considered exemplary only, with a true scope and spirit of the invention being indicated by the broad meaning of the claims.
Claims (20)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US15/522,886 US20170336096A1 (en) | 2014-10-31 | 2015-10-30 | Heat exchanger refrigerant drain |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201462073494P | 2014-10-31 | 2014-10-31 | |
PCT/US2015/058307 WO2016070040A1 (en) | 2014-10-31 | 2015-10-30 | Heat exchanger refrigerant drain |
US15/522,886 US20170336096A1 (en) | 2014-10-31 | 2015-10-30 | Heat exchanger refrigerant drain |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/US2015/058307 A-371-Of-International WO2016070040A1 (en) | 2014-10-31 | 2015-10-30 | Heat exchanger refrigerant drain |
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US17/085,686 Continuation US20210048221A1 (en) | 2014-10-31 | 2020-10-30 | Heat exchanger refrigerant drain |
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US20170336096A1 true US20170336096A1 (en) | 2017-11-23 |
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US15/522,886 Abandoned US20170336096A1 (en) | 2014-10-31 | 2015-10-30 | Heat exchanger refrigerant drain |
US17/085,686 Abandoned US20210048221A1 (en) | 2014-10-31 | 2020-10-30 | Heat exchanger refrigerant drain |
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US17/085,686 Abandoned US20210048221A1 (en) | 2014-10-31 | 2020-10-30 | Heat exchanger refrigerant drain |
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US (2) | US20170336096A1 (en) |
CN (1) | CN208254307U (en) |
DE (1) | DE212015000255U1 (en) |
WO (1) | WO2016070040A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110017633A (en) * | 2018-01-03 | 2019-07-16 | 开利公司 | The condenser ballast of tape channel |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2021021463A1 (en) | 2019-07-29 | 2021-02-04 | Carrier Corporation | Condensate receptor with heat shield for vertical mounted v-coil heat exchanger |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1869973A (en) * | 1929-12-20 | 1932-08-02 | Babcock & Wilcox Co | Combined condenser and heater |
US3742866A (en) * | 1971-05-17 | 1973-07-03 | Acf Ind Inc | Tank car having sloping bottom |
US3991820A (en) * | 1975-12-18 | 1976-11-16 | Modine Manufacturing Company | Recuperator structure |
US3998069A (en) * | 1975-09-18 | 1976-12-21 | General Motors Corporation | Refrigerator receptacle support and adjustable air deflector-drip tray |
US4193443A (en) * | 1977-11-28 | 1980-03-18 | Orion Machinery Co., Ltd. | Heat exchanger for cooling system compressed air dehumidifiers |
US4415018A (en) * | 1981-06-01 | 1983-11-15 | Kaydee Engineering, Inc. | Heat transfer apparatus for transportable liquid containers |
JPS59180281A (en) * | 1983-03-30 | 1984-10-13 | Mitsubishi Heavy Ind Ltd | Condenser |
DE3732633A1 (en) * | 1987-09-28 | 1989-04-06 | Siemens Ag | Condenser for the water/steam circuit of power station installations |
US5320161A (en) * | 1992-08-14 | 1994-06-14 | Atlantic Richfield Company | Gelled formaldehyde transport method |
US6276442B1 (en) * | 1998-06-02 | 2001-08-21 | Electric Boat Corporation | Combined condenser/heat exchanger |
US6868689B1 (en) * | 2001-04-20 | 2005-03-22 | Buffalo Air Handling Company | Condensate drain pan |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2068074A (en) * | 1934-12-20 | 1937-01-19 | Fay T Rodgers | Refrigerator |
US5509466A (en) * | 1994-11-10 | 1996-04-23 | York International Corporation | Condenser with drainage member for reducing the volume of liquid in the reservoir |
US7971636B2 (en) * | 2004-07-05 | 2011-07-05 | Showa Denko K.K. | Heat exchanger with drain grooves |
CN101903736A (en) * | 2007-12-18 | 2010-12-01 | 开利公司 | Heat exchanger for shedding water |
-
2015
- 2015-10-30 WO PCT/US2015/058307 patent/WO2016070040A1/en active Application Filing
- 2015-10-30 CN CN201590001076.4U patent/CN208254307U/en active Active
- 2015-10-30 US US15/522,886 patent/US20170336096A1/en not_active Abandoned
- 2015-10-30 DE DE212015000255.1U patent/DE212015000255U1/en active Active
-
2020
- 2020-10-30 US US17/085,686 patent/US20210048221A1/en not_active Abandoned
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1869973A (en) * | 1929-12-20 | 1932-08-02 | Babcock & Wilcox Co | Combined condenser and heater |
US3742866A (en) * | 1971-05-17 | 1973-07-03 | Acf Ind Inc | Tank car having sloping bottom |
US3998069A (en) * | 1975-09-18 | 1976-12-21 | General Motors Corporation | Refrigerator receptacle support and adjustable air deflector-drip tray |
US3991820A (en) * | 1975-12-18 | 1976-11-16 | Modine Manufacturing Company | Recuperator structure |
US4193443A (en) * | 1977-11-28 | 1980-03-18 | Orion Machinery Co., Ltd. | Heat exchanger for cooling system compressed air dehumidifiers |
US4415018A (en) * | 1981-06-01 | 1983-11-15 | Kaydee Engineering, Inc. | Heat transfer apparatus for transportable liquid containers |
JPS59180281A (en) * | 1983-03-30 | 1984-10-13 | Mitsubishi Heavy Ind Ltd | Condenser |
DE3732633A1 (en) * | 1987-09-28 | 1989-04-06 | Siemens Ag | Condenser for the water/steam circuit of power station installations |
US5320161A (en) * | 1992-08-14 | 1994-06-14 | Atlantic Richfield Company | Gelled formaldehyde transport method |
US6276442B1 (en) * | 1998-06-02 | 2001-08-21 | Electric Boat Corporation | Combined condenser/heat exchanger |
US6868689B1 (en) * | 2001-04-20 | 2005-03-22 | Buffalo Air Handling Company | Condensate drain pan |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110017633A (en) * | 2018-01-03 | 2019-07-16 | 开利公司 | The condenser ballast of tape channel |
US10989452B2 (en) * | 2018-01-03 | 2021-04-27 | Carrier Corporation | Channeled condenser ballast |
CN110017633B (en) * | 2018-01-03 | 2022-09-23 | 开利公司 | Condenser ballast with channel |
Also Published As
Publication number | Publication date |
---|---|
WO2016070040A1 (en) | 2016-05-06 |
US20210048221A1 (en) | 2021-02-18 |
DE212015000255U1 (en) | 2017-06-06 |
CN208254307U (en) | 2018-12-18 |
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