The subject matter disclosed herein relates to heating, ventilation and air conditioning (HVAC) systems. More specifically, the subject matter disclosed herein relates to falling film evaporators for HVAC systems.
HVAC systems, such as chillers, use an evaporator to facilitate a thermal energy exchange between a refrigerant in the evaporator and a medium flowing in a number of evaporator tubes positioned in the evaporator. In a flooded evaporator, the tubes are submerged in a pool of refrigerant. This results in a particularly high volume of refrigerant necessary, depending on a quantity and size of evaporator tubes, for efficient system operation. Another type of evaporator used in chiller systems is a falling film evaporator. In a falling film evaporator, the evaporator tubes are positioned typically below a distribution manifold from which refrigerant is urged, forming a “falling film” on the evaporator tubes.
Falling film evaporators commonly employ a distribution system whose function is to convey liquid refrigerant equitably over the falling film tube bundle. The uniformity of liquid refrigerant supplied to the falling film bundle is critical to the performance of a falling film evaporator. One of the more effective approaches uses a separator to separate liquid refrigerant from the liquid-vapor refrigerant mixture that enters the separator. The liquid refrigerant is then drained from the separator and conveyed to a distribution manifold that meters the flow of liquid refrigerant equitably over the evaporator tubes. The separator may be located externally or internally to the evaporator however it is commonly the latter due to the added cost and complexity of the former by way of external piping, packaging and the requirement for the separator to meet pressure vessel certification standards, for example ASME VIII.
In one embodiment, a heating, ventilation and air conditioning (HVAC) system includes a compressor flowing a flow of refrigerant therethrough and a falling film evaporator in flow communication with the compressor. The falling film evaporator includes a plurality of evaporator tubes through which a volume of thermal energy transfer medium is flowed and a separator to separate a flow of liquid refrigerant from a vapor and liquid refrigerant mixture. A distributor distributes a flow of liquid refrigerant over the plurality of evaporator tubes. One or more vents stacks direct a flow of vapor or mostly vapor refrigerant from the separator into the vicinity of a refrigerant pool of the evaporator.
In another embodiment, a falling film evaporator includes a plurality of evaporator tubes through which a volume of thermal energy transfer medium is flowed and a separator to separate a flow of liquid refrigerant from a vapor and liquid refrigerant mixture. A distributor distributes a flow of liquid refrigerant over the plurality of evaporator tubes. One or more vents stacks direct a flow of vapor or mostly vapor refrigerant from the separator into the vicinity of a refrigerant pool of the evaporator.
These and other advantages and features will become more apparent from the following description taken in conjunction with the drawings.
The subject matter, which is regarded as the invention, is particularly pointed out and distinctly claimed in the claims at the conclusion of the specification. The foregoing and other features, and advantages of the invention are apparent from the following detailed description taken in conjunction with the accompanying drawings in which:
The detailed description explains embodiments of the invention, together with advantages and features, by way of example with reference to the drawing.
Shown in
Referring now to
A separator 42 is located in the housing 26 upstream of the distributor 30. In some embodiments, the separator 42 abuts the distributor 30, sharing a common wall. The separator 42 includes a refrigerant inlet 44 for vapor and liquid refrigerant mixture 24 to enter the separator 42. In some embodiments, the refrigerant inlet 44 is disposed at a lateral center of the separator 42. The separator 42 utilizes gravity to separate the liquid refrigerant 32 from the vapor and liquid refrigerant mixture 24, resulting in a volume of vapor refrigerant 36 in the separator 42. In some embodiments, the separator 42 also utilizes a mechanical eliminator 56 to further enhance liquid-vapor separation. Liquid refrigerant 32 leaves the separator 42 and enters the distributor 30 via one or more drains 46.
The liquid refrigerant 32 enters the sparge channel 48 via drains 46 in the separator 42. The sparge channel 48 may be a pipe having a circular cross-section, or may have other cross-sectional shapes, such as curvilinear, oval, triangular, rectangular or the like. Sparge channel openings 50 arranged on an upper portion 52 of the sparge channel 48 allow flow of the liquid refrigerant 32 out of the sparge channel 48, into the distributor chamber 30, and through a distribution sheet 54 forming a falling film over the evaporator tubes 28.
The vapor refrigerant 36 flows through the mechanical eliminator 56 if needed, which is, in some embodiments, one or more perforated plates or one or more mesh screens, toward a separator outlet 58. The mechanical eliminator 56 captures additional liquid refrigerant 32 entrained in the vapor refrigerant 36. Once through the separator outlet 58, the vapor refrigerant 36 and remainder of entrained liquid refrigerant 32 flows through a vent stack 60 downwardly into the evaporator 12, specifically with its' outlet in proximity with a refrigerant pool 62 at a bottom of the evaporator 12. The entrained liquid refrigerant in the vapor refrigerant 36 exiting the vent stack is captured in the refrigerant pool 62 thus allowing only vapor refrigerant 36 to return to the compressor 16 via the suction nozzle 38 and through the suction line 40. In the embodiments shown in
Another embodiment of evaporator 12 is illustrated in
Referring now to
Positioning the separator 42 inside of the evaporator housing 26 and closely coupling the separator 42 with the distributor 30 eliminates a need for large, expensive drain piping as well as eliminating the necessity of having the separator certified as an ASME VIII pressure vessel. Routing the vapor refrigerant 36 through the vent stacks 60 into the refrigerant pool 62 allows for higher tolerance of liquid entrainment in the vapor refrigerant 36 leaving the separator 42, as compared to systems where the vapor refrigerant is routed from the separator directly to the compressor. In some embodiments, the portion of liquid entrainment in the vapor refrigerant 36 is up to about 15-20%. As such, the separator 42 size can be reduced by 30-50% compared to a typical system, without affecting a size of the evaporator 12.
While the invention has been described in detail in connection with only a limited number of embodiments, it should be readily understood that the invention is not limited to such disclosed embodiments. Rather, the invention can be modified to incorporate any number of variations, alterations, substitutions or equivalent arrangements not heretofore described, but which are commensurate with the spirit and scope of the invention. Additionally, while various embodiments of the invention have been described, it is to be understood that aspects of the invention may include only some of the described embodiments. Accordingly, the invention is not to be seen as limited by the foregoing description, but is only limited by the scope of the appended claims.
Filing Document | Filing Date | Country | Kind |
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PCT/US2014/044785 | 6/30/2014 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
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WO2015/034573 | 3/12/2015 | WO | A |
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Entry |
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Notification of Transmittal of the International Search Report and the Written Opinion of the International Searching Authority, or the Declaration; Application No. PCT/US2014/044785; dated Oct. 29, 2014; 9 pages. |
Chinese Office Action Issued in on Application No. 201480048901.6, dated May 25, 2015, 8 pages. |
Number | Date | Country | |
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20160201991 A1 | Jul 2016 | US |
Number | Date | Country | |
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61874614 | Sep 2013 | US |