Not applicable.
Not applicable.
This disclosure is related to the field of refrigeration and heat pumping technology, primarily, but not exclusively to home and industrial applications.
An ejector heat cycle device is known in the art using oil in a refrigeration recycle loop comprising a heater-cooler system. In such device, refrigerant circulates through a cooler absorbing heat from outside of the cycle, and then through the heater exchanges excess heat to the outside of the refrigeration cycle. In the foregoing device the heater is connected with a cooler through an ejector and a separator. The ejector motive fluid is a second liquid—immiscible with the refrigerant fluid—is circulated by a mechanical compressor (see, e.g., U.S. Pat. No. 7,086,248 issued to Sakai et al. on Aug. 8, 2006, incorporated herein by reference).
There is a need for a method and system having higher energy efficiency than the device shown in the Sakai et al. '248 patent.
One aspect of the invention is a heat pumping unit including a first heat exchanger, a second heat exchanger and a pump. An outlet of the first heat exchanger is connected to a vapor inlet of a liquid jet-ejector. A liquid outlet of the ejector is connected to an inlet of the second heat exchanger. An outlet of the second heat exchanger is connected at the same time to an inlet of the pump and through a pressure reducing device to an inlet of the first heat exchanger. The pump outlet is connected to the liquid-jet ejector liquid inlet.
Other aspects and advantages of the invention will be apparent from the description and claims which follow.
The liquid knockout drum (6) has a vapor outlet port connected to the vapor inlet port (2B) of the liquid-jet ejector (2), wherein the liquid inlet port (2A) thereof is connected to the discharge port (5B) of the circulating pump (5). Condensed liquid from the liquid-jet ejector liquid outlet nozzle (2C) is directed to the second heat exchanger (3). Liquid cooled in the second heat exchanger (3) may be directed to the suction port (5A) of the circulating pump (5), and another portion thereof is directed to a pressure reducing device (e.g., a valve) (4) and then to the first heat exchanger (1).
The liquid knockout drum (7) vapor outlet port is connected to the vapor inlet port (2B) of the condensing liquid-jet ejector (2), wherein the liquid inlet port (2A) thereof is connected to the discharge port (5B) of the circulating pump (5), and condensed liquid from the liquid-jet ejector liquid outlet nozzle (2C) is directed to the second heat exchanger (3). The liquid cooled in the second heat exchanger (3) is directed to the accumulator drum (6). A portion of cooled liquid from the second heat exchanger (3) is sent to the suction port (5A) of the circulating pump (5), and another portion thereof is directed to the pressure reducing device (e.g., a valve) (4) and then to the first heat exchanger (1).
The liquid knockout drum (6) vapor outlet port is connected to the vapor inlet port (2B) of the condensing liquid-jet ejector (2), The liquid inlet port (2A) thereof is connected to the discharge port (5B) of the circulating pump (5), and condensed liquid from liquid-jet ejector liquid outlet nozzle (2C) is directed to the second heat exchanger (3). Liquid cooled in the second heat exchanger (3) is directed to the accumulator drum (7), wherein a portion of the cooled liquid from the second heat exchanger (3) is sent to the suction port (5A) of the circulating pump (5), and another portion of the cooled liquid is directed to a multi-pass heat exchanger (1D) wherein the pressure reducing device (valve) (4) is located between a first heat exchanger pass (1F) and a second heat exchanger pass (1E).
The liquid knockout drum (7) vapor outlet port is connected to the vapor inlet port (2B) of the liquid-jet ejector (2), wherein the liquid inlet port (2A) thereof is connected to the discharge port (5B) of the circulating pump (5). Condensed liquid from the liquid-jet ejector liquid outlet nozzle (2C) is directed to the second heat exchanger (3), wherein cooled liquid from the heat exchanger (3) is directed to the accumulator drum (4). A portion of cooled liquid from the second heat exchanger (3) is sent to the suction port (5A) of the circulating pump (5). Another two portions of liquid from the heat exchanger (3), is each directed to a corresponding pressure reducing device (e.g., valves) (4A) and (4B) and then to corresponding first heater exchangers (1G) and (1H). The parallel first heat exchangers (1G, 1H) perform similar functions to the first heat exchanger (1) shown in
The above described example refrigeration and heat pumping units can be applied in refinery, natural gas processing, chemical and petrochemical, food and other industries, as well as in residential air conditioning and refrigeration applications.
While the invention has been described with respect to a limited number of embodiments, those skilled in the art, having benefit of this disclosure, will appreciate that other embodiments can be devised which do not depart from the scope of the invention as disclosed herein. Accordingly, the scope of the invention should be limited only by the attached claims.
Number | Name | Date | Kind |
---|---|---|---|
3277660 | Kemper et al. | Oct 1966 | A |
3659401 | Giammarco | May 1972 | A |
4007776 | Alkasab | Feb 1977 | A |
5209284 | Okamoto et al. | May 1993 | A |
6398918 | Popov | Jun 2002 | B1 |
6675609 | Takeuchi et al. | Jan 2004 | B2 |
7061763 | Tsoi | Jun 2006 | B2 |
7086248 | Sakai et al. | Aug 2006 | B2 |
7254961 | Oshitani et al. | Aug 2007 | B2 |
7399545 | Fly | Jul 2008 | B2 |
8012247 | Popov et al. | Sep 2011 | B2 |
20040231833 | Wang et al. | Nov 2004 | A1 |
20050048339 | Fly | Mar 2005 | A1 |
20050083654 | Tsoi | Apr 2005 | A1 |
20090292084 | Sellmann et al. | Nov 2009 | A1 |
20100258007 | Popov et al. | Oct 2010 | A1 |
20100313582 | Oh et al. | Dec 2010 | A1 |
20110220729 | Bucknell | Sep 2011 | A1 |
Number | Date | Country | |
---|---|---|---|
20140196494 A1 | Jul 2014 | US |