|Publication number||US2511565 A|
|Publication date||Jun 13, 1950|
|Filing date||Mar 3, 1948|
|Priority date||Mar 3, 1948|
|Publication number||US 2511565 A, US 2511565A, US-A-2511565, US2511565 A, US2511565A|
|Inventors||Franklyn Y Carter|
|Original Assignee||Detroit Lubricator Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (2), Referenced by (24), Classifications (6)|
|External Links: USPTO, USPTO Assignment, Espacenet|
June 13, 1950 F. Y. CARTER 1 2,511,565
REFRIGERATION EXPANSION VALVE Filed March 3, 1948 Fl pd g I TEMP g Fl(5 2 2 INVENTOR.
I BY W 90 SUCTION TEMP 0 K v ATTORNEY Patented June 13, 1950 aararcaaa'nou man sron vanva 1 I Franklyn Y. Carter, Dcarborn, Mich, assignor to Detroit Llbrieator Company. 1m a corporation of Michigan Application March a. 1m. Serial N 12,816
This invention relates tonew and useful improvements in refrigeration expansion valves.
. ing temperatures.
Other objects will be apparent from time to time throughout the specification and claims as hereinafter related.
This invention comprises the new and improved construction and combination of parts and the cooperative relation therebetween which will be described more fully hereinafter and the novelty of which will be particularly pointed out and distinctlyclaimed.
. In the accompanying drawings, to be takenas part of the specification thereis clearly and fully illustrated one preferred embodiment of this invention in which drawing:
Figure 1 is a view in longitudinal cross section of a refrigeration expansion valve embodying one form of this invention, which valve is shown diagrammatically in a, refrigeration system,
Fig. 2 is an illustrative pressure-temperature curve to show the variation of required temperature diiferentials for opening an expansion valve upon change of operating temperature, and
Fig. 3 is a curve showing change of superheat setting of a conventional expansion valve upon decrease of operating temperature. Referring to the drawing by characters of ref erence, there is a compressor driven by a motor 2 which supplies refrigerant to a condenser 2 and a receiver 4. From the liquid refrigerant receiver 4 refrigerant passes through a conduit 5 to the inlet 2 of a thermostatic expansion valve 1 which embodies this invention. The outlet 2 of the expansion valve I is connected to an evaporator 2 which is in turn connected to the suction side of the compressor The expansion valve I comprises a main body portion Ill having an inlet projecting portion H and an outlet projecting portion i2. There is a cavity I: in the inlet proiecting portion H which houses a strainer II which is held in position by an inlet fitting it into which opens the inlet 6. The valve casin 4 Claims. (01. 2-4) II has an enlarged end portion i2 withjan annular cavity i'l therein. Therejis an wallinember l2 which covers the enlarged end portion l2 and closes the annular cavity ii. The inlet cavity I2 is connected by a passageway is to the annular cavity II which is'in turn connected by passageways 20 and 2| to a longitudinal cavity 22 in the valve casing II. There is a hollow plug member 22 screw-threadedly'secured in the passageway 2| and forming a valve port 24 for'discharge of refrigerant into the cavity 22. There is an outlet passageway 22 leading from the cavity 22 through the outletprojecting'portion l2. Positioned in the valve'cavity22'there is a valve carrier'member 2| which is'operableto have longitudinal movement therein andwhich carries a valve member 21 whichis cooperable with the plug or valve seat member 22. There is a helical spring 22 which is compressively' positioned against the valve carrier member 22 and is operable to urgethe valve memberffl toward closed position. At the enlarged end," of the valve casing ll there is a dish-shaped cover member 29 which covers the end cover member I! and which is secured thereto 'by an intumed flange portion 22 of the end member-i2. Positioned between the end member II and the cover member 29 is a flexible diaphragm 2| which is sealed between the circumferential edges of the'end membet I! and the cover member 22 and which forms with the cover member 22 an enclosed chamber 22. There is a conduit 22 which is secured in an aperture in the end wall portion; 24 of the cover member 29 and which opens'into the chamber 22. The other end of the conduit 22 has secured thereon a thermostatic bulb element 25 which contains a volatile thermostatic fluid responsive to temperature changes and operable to transmit pressure to the enclosed chamber '22 to actuate the diaphragm 2|. Within the'cha'mbe'r 22 there is a plate member 26 positioned on the diaphragm 2|. Also within the chamber 22 there is a'helical spring 21 compressively positioned between the cover member end wall portion 24 and the plate member 26. On the other side of the diaphragm 3| there is another plate member 32, which is operable to transmit movement of the diaphragm 2| to a plurality of thrust rods 2! which are slidably positioned in longitudinal passageways in the valve casing It. The thrust rods 39 are operable to transmit movement from the diaphragm 2| to the valve carrier member 22 and operate to move the valve member 21 in opposition to the compressive force of the spring 22. There is a Projecting casing portion 40 which is begin opening of the valve.
screw-threadedly secured to the valve casing it as at ll and which is formed in two sections l2, 43 which are screw-threadedly secured to ether as at N. There is a hollow cavity 45 in the easing portion ll which is connected by an, aperture l to the cavity 2! in the main casing II. The casing portion ll has a hollow end portion 41 in which is positioned an adjustment screw 40 which extends through an aperture in the end wall 40 of the casing portion ll. Secured on the end of the adjustment screw ll is the base portion ll of a cylindrical member II in which is positioned an expansible-contractable bellows II. The bellows I2 is sealed to the base portion I and has a cloud end wall member it from which extends the projecting cylindrical abutment I4 whichextends through the aperture It and engages the base of a supporting member I for thehelical spring as. Positioned within the bellows I! is a helical spring II which urges the bellows toward an expanded position. The bellows 52 is charged through a filler tube 51 with volatile thermostatic fluid which has .a different rate of change of pressure with temperature than the refrigerant fluid used in the system. The superheat setting of this valve is determined by adjustment of the screw 48 which varies the compression of the spring 28 acting on the valve carrier member 28. There is a cover member is which closes the adjustment screw end portion of the projecting portion 41.
In operation this form of the invention functions as follows:
This expansion valve, at normal operating temperatures, functions as a conventional expansion valve, the operation of which is obvious from the system illustrated. Refrigerant vapor is compressed by the compremor I, condensed in the condenser 3 and supplied to the receiver 4 from which liquid refrigerant passes through the conduit 8 to the inlet 6 of the expansion valve. From the outlet I of the expansion valve 1 refrigerant passes to the evaporator I wherein the refrigerant fluid is evaporated for cooling and from which evaporator the refrigerant vapor passes to the suction side of the compressor I. The expansion valve I is designed to respond normally to the pressure at the inlet and to the temperature at the outlet end portion of the evaporator 9. Changes in temperature at the outlet of the evaporator I and the bulb 35 result in a change of pressure within the chamber 32 thereby changing the differential of pressure acrossthe diaphragm II to cause movement thereof thereby to move the pins or thrust rods 39 to move the valve member 21 toward or away from its seat to permit greater or less flow, ofrefrigerant through the valve. The difl'erential of pressure across the diaphragm ll. necessary to move the valve member 21 is determined by the extent of compression of the spring 28 acting in opposition thereto. The spring 2. as heretofore mentioned is operable to determine the superheat setting of the valve.
Referring to Fig. 2 there is shown a pressuretemperature curve for a volatile liquid refrigerant. For operation of the expansion valve in the usual temperature range of say 30 to 40 F. a certain pressure differential will be required to On the pressure temperature curve this opening pressure differential (commonly known as superheat when expressed as a temperature diiferential) is shown as m; projecting the pressure differential in on the pressure'-temperature curve and then P jecting the temperature diiferential to the temperature axis we flnd that a temperature differential t1 is required to begin to open the valve. when the valve is operated at a very low temperature such as minus 60' I". or lower the pressure differential required to open the valve will be substantially the same as that which is indicated on the curve as pa. While the pressure requirement in and p: are substantially equal the pressure-temperature curve at this extremely low temperature is of a much lower slope than at plus 30 to 40 ll; hence, the temperature differential required to produce this pressure differential for opening the valve will be much greater, as for example. is. It is seen then from this referenceto the pressure temperature curve that the opening temperature diil'erential of the valve is affected by operation at extremely low temperatures. I
Referring to the superheat curve in Fig. 3 we find that if a valve of the single diaphragm type is operated at say with a superheat setting and this same valve is then operated at say minus 90 the superheat setting of the valve will be found to have increased to about 25. This increase of superheat setting is characteristic of single diaphragm type valves when operated at extremely low temperatures and the cause is apparent from the previous reference to the pressure temperature curve of Fig. 2. The change of superheat setting is especially pronounced when the bulb element is charged with the same fluid as that used in the system. In the expansion valve shown in Fig. 1 there has been provided a means to compensate for this tendency for excessive increase in superheat upon operation of the valve at extremely low temperatures. The spring 28 which determines the superheat setting of the valve is held in its compressed position by the bellows I2 and thrust member portion 54. The bellows 52 is normally charged with a volatile fluid having a greater rate of change of pressure with temperature than the refrigerant used in the system so that upon decrease of operating temperature of the valve the pressure within the bellows 62 will decrease at a slightly greater I rate than the pressure outside the bellows. The bellows 52 by reason of being only partly fllled with volatile liquid is responsive to temperature and pressure of fluid refrigerant on the outlet side of the valve port 24 which enters the chamher or cavity 48 through the aperture 48. This described decrease of-pressure within the bellows 52 will cause the bellows to collapse a predeter- 55 mined amount in accordance with the temperature and pressure of the refrigerant outside the bellows relative to the pressure inside the bellows thereby decreasing the compressive force of the spring 28 and permitting the valve member 21 so to be moved by lower pressure diilerentials across the diaphragm 3| This decreasein pressure differential required to open the valve member II will cause a decrease in the superheat setting of the valve for the temperature at which it is operated so that the increase of superheat setting at extremely low temperatures will be greatly reduced and will follow a compensated curve such as the dotted superheat curve a" in Fig. 3. The following example is given to illustrate fully the operating characteristics of this valve. It should be understood, however, that other refrigerants could be used subject to proper selection of the relative sizes of the springs and bellows. ,Assume that the system, the bulb elezs ment 3!, and the space 82 are charged with a force of 5 pounds for the spring 31, and a superheat setting of 10' at 1". .At 0 1!. bulb temperature the pressure of the refrigerant 1"-l2" in the chamber 32 acting on the diaphragm 3| is 23.9 p. s. i. (or 23.9 pounds for a one square inch diaphragm).
The total pressure acting downward on the diaphragm ll then is 23.9 pounds plus the 5 pounds force of the spring 31 or a total of 23.9 pounds. At a superheatsettlng the suction temperature in the valve is minus 10 1". and the pressure of "1'42" acting upward against the diaphragm II is 19.2 pounds. The diiierence between the downward and upward iorces on the diaphragm ii is 9.! pounds net downward force which force is equalized by the spring 23 which is calibrated to resist this force. Assume, for a moment, that this expansion valve has no compensating bellows and the rise in superheat at very low temperatures will be demonstrated. When the valve is operated at a suction temperature of minus l". the pressure of the "F-12 upward on the diaphragm 3! is only 2.9 pounds which plus the 4.7 pounds net force of the spring 23 over the spring l'l gives a total upward force of 7.6 pounds which is counteracted by bulb element pressure above the diaphragm 3|. This 7.6 pounds (or p. s. i.) above the diaphragm 3| represents a bulb temperature of minus 47 F. and a superheat 33". It is thus seen that an initial superheat setting of 10' at minus 10 1''. suction temperatures will increase to 33 at minus 80 F. The compensating effect of the bellows 62 will now be demonstrated. The bellows l2 and its internal spring 96 must carry the reactive thrust of the spring 22. At the initial suction temperature of minus 10 F. the bellows 92 is fully extended against the inturned end of the cup-shaped member II. The bellows at this point is carrying the 9.1 pound reactive thrust of the spring 23. The pressure of I -22" within the bellows 52 (at minus 10 F.) is 31.3 p. s. i. and the pressure of F-12 around the bellows is 19.2 p. s. i. The net expansive force of the bellows then is 12.1 p. s. i. times .31 square inch or a total force of 3.7 pounds. The force of the spring 86 then must be 6 pounds (1. e., the difference between the 9.! pound thrust of the spring 29 and the 3.7 pound expansive force of the bellows 52). When the valve is operated at a suction temperature of minus 80' F. the pressure of '-F-22 within the bellows I2 is 4.8 p. s. l. and the pressure around the bellows is 2.9 p. s. i. (pressure of F-12). This pressure difl'erential is 1.9 p. s. i. or .6 pound (1.9 times .31). The total expansive force of the bellows S2 and spring 66' has thus been reduced to 6.6 pounds (6 pounds spring force plus. .6 pounds expansive force) which represents the force now exerted on the diaphragm II by the spring 23. The net upward spring force on the diaphragm 3| of 1.6 pounds (i. e., the force of spring 23 of 6.6 pounds minus the 5.0 pound downward force of spring 31) plus the 2.9 pound pressure 01' F-12" (at minus 80 F.) on the diaphragm 3| totals 4.5 pounds upward diaphragm force which is counteracted by bulb element pressure above the diaphragm. This 4.5 pound bulb element pressure represents a bulb temperature of minus 65' F. and a superheat setting of 15. From the foregoing it is seen that the compensating bellows element has a. .materialiy reduced the increase in superheat by the use of vapor pressures of diiierent refriger- I ants (inside and outside the bellows) for compensation the compensation of the superheat curve is logarithmic in nature so that the superheat curve will approach a straight line. Bimilar compensation can be obtained by use of other refrigerants having high rates of pressure change,
such as ammonia, carbon dioxide or ethane and the superheat can actually be reduced below its initial setting if the bulb element and diaphragm chamber are charged with a refrigerant having a very low rate of pressure change (such v as methyl chloride).
In summary, it is seen that there is provided a conventional single diaphragm type expansion valve which has the characteristic increase of superheat setting at extremely low operating temperatures. There is also provided a bellows which is charged with a fluid having a rate of pressure change greater that that of the refrigerant used in the system so that upon decrease of operating temperature the bellows will tend to collapse. The collapsing of the bellows as described heretofore is operable to decrease the compression of the spring which tends toclose the valve and thus the superheat setting of the valve is reduced so that a much smaller increase of superheat at extremely low temperature is accomplished.
It should be obvious that-if for any reason it is desired to increase the superheat setting of the valve at lower temperatures, it would merely be necessary to charge the bellows I2 with a volatile fluid which had a lower rate of change of pressure with temperature than the refrigerant used in the system so that upon decrease of operating compression of the spring 23 and with it the superheat setting of the valve. It should also be obvious that by proper selection of a volatile,
fluid for charging the bellows 92 the superheat curve as shown in Fig. 3 may be compensated in either direction to almost any extent for'any desired operating temperature.
Having thus described the invention what is claimed and is desired to be secured by Letters Patent of the United States is:
1. In a refrigeration expansion valve. a movable valve member for controlling flow of refrigerant, thermostatic means cooperable with and operable to move said valve member toward an open position, spring means urging said valve member toward closed position in opposition to said thermostatic means and determining the superheat setting of said valve, an expansible and contractable-bellows,positioned on the outlet side of the valve and charged with a volatile fluid having a different rate of change of pressure relative to change in temperature than the refrigerant passing through said valve, said bel- 7. iows' being cooper-able with said spring means and being responsive to the temperature and pressure of refrigerant flowing from the valve, and said bellows expanding and contracting in accordance with the diflerential of internal and external pressure therearound to vary the coma,su,ses
pressive force of said spring means and thereby to vary-the superheat setting of said valve.
2. A refrigeration expansion valve comprising a valve casing having an inlet passageway and an outlet passageway, an internal passageway interconnecting said inlet and outlet passageways and having a valve port forming a valve seat, a valve member cooperable with said valve seat to control flow of refrigerant fluid through said port, said outlet passageway being operable to discharge refrigerant fluid to an evaporator, a flexible diaphragm covering one end of said casing, a dish-shaped cover member secured to said casing end and sealing said diaphragm to said casing end, said cover member and said diaphragm forming an expansible and contractable chamber, a thrust rod slidably positioned in said casing and extending from said diaphragm to said valve member. a tube opening at one end into said chamber through said cover member andextending from said cover member, a bulb element secured to the other end of said tube and opening into said tube, said bulb element being charged with a volatile fluid and operable to respond to the temperature of a refrigerant evaporator by transfer of fluid pressure through said tube to said chamber for actuating said diaphragm, said diaphragm being operable in response to the differential between fluid pressure from said bulb element and refrigerant pressure in said valve to move said thrust rod thereby to move said valve member away from said valve seat, a helical spring compressively positioned v heat setting of said valve, a supporting member for said spring, an expansible and contractable bellows positioned on the outlet side of the valve and charged with a volatile fluid having a greater rate of change of pressure relative to change in temperature than the refrigerant fluid passing through said valve, said bellows having an abutment abutting said spring supporting member and being operable upon movement to determine the compression of said spring, said bellows being, responsive to the temperature and pressure of refrigerant fluid flowing from said valve port, and said bellows contracting in accordance with the differential of internal and external pressures therearound to reduce the compressive force of said spring at low refrigerant fluid temperature to reduce the superheat setting of said valve thereby to compensate for the increase in superheat setting of said valve at low temperatures.
3. In a refrigeration expansion valve, a movable valve member for controlling flow of refrigerant, thermostatic means cooperable with and operable to move said valve member toward an open position, a spring having one end engaging said valve member and urging the same toward closed position, the compressive force of said spring determining the superheat setting of said valve, a sealed thermostatic element including an expansible and contractible member operatively engageable with and supporting the other end of said spring, said thermostatic element containing a partial charge of volatile liquid having a different rate of change of pressure relative to change in temperature from that of-the refrigerant passing through said valve,- and said expansible and contractible member being positioned for subjection to the temperature and pressure of the refrigerant on the outlet side of said valve member such that the differential of internal and external fluid pressures acting on said .expansible and contractible member determines the compressive force of said spring.
4. In a thermostatic refrigeration expansion valve, a valve casing having a port, a movable valve member cooperable with said port to control flow of refrigerant, thermostatic means operable upon temperature increase to urge said valve member toward open position, means to compensate for change in the valve superheat setting and comprising a sealed thermostatic element including a resilient wall member, said element being partially fllled with a' volatile liquid having a greater rate of change of pressure relative to change in temperature than the refrigerant to be controlled, said casing having an open chamber on the outlet side of said valve member, said wall member being positioned in said chamber for response to the temperature and pressure of the refrigerant on the outlet side of saidv'alve member, and a spring interposed between said wall member and said valve and urging said valve membertoward closed position, the force exerted by said spring being determined by the diiferential of the fluid pressures acting on the opposite sides of said wall member.
FRANKLYN Y. CARTER.
nsrnnnncns crrnn The following references are of record in the
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US1965552 *||Nov 19, 1932||Jul 3, 1934||Fedders Mfg Co Inc||Refrigerant control device|
|US2363010 *||Apr 29, 1941||Nov 21, 1944||Gen Controls Co||Refrigerant control system|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US2755025 *||Apr 18, 1952||Jul 17, 1956||Gen Motors Corp||Refrigeration expansion valve apparatus|
|US2971348 *||Sep 6, 1957||Feb 14, 1961||Controls Co Of America||Thermostatic expansion valve|
|US5065595 *||Dec 5, 1990||Nov 19, 1991||Sporlan Valve Company||Thermostatic expansion valve|
|US5615560 *||Apr 16, 1996||Apr 1, 1997||Sanden Corporation||Automotive air conditioner system|
|US6185958||Nov 2, 1999||Feb 13, 2001||Xdx, Llc||Vapor compression system and method|
|US6314747||Jan 12, 1999||Nov 13, 2001||Xdx, Llc||Vapor compression system and method|
|US6393851||Sep 14, 2000||May 28, 2002||Xdx, Llc||Vapor compression system|
|US6397629||Dec 6, 2000||Jun 4, 2002||Xdx, Llc||Vapor compression system and method|
|US6401470||Sep 14, 2000||Jun 11, 2002||Xdx, Llc||Expansion device for vapor compression system|
|US6401471||Nov 20, 2001||Jun 11, 2002||Xdx, Llc||Expansion device for vapor compression system|
|US6581398 *||Jul 10, 2001||Jun 24, 2003||Xdx Inc.||Vapor compression system and method|
|US6644052||Nov 18, 1999||Nov 11, 2003||Xdx, Llc||Vapor compression system and method|
|US6751970||Nov 26, 2002||Jun 22, 2004||Xdx, Inc.||Vapor compression system and method|
|US6857281||Mar 16, 2001||Feb 22, 2005||Xdx, Llc||Expansion device for vapor compression system|
|US6915648||Dec 20, 2002||Jul 12, 2005||Xdx Inc.||Vapor compression systems, expansion devices, flow-regulating members, and vehicles, and methods for using vapor compression systems|
|US6951117 *||May 26, 2000||Oct 4, 2005||Xdx, Inc.||Vapor compression system and method for controlling conditions in ambient surroundings|
|US7225627||Sep 23, 2004||Jun 5, 2007||Xdx Technology, Llc||Vapor compression system and method for controlling conditions in ambient surroundings|
|US9127870||Oct 28, 2010||Sep 8, 2015||XDX Global, LLC||Surged vapor compression heat transfer systems with reduced defrost requirements|
|US20030121274 *||Dec 20, 2002||Jul 3, 2003||Wightman David A.||Vapor compression systems, expansion devices, flow-regulating members, and vehicles, and methods for using vapor compression systems|
|US20050257564 *||Sep 23, 2004||Nov 24, 2005||Wightman David A||Vapor compression system and method for controlling conditions in ambient surroundings|
|US20070220911 *||May 14, 2007||Sep 27, 2007||Xdx Technology Llc||Vapor compression system and method for controlling conditions in ambient surroundings|
|US20110126560 *||Oct 28, 2010||Jun 2, 2011||Xdx Innovative Refrigeration, Llc||Surged Vapor Compression Heat Transfer Systems with Reduced Defrost Requirements|
|WO1996007066A1 *||Jul 8, 1995||Mar 7, 1996||Ernst Flitsch Gmbh & Co.||Process for setting the static overheating in expansion valves for coolant circuits|
|WO2008080436A1 *||Jan 4, 2007||Jul 10, 2008||Carrier Corporation||Superheat control for refrigeration circuit|
|U.S. Classification||62/212, 236/92.00B|
|Cooperative Classification||F25B2600/21, F25B41/062|