US1704177A - Heat-transforming apparatus - Google Patents
Heat-transforming apparatus Download PDFInfo
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- US1704177A US1704177A US171465A US17146527A US1704177A US 1704177 A US1704177 A US 1704177A US 171465 A US171465 A US 171465A US 17146527 A US17146527 A US 17146527A US 1704177 A US1704177 A US 1704177A
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- condenser
- evaporator
- orifice
- liquid
- pump
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- 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
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
Definitions
- This invention relates to apparatus for transforming heat, particularly refrlgerating system of the closed cycle type. While the invention has general application, it has been developed with particular relation to small automatic' and self-contained refrigerating outfits such asthose intended for household use. v
- the feeding means In systems Operating on the conventional oycle the feeding means usually takes the form of a valve or variable orifice, the Variation being controlled by changes either in the vaportension or in the level of the liquid 1n 'the evaporator and is generally called by the misleading name of expansion valve.
- One object of my invention is to provide a simplified form of apparatus for refrigeration by changes of state of the refrigerant fluid* liquid.
- ⁇ Another object is to permit easy control of the Operating characteristics4 of a closed cycle system.
- Still another ob- ⁇ ject is to provide simple ways and means for interposing the necessary resistance to the passing of the working -substance from the high side to the lower side of the system, as from the condenser to the evaporator.
- valve or variable orifice theinvention involves the use in a particular location of a fixed orifice having a Critical relation to the capacity of the pump or com'- pressor.
- the orifice is formed in a disk shaped member or diaphragm which may serve the 'additional 'purpose of a sealing gasket 1n a detachable fitting provided in the connection between the condenser and the evaporator.
- Figs. 1 and 2 are dlagrammatic views illustrating different arrangements of parts in closed cycle systems.
- the feeding device infeach view beo discharging the fluid drawn from the evap-' Orator 7 at a higher pressure and temperature -into a condenser 8 from which the condensed i refrlgerant 1s fedl ⁇ back into evaporator 7 through the feeding device or control memher 9.
- Control device 9, to which the inven- .tion particularly relates, is shown in full detail in F ig. 3 and in its preferred form comprises a slmple fittmg or ⁇ un1onhav1ng a part 10 secured to the condenser connection and a ⁇ part 11 secured to the evaporator connection,
- Figs. 4: and 5 show in plan typical disk members or diaphragms 13 with orifices 14 of different sizes.
- the disk members or diaphragms 13 shown in Figs. 2, 3 and 4 have an orifice of suificient size to pass at the same time both the liquid and the gaseous products of the condenser 8 so that the system may operate upon the vapor gas principle referred to above.
- the diaphragm member 18 shown in Fig. 5 has a smaller'orifice 14 which so restricts the passage of fiuid from the condenser to the evaporator that a body of liquid will gather at the left of feeding device 9 in Fig. 1 or above the feeding device 9 in Fig.
- the proper size of the orifice to cause the system to operate on the desii'ed cycle is determined to some extent by the density, viscosity, and other characteristics of the selected working' substance and to a far greater extent by the capacity or displacement of the pump which is used. In any event the size of the orifice bears a critical relation to the pump capacity with a given displacement and given working substance.
- the size of the orifice for securing the desired Operating characteristics of the system may be easily determined rempirically, and once determined may be standardized for the range of conditions commercially encountered.
- orifice must be large enough to revent the accumulation of liquid for more t an a short period directly after starting the machine with the refrigerator at the upper end of its Operating temperature range. With an orifice of proper size it will be found, of course, that on the initial running of the apparatus with the refrigerator at room temperature there will be a temporary loading u of liquid at the orifice but this lasts only a s ort time and is 'an advantage rather than a disadvantage as it tends toward the self-limiting of the load imposed on the compressor.
- the upper size limit for a feed orifice in a given system is reached when the low side or i'ator.
- the condenser 8 be disposed at a higher level than the feeding device 9. At least the connection from the condenser to the feeding device 9 should be so disposed that the condensate shall drain by gravity to the latter.
- the preferred arrangements of parts are shown diagrammatically in Figs. 1 and 2. While the system will operate efliciently on the vapor gas cycle witheither of the arrangements shown in Fig. 2 the particular dis osition of the feeding device which is pre erable is shown in Figs.
- disk 18 is disposed horizontally and is slightly dished upwardly so that the condensate intercepted by the diaphragm drains toward the orifice and is blown or carried through the orifice by the gaseous component of the working substance.
- Apparatus for produeing heat transforming effects comprising an evaporator, a
- Apparatus for producing heat ⁇ transforming effects comprising an evaporator, a pump, and a condenser connected together to form a closcdcycle system, a detachable fitting in the 'connection between said condenser and said evaporator, and havin a removable feeding element, said fitting bemg arranged for interchangeable association with another feeding element for varying the a Operating characteristics of said system.
- Apparatus for producing heat transforming eflects comprising an evaporator, a pump, and a condenser connected together to form a closed cycle system, a .detachable fitting in the connection between said condenser and said evaporator, and having a perforated disk as a feeding element arranged to assist in the sealing o f said fitting,
- Apparatus for prod-ucing heat transforming. effects comprising an evaporator, a
- Refrigerating apparatus comprising an evaporator, a pump, and a condenser, connections between said parts to form a closed cycle system, and a horizontally disposed member extending transversely of theconnection ⁇ between said condenser and said evaporator, said member havin an opening theretlirough bearing a critica relation to the capacity of said pump and arranged to pass the liquid products of the condenser around the peripliery of the opening and the gaseous products through the center of the opening.
- Refrigerating apparatus comprising an evaporator, a pump, and a condenser, connections between said parts to form a closed cycle system, and a horizontally disposed member extending transversely of the connection' between said condenser and said evaporator, said member having an opening therethrough bearing a Critical relation to the capacity of said pump, said condenser being disposed above said member and arranged to .drain by gravity directly tliereto so that the liquid ing a Critical relation to the capacity of said pump for controlling the feeding of fluid from the condenser to the evaporator.
- Refrigerating apparatus comprising an'- ⁇ evaporat'or, a pump, and a condenser, connections between said parts to form a closed cycle system, a detachable fitting in a substantially Vertical portioii of the connection between said condenser and said evaporator, and 'an upwardly dished diaphragm in said fitting having an-opening tlieretlirough bearing a 'Critical relation to the capacity of said pump for controlling the feeding of fluid from the condenser 'to the evaporator, said diapliragm also serving as a sealing ⁇ gasket for said fitting.
Description
March 5, 1929. R. w. DAvENPoRT 1,'704'177 HEAT TRNSFORMING APPRATUS Filed Feb. 28, 1927 I N VEN TOR.
A TTORNEY.
Pal/750m W Dave/Yporf Patented Mar. 5, 1929.
. 1,74,177` UNITED sTATEs -PATENT oFF1cE.-
RANSOMI W. DAVENPORT, OF DETROIT, MICHIGAN, SIGNOR TO CHICAGO PNU'- MATIC TOOL COMPANY, OF NEW YORK, N. Y., A CORPORATION OF NEW JERSEY.
` HEAT-TRANSFORMING APPARATUS.
Application filed February 28, 1927. Serial No.v171,465.
This invention relates to apparatus for transforming heat, particularly refrlgerating system of the closed cycle type. While the invention has general application, it has been developed with particular relation to small automatic' and self-contained refrigerating outfits such asthose intended for household use. v
In a closed cycle refrigerating system of the condenser-compressor-evaporator type 1t is necessary to provide means for feedmg condensed refrigerantcfrom the condenser to the evaporator to make up for the liquid evaporated in the latter by the action of the compressor. If liquid alone is passed from condenser to evaporator the system operates upon the conventional or straight .cycle Tf the system contains a gas in addltlon to a volatile liquid andif the feeding means between the condenser and the evap'orator passes the gas along with the condensed liquid the system operates upon thevapor gas principle, disclosed in my co-pendmg application' Serial No. 15,172, filed March 12"1,
In systems Operating on the conventional oycle the feeding means usually takes the form of a valve or variable orifice, the Variation being controlled by changes either in the vaportension or in the level of the liquid 1n 'the evaporator and is generally called by the misleading name of expansion valve.
`Such a valve is simply a boiler feedereno! vapor or gas and therefore nothlng capable of expanding'being allowed to pass, but only liquid which evaporates atv a. constant pressure in the boiler, a part at once and a part later.
One object of my invention is to provide a simplified form of apparatus for refrigeration by changes of state of the refrigerant fluid* liquid. `Another object is to permit easy control of the Operating characteristics4 of a closed cycle system. Still another ob-` ject is to provide simple ways and means for interposing the necessary resistance to the passing of the working -substance from the high side to the lower side of the system, as from the condenser to the evaporator. Other objects of the invention will be apparent from the detailed description which follows.
Instead of a valve or variable orifice theinvention involves the use in a particular location of a fixed orifice having a Critical relation to the capacity of the pump or com'- pressor. By providing interchangeable members each having an orifice of a different size the operati'ng characteristics of the system can be varied widely and the same mav be caused to run either on the conventional cycle or on the vapor gas principle. By preference the orifice is formed in a disk shaped member or diaphragm which may serve the 'additional 'purpose of a sealing gasket 1n a detachable fitting provided in the connection between the condenser and the evaporator.
In order to illustrate the 'invention concrete embodiments thereof'are shown in the accompanying drawings in which Figs. 1 and 2 are dlagrammatic views illustrating different arrangements of parts in closed cycle systems. of the condenser-compressor-evaporator type, the feeding device infeach view beo discharging the fluid drawn from the evap-' Orator 7 at a higher pressure and temperature -into a condenser 8 from which the condensed i refrlgerant 1s fedl` back into evaporator 7 through the feeding device or control memher 9. Control device 9, to which the inven- .tion particularly relates, is shown in full detail in F ig. 3 and in its preferred form comprises a slmple fittmg or`un1onhav1ng a part 10 secured to the condenser connection and a `part 11 secured to the evaporator connection,
these parts having clamping faces 10'FL and 11HL which are forced together by a nut 12 rotatively mounted on part 10 and having screw threaded engagement with part 11. By unsc'rewing'nut `12 the fitting is easily disconnected 'and the connection is as quickly re- `stored in an obvious manner. ATo provide a tight seal removable and interchangeablc gasket members 18 in the form of circular disks or diaphragms of thin sheet material such as metal vare clamped between the engaging faces 101 and 11a, which facesiare so shaped as to force member 11 into a slightly dished shape. Each gasketsmember or diaphragm 13 has a fixed orifice 14 which provides the necessary resistance to the passage of fluid from con'denser 8 to evaporator 7 to mark the line of division between the high and low sdes of the system.
Figs. 4: and 5 show in plan typical disk members or diaphragms 13 with orifices 14 of different sizes. The disk members or diaphragms 13 shown in Figs. 2, 3 and 4 have an orifice of suificient size to pass at the same time both the liquid and the gaseous products of the condenser 8 so that the system may operate upon the vapor gas principle referred to above. The diaphragm member 18 shown in Fig. 5 has a smaller'orifice 14 which so restricts the passage of fiuid from the condenser to the evaporator that a body of liquid will gather at the left of feeding device 9 in Fig. 1 or above the feeding device 9 in Fig. 2 so that the system will operate on the conventional cyele. The proper size of the orifice to cause the system to operate on the desii'ed cycle is determined to some extent by the density, viscosity, and other characteristics of the selected working' substance and to a far greater extent by the capacity or displacement of the pump which is used. In any event the size of the orifice bears a critical relation to the pump capacity with a given displacement and given working substance. The size of the orifice for securing the desired Operating characteristics of the system may be easily determined rempirically, and once determined may be standardized for the range of conditions commercially encountered.
For example, -.in the case of a refrigerating outfit for domestic use where the Variation in the refrigeration required (caused only by Variation in room temperature) is obtained by operatin the apparatus for longer or shorter perio s at a praetieally constant speed and Within a few degrees temperature scale, the orifice should be small enough so that toward the close of the running period and with the refrigerator temperature approaching the minimum desired, there will still be ample liquid to seal off and cover the orifice in the diaphragm, if it is desired to employ the conventional or reversed Rankine cyele. On the contrary when a vapor gas principle is to be employed, the
orifice must be large enough to revent the accumulation of liquid for more t an a short period directly after starting the machine with the refrigerator at the upper end of its Operating temperature range. With an orifice of proper size it will be found, of course, that on the initial running of the apparatus with the refrigerator at room temperature there will be a temporary loading u of liquid at the orifice but this lasts only a s ort time and is 'an advantage rather than a disadvantage as it tends toward the self-limiting of the load imposed on the compressor.
The upper size limit for a feed orifice in a given system is reached when the low side or i'ator.
evaporator pressure begins to rise on successive increases in the orifice area. In experimenting with diaphragm members having orifices of gradually increasing size the following phenomena are noted `With a closed cycle system containing a quantity of liquid having a volatile component and the remainder of the system filled `with a gas such as air and starting with a fecding device having an orifice so small as to pass only liquid and then gradually enlarging the orifice until it begins to pass the gaseous component of the working substance in greater and greater quantity, the temperature of the cvaporator closeto theorifice will gradually fall while the total or gauge pressure also falls until a point is reached where more orifice area eauses the low side pressure to rise abruptly and the temperature near the orifice then also rises to a point even above that of the remoter parts of the evapo- This turning point is sharply marked and. no difficulty will be experienced in avoiding too large an orifice in any given combination.
I am aware that it has previously been proposed to use a fixed orifice in a closed cyele system as in the patent to A. T. Marshall No. 1,436,815 of Nov. 28, 1922. Such proposed use, however, is for an entirely di fi'erent purpose from my invention since the orifice is provided on the low or suction side of the system and for a distinctly different purpose, namely, to prevent liquid from being drawn into the pump or compressor. I
In practice it has been found to be highly desirable, if not essential, that the condenser 8 be disposed at a higher level than the feeding device 9. At least the connection from the condenser to the feeding device 9 should be so disposed that the condensate shall drain by gravity to the latter. In general the preferred arrangements of parts are shown diagrammatically in Figs. 1 and 2. While the system will operate efliciently on the vapor gas cycle witheither of the arrangements shown in Fig. 2 the particular dis osition of the feeding device which is pre erable is shown in Figs. 2 and 3 wherein disk 18 is disposed horizontally and is slightly dished upwardly so that the condensate intercepted by the diaphragm drains toward the orifice and is blown or carried through the orifice by the gaseous component of the working substance.
While my invention has been herein disclosed in what is now considered to be its preferred form or forms, it is to be understood that the invention is not limited to the specific details thereto but covers all changes, modifications and adaptations within the scope of the appended claims.
I claim as my invention:
1. Apparatus for produeing heat transforming effects comprising an evaporator, a
pump, and a condenser connected together to form a closed cycle system, and a feeding device mounted in the connection between said condenser and said evaporator and having a feeding element, said device being de- 'mountable and arrangedfor interchangeable 'association with difl'erent feeding elements,
lvice mounted in tlie connection between said condenser and said evaporator and having a perforated disk for passing condensate from said condenser to said evaporator, said device beingdemountable and arranged for interchangeable association with a second disk having a perforation of a different size, thereby to determine whether the system shall operate on the conventional cycle or on the vapor-gas principle.
3. Apparatus for producing heat` transforming effects comprising an evaporator, a pump, and a condenser connected together to form a closcdcycle system, a detachable fitting in the 'connection between said condenser and said evaporator, and havin a removable feeding element, said fitting bemg arranged for interchangeable association with another feeding element for varying the a Operating characteristics of said system.
4. Apparatus for producing heat transforming eflects comprising an evaporator, a pump, and a condenser connected together to form a closed cycle system, a .detachable fitting in the connection between said condenser and said evaporator, and having a perforated disk as a feeding element arranged to assist in the sealing o f said fitting,
the latter being arranged for interchangeable association with disks having perfora- ,tioiis of different sizes for-'determining the Operating characteristics of said system.
5. Apparatus for prod-ucing heat transforming. effects comprising an evaporator, a
' pump, and a condenser connected together to form a closed cycle system, a detachable fitting in the connection between said condenser and said cvaporator, and a diapliragm forming a gasket for said fitting4 and having an opening for controlling the feeding of fluid to said vevaporator.
6. Refrigerating apparatus comprising an evaporator, a pump, and a condenser, connections between said parts to form a closed cycle system, and a horizontally disposed member extending transversely of theconnection `between said condenser and said evaporator, said member havin an opening theretlirough bearing a critica relation to the capacity of said pump and arranged to pass the liquid products of the condenser around the peripliery of the opening and the gaseous products through the center of the opening.
7. Refrigerating apparatus comprising an evaporator, a pump, and a condenser, connections between said parts to form a closed cycle system, and a horizontally disposed member extending transversely of the connection' between said condenser and said evaporator, said member having an opening therethrough bearing a Critical relation to the capacity of said pump, said condenser being disposed above said member and arranged to .drain by gravity directly tliereto so that the liquid ing a Critical relation to the capacity of said pump for controlling the feeding of fluid from the condenser to the evaporator.
9. Refrigerating apparatus comprising an'-` evaporat'or, a pump, and a condenser, connections between said parts to form a closed cycle system, a detachable fitting in a substantially Vertical portioii of the connection between said condenser and said evaporator, and 'an upwardly dished diaphragm in said fitting having an-opening tlieretlirough bearing a 'Critical relation to the capacity of said pump for controlling the feeding of fluid from the condenser 'to the evaporator, said diapliragm also serving as a sealing` gasket for said fitting.
Signed by me at Detroit, in the county of Wayne, and State of Michigan, this 24th day of Februar 1927.
ANSOM W. DAVENPORT.
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US171465A US1704177A (en) | 1927-02-28 | 1927-02-28 | Heat-transforming apparatus |
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US171465A US1704177A (en) | 1927-02-28 | 1927-02-28 | Heat-transforming apparatus |
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US1704177A true US1704177A (en) | 1929-03-05 |
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2563575A (en) * | 1951-08-07 | Absorption refrigeration | ||
US2676470A (en) * | 1950-04-24 | 1954-04-27 | Alquin J Streitz | Flow regulator in a refrigerating system |
US2694296A (en) * | 1951-10-15 | 1954-11-16 | Int Harvester Co | Flow restricting device |
US2703146A (en) * | 1951-09-07 | 1955-03-01 | Nat Foam System Inc | Fire extinguishing foam chamber |
FR2333209A1 (en) * | 1975-11-28 | 1977-06-24 | Danfoss As | COMPRESSION COOLING SYSTEM |
US4096708A (en) * | 1975-11-28 | 1978-06-27 | Danfoss A/S | Compressor refrigeration plant |
US4418546A (en) * | 1982-03-25 | 1983-12-06 | Buswell Harrie R | Continuous tube refrigeration system |
WO2002077542A2 (en) * | 2001-03-22 | 2002-10-03 | David Smolinsky | Heating and refrigeration systems using refrigerant mass flow |
EP1429090A2 (en) * | 2002-12-13 | 2004-06-16 | Otto Egelhof GmbH & Co. KG | Cold or heat producing circuit |
-
1927
- 1927-02-28 US US171465A patent/US1704177A/en not_active Expired - Lifetime
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2563575A (en) * | 1951-08-07 | Absorption refrigeration | ||
US2676470A (en) * | 1950-04-24 | 1954-04-27 | Alquin J Streitz | Flow regulator in a refrigerating system |
US2703146A (en) * | 1951-09-07 | 1955-03-01 | Nat Foam System Inc | Fire extinguishing foam chamber |
US2694296A (en) * | 1951-10-15 | 1954-11-16 | Int Harvester Co | Flow restricting device |
FR2333209A1 (en) * | 1975-11-28 | 1977-06-24 | Danfoss As | COMPRESSION COOLING SYSTEM |
US4096708A (en) * | 1975-11-28 | 1978-06-27 | Danfoss A/S | Compressor refrigeration plant |
US4418546A (en) * | 1982-03-25 | 1983-12-06 | Buswell Harrie R | Continuous tube refrigeration system |
US20030221445A1 (en) * | 1999-10-22 | 2003-12-04 | David Smolinsky | Heating and refrigeration systems using refrigerant mass flow |
US20050166621A1 (en) * | 1999-10-22 | 2005-08-04 | David Smolinsky | Heating and refrigeration systems and methods using refrigerant mass flow |
WO2002077542A2 (en) * | 2001-03-22 | 2002-10-03 | David Smolinsky | Heating and refrigeration systems using refrigerant mass flow |
WO2002077542A3 (en) * | 2001-03-22 | 2009-08-06 | David Smolinsky | Heating and refrigeration systems using refrigerant mass flow |
EP1429090A2 (en) * | 2002-12-13 | 2004-06-16 | Otto Egelhof GmbH & Co. KG | Cold or heat producing circuit |
EP1429090A3 (en) * | 2002-12-13 | 2006-05-10 | Otto Egelhof GmbH & Co. KG | Cold or heat producing circuit |
US20060117792A1 (en) * | 2002-12-13 | 2006-06-08 | Ralf Winterstein | Circuit for the generation of cold or heat |
US7328592B2 (en) | 2002-12-13 | 2008-02-12 | Otto Egelholf Gmbh & Co. Kg | Circuit for the generation of cold or heat |
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