US2229032A - Heating apparatus - Google Patents
Heating apparatus Download PDFInfo
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- US2229032A US2229032A US241906A US24190638A US2229032A US 2229032 A US2229032 A US 2229032A US 241906 A US241906 A US 241906A US 24190638 A US24190638 A US 24190638A US 2229032 A US2229032 A US 2229032A
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- tubes
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- air
- condensate
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- 238000010438 heat treatment Methods 0.000 title description 17
- 238000007710 freezing Methods 0.000 description 8
- 230000008014 freezing Effects 0.000 description 8
- 238000005192 partition Methods 0.000 description 8
- 229910000679 solder Inorganic materials 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 6
- 239000012530 fluid Substances 0.000 description 6
- 238000005755 formation reaction Methods 0.000 description 6
- 125000006850 spacer group Chemical group 0.000 description 5
- 238000005476 soldering Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
Images
Classifications
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- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
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- 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
- F28D7/10—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 one within the other, e.g. concentrically
- F28D7/12—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 one within the other, e.g. concentrically the surrounding tube being closed at one end, e.g. return type
Definitions
- This invention relates to heat exchange apparatus, and more particularly to heat exchange apparatus of the type in which a fluid such as steam is utilized to heat a fluid such as air.
- the general object of the invention is to provide an improved device for heating air or the like by heat exchange with steam or similar fluid, in which freezing due to low temperatures of the entering air is effectively prevented.
- heating medium such as steam
- Still another object of the invention is to provide a steam heating device for heating air or the like which is relatively simple and inexpensive to construct, and which is highly reliable and effective in operation.
- a feature of the invention resides in the provision of an apparatus for heating air or the like by means of steam or the like, which comprises a plurality of outer tubes each containing an inner tube provided with a series of orifices spaced intermediate the extremities of the inner tube, each inner tube being spaced from its surrounding outer tube, steam being supplied to each inner tube and condensate being withdrawn from each outer tube at the same side of the apparatus.
- Another feature of the invention resides in the provision of an air heating apparatus as referred to in the preceding paragraph in which steam passing through the oriflces formed in each inner tube is discharged back toward the steam inlet end of the apparatus through a plurality of tend to be trapped therein, thus to prevent airbinding of the apparatus.
- Another feature of the invention resides in the provision of an apparatus as referred to above, in which the steam supply header and condensate return header are at the same side of the apparatus, and in which the fluid in said supply header is in heat exchange relation with fluid in said return header.
- Another feature of the invention resides in the provision of a header structure comprising a steam supply portion and a condensate return portion, both of said portions forming part of an integral structure and being separated by a partition adapted to promote heat exchange between fluids contained in said respective portions.
- Fig. 1 is a side elevational view, partly in section, of a heating apparatus embodying the invention in a preferred form
- Fig. 2 is an end elevational view of the structure of Fig. 1, partly broken away, and with a portion of the surrounding casing removed;
- Fig. 3 is a view, in section, taken on the line 3-3 of Fig. 1;
- Fig. 4 is a view similar to Fig. 3, of a modified form of the invention.
- Fig. 5 is a fragmentary detail view, taken on the line 5-5 of Fig. 3, and
- Fig. 6 is a fragmentary detail view, taken on the line 66 of Fig. 4.
- the numeral Ill designates the end wall of a casing structure including top wall II, a second end wall l2, and a bottom wall l3.
- the casing thus formed is generally of rectangular shape, and is relatively shallow.
- the casing may be so positioned in an air duct or the like, that the top wall II and bottom wall l2 are substantially horizontal and so that air flows through the casing in substantially horizontal direction, as indicated generally by arrows I4 in Fig. 2.
- the heater may also be used advantageously in a variety of other positions permitting the return of condensate by gravity.
- header structure I6 Suitably mounted within the outer casing, as by bolts IE or in any other desired manner, is a header structure generally designated I6, situate adjacent the end wall I I. Header structure I6 is preferably shrouded by casing plates I1, so that it is protected from direct contact with the air or other gas to be heated which is caused to flow through the casing under the influence of a fan or the like.
- the header structure I6 includes a partition IIa which is preferably cast orotherwise formed integral with the outer portion of the header structure, and which is formed of any suitable material having a relatively high heat conductivity.
- Partition I'Ia extends substantially throughout the length of' the header structure, thus providing an inlet header I8 for steam or similar heating medium and a return header I9 for condensate.
- Inlet header I8 is provided with an inlet connection through which steam is supplied to header I8, and header I9 is provided with a return connection 2I, through which condensate may be drained therefrom.
- each steam tube is positioned within an outer or return tube 23 which is received within an extension 24 of the header structure and which communicates with return header I9.
- Each outer tube extends throughout the length of the outer casing and extends through openings 25 formed in the end wall I2, which constitutes, in effect, a tube sheet supporting the outer tubes. The far end of each outer tube is sealed, as by plugs 22.
- the outer tubes are approximately horizontally disposed one above the other, but are inclined downwardly toward the return header I9 at a slight angle to promote the return of condensate, by gravity, to the return header I9.-
- the outer tubes 23 are provided with extended surface, generally designatcd 21, of any desired type, such as spiral fins, to promote heat transfer from the tubes to air passing through the heater.
- the inner tubes 22 extend substantially completely throughout the length of the outer tubes 23 and are preferably concentric therewith.
- the far ends of the inner tubes 23 are preferably closed, but the tubes are provided with a plurality of apertures or orifices 28 spaced lengthwise of the tubes and preferably arranged peripherally therearound. These orifices serve to deliver steam from within the inner tubes 22 into the annular spaces between the inner tubes and the outer tubes.
- the orifices 28 are provided with nozzle or deflector formations arranged to discharge the steam delivered from within the tubes 22 back toward return header I 9 at relatively high velocity.
- nozzle or deflector arrangement While any desired nozzle or deflector arrangement may be used, it is preferred to form these by punching out portions of the inner tubes 22, as indicated at 29, whereby the orifices 28 and nozzle discharge formations may readily be provided in a single simple operation.
- the nozzle formations 23 may serve, if desired, as spacer members for maintaining the inner tubes 22 in desired spaced relationship with the surrounding tubes 23. Due to the manner in which steam is discharged from within the inner tubes, there occurs an ejector action whereby the steam tends to entrain any air which may be in the tubes of the heater. This air is removed from the tubes and delivered to the return header I9, from which it may be relieved in any suitable manner.
- the orifice 28 which is nearest the header I8 is spaced from the header at a greater distance than the distance between successive or adjacent orifices. This increased distance results in the formation of a relatively low pressure in the return tube near the return header, due to the greater cooling of the steam, and this lower pressure causes air to flow toward the header from all parts of the tubes. Removing air from the tubes of the heater renders all of the heat transfer service available for effective heat transfer, so that highly efficient operation of the heater is obtained.
- the outer casing is preferably provided with baffles 30 and 3
- the header structure I6 is preferably provided with a plurality of solder channels 32, adapted to provide communication between the exterior of the header structure and a plurality of annular solder grooves 33 formed in the partition I'Ia, one of such grooves extending around each tube 22 introduced within partition I'Ia. In this manner the tubes 22 may be soldered to partition IIa with great facility. Similarly, solder holes 34 formed in header extension 24 communicate with solder grooves 35 extending around each outer tube 23, so that these tubes also may readily be soldered to the header structure.
- the condensate within header I9 is heated by steam in the header I8, this heat being transmitted through partition Ma.
- the condensate in header I9 is also heated by heat transmitted through the outer walls of the header structure from steam in supply header I8.
- the supply of steam may be throttled very considerably without afiecting the substantially even heating of air throughout all portions of the heater.
- discharge or nozzle formations 29 serve to facilitate the return of condensate to return header I9.
- aeaaoaa desired number of banks may be provided. Also, while it is preferred to have but a single steam tube it within each outer tube it, two or more steam tubes may be provided Within each outer tube, if desired.
- V-shaped baffles it at the air outlet side of the heat exchanger, one of these baffles being nested between and in contact with each pair of finned tubes.
- Such location of the baffles routes the air in contact with the fins in a devious course and hence for a longer time. and thus increases the rate of heat transfer.
- Fig. 4 illustrates a modified form of the invention which embodies the same basic design as described above. However, it will be observed that in this embodiment of the invention, the solder channels 32 and the solder holes 3d are eliminated.
- the solder grooves 330 and 35a are prefilled with suitable soldering material, and after the tubes have been inserted in desired position heat is applied, as by means of a gas torch or the like, to melt the solder and efi'ect the desired soldering of the tubes within the header structure.
- Fig. 4 the orifices 29a, through which steam is discharged from the inner tubes 22, are distributed along and around the tubes 22 as above described. However, in this embodiment, the directional nozzle formations are dispensed with.
- a plurality of spacers 31 may comprise short lengths of copper wire or the like, preferably soldered or otherwise firmly secured to the inner tubes 22 and extending axially therealong.
- a spacer 31 is positioned diametrically opposite each orifice 29a, to insure minimum interference with the flow of steam and condensate.
- the spacers may be eliminated by "bumping out the tube at diii'erent points, the bumps thus formed serving to maintain the desired spaced relationship of the tubes.
- a suitable strainer or filter may be provided in connection with the steam inlet to prevent particles of boiler scale and other foreign matter from entering the tubes.
- a suitable strainer or filter is indicated at it in Fig. i, and is preferably of the type which may be snapped into and out of desired position at the steam inlet connection ill.
- a heating apparatus comprising a header structure, means for supplying steam to an inlet portion of the header structure and for removing steam and condensate from an outlet portion thereof, steam distributing tubes connected to said inlet portion of the header structure, steam and condensate return tubes surrounding each of said distributing tubes and connected to said outlet portion, said return tubes being closed at their ends remote from the header structure, said distributing tubes having perforations spaced substantially throughout the length thereof, said tubes being inclined so that condensate from steam supplied to a portion of the distributing tubes will flow back to the header structure and not proceed in a direction from the header structure beyond the points where condensation occurs in the tubes.
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
Jan. 21, 1941. c M s 2,229,032
HEATING APPARATUS Filed Nov. 23, 1938 2 Sheets-Sheet l M ii i ii I i l 3% 1 1 l 1! E i F- INVENTOR CARLYLE M. AsHLEY BYM ATTORNEY Jan. 21, 1941. c. M. ASHLEY \HEATING APPARATUS Filed Nov. 25, 1938 2 Sheets-Sheet 2 IRIJIIIAUIIIIIMII INVENTOR Chane-Miami! BY ?f g ATTORNEY Patented Jan. 21, 1941 UNITED STATES PATENT OFFICE Carrier Corporation, Syracuse,
poration of Delaware N. Y., a cor- Application November 23, 1938, Serial No. 241,906
2 Claims.
- This invention relates to heat exchange apparatus, and more particularly to heat exchange apparatus of the type in which a fluid such as steam is utilized to heat a fluid such as air.
The general object of the invention is to provide an improved device for heating air or the like by heat exchange with steam or similar fluid, in which freezing due to low temperatures of the entering air is effectively prevented.
In various types of air heaters heretofore known, the efficiency of the heaters has been considerably reduced by the presence in the heaters of quantitles of air locked therein. Efficiency losses of '15% or more due to such air-binding have not been uncommon. It is an object of the present invention to substantially completely eliminate air-binding, to insure a relatively high heat transfer efficiency.
It is another object of the invention to provide an improved air heater particularly well adapted to be installed in duct-work or the like comprising a part of an air conditioning or ventilating system.
It is another object of the invention to provide a heating apparatus in which the supply of heating medium such as steam may be throttled, if desired, without danger of freezing condensate resulting from cooling of the steam, and with the assurance that all portions of the air stream contacting the heater will be tempered substantially uniformly.
Still another object of the invention is to provide a steam heating device for heating air or the like which is relatively simple and inexpensive to construct, and which is highly reliable and effective in operation.
A feature of the invention resides in the provision of an apparatus for heating air or the like by means of steam or the like, which comprises a plurality of outer tubes each containing an inner tube provided with a series of orifices spaced intermediate the extremities of the inner tube, each inner tube being spaced from its surrounding outer tube, steam being supplied to each inner tube and condensate being withdrawn from each outer tube at the same side of the apparatus.
- Another feature of the invention resides in the provision of an air heating apparatus as referred to in the preceding paragraph in which steam passing through the oriflces formed in each inner tube is discharged back toward the steam inlet end of the apparatus through a plurality of tend to be trapped therein, thus to prevent airbinding of the apparatus.
Another feature of the invention resides in the provision of an apparatus as referred to above, in which the steam supply header and condensate return header are at the same side of the apparatus, and in which the fluid in said supply header is in heat exchange relation with fluid in said return header.
Another feature of the invention resides in the provision of a header structure comprising a steam supply portion and a condensate return portion, both of said portions forming part of an integral structure and being separated by a partition adapted to promote heat exchange between fluids contained in said respective portions.
Other objects, features and advantages of the invention will be more apparent from the following description, to be read in connection with the accompanying drawings in which:
Fig. 1 is a side elevational view, partly in section, of a heating apparatus embodying the invention in a preferred form;
Fig. 2 is an end elevational view of the structure of Fig. 1, partly broken away, and with a portion of the surrounding casing removed;
Fig. 3 is a view, in section, taken on the line 3-3 of Fig. 1;
Fig. 4 is a view similar to Fig. 3, of a modified form of the invention;
Fig. 5 is a fragmentary detail view, taken on the line 5-5 of Fig. 3, and
Fig. 6 is a fragmentary detail view, taken on the line 66 of Fig. 4.
Referring to the drawings, the numeral Ill designates the end wall of a casing structure including top wall II, a second end wall l2, and a bottom wall l3. The casing thus formed is generally of rectangular shape, and is relatively shallow. The casing may be so positioned in an air duct or the like, that the top wall II and bottom wall l2 are substantially horizontal and so that air flows through the casing in substantially horizontal direction, as indicated generally by arrows I4 in Fig. 2. However, the heater may also be used advantageously in a variety of other positions permitting the return of condensate by gravity.
Suitably mounted within the outer casing, as by bolts IE or in any other desired manner, is a header structure generally designated I6, situate adjacent the end wall I I. Header structure I6 is preferably shrouded by casing plates I1, so that it is protected from direct contact with the air or other gas to be heated which is caused to flow through the casing under the influence of a fan or the like.
The header structure I6 includes a partition IIa which is preferably cast orotherwise formed integral with the outer portion of the header structure, and which is formed of any suitable material having a relatively high heat conductivity. Partition I'Ia extends substantially throughout the length of' the header structure, thus providing an inlet header I8 for steam or similar heating medium and a return header I9 for condensate. Inlet header I8 is provided with an inlet connection through which steam is supplied to header I8, and header I9 is provided with a return connection 2I, through which condensate may be drained therefrom.
Extending outwardly from the header I8 through suitable openings formed in partition Ila are a plurality of steam tubes 22, each steam tube being positioned within an outer or return tube 23 which is received within an extension 24 of the header structure and which communicates with return header I9. Each outer tube extends throughout the length of the outer casing and extends through openings 25 formed in the end wall I2, which constitutes, in effect, a tube sheet supporting the outer tubes. The far end of each outer tube is sealed, as by plugs 22. The outer tubes are approximately horizontally disposed one above the other, but are inclined downwardly toward the return header I9 at a slight angle to promote the return of condensate, by gravity, to the return header I9.- The outer tubes 23 are provided with extended surface, generally designatcd 21, of any desired type, such as spiral fins, to promote heat transfer from the tubes to air passing through the heater.
The inner tubes 22 extend substantially completely throughout the length of the outer tubes 23 and are preferably concentric therewith. The far ends of the inner tubes 23 are preferably closed, but the tubes are provided with a plurality of apertures or orifices 28 spaced lengthwise of the tubes and preferably arranged peripherally therearound. These orifices serve to deliver steam from within the inner tubes 22 into the annular spaces between the inner tubes and the outer tubes. Preferably the orifices 28 are provided with nozzle or deflector formations arranged to discharge the steam delivered from within the tubes 22 back toward return header I 9 at relatively high velocity. While any desired nozzle or deflector arrangement may be used, it is preferred to form these by punching out portions of the inner tubes 22, as indicated at 29, whereby the orifices 28 and nozzle discharge formations may readily be provided in a single simple operation. The nozzle formations 23 may serve, if desired, as spacer members for maintaining the inner tubes 22 in desired spaced relationship with the surrounding tubes 23. Due to the manner in which steam is discharged from within the inner tubes, there occurs an ejector action whereby the steam tends to entrain any air which may be in the tubes of the heater. This air is removed from the tubes and delivered to the return header I9, from which it may be relieved in any suitable manner.
Further to insure the elimination of air from the tubes, the orifice 28 which is nearest the header I8 is spaced from the header at a greater distance than the distance between successive or adjacent orifices. This increased distance results in the formation of a relatively low pressure in the return tube near the return header, due to the greater cooling of the steam, and this lower pressure causes air to flow toward the header from all parts of the tubes. Removing air from the tubes of the heater renders all of the heat transfer service available for effective heat transfer, so that highly efficient operation of the heater is obtained.
To prevent bypassingair around the heater tubes, the outer casing is preferably provided with baffles 30 and 3|, located, respectively, at the top and bottom of the casing structure and extending substantially completely thereacross.
To facilitate fabrication of the apparatus, the header structure I6 is preferably provided with a plurality of solder channels 32, adapted to provide communication between the exterior of the header structure and a plurality of annular solder grooves 33 formed in the partition I'Ia, one of such grooves extending around each tube 22 introduced within partition I'Ia. In this manner the tubes 22 may be soldered to partition IIa with great facility. Similarly, solder holes 34 formed in header extension 24 communicate with solder grooves 35 extending around each outer tube 23, so that these tubes also may readily be soldered to the header structure.
In air heaters heretofore known, much difllculty has been experienced due to freezing of condensate because of the low temperature of the air passed into contact with the heater. The construction herein described, however, renders freezing of condensate virtually impossible. It will be appreciated that all condensate returning to the header I9 through tubes 23 'is in heat exchange relation with steam being supplied within tubes 22. Further, since the outer tubes are thermally bonded to the header structure I6 and hence to the steam supply header ill, the outer tubes are heated by the steam contained within the supply header. The fact that the outer tubes are thus heated further tends to prevent the temperature of the condensate from falling below the freezing point. Again, the condensate within header I9 is heated by steam in the header I8, this heat being transmitted through partition Ma. The condensate in header I9 is also heated by heat transmitted through the outer walls of the header structure from steam in supply header I8. Thus, freezing of condensate is prevented in both the tubes and in the return header, so that at all times during operation of the apparatus unimpeded flow of steam and condensate therethrough is maintained.
If it is desired to throttle the supply of steam to the heater, in order to reduce the heating effeet on the air passing therethrough, this may be done without danger of freezing. Thus, if the pressure at which steam is supplied is reduced to such a point that steam is contained within, for example, only half of the length of the inner tubes, all of the returning condensate will still be in good heat exchange relation with the steam being supplied within the inner tubes, and freezing will be effectively prevented as above indicated. The remaining portions of the tubes, under such operating conditions, will be inert and inactive, but this fact in no way interferes with the free and continuous circulation of steam and condensate through the apparatus.
Moreover, the supply of steam may be throttled very considerably without afiecting the substantially even heating of air throughout all portions of the heater.
The provision of the discharge or nozzle formations 29 serve to facilitate the return of condensate to return header I9.
While a single bank of heating elements has been illustrated it will be understood that any lid Jim
till
aeaaoaa desired number of banks may be provided. Also, while it is preferred to have but a single steam tube it within each outer tube it, two or more steam tubes may be provided Within each outer tube, if desired.
To insure effective contact between the air being heated and the fins H of the heat exchanger, there preferably are provided V-shaped baffles it at the air outlet side of the heat exchanger, one of these baffles being nested between and in contact with each pair of finned tubes. Such location of the baffles routes the air in contact with the fins in a devious course and hence for a longer time. and thus increases the rate of heat transfer.
Fig. 4 illustrates a modified form of the invention which embodies the same basic design as described above. However, it will be observed that in this embodiment of the invention, the solder channels 32 and the solder holes 3d are eliminated. To effect desired soldering of the tubes 22 and 23, the solder grooves 330 and 35a are prefilled with suitable soldering material, and after the tubes have been inserted in desired position heat is applied, as by means of a gas torch or the like, to melt the solder and efi'ect the desired soldering of the tubes within the header structure.
In Fig. 4 the orifices 29a, through which steam is discharged from the inner tubes 22, are distributed along and around the tubes 22 as above described. However, in this embodiment, the directional nozzle formations are dispensed with. To provide for maintained concentric spacing of the tubes 22 within the tubes 23, there are provided a plurality of spacers 31. These spacers may comprise short lengths of copper wire or the like, preferably soldered or otherwise firmly secured to the inner tubes 22 and extending axially therealong. Preferably a spacer 31 is positioned diametrically opposite each orifice 29a, to insure minimum interference with the flow of steam and condensate.
If desired, the spacers may be eliminated by "bumping out the tube at diii'erent points, the bumps thus formed serving to maintain the desired spaced relationship of the tubes.
If desired, a suitable strainer or filter may be provided in connection with the steam inlet to prevent particles of boiler scale and other foreign matter from entering the tubes. Such a filter is indicated at it in Fig. i, and is preferably of the type which may be snapped into and out of desired position at the steam inlet connection ill.
Since many changes may be made in the invention without departing from its scope, it is intended that all matter contained in the above description or shown in the accompanying drawings shall be interpreted as illustrative and not in a limiting sense, applicant limiting himself only as indicated in the appended claims.
I claim:
1. A heating apparatus comprising a header structure, means for supplying steam to an inlet portion of the header structure and for removing steam and condensate from an outlet portion thereof, steam distributing tubes connectedto said inlet portion of the header structure, steam and condensate return tubes surrounding each of said distributing tubes and connected to said outlet portion, said distributing and return tubes being closed at their ends remote from the header structure, said distributing tubes having perfora-= tions spaced substantially throughout the lengththereof, said tubes being inclined so that condensate from steam supplied to a portion of the distributing tubes will flow. back to the header structure and not proceed in a direction from the,
header structure beyond the points where condensation occurs in the tubes.
2. A heating apparatus comprising a header structure, means for supplying steam to an inlet portion of the header structure and for removing steam and condensate from an outlet portion thereof, steam distributing tubes connected to said inlet portion of the header structure, steam and condensate return tubes surrounding each of said distributing tubes and connected to said outlet portion, said return tubes being closed at their ends remote from the header structure, said distributing tubes having perforations spaced substantially throughout the length thereof, said tubes being inclined so that condensate from steam supplied to a portion of the distributing tubes will flow back to the header structure and not proceed in a direction from the header structure beyond the points where condensation occurs in the tubes.
CARLYLE M. ASHLEY.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US241906A US2229032A (en) | 1938-11-23 | 1938-11-23 | Heating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US241906A US2229032A (en) | 1938-11-23 | 1938-11-23 | Heating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2229032A true US2229032A (en) | 1941-01-21 |
Family
ID=22912647
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US241906A Expired - Lifetime US2229032A (en) | 1938-11-23 | 1938-11-23 | Heating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2229032A (en) |
Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2423697A (en) * | 1943-12-24 | 1947-07-08 | Ice Air Conditioning Co Inc | Method of assembling headers and tubes |
| US2463996A (en) * | 1947-02-19 | 1949-03-08 | American Blower Corp | Heat exchange apparatus |
| US2499608A (en) * | 1944-07-31 | 1950-03-07 | Charles N Rink | Heat exchange device |
| US2611584A (en) * | 1947-03-22 | 1952-09-23 | Trane Co | Heat exchanger |
| US2614816A (en) * | 1947-02-24 | 1952-10-21 | Engineering Controls Inc | Condenser |
| US2626783A (en) * | 1949-10-26 | 1953-01-27 | Aerofin Corp | Heat exchanger |
| US2650799A (en) * | 1950-08-11 | 1953-09-01 | Aerofin Corp | Heat exchanger |
| US2794332A (en) * | 1955-11-09 | 1957-06-04 | Ralph A Boss | Heat exchange method and apparatus |
| US2942858A (en) * | 1958-04-21 | 1960-06-28 | American Air Filter Co | Heat exchange apparatus |
| US2991978A (en) * | 1959-07-29 | 1961-07-11 | Westinghouse Electric Corp | Steam heaters |
| US3229761A (en) * | 1963-07-05 | 1966-01-18 | Trane Co | Spur tube with alternate oppositely directed orifices |
| FR2068575A1 (en) * | 1969-11-21 | 1971-08-27 | Daimler Benz Ag | |
| US4067552A (en) * | 1974-07-15 | 1978-01-10 | Mendenhall Robert Lamar | Asphalt-aggregate recycle |
| DE3714879A1 (en) * | 1987-05-05 | 1988-11-24 | Reininger Klaus Dieter | Apparatus for utilising waste-gas heat |
| US5323850A (en) * | 1993-03-29 | 1994-06-28 | Roberts Thomas H | Steam coil with alternating row opposite end feed |
| US5470146A (en) * | 1986-06-30 | 1995-11-28 | Standard Havens, Inc. | Countercurrent drum mixer asphalt plant |
| US5509467A (en) * | 1994-06-28 | 1996-04-23 | Champion Clam Traps, Inc. | Heat exchanger tube strainer |
| ITUB20150332A1 (en) * | 2015-05-06 | 2016-11-06 | Cordivari S R L | RADIATOR AND PROCEDURE FOR MAKING THE SAID RADIATOR. |
| US10495390B2 (en) * | 2018-02-08 | 2019-12-03 | Tsung-Hsien Huang | Liquid cooling radiator with impurities filtering |
-
1938
- 1938-11-23 US US241906A patent/US2229032A/en not_active Expired - Lifetime
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2423697A (en) * | 1943-12-24 | 1947-07-08 | Ice Air Conditioning Co Inc | Method of assembling headers and tubes |
| US2499608A (en) * | 1944-07-31 | 1950-03-07 | Charles N Rink | Heat exchange device |
| US2463996A (en) * | 1947-02-19 | 1949-03-08 | American Blower Corp | Heat exchange apparatus |
| US2614816A (en) * | 1947-02-24 | 1952-10-21 | Engineering Controls Inc | Condenser |
| US2611584A (en) * | 1947-03-22 | 1952-09-23 | Trane Co | Heat exchanger |
| US2626783A (en) * | 1949-10-26 | 1953-01-27 | Aerofin Corp | Heat exchanger |
| US2650799A (en) * | 1950-08-11 | 1953-09-01 | Aerofin Corp | Heat exchanger |
| US2794332A (en) * | 1955-11-09 | 1957-06-04 | Ralph A Boss | Heat exchange method and apparatus |
| US2942858A (en) * | 1958-04-21 | 1960-06-28 | American Air Filter Co | Heat exchange apparatus |
| US2991978A (en) * | 1959-07-29 | 1961-07-11 | Westinghouse Electric Corp | Steam heaters |
| US3229761A (en) * | 1963-07-05 | 1966-01-18 | Trane Co | Spur tube with alternate oppositely directed orifices |
| FR2068575A1 (en) * | 1969-11-21 | 1971-08-27 | Daimler Benz Ag | |
| US4067552A (en) * | 1974-07-15 | 1978-01-10 | Mendenhall Robert Lamar | Asphalt-aggregate recycle |
| US5470146A (en) * | 1986-06-30 | 1995-11-28 | Standard Havens, Inc. | Countercurrent drum mixer asphalt plant |
| DE3714879A1 (en) * | 1987-05-05 | 1988-11-24 | Reininger Klaus Dieter | Apparatus for utilising waste-gas heat |
| US5323850A (en) * | 1993-03-29 | 1994-06-28 | Roberts Thomas H | Steam coil with alternating row opposite end feed |
| US5509467A (en) * | 1994-06-28 | 1996-04-23 | Champion Clam Traps, Inc. | Heat exchanger tube strainer |
| ITUB20150332A1 (en) * | 2015-05-06 | 2016-11-06 | Cordivari S R L | RADIATOR AND PROCEDURE FOR MAKING THE SAID RADIATOR. |
| EP3091325A1 (en) | 2015-05-06 | 2016-11-09 | Cordivari S.r.l. | Radiator and process for making said radiator |
| US10495390B2 (en) * | 2018-02-08 | 2019-12-03 | Tsung-Hsien Huang | Liquid cooling radiator with impurities filtering |
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