US2596622A - Recuperative heat exchanger of the counterflow type for gaseous media - Google Patents

Recuperative heat exchanger of the counterflow type for gaseous media Download PDF

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US2596622A
US2596622A US722920A US72292047A US2596622A US 2596622 A US2596622 A US 2596622A US 722920 A US722920 A US 722920A US 72292047 A US72292047 A US 72292047A US 2596622 A US2596622 A US 2596622A
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rotor
heat exchanger
air
channels
discs
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Vannerus Torbjorn
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D11/00Heat-exchange apparatus employing moving conduits
    • F28D11/02Heat-exchange apparatus employing moving conduits the movement being rotary, e.g. performed by a drum or roller
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/135Movable heat exchanger
    • Y10S165/139Fully rotatable
    • Y10S165/14Rotating heat exchanger having rotating flow confining structures or chambers for two separate heat exchange fluids

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  • VANNERUS RECUPERATIVE HEAT EXCHANGER OF THE COUNTERFLOW TYPE FOR GASEOUS MEDIA 7 Sheets-Sheet 1 Filed Jan. 18, 1947 I]? Imue-nior T- Vmnmrus y 13, 1952 T. VANNERUS 2,596,622
  • heat exchangers consist of a rotor arranged in a housing and fixed to a driving shaft rotor comprising a plurality of annular metal discs having substantially smooth surfaces and acting as heat exchanger members, said discs being placed substantially perpendicularly to the axis of rotation and confining a corresponding number of slotshaped flow passages alternately for one and the other medium respectively each set of flow passages respectively communicates with a separate inlet chamber arranged adjacent to the driving shaft and with a separate outlet chamber, whereby the conveying action of the rotating discs on the gaseous media wholly or substantially in a peripheral direction is produced by the friction between the discs and the two media for the purpose of attaining at a high velocity of rotation of the discs a peripheral lagging of the gaseous media during the motion in the radial outward direction of the latter.
  • this is attained by having one of the two media conducted from inside and outwards through the passages of flow provided for said medium in the rotor, while the other medium by means of pressure and/or suction action is conducted from outside and inwards through the passages of flow provided for said latter medium in the rotor.
  • the air can, for instance, be conducted from outside and inwards through the slot-shaped flow passages of the rotor, while the flue gases are conducted from inside and outwards through the flow passages of the rotor, which arrangement may be preferable from the point of view that the hue gases thus have to pass the shortest way through the heat exchanger, and that no special flue gas fan is required.
  • Fig. 1 shows an embodiment of the heat exchanger in vertical sectional elevation
  • Fig. 2 an end view of the same seen from the lefthand side in Fig. 1.
  • Figs. 3, 4, 5 and 6 respectively show cross-sections through the rotor along the lines III-III, IV-IV, V--V and V I-VIrespectively in Fig. 1.
  • Fig. 7 shows the heat exchanger illustrated in Fig. 1, whereby the part above the centre line shows the passage of air .through the rotor, while the part below the centre line shows thepassage of gas'through the rotor of the heat exchanger.
  • Fig. 8 illustrates in vertical sectional elevation the rotor of the heat exchanger according to the other embodiment, while Fig. 9 is a cross-section along the line IX-IX in Fig. 8.
  • Fig. 10 is a cross-section along theline X-X in Fig. 8 illustrating three difierent possibilities for one of the two media to flow into the passages of flow of the rotor from the hoods axially positioned, at the circumference of the rotor.
  • Fig. 11 is a sectional view on the line XI-XI of Fig. 8.
  • I designates the driving shaft of the rotor.
  • the rotor; which by means of the hub 2 is fixed to the shaft l is built up of a plurality of annular, substantially smooth and preferably plane metal discs 3 set perpendicularly to the shaft, between which discs slot-shaped flow passages 4, 5 are formed.
  • the end discs 6, 1 of the rotor are secured to the hub 2 in the manner. shown.
  • the rotor is. enclosed by a stationary housing 8, one
  • the housing 8 which is spiral-shaped in relation to the rotor, is further provided with a tangential outlet l2 (Fig. 2) for the same medium.
  • wall I3 is provided with an inlet 14 for the other medium, in the present case flue gases, which inlet opens into an axial inlet chamber [5 of the rotor.
  • the spiral-shaped housing 8 is further provided with a tangential outlet l6 (Fig. 2) for the latter medium.
  • the channels 26a and 26!) extend somewhat beyond the outermost rotor disc 3a andcommunicate with the inner inlet of a fan wheel 28 built together with the rotor, said fan wheel beingprovided with fan blades 29 arranged along the circumference.
  • the housing 8 i divided, about in the plane of rotor disc 3a, by a stationary partition wall 30 into two chambers 3i and 32 respectively for receiving the two different media after their exit from the rotor.
  • forms a spiralshaped outlet channel of the fan wheel 28, 29, and the outlet channel [2 is connected to this cham- 7 her.
  • the partition wall 30 forms a seal with the adiacent wall of the rotating fan 28 by means of a labyrinth packing 33.
  • the radial channels I1 bring along the medium (air) entering through the inlet I0, ll, so that said medium is exposed to the influence of the centrifugal force and is thrown outwards, whereby a certain excess of pressure arises in the channel 22.
  • the medium flowing through the flow passages 4 from the outside and inwards is, in the shown example, further exposed to the suction action produced by the fan 28, 29 and transferred through the channels 26a and 26b, and is finally forced by this fan out into the spiral-shaped outlet channel 3 I. and the outlet 12.
  • the other medium (the flue gases), which enters through the inlets l4, l5, flows into the channels 21a and 21b through the two openings provided in the hub part 2a. and facing these channels, and is conducted from these channels, which are separated from the channels 26a. 26b, into the flow passages 5 of the rotor (Fig.7) and passes through these from inside and outwards, thereby exchanging heat with the other medium passing in counter flow through the flow passages 4.
  • the passages 5 are separated at their outer circumference from the channels 22 by the partition walls 24 but are in direct communication with the chamber 32 by means of openings 35 between the channels 22 (Fig. 5), which chamber forms an eccentric outlet channel about the rotor. From the chamber 32 the medium is led out through the outlet channel 16 (Fig. 2).
  • hoods or channels projecting from the circumference of the rotor will operate as fan blades which in connection with the spiralshaped outlet channel 32 will produce a suction action on the medium flowing from the inside and outwards through the rotor.
  • 36 designates the rotor hub which is secured to the driving shaft.
  • the rotor consists of a plurality of annular, substantially smooth and preferably plane metal discs 31 arranged perpendicularly to the driving shaft, between which discs slot-shaped flow passages 38, 39 are formed.
  • of the rotor are in the manner shown secured to the hub 35.
  • the air enters through the inlet 43 arranged in an outer end wall 42 connected to the rotor itself, said inlet being confined by the central pipe 44 and the ring 45.
  • every other channel 46 is open outwards permitting air from outside to flow into these channels.
  • the air passes through these channels radially outwards towards the air hoods 41 extending axially on the circumference of the rotor, into which hoods the air is introduced through the openings 48; 7
  • the air is distributed to all the passages for the flow of air through the rotor and passes through these flow passages 38 towards the centre of the rotor.
  • the air is conducted through openings 49 to the radial channels 50 provided between the end walls 4! and 42 and between above mentioned channels 46, said channels 50 being open inwards towards the centre portion of the rotor.
  • the latter embodiment has the advantage that the totalwidth of the rotor is considerably decreased corresponding to a reduction of at least the channel width of the radial air channels.
  • a further advantage is that no leakage from flue gases to air or vice versa will occur at the central seals of the rotor due to the fact that the air enters and flows out on the same side of the rotor.
  • the air which is introduced into the space between the pipe 44 and the ring 45, flows radially outwards through the channels 46 formed by the radially placed partition walls 53, 5'4 and the end walls, 41 and 42, whereafter it flows through the openings 48 into'the air hoods 4i, and passes thereafter inwards through the flow passages 38.
  • the air hoods t extending axially at the circumference of th rotor may be provided with throttling member lit arranged where the air flows out from th hoods into the flow passages 33 of the rotor.
  • these throttling may be directed in or opposite to the direc in of rotation of the rotor, thus permitting the direction of how of the air into the flow passages of the rotor determined.
  • the speed of the air nowing out from the hoods can be regulated.
  • the embodiment illustrated may be modified in many different ways within the scope or the invention. Thus it may be so arranged that the hot gas (the flue gases) instead is conducted from the outside and inwards through the flow paesages of the rotor, while the cold gas (the air) is conducted from the inside and outwards.
  • the two media conducted to the rotor by axial inlets whereaiter one of the media is conducted through radial channels out to the outer circumference of the rotor.
  • one of the media (the cold or the hot one) may be conducted directly to a channel or chamber enclosing the rotor without said medium being at first axially conducted to the rotor.
  • a recuperative heat exchanger for two gaseous media at different temperatures comprising a housing; a shaft rotatably mounted in said housing; a rotor hub secured to said shaft; 2. plurality of mechanically interconnected, axially spaced, substantially plane radially extending annular discs secured to rotate with said rotor hub, the spaces between said discs forming alternate gaseous media flow passages in said housing separated by intermediate flow passages; a first axial inlet in said housing for one gaseous medium; conduit means-connecting said first axial inlet to the radially outer ends of alternate flow passages; first passage means at said rotor hub communicating with the radially inner ends of such alternate flow passages; a first outlet in said housing in communication with said first passage means; means sealing the intermediate flow passages from said conduit means and said first passage means; whereby such one gaseous medium will enter said first axial inlet, fiow radially outward into said conduit means, then radially inward through such alternate flow passages to said first passage means, and be discharged
  • a recuperative heat exchanger as claimed in claim 1 including draft creating means operatively associated with said discs and having an inlet in. communication with said first passage means and an outlet in communication with said first housing outlet.
  • a recuperative heat exchanger as claimed in claim 1 including a fan carried by said discs and having an inlet in communication with said first passage means and an outlet in communication with said first housing outlet.
  • a recuperative heat exchanger as claimed in claim 1 in which said conduit means comprises axially extending circumferentially spaced hoods on the peripheries of said discs.
  • a recuperative heat exchanger as claimed in claim 1 in which said first and second passage means are defined by axially extending, substantially radially projecting walls secured to rotate with said discs and said rotor hub, and said first named sealing means includes circumferentially curved wall sections interconnecting the outer ends of pairs of said walls alternately in a circumferential and in an axial direction.
  • a recuperative heat exchanger as claimed in claim 1 in which said first and second passage means are defined by axially extending, substantially radially projecting, radially curved walls secured to rotate with said discs and said rotor hub, and said first named sealing means includes circumierentially curved wall sections interconnectin the outer ends of pairs of said walls alternately in a circumferential and in an axial direction.
  • a recuperative heat exchanger as claimed in claim 1 in which said first axial inlet is annular and said conduit means comprises axially extending circumferentially spaced hoods on the peripheries of said discs, and including radial vanes forming alternate radial channels connectin each hood individually to said first axial inlet and intermediate radial channels connecting said first passage means to said first housing outlet.
  • a recuperative heat exchanger as claimed in claim 1 in which said conduit means comprises axially extending circumferentially spaced hoods on the peripheries of said discs, and including throttling means controlling flow of such one gas eous medium into the alternate flow passages.

Description

May 13, 1952 'r. VANNERUS RECUPERATIVE HEAT EXCHANGER OF THE COUNTERFLOW TYPE FOR GASEOUS MEDIA 7 Sheets-Sheet 1 Filed Jan. 18, 1947 I]? Imue-nior T- Vmnmrus y 13, 1952 T. VANNERUS 2,596,622
RATIVE HEAT EXCHA R RECUPE OF THE COUNTERFLOW TYPE FOR GA US MEDI Filed Jan. 18, 1947 Sheets-Sheet 2 1m) 2min? Tvrrnnarus y 13, 1952 T VANNERUS 2,596,622
RECUPERATIVE HEAT EXCHANGER OF THE COUNTERFLOW TYPE FOR GASEOUS MEDIA Filed Jan. 18, 1947 7 Sheets-Sheet 15 Inventor T Vccnnerus May 13, 1952 T. VANNERUS RECUPERATIVE HEAT EXCHANGER OF THE COUNTERFLOW TYPE FOR GASEOUS MEDIA 7 Sheets-Sheet 4 Filed Jan. 18, 1947 mm miter May 13, 1952 T. VANNERUS RECUPERATIVE HEAT EXCHANGER OF THE COUNTERFLOW TYPE FOR GASEOUS MEDIA 7 Sheets-Sheet 5 Filed Jan. 18, 1947 111021110: T m'merus May 13, 1952 T. VANNERUS RECUPERATIVE HEAT EXCHANGER OF THE COUNTERFLOW TYPE FOR GASEOUS MEDIA '7 Sheets-Sheet 6 Filed Jan. 18, 1947 lumen: or
s u r e n n Q T May 13, 1952 v E s 2,596,622
RECUPERATIVE HEAT EXCHANGER OF THE COUNTERFLOW TYPE FOR GASEOUS MEDIA Filed Jan. 18, 1947 7 Sheets-Sheet 7 W M 'l 55 i- I 6 l l r l I l I I Imuavio'r T- Vanna-: 5
Patented May 13, 1952 OFFICE RECUPERATIVE HEAT EXCHANGER OF THE COUNTERFLOW TYPE FOR GAS- EOUS MEDIA Torbjiirn Vannrus, Motala Verkstad, Sweden Application January 18, 1947, Serial No. 722,920 In Sweden September 25, 1944 I Section 1, Public Law 690, August 8, 1946 Patent expires September 25, 1964 9Claims. (Cl.257-241) I The present invention relates to improvements 1 in gaseous media heat exchangers of the type shown in U. S. Patent No. 2,402,307. These heat exchangers consist of a rotor arranged in a housing and fixed to a driving shaft rotor comprising a plurality of annular metal discs having substantially smooth surfaces and acting as heat exchanger members, said discs being placed substantially perpendicularly to the axis of rotation and confining a corresponding number of slotshaped flow passages alternately for one and the other medium respectively each set of flow passages respectively communicates with a separate inlet chamber arranged adjacent to the driving shaft and with a separate outlet chamber, whereby the conveying action of the rotating discs on the gaseous media wholly or substantially in a peripheral direction is produced by the friction between the discs and the two media for the purpose of attaining at a high velocity of rotation of the discs a peripheral lagging of the gaseous media during the motion in the radial outward direction of the latter.
In the above mentioned type of heat exchangers the two heat exchanging media both pass from the inside radially outwards through the passages between the metal discs of the rotor, for which reason this heat exchanger thus operates as a direct flow apparatus. However, in many cases it is desirable that the heat exchange takes place in counter flow.
Due to the fact that the heat supplying gas by this means can be cooled down to a temperature which approaches more nearly to that of the entering cold gas it is evident that a greater heat exchange can be expected thereby.
According to the invention this is attained by having one of the two media conducted from inside and outwards through the passages of flow provided for said medium in the rotor, while the other medium by means of pressure and/or suction action is conducted from outside and inwards through the passages of flow provided for said latter medium in the rotor.
In exchanging heat between air and. flue gases, the air can, for instance, be conducted from outside and inwards through the slot-shaped flow passages of the rotor, while the flue gases are conducted from inside and outwards through the flow passages of the rotor, which arrangement may be preferable from the point of view that the hue gases thus have to pass the shortest way through the heat exchanger, and that no special flue gas fan is required.
Two embodiments of a recuperativeheat exchanger according to the invention are by way of example schematically illustrated on the accompanying drawings, in which:
Fig. 1 shows an embodiment of the heat exchanger in vertical sectional elevation, and Fig. 2 an end view of the same seen from the lefthand side in Fig. 1.
Figs. 3, 4, 5 and 6 respectively show cross-sections through the rotor along the lines III-III, IV-IV, V--V and V I-VIrespectively in Fig. 1.
Fig. 7 shows the heat exchanger illustrated in Fig. 1, whereby the part above the centre line shows the passage of air .through the rotor, while the part below the centre line shows thepassage of gas'through the rotor of the heat exchanger.
Fig. 8 illustrates in vertical sectional elevation the rotor of the heat exchanger according to the other embodiment, while Fig. 9 is a cross-section along the line IX-IX in Fig. 8.
Fig. 10 is a cross-section along theline X-X in Fig. 8 illustrating three difierent possibilities for one of the two media to flow into the passages of flow of the rotor from the hoods axially positioned, at the circumference of the rotor.
Fig. 11 ,is a sectional view on the line XI-XI of Fig. 8.
In all figures the same reference numerals indicate the same parts and the arrows in solid lines and in broken lines represent the flow of air and flue gas respectively.
At the embodiment according to Figs. 1-7, I designates the driving shaft of the rotor. The rotor; which by means of the hub 2 is fixed to the shaft l is built up of a plurality of annular, substantially smooth and preferably plane metal discs 3 set perpendicularly to the shaft, between which discs slot- shaped flow passages 4, 5 are formed. The end discs 6, 1 of the rotor are secured to the hub 2 in the manner. shown. The rotor is. enclosed by a stationary housing 8, one
'end wall 9 of which is provided with an axial .inlet opening In for one of the media, in the present case air, which opening leads to an axial inlet chamber l I of the rotor. The housing 8, which is spiral-shaped in relation to the rotor, is further provided with a tangential outlet l2 (Fig. 2) for the same medium.
At the opposite end of the housing, wall I3 is provided with an inlet 14 for the other medium, in the present case flue gases, which inlet opens into an axial inlet chamber [5 of the rotor. The spiral-shaped housing 8 is further provided with a tangential outlet l6 (Fig. 2) for the latter medium.
From the axial inlet ll of the first-mentioned medium (air) proceed a plurality of radially extending channels I1, Figs. 1, 3 and 7, each of which is formed by two walls l8 arranged between the end wall 6 of the rotor and an outer wall IS. The inner edge of the wall I9 is connected to a ring 20, which cooperates with a corresponding flange 2| on the end wall 9 of the housing to form V a gaseous medium seal. Theouter ends of the channels I! each communicate with an axially directed hood or channel 22 extending along the rotor immediately outside the outer edges of g the metal discs 3 to the last enlarged metal disc cut off from the flow passages by curved walls such as 26c. V
r The channels 26a and 26!) extend somewhat beyond the outermost rotor disc 3a andcommunicate with the inner inlet of a fan wheel 28 built together with the rotor, said fan wheel beingprovided with fan blades 29 arranged along the circumference.
The housing 8 i divided, about in the plane of rotor disc 3a, by a stationary partition wall 30 into two chambers 3i and 32 respectively for receiving the two different media after their exit from the rotor. The chamber 3| forms a spiralshaped outlet channel of the fan wheel 28, 29, and the outlet channel [2 is connected to this cham- 7 her. The partition wall 30 forms a seal with the adiacent wall of the rotating fan 28 by means of a labyrinth packing 33.
In the fast rotation of the rotor the radial channels I1 bring along the medium (air) entering through the inlet I0, ll, so that said medium is exposed to the influence of the centrifugal force and is thrown outwards, whereby a certain excess of pressure arises in the channel 22. The medium flowing through the flow passages 4 from the outside and inwards is, in the shown example, further exposed to the suction action produced by the fan 28, 29 and transferred through the channels 26a and 26b, and is finally forced by this fan out into the spiral-shaped outlet channel 3 I. and the outlet 12. r i
The other medium (the flue gases), which enters through the inlets l4, l5, flows into the channels 21a and 21b through the two openings provided in the hub part 2a. and facing these channels, and is conducted from these channels, which are separated from the channels 26a. 26b, into the flow passages 5 of the rotor (Fig.7) and passes through these from inside and outwards, thereby exchanging heat with the other medium passing in counter flow through the flow passages 4. The passages 5 are separated at their outer circumference from the channels 22 by the partition walls 24 but are in direct communication with the chamber 32 by means of openings 35 between the channels 22 (Fig. 5), which chamber forms an eccentric outlet channel about the rotor. From the chamber 32 the medium is led out through the outlet channel 16 (Fig. 2).
The hoods or channels proiecting from the circumference of the rotor will operate as fan blades which in connection with the spiralshaped outlet channel 32 will produce a suction action on the medium flowing from the inside and outwards through the rotor.
During the flow of the gases through the smooth flow passages 4, 5 of the rotor only the friction between the discs 3 and the gases tends to bring along the latter in the direction of rotation by means of which a great lag, i. e. a high relative speed in peripheral direction, arises between the discs 3 and the passing gases, whereby the heat exchange is influenced in a favourable manner.
In the other embodiment according to Figs. 840, 36 designates the rotor hub which is secured to the driving shaft. Also in this em bodiment of the apparatus the rotor consists of a plurality of annular, substantially smooth and preferably plane metal discs 31 arranged perpendicularly to the driving shaft, between which discs slot- shaped flow passages 38, 39 are formed.
The end walls 40, 4| of the rotor are in the manner shown secured to the hub 35. The air enters through the inlet 43 arranged in an outer end wall 42 connected to the rotor itself, said inlet being confined by the central pipe 44 and the ring 45.
Between the'endf walls 4| and 42 radially extending channels are provided, whereby at the centre of the rotor, as shown in Fig. 9, every other channel 46 is open outwards permitting air from outside to flow into these channels. The air passes through these channels radially outwards towards the air hoods 41 extending axially on the circumference of the rotor, into which hoods the air is introduced through the openings 48; 7
Herefrom the air is distributed to all the passages for the flow of air through the rotor and passes through these flow passages 38 towards the centre of the rotor. From the centre portion of the rotor the air is conducted through openings 49 to the radial channels 50 provided between the end walls 4! and 42 and between above mentioned channels 46, said channels 50 being open inwards towards the centre portion of the rotor.
The air then flows through these radial channels which pass between the axially extending ir hoods 41 and radially outwards into a housing (not shown) located outside the rotor. The flue gases are introduced into the rotor through the inlet 5| provided at the centre portion of the rotor and flow radially outwards through the flow passages 39 provided in the rotor for the gases and'to a collecting chamber (not shown) located outside the rotor. 52 designates the sealprovided between the outlets of gas and of air at the outside of the rotor. As will be seen from a comparison between the embodiment according to Figs. 1-7 and the embodiment of Fig. 8, the latter embodiment has the advantage that the totalwidth of the rotor is considerably decreased corresponding to a reduction of at least the channel width of the radial air channels. A further advantage is that no leakage from flue gases to air or vice versa will occur at the central seals of the rotor due to the fact that the air enters and flows out on the same side of the rotor.
The air, which is introduced into the space between the pipe 44 and the ring 45, flows radially outwards through the channels 46 formed by the radially placed partition walls 53, 5'4 and the end walls, 41 and 42, whereafter it flows through the openings 48 into'the air hoods 4i, and passes thereafter inwards through the flow passages 38.
From the centre portion of the rotor the air flows through the openings 59 out into the radial channels 55 located between the channels as to escape from the heat exchanger at the circumference the rotor.
Fig. 10 it will he seen that the air hoods t extending axially at the circumference of th rotor may be provided with throttling member lit arranged where the air flows out from th hoods into the flow passages 33 of the rotor. seen from the figure these throttling may be directed in or opposite to the direc in of rotation of the rotor, thus permitting the direction of how of the air into the flow passages of the rotor determined. By means of these throttling members also the speed of the air nowing out from the hoods can be regulated. 1%) also illustrates the case when no throttling members are provided, in which case the air flows radially into the flow passages will also be seen that the partition walls lit between the air and the gas, which walls are secured to the rotor hub 36, are formed as fan blades.
The embodiment illustrated may be modified in many different ways within the scope or the invention. Thus it may be so arranged that the hot gas (the flue gases) instead is conducted from the outside and inwards through the flow paesages of the rotor, while the cold gas (the air) is conducted from the inside and outwards. In the embodiments illustrated the two media conducted to the rotor by axial inlets whereaiter one of the media is conducted through radial channels out to the outer circumference of the rotor. Instead of that, one of the media (the cold or the hot one) may be conducted directly to a channel or chamber enclosing the rotor without said medium being at first axially conducted to the rotor.
Having now particularly described the nature of my invention and the manner of its operation what I claim is;
1. A recuperative heat exchanger for two gaseous media at different temperatures comprising a housing; a shaft rotatably mounted in said housing; a rotor hub secured to said shaft; 2. plurality of mechanically interconnected, axially spaced, substantially plane radially extending annular discs secured to rotate with said rotor hub, the spaces between said discs forming alternate gaseous media flow passages in said housing separated by intermediate flow passages; a first axial inlet in said housing for one gaseous medium; conduit means-connecting said first axial inlet to the radially outer ends of alternate flow passages; first passage means at said rotor hub communicating with the radially inner ends of such alternate flow passages; a first outlet in said housing in communication with said first passage means; means sealing the intermediate flow passages from said conduit means and said first passage means; whereby such one gaseous medium will enter said first axial inlet, fiow radially outward into said conduit means, then radially inward through such alternate flow passages to said first passage means, and be discharged from the latter through said first housing outlet; a second axial inlet in said housing for the other gaseous medium; second passage means at said rotor hub in communication with said second axial inlet and the radially inner ends of the intermediate fiow channels; an outlet chamber in said housing in communication with the radially outer ends of the intermediate flow passages; means sealing the alternate fiow passages from n co 2 said chamber and said second passage means; and a second outlet in said housing in communication with said outlet chamber; whereby the other gaseous me-dium will fiow between said discs in counter flow heat exchange relation with the first gaseous medium.
2. A recuperative heat exchanger as claimed in claim 1 including draft creating means operatively associated with said discs and having an inlet in. communication with said first passage means and an outlet in communication with said first housing outlet.
3. A recuperative heat exchanger as claimed in claim 1 including a fan carried by said discs and having an inlet in communication with said first passage means and an outlet in communication with said first housing outlet.
1. A recuperative heat exchanger as claimed in claim 1 in which said conduit means comprises axially extending circumferentially spaced hoods on the peripheries of said discs.
5. A recuperative heat exchanger as claimed in claim 1 in which said first and second passage means are defined by axially extending, substantially radially projecting walls secured to rotate with said discs and said rotor hub, and said first named sealing means includes circumferentially curved wall sections interconnecting the outer ends of pairs of said walls alternately in a circumferential and in an axial direction.
6. A recuperative heat exchanger as claimed in claim 1 in which said housing outlets are tangentially directed.
7. A recuperative heat exchanger as claimed in claim 1 in which said first and second passage means are defined by axially extending, substantially radially projecting, radially curved walls secured to rotate with said discs and said rotor hub, and said first named sealing means includes circumierentially curved wall sections interconnectin the outer ends of pairs of said walls alternately in a circumferential and in an axial direction.
8. A recuperative heat exchanger as claimed in claim 1 in which said first axial inlet is annular and said conduit means comprises axially extending circumferentially spaced hoods on the peripheries of said discs, and including radial vanes forming alternate radial channels connectin each hood individually to said first axial inlet and intermediate radial channels connecting said first passage means to said first housing outlet.
9. A recuperative heat exchanger as claimed in claim 1 in which said conduit means comprises axially extending circumferentially spaced hoods on the peripheries of said discs, and including throttling means controlling flow of such one gas eous medium into the alternate flow passages.
"roanJoaN VANNERUS.
CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,6563% ileijlrzenslriold Jan. 17, 1928 1,723,294 Falla Sept. 17, 1929 Vannrus June 18, 19%
FOREIGN PATENTS Nu: her Country Date 559,896 Great Britain Mar. 9, 1944 640,183 France Mar. 24, 1928 539,730 Germany Dec. 1, 1931
US722920A 1944-09-25 1947-01-18 Recuperative heat exchanger of the counterflow type for gaseous media Expired - Lifetime US2596622A (en)

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Cited By (11)

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US2963279A (en) * 1956-05-09 1960-12-06 Air Preheater Heat exchanger
US3007685A (en) * 1953-03-13 1961-11-07 Parsons C A & Co Ltd Heat exchangers
US3068877A (en) * 1958-09-12 1962-12-18 Gen Motors Corp Dishwasher
US3232339A (en) * 1962-12-20 1966-02-01 Licencia Tal Almanyokat Erteke Air or gas heating plant
US3333346A (en) * 1965-03-30 1967-08-01 Gen Motors Corp Domestic clothes dryer
FR2571838A1 (en) * 1984-10-12 1986-04-18 Nishimura Jinichi Heat exchanger structure comprising a rotating drum provided with fins
WO1993004332A1 (en) * 1991-08-12 1993-03-04 Raymond Leroy Anderson Heat exchanger
US5513697A (en) * 1991-04-17 1996-05-07 Gudmundsson; Bjorn Method and device for transfer of heat
US20040188077A1 (en) * 2002-10-03 2004-09-30 Holl Technologies Company Apparatus for transfer of heat energy between a body surface and heat transfer fluid
WO2007084063A1 (en) * 2006-01-23 2007-07-26 Eva Gudmundsson Method for heat exchanging and heat exchanger device
WO2007117194A1 (en) * 2006-04-07 2007-10-18 Eva Gudmundsson Method and means for pumping in heat exchange applications

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US1656790A (en) * 1921-05-31 1928-01-17 Heijkenskjold Gustaf Wolfgang Heat-exchange apparatus
FR640183A (en) * 1927-08-10 1928-07-07 Air heater
US1728204A (en) * 1927-11-29 1929-09-17 Edge Moor Iron Company Double-flow fan
DE539730C (en) * 1931-12-01 Babcock & Wilcox Dampfkessel W Circulating air heater
GB559896A (en) * 1942-09-07 1944-03-09 Stanley Edward Bowrey An improved type of centrifugal apparatus for effecting transfer of heat between fluids
US2402307A (en) * 1942-04-28 1946-06-18 Vannerus Torbjorn Recuperative heat exchanger for gaseous media

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DE539730C (en) * 1931-12-01 Babcock & Wilcox Dampfkessel W Circulating air heater
US1656790A (en) * 1921-05-31 1928-01-17 Heijkenskjold Gustaf Wolfgang Heat-exchange apparatus
FR640183A (en) * 1927-08-10 1928-07-07 Air heater
US1728204A (en) * 1927-11-29 1929-09-17 Edge Moor Iron Company Double-flow fan
US2402307A (en) * 1942-04-28 1946-06-18 Vannerus Torbjorn Recuperative heat exchanger for gaseous media
GB559896A (en) * 1942-09-07 1944-03-09 Stanley Edward Bowrey An improved type of centrifugal apparatus for effecting transfer of heat between fluids

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3007685A (en) * 1953-03-13 1961-11-07 Parsons C A & Co Ltd Heat exchangers
US2963279A (en) * 1956-05-09 1960-12-06 Air Preheater Heat exchanger
US3068877A (en) * 1958-09-12 1962-12-18 Gen Motors Corp Dishwasher
US3232339A (en) * 1962-12-20 1966-02-01 Licencia Tal Almanyokat Erteke Air or gas heating plant
US3333346A (en) * 1965-03-30 1967-08-01 Gen Motors Corp Domestic clothes dryer
FR2571838A1 (en) * 1984-10-12 1986-04-18 Nishimura Jinichi Heat exchanger structure comprising a rotating drum provided with fins
US5513697A (en) * 1991-04-17 1996-05-07 Gudmundsson; Bjorn Method and device for transfer of heat
WO1993004332A1 (en) * 1991-08-12 1993-03-04 Raymond Leroy Anderson Heat exchanger
US20040188077A1 (en) * 2002-10-03 2004-09-30 Holl Technologies Company Apparatus for transfer of heat energy between a body surface and heat transfer fluid
US6938687B2 (en) * 2002-10-03 2005-09-06 Holl Technologies Company Apparatus for transfer of heat energy between a body surface and heat transfer fluid
WO2007084063A1 (en) * 2006-01-23 2007-07-26 Eva Gudmundsson Method for heat exchanging and heat exchanger device
WO2007117194A1 (en) * 2006-04-07 2007-10-18 Eva Gudmundsson Method and means for pumping in heat exchange applications
US20090321051A1 (en) * 2006-04-07 2009-12-31 Eva Gudmundsson Method and means for pumping in heat exchange applications

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