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US1800329A - Superheater - Google Patents

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Publication number
US1800329A
US1800329A US401921A US40192129A US1800329A US 1800329 A US1800329 A US 1800329A US 401921 A US401921 A US 401921A US 40192129 A US40192129 A US 40192129A US 1800329 A US1800329 A US 1800329A
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Prior art keywords
steam
heating
container
tubes
superheater
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Expired - Lifetime
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US401921A
Inventor
Uhde Robert
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Schmidtsche Heissdampf GmbH
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Schmidtsche Heissdampf GmbH
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22GSUPERHEATING OF STEAM
    • F22G1/00Steam superheating characterised by heating method
    • F22G1/005Steam superheating characterised by heating method the heat being supplied by steam
    • 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02Heat-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 helically coiled
    • F28D7/024Heat-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 helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
    • 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
    • Y10S165/355Heat exchange having separate flow passage for two distinct fluids
    • Y10S165/40Shell enclosed conduit assembly
    • Y10S165/401Shell enclosed conduit assembly including tube support or shell-side flow director
    • Y10S165/416Extending transverse of shell, e.g. fin, baffle
    • Y10S165/417Extending transverse of shell, e.g. fin, baffle including spacer or support for transverse tube support or shell-side flow director

Definitions

  • the invention relates to superheaters with tubular heating elements, through which the heating medium, for example superheated steam or a highly-heated liquid, flows from 5 above downwards while the working steam to .be superheated is admitted atthe bottom of the superheater and withdrawnat the top.
  • the heating medium for example superheated steam or a highly-heated liquid
  • the heating elements in such-an arrange ment may take the form of serpentine tubes With U-shaped return "bends and lying side by side or of co-axial helical coils.
  • the superheater is divided into sections by transverseparti'tions having openings for the workingsteam arrangedin staggered relation.
  • the working steam flows through theopening of onetransverse partitioninto a certain section of the container, distributes itself among the individual tubes and follows these along their length to the oppositely-disposed opening inv the next higher partition.
  • the fitting of the heating elements in the superheater container and their connection 'with'the heating-steam inlet and the condensate outlet are efi'ected according tothe present invention in such a way that a heating element can be replaced with very little labour and at a small cost.
  • Figure 2 a cross-section on the line 11-11 of Figure 1, while Figure 3 shows in section to a larger scale a method of passing a collector tube of the heating coils steam-tight through the bottom of the superheater container.
  • heater container comprises a cylindrical shell, 1, having a detachable cover, 2, and
  • the'shell, 1 being provided at its lower end with the inlet connection, 4, and at its upper end with the outlet connection, 5, for the working steam to be superheated.
  • six coils, 6 to '11 are provided, wound in the form of helices lying coaxially one within the other as shown.
  • each coil In the form' of the invention shown, four convolutions of each coil are disposed one above the other in each annular section.
  • the number of tubes lying in a given section can, however, be chosen as desired in order to obtain the vertical distance between the convolutions-which gives the desiredvelocity of flow of the working steam through the interspaces.
  • Each transverse partition, 13, is provided with a sector-shaped opening, 14, and for the convenience of assembly and dismantling is preferably made in two pieces.”
  • the sectors, 14, are oppositely disposed in adjacent partitions so that the working steam is compelled on its path from the inlet, l, to the outlet, 5, to flow to'and fro in a serpentine path.
  • the transverse partitions, 13, are carried by vertical rails, 15 and 16, provided with ears or lugs, the rails, '15, with ears, 17, and the rails, 16, with ears, 18, on which the partitions, 13, rest.
  • the inner rails, 15, are suspended from the upper edge of the cylinder, 12, by means of the hooks, 20, while the outer rails, 16, rest on projections, 21, which are fastened to the container shell,
  • the rails, 15 and 16 are connected in pairs by easily detachable crosspieces, 19, and at their upper ends by screw bolts, 22,
  • the heating coils are arranged in pairs, each with a common steam inlet and also a common condensate outlet; thus, in the example shown, the upper ends, 25, 26, of the sleeve, 33, either rolled into the bottom, 3,' of the container or made in one piece therewith.
  • the sleeves, 33 instead of being secured to the bottom and cover could be provided on the shell of the container.
  • the sleeve, 33 carries at its outer end'a'flange, 34, which is fastened'to a ring, 35, by screw bolts, 36, and nuts, 37.
  • the ring, 35 passes loosely over a part, 38, of thecollector tube,
  • the collector tube 32 can be drawn up so that its shoulder, 41, butts against the other face of the ring,35.
  • a packing ring, 42 is interposed between the ring, 35, on the'one hand and the shoulder, 41, of the collectortube and the flange, 34;, of the sleeve, 33, on the other hand.
  • the common tubes for the steam inlet and the condensate outlet are offset with reference to the two corresponding heating coils in such a waythat the one tube,,for example, lies about on the horizontal projection of the outer coil and the other tube about on the horizontal projection of the inner coil.
  • the common tube, 28, for the heating-steam inlet thus lies on the projection of the coil, 6;
  • the common tube, 32, for the condensate outlet lies on the projection of the coil, 7
  • This offset arrangement of distributor and collector tubes has the advantage that if one .coil is damaged, it can be replaced'without damaged, the pair of coils, 6, 7, is removed and the connection of the coil, 7, with the common tubes, 28 and 32, broken. The coil, 7, can then be at once withdrawn towards the end where the distributor tube, 28, is situated, since the latter is offset with reference to the coil, 7. The connection of the common tubes, 28 and 32, with the coil, 6, can thereforeremain unbroken.
  • pairs of doublethreaded coils may replace the single coils described and be secured tocommon tubes at the two ends; with such a constructioma double coil can be replaced in'exactly the same simple manner as described with reference to a single coil.
  • the flow of working steam essential for the present invention in a substantially horizontal direction along the heating tubes can also be efiected if the openings through the partitions take the form of annuli' disposed alternately on the inner and outer edges of successive partitions.
  • a superheater in a superheater a container, coaxial heating coils lying one within the other, inlet connections for the heating medium at one end and outlet connections at the other end of the container, the heating coils being connected in pairs to a common inlet header and a common outlet header, these common headers being so offset that the one header lies. about on the projection of the outer of the two coils and the other header about on the. projection of the inner of the two coils.
  • each header tube being led through one of said sleeves, that portion of the header tube which projects from the sleeve being reucked in diameter to form a shoulder, a ring loosely fitting over thereduced part of the header tube means for forcing said ring against the shoulder of the header tube and. means for clamping the ring against the sleeve.
  • a superheater in which a heating medium is conducted in one direction and in I posed within the container, means for admitt-ing the heating medium to said tubular elements adjacent one end of the container, means for admitting working steam to the partitions located in the container subdividing the container into transverse sections, adj acent partitions being provided with opencontainer at its opposite end, and transverse V signature.
  • tubular heating elements passing through said staggered openings and being arranged V to form in section a plurality of superposed substantially parallel layers of tube Windings, said layers having spaces therebetween whereby the working steam passing through the superheater moves between said layers in its passage through the Various sections of the container.
  • a structure as claimed in claim 3 wherein the distance between adjacent layers of tube windings is greater than that betweens'adjacent sections of tubing in the layers.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

R. UHDE SUPERHEATER Filed Oct. 25, 1929 0 0000000 0000000 o ooooo,o 0000000 00 OOOOO0 0 000000000000000 0000000 00 000000000000000 0000000 0000000 4 00 0000000 0000000 0000000 0000000 2 00 0000000 0000 00 0000 00 0000 00 O0 0000 O0 0000 O0 0000 O0 0000 O0 3 0 f o o o o o o o o u? o o o o o m? o o o o m? o o o o o Q00 0 0 000 0000000 000 O0 000 O0 h.\ 0000 0 0000000 OOOOOOO 00 0000 00 O00 000 0000000 0000000 0 00000 00 M O0 000 OOOOOOO 0000000 0 00000 00 Q 0 000 OOOOOOO 0000000 0 0 000 b 8 0 56 87 Z 37 8 w 77 7 7 7 7 w fifi Q fl I 15 size of container.
Patented Apr. 14, 1931 warren yer-Ares PATENT orries ROBERT UHDE, or KASSEL-WILHELMSHOHE, GERMANY, AssIGNoRjro scrnvrrnrson'n nnrssnnivrrrensnnrsonnrr .MI'I nnsonnnnxrnn HAFT'UNG, or- KASSEL- WIL- HELMSHOHE, GERMANY, A conronnrron or GERMANY 3 surnnrrnn'rnn Application filed October 23, 1929, Serial No.401,921 ,and in Germany January 9, 1929. I v
' The invention relates to superheaters with tubular heating elements, through which the heating medium, for example superheated steam or a highly-heated liquid, flows from 5 above downwards while the working steam to .be superheated is admitted atthe bottom of the superheater and withdrawnat the top.
The heating elements in such-an arrange ment may take the form of serpentine tubes With U-shaped return "bends and lying side by side or of co-axial helical coils.
This known method of 'superheater construction has the-advantage that a very large heating surface can be arranged in a given If the working steam to be superheated flows, as is, usual, in asubstantially Vertical direction through the superheater container, the velocityof flowis determined by the area of the interspaces between the individual elements lying side by side or within one another, or between individualielements and the container wall. As these interspaces, having regard to the manufacture and assembly of the elements, must be comparatively large,
in the aggregate their cross-sectional area is so considerable that the velocity of flow of the working steam remains low under all circumstances.
Further, the working steam flowing in a vertical direction'between the heatingtubes is in contact withtheir outer surface along only two narrow strips. Q c
For both these reasons, namely, the low velocity of flow of the working steam and its unfavourable contact with the heating surface, the co-efficient of heat transmission is low and the heatingsurface must be cor-respondingly large. The eificiency of the superheater as a whole is therefore poor and its cost of production high, quite apart from the fact that .in many cases the necessary space for its installation is not available.
The above-mentioned disadvantages are avoided accordingto the present invention, which, while retaining the serpentine or helical coils, replaces the vertical direction of flow of the working steam by a substantially horizontal to-and-fro movement along the tubes of the heating elements.
With this object, the superheater is divided into sections by transverseparti'tions having openings for the workingsteam arrangedin staggered relation.
The working steam flows through theopening of onetransverse partitioninto a certain section of the container, distributes itself among the individual tubes and follows these along their length to the oppositely-disposed opening inv the next higher partition.
Through this opening, the steam passes into the followingsection and flows in the opposite direction along the tubes disposed therein, this to-and-fro direction of flow of the steam parallel to the heating-tubes bein continued to the outlet.-- l
With the improved method of construction according to the present invention, it is no longer necessary to-keep the interspaces small between adjacent serpentines or coils and between these and the container wall in order to obtain ashigh a velocity of flow as possible ofthe working steam and thereby a good heat transmission. The velocity of flow being no longer dependent on the area .of these interspaces, it is possible,in accordance with the present invention, to choose as desired the velocity of flow of the working steam, in the vertical direction by appropriatelyproportioning the openings through the partitions and in the horizontal direction the distance apart of the heating tubes I lying one above the other. The upper-limit of the velocity is then determined solely by the permissible frictional lossesof the steam passing over the smooth heating'tubes.
With the 'to-and-fro movement of the steam as explained above, the further advantage is secured that steam sweeps over the heating tubes not only over narrow strips but on all sides along their entire length;
In addition, the difliculties connected with helical coils of unequal lengths are likewise overcome by the present invention.
By raising the velocity of flow on the one handand by leading the steam. to and fro along the length of the tubes in continuous contact with their entire surface on the other hand, a substantial increase in the heat transmitted and an efficient utilization of the heating surface are secured, these factors resulting in a corresponding reduction of the heating surface necessary in a given case and therefore in a reduction also of the space required for the superheater and of its cost of production.
The fitting of the heating elements in the superheater container and their connection 'with'the heating-steam inlet and the condensate outlet are efi'ected according tothe present invention in such a way that a heating element can be replaced with very little labour and at a small cost.
Referring to the accompanying drawings, in which one constructional form of the invention is shown byway of example Figure 1 is a vertical longitudinal section through the superheater, and
Figure 2 a cross-section on the line 11-11 of Figure 1, while Figure 3 shows in section to a larger scale a method of passing a collector tube of the heating coils steam-tight through the bottom of the superheater container.
According to the form shown, the super:
heater container comprises a cylindrical shell, 1, having a detachable cover, 2, and
bottom, 3, the'shell, 1, being provided at its lower end with the inlet connection, 4, and at its upper end with the outlet connection, 5, for the working steam to be superheated. For the accommodation of the heating steam, six coils, 6 to '11, are provided, wound in the form of helices lying coaxially one within the other as shown. In the space within the innermost coil, 11, is arranged a sheet metal cylinder, 12, closed at both ends, so that this space is shut oif completely from the annular space within the cont'ainerthrough whichthe working steam flows. r
The division of this annular space into number of annular sections by transverse partitions, 13, is an important feature of the present invention.
- In the form' of the invention shown, four convolutions of each coil are disposed one above the other in each annular section. The number of tubes lying in a given section can, however, be chosen as desired in order to obtain the vertical distance between the convolutions-which gives the desiredvelocity of flow of the working steam through the interspaces. Y
Each transverse partition, 13, is provided with a sector-shaped opening, 14, and for the convenience of assembly and dismantling is preferably made in two pieces." The sectors, 14, are oppositely disposed in adjacent partitions so that the working steam is compelled on its path from the inlet, l, to the outlet, 5, to flow to'and fro in a serpentine path.
The transverse partitions, 13, are carried by vertical rails, 15 and 16, provided with ears or lugs, the rails, '15, with ears, 17, and the rails, 16, with ears, 18, on which the partitions, 13, rest. The inner rails, 15, are suspended from the upper edge of the cylinder, 12, by means of the hooks, 20, while the outer rails, 16, rest on projections, 21, which are fastened to the container shell, At their lower ends, the rails, 15 and 16, are connected in pairs by easily detachable crosspieces, 19, and at their upper ends by screw bolts, 22,
with nuts, 23, and distance pieces, 24:,
The heating coils are arranged in pairs, each with a common steam inlet and also a common condensate outlet; thus, in the example shown, the upper ends, 25, 26, of the sleeve, 33, either rolled into the bottom, 3,' of the container or made in one piece therewith. Alternatively, the sleeves, 33, instead of being secured to the bottom and cover could be provided on the shell of the container. The sleeve, 33, carries at its outer end'a'flange, 34, which is fastened'to a ring, 35, by screw bolts, 36, and nuts, 37. The ring, 35, passes loosely over a part, 38, of thecollector tube,
32, of smaller diameter provided with screw threads, 39. By means of a nut,40, engaging with the threads,-39, on the collector tube, 32,
and butting against one face of the ring, 35,
the collector tube 32, can be drawn up so that its shoulder, 41, butts against the other face of the ring,35.' To assist in securing steam-tightness, a packing ring, 42, is interposed between the ring, 35, on the'one hand and the shoulder, 41, of the collectortube and the flange, 34;, of the sleeve, 33, on the other hand.
' This arrangement has the advantage that the joint lies outside the container Due to this fact any leakage at once becomes visible and can be readily dealt with. I
The common tubes for the steam inlet and the condensate outlet are offset with reference to the two corresponding heating coils in such a waythat the one tube,,for example, lies about on the horizontal projection of the outer coil and the other tube about on the horizontal projection of the inner coil.
In the form ofthe invention described, the common tube, 28, for the heating-steam inlet thus lies on the projection of the coil, 6;, and the common tube, 32, for the condensate outlet lies on the projection of the coil, 7
This offset arrangement of distributor and collector tubes has the advantage that if one .coil is damaged, it can be replaced'without damaged, the pair of coils, 6, 7, is removed and the connection of the coil, 7, with the common tubes, 28 and 32, broken. The coil, 7, can then be at once withdrawn towards the end where the distributor tube, 28, is situated, since the latter is offset with reference to the coil, 7. The connection of the common tubes, 28 and 32, with the coil, 6, can thereforeremain unbroken.
If the coil, 6, is damaged, it can be detached in the same way and withdrawn at the end where the collector tube, 32, is
situated.
By thus arranging the coils in pairs and ofl'setting thecommon tubes as described, the
work required in replacing a coil is reduced to a minimum.
When the convolutions have a comparatively large diameter, pairs of doublethreaded coils may replace the single coils described and be secured tocommon tubes at the two ends; with such a constructioma double coil can be replaced in'exactly the same simple manner as described with reference to a single coil.
The path of the working steam through the annular. sections of the superheater formed by the intermediate walls, 13, is shown in Figure 1 by arrows. The steam entering through the inlet connection, 4, flows into the annular section lying immediately above the lowest partition, 13, and passes by way of the interspaces between the convolutions of the coils lying one above the other to the opposite side where it flows upwards through the opening, 14, of the second lowest partition, 13, into the next section, this upward flow being effected through the annular spaces present between the individual convolutions and bet-ween the inner and outer convolutions and the container shell. The steam flowing upwards through these annular spaces is deflected and passes along the convolutions of the coils in the intersp'aces between them to the opposite side, where it is transferred to the next higher annular section and so on.
In this way the convolutions of the heating coils are surrounded as completely as possible by working steam.
As the steam is in cont-act not only with the under side of the convolutions but also with their upper side, in the lower annular sections in which the convolutions contain more or less condensate and have steam only in the upper part, transference of-lieat from this remaining heating steam to the working steam to be superheated can be eliected in tavourable circumstances directly through the tube wall, a circumstancecontributing substantially to a complete utilization of the v heat available in the heating steam. 7
When the container with its heating tubes is of' suflicient breadth, the flow of working steam essential for the present invention in a substantially horizontal direction along the heating tubes,can also be efiected if the openings through the partitions take the form of annuli' disposed alternately on the inner and outer edges of successive partitions. 1
Ifserpentine tubes are used inst ad of the helical coils described, the partitions must I be so arranged that their openings lie on the same side of the container as the reverse bends of the serpentines. The working steam after passing through "the'opening in a partition into the next container section, then meets the heating tubes in this section asubstantially horizontal direction. What I claim is:
1. In a superheater a container, coaxial heating coils lying one within the other, inlet connections for the heating medium at one end and outlet connections at the other end of the container, the heating coils being connected in pairs to a common inlet header and a common outlet header, these common headers being so offset that the one header lies. about on the projection of the outer of the two coils and the other header about on the. projection of the inner of the two coils.
2. In a superheater a container, heating elements located therein, header tubes to which said heating elements are connected, hollow sleeves provided in the container wall, each header tube being led through one of said sleeves, that portion of the header tube which projects from the sleeve being re duced in diameter to form a shoulder, a ring loosely fitting over thereduced part of the header tube means for forcing said ring against the shoulder of the header tube and. means for clamping the ring against the sleeve.
3. A superheater in which a heating medium is conducted in one direction and in I posed within the container, means for admitt-ing the heating medium to said tubular elements adjacent one end of the container, means for admitting working steam to the partitions located in the container subdividing the container into transverse sections, adj acent partitions being provided with opencontainer at its opposite end, and transverse V signature.
ings in staggered relation to each other, the tubular heating elements passing through said staggered openings and being arranged V to form in section a plurality of superposed substantially parallel layers of tube Windings, said layers having spaces therebetween whereby the working steam passing through the superheater moves between said layers in its passage through the Various sections of the container. I
4. A structure ,as claimed in claim 3 wherein the distance between adjacent layers of tube windings is greater than that betweens'adjacent sections of tubing in the layers.
In testimony whereof I have affixed my ROBERT UHDE.
US401921A 1929-01-09 1929-10-23 Superheater Expired - Lifetime US1800329A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3799121A (en) * 1972-12-13 1974-03-26 Combustion Eng Superheater flow baffling
US4253225A (en) * 1979-10-10 1981-03-03 Carrier Corporation Method of manufacturing a heat exchanger element
US20100096115A1 (en) * 2008-10-07 2010-04-22 Donald Charles Erickson Multiple concentric cylindrical co-coiled heat exchanger

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3799121A (en) * 1972-12-13 1974-03-26 Combustion Eng Superheater flow baffling
US4253225A (en) * 1979-10-10 1981-03-03 Carrier Corporation Method of manufacturing a heat exchanger element
US20100096115A1 (en) * 2008-10-07 2010-04-22 Donald Charles Erickson Multiple concentric cylindrical co-coiled heat exchanger

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