US1883124A - Indirectly heated steam generator - Google Patents

Indirectly heated steam generator Download PDF

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Publication number
US1883124A
US1883124A US581252A US58125231A US1883124A US 1883124 A US1883124 A US 1883124A US 581252 A US581252 A US 581252A US 58125231 A US58125231 A US 58125231A US 1883124 A US1883124 A US 1883124A
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Prior art keywords
tubes
header
heating elements
condensate
highly heated
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Expired - Lifetime
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US581252A
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Trede Hans
Otto H Hartmann
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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
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B21/00Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically
    • F22B21/34Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically built-up from water tubes grouped in panel form surrounding the combustion chamber, i.e. radiation boilers
    • F22B21/36Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically built-up from water tubes grouped in panel form surrounding the combustion chamber, i.e. radiation boilers involving an upper drum or headers mounted at the top of the combustion chamber
    • F22B21/363Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically built-up from water tubes grouped in panel form surrounding the combustion chamber, i.e. radiation boilers involving an upper drum or headers mounted at the top of the combustion chamber involving a horizontal drum mounted in an upper corner of the boiler
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00Methods of steam generation characterised by form of heating method
    • F22B1/02Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/08Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being steam
    • F22B1/12Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being steam produced by an indirect cyclic process

Definitions

  • the invention relates to indirectly heated steam generators having a closed circuit in which the heating medium is evaporated in heat receiving tubes outside the boiler drum f and condensed in heating elements within the boiler drum.
  • the heating medium is evaporated in heat receiving tubes outside the boiler drum f and condensed in heating elements within the boiler drum.
  • an intermediate header serving as a fluid separator and to return the separated fiuid to the circuit by downcomers at suitable points.
  • increased circulation ofthe fluid through the heated tubes of the circuit is secured so that the tubes are well cooled and protected against burning.
  • T heating fluid is lost, by leakage, for instance, at the connections in the circuit, it may happen that the fluid level in the circuit is lowered to such an extent that an insufficient amount of fluid, or even no fluid at all., will iow through the highly heated parts of the heat receiving tubes and these parts will therefore not be cooled sufiiciently.
  • boiler parts such as the tubes forming the roof1 of the combustion chamber, fire-bridge tubes, grate cooling tubes Aand the like, which are exposed to the greatest heat, .'.oare connected in the return path of the condensate of the heating medium as itflows from the heating elements of the boiler drum to the heating elements of the furnace.
  • the condensate of the heating medium or a part of it only if the arrangement is applied only t-o a part of the heat receiving tubes, must flow through the highly heated parts entirely independently of the level of the fluid in the system, because the condensate formed can reach the less highly heated tubes only through the above mentioned intermediate header after it has passed through the highly heated tubes.
  • connection according to the invention may be such that the tubes which are first traversed by the condensate are connected to a special intermediate header which in turn is connected with the intermediate headers of the remaining heat receiving tubes.
  • a joint intermediate header may be provided for all the heat receiving tubes in which a chamber is formed by walls serving as overflow elements to which the heat receiving tubes which are first traversed by the condensate and their downcomers are connected.
  • Fig. l is a longitudinal section through one modification.
  • Fig. 2 is a cross section upon line II-II of Fig. l.
  • Fig. 3 is a longitudinal section through another modification.
  • Fig. 4 is at the left a cross section on line IV L-IV L and at the right a cross section on line IV R-IV R of Fig. 3.
  • l is the indirectly heated boiler drum, 2 the heating elements in the boiler drum, and 3 the heat receiving tubes outside the drum, which are connected at their lower ends to headers 4 and at their upper ends to intermediate headers 5. From these intermediate headers 5 pipes 6 lead to the heating elements 2. It is assumed that the tubes S'form the side walls of the furnace' chamber. In this furnace chamber a fire bridge wall 8 is arranged, which rests on bent tubes 9. These tubes 9 are connected at their lower ends to a header l0 and at their upper ends to an intermediate header 12. The header l0 is separated from the headers 4. The intermediate header l2 is connected-to the intermediate headers 5 by couplings 13 so that any steam generated in the fire bridge tubes 9 is led through the pipes 6 to the heat- -at their lower ends.
  • the heating elements 2 are connected by a condensate discharge pipe 14 to the header 10.
  • the condensate from the heating elements therefore flows first through the fire bridge tubes 9 and thereafter through the intermediate header 12 into the intermediate headers 5 and from these further into the water tubes 3. In such a way an effective cooling of the especially highly heated bridge wall supporting tubes is secured by the condensate as it flows from the heating elements.
  • the intermediate headers 5 are connected by the downcomers 15 to the headers 4 and the intermediate header 12 is connected by a downcomer 16 to the header 10,
  • a downcomer 16 to the header 10
  • fluid circuits having shorter paths are formed as well by the water tubes 3 and'by the fire bridge tubes 9.
  • a non-return valve or other device 13 is connected which permits the circulation in the shorter circuit 10, 9, 12, 16 in one direction only.
  • 1 is the indirectly heated boiler drum, 2 the heating elements in this drum, and 3 the Water tubes arranged as side wall tubes.
  • the tubes 20 forming the roof of the combustion chamber are connected.
  • These tubes 2O are connected at their lower ends to a header 21 and at their upper ends to an intermediate header 22.
  • the condensate return pipe 23 connects the heating elements 2 with the header 21.
  • the inlets of the roof tubes 20 into the intermediate header 22 lie in a middle chamber of the header which is sep arated by intermediate walls 24 from the side chambers 25 of the header.
  • the intermediate walls 24 do not extend completely across the header 22 but only alittle above a central horizontal plane, and serve therefore as overflows over which the heating medium can flow from the middle part of the header to the side chambers when it is at its normal level.
  • VHeaders 26 enter the side chambers 25 and water tubes 3 are connected at their upper ends to these headers.
  • Downcomers 28 also start from these side chambers 25 and lead to headers 29 to which the water tubes 3 are connected
  • Downcomer 30 leads to the header 21 from the middle chamber of the intermediate header 22.
  • A. device 31 is connected in the downcomer 30 which permits the fluid to circulate only in one direction.
  • the main circuit of the heating medium is completed by a pipe 32 connecting the intermediate header 22 with the heating elements 2.
  • This circuit leads from the heat receiving tubes, that is, from the side wall tubes 3 and the roof tubes 20, through the intermediate header 22, the pipe 32, the heating elements 2 and the condensate return 23 to the header 21.
  • fluid circuits having shorter paths are provided through the intermediate header 22 for the side wall tubes 3 and for the roof tubes 20,that for the side wall tubes 3 through the downcomers 28 and the headers 29, 26 and that for the roof tubes 2O through the downcomer 30 and the header 21. Since the condensate from the heating elements 2 must flow first through the roof tubes 2O before it can get to the intermediate yheader 22 and from this header to the water tubes 3, al suiiicient cooling action on these especially highly heated roof tubes is secured.
  • said circuit including heat receiving tubes some of which are more highly heated than others and heating elements, a substantially horizontal header, an overflow wall in said header dividing the same into a plurality of,
  • the highly heated tubes being connected to one of said chambers, the less highly heat-ed tubes being connected to the other of said cb ambers, and means to conduct the condensate from said heating elements first to said highly heated tubes and through said tubes to said first chamber.
  • steam generator in which steam is liv generated by the indirect system by means of a heating medium flowing in a closed circuit, said circuit including heat receiving tubes some of which are more highly heated than others and heating elements, lower and intermediate headers to which said highly heated tubes are connected, other lower and intermediate headers to which said less highly heated tubes are connected, means connecting said first intermediate header to said second interv5 mediate header, means to conduct the condensate from said heating elements first to said first lower header and through the highly heated tubes to said first intermediate header, and downcomers connecting each intermedi- 313 ate header to the corresponding lower header. 5.
  • a heating medium flowing in a closed circuit said circuit including heat receiving tubes some of which are more highly heated than others and heating elements, a substantially horizontal header, an overflow wall in said header dividing the same into a plurality of 120 chambers, the highly heated tubes being connected to one of said chambers, the less highly heated tubes .being connected to the other of said chambers, a lower header to which the highly heated tubes are connected, a second 125 lower header to which the less highly heated tubes are connected, means to conduct the condensate from said heating elements to said first lower header, and downcomers connecting said first chamber to said flrst lower head- "-30

Description

Oct. 18, 1932.
H. TRI-:DE ETAL 1,883,124 m'macmr HEME Smm GENERATOR Filed Dec. l5, 1951 @www Gct. 18, A1932. H. TREDE ET AL INDIRECTLY HEATED STEAM GENERATOR 2 Sheets-Sheet 2 Filed Dec. 15, 1951 A zzorzz gy.-
Patented Oct. 18, 1932 PATENT OFFICE HANS TBEDE AKND OTTO H. HARTMANN, OF KASSEL-WILHELMSHOHE, GERMANY, AS-
SIGNORS T SCHMIDTSCHE HEISSDAMPF-GESELLSCHAFT MIT BESCHRANKTER HAFTUNG, OF KASSEL-WILHELMSI-IOHE, GERMANY, A CORPORATION 0F GERMANY INDIRECTLY HEATED STEAM GENERATOR Application led December 15, 1931, Serial No. 581,252, and n Germany January 10, 1931.
The invention relates to indirectly heated steam generators having a closed circuit in which the heating medium is evaporated in heat receiving tubes outside the boiler drum f and condensed in heating elements within the boiler drum. In such steam generators it is usual to connect into the circuit of' the heating medium an intermediate header serving as a fluid separator and to return the separated fiuid to the circuit by downcomers at suitable points. In such a way, increased circulation ofthe fluid through the heated tubes of the circuit is secured so that the tubes are well cooled and protected against burning. If
(T heating fluid is lost, by leakage, for instance, at the connections in the circuit, it may happen that the fluid level in the circuit is lowered to such an extent that an insufficient amount of fluid, or even no fluid at all., will iow through the highly heated parts of the heat receiving tubes and these parts will therefore not be cooled sufiiciently. In order to secure .even under such unfavorable conditions an effective cooling of the exposed or otherwise high- .125 ly heated parts of the circuit, according to the invention those boiler parts, such as the tubes forming the roof1 of the combustion chamber, fire-bridge tubes, grate cooling tubes Aand the like, which are exposed to the greatest heat, .'.oare connected in the return path of the condensate of the heating medium as itflows from the heating elements of the boiler drum to the heating elements of the furnace.
Therefore, the condensate of the heating medium, or a part of it only if the arrangement is applied only t-o a part of the heat receiving tubes, must flow through the highly heated parts entirely independently of the level of the fluid in the system, because the condensate formed can reach the less highly heated tubes only through the above mentioned intermediate header after it has passed through the highly heated tubes.
The connection according to the invention may be such that the tubes which are first traversed by the condensate are connected to a special intermediate header which in turn is connected with the intermediate headers of the remaining heat receiving tubes. On H150 the other hand, a joint intermediate header may be provided for all the heat receiving tubes in which a chamber is formed by walls serving as overflow elements to which the heat receiving tubes which are first traversed by the condensate and their downcomers are connected. This arrangement has the advantage that in regular operation, that is, with the usual high fluid level in the system, in addition to the passage of' the condensate through these heat receiving tubes, a fluid circulation independent of the flow of the condensate occurs in a shorter path through the intermediate header. If the fiuid level in the system sinks below the upper edge of the overflow walls of the separated chamber, cooling is still effected by the condensate from the heating elements because this condensate then moves in what is, in effect, a closed circuit thr-ough the most exposed heat receiving surfaces or tubes.
In the drawings, two forms of the invention are shown by way of example.
Fig. l is a longitudinal section through one modification.
Fig. 2 is a cross section upon line II-II of Fig. l.
Fig. 3 is a longitudinal section through another modification.
Fig. 4 is at the left a cross section on line IV L-IV L and at the right a cross section on line IV R-IV R of Fig. 3.
4In Figs. l and 2, l is the indirectly heated boiler drum, 2 the heating elements in the boiler drum, and 3 the heat receiving tubes outside the drum, which are connected at their lower ends to headers 4 and at their upper ends to intermediate headers 5. From these intermediate headers 5 pipes 6 lead to the heating elements 2. It is assumed that the tubes S'form the side walls of the furnace' chamber. In this furnace chamber a fire bridge wall 8 is arranged, which rests on bent tubes 9. These tubes 9 are connected at their lower ends to a header l0 and at their upper ends to an intermediate header 12. The header l0 is separated from the headers 4. The intermediate header l2 is connected-to the intermediate headers 5 by couplings 13 so that any steam generated in the fire bridge tubes 9 is led through the pipes 6 to the heat- -at their lower ends.
ing elements 2 in the drum 1. The heating elements 2 are connected by a condensate discharge pipe 14 to the header 10. The condensate from the heating elements therefore flows first through the fire bridge tubes 9 and thereafter through the intermediate header 12 into the intermediate headers 5 and from these further into the water tubes 3. In such a way an effective cooling of the especially highly heated bridge wall supporting tubes is secured by the condensate as it flows from the heating elements.
The intermediate headers 5 are connected by the downcomers 15 to the headers 4 and the intermediate header 12 is connected by a downcomer 16 to the header 10, In this way, in addition to the main circuit of the heating medium which leads from the water tubes, that is, the tubes 3 and the bridge wall supporting tubes 9, through the intermediate headers 12 and 5 and the pipes 6 to the heating elements 2, fluid circuits having shorter paths are formed as well by the water tubes 3 and'by the fire bridge tubes 9. Into the downcomer 16 a non-return valve or other device 13 is connected which permits the circulation in the shorter circuit 10, 9, 12, 16 in one direction only.
In Figs. 3 and 4, 1 is the indirectly heated boiler drum, 2 the heating elements in this drum, and 3 the Water tubes arranged as side wall tubes. In the return path of the condensate from the heating elements the tubes 20 forming the roof of the combustion chamber are connected. These tubes 2O are connected at their lower ends to a header 21 and at their upper ends to an intermediate header 22. The condensate return pipe 23 connects the heating elements 2 with the header 21. The inlets of the roof tubes 20 into the intermediate header 22 lie in a middle chamber of the header which is sep arated by intermediate walls 24 from the side chambers 25 of the header. The intermediate walls 24 do not extend completely across the header 22 but only alittle above a central horizontal plane, and serve therefore as overflows over which the heating medium can flow from the middle part of the header to the side chambers when it is at its normal level. VHeaders 26 enter the side chambers 25 and water tubes 3 are connected at their upper ends to these headers. Downcomers 28 also start from these side chambers 25 and lead to headers 29 to which the water tubes 3 are connected Downcomer 30 leads to the header 21 from the middle chamber of the intermediate header 22. A. device 31 is connected in the downcomer 30 which permits the fluid to circulate only in one direction. The main circuit of the heating medium is completed by a pipe 32 connecting the intermediate header 22 with the heating elements 2. This circuit leads from the heat receiving tubes, that is, from the side wall tubes 3 and the roof tubes 20, through the intermediate header 22, the pipe 32, the heating elements 2 and the condensate return 23 to the header 21. In addition to the main circuit of the heating medium, fluid circuits having shorter paths are provided through the intermediate header 22 for the side wall tubes 3 and for the roof tubes 20,that for the side wall tubes 3 through the downcomers 28 and the headers 29, 26 and that for the roof tubes 2O through the downcomer 30 and the header 21. Since the condensate from the heating elements 2 must flow first through the roof tubes 2O before it can get to the intermediate yheader 22 and from this header to the water tubes 3, al suiiicient cooling action on these especially highly heated roof tubes is secured. It is also obvious that, even if the fluid level becomes so low that the quantity in the middle chamber of the header 22 is insuicient to overflow the walls 24, there will still be a circulation through the shorter circuit including the roof tubes 20 and the downcomer 30 which will cool the roof tubes enough to prevent them from burning out. At the same time, any steam generated ,in these tubes will pass to the heatlng elements, and the condensate will be returned to the roof tubes.
In the described examples it has been as! sumed that all the condensate of the heating elements in the drum 1 is led first to the tubes which are most highly heated. If the highly heated heating surface which is to be cooled forms only a very small part of lthe complete heating surface it is of course aV heating medium flowing in a closed circuit,
said circuit including heat receiving tubes some of which are more highly heated than others and heating elements, a substantially horizontal header, an overflow wall in said header dividing the same into a plurality of,
chambers, the highly heated tubes being connected to one of said chambers, the less highly heat-ed tubes being connected to the other of said cb ambers, and means to conduct the condensate from said heating elements first to said highly heated tubes and through said tubes to said first chamber.
2. In a steam generator in which steam is generated by the indirect system by means of a heating medium flowing in a closed circuit, said circuit including heat receiving er and said second chamber to said second tubes some of which are more highly heated lower header. than others and heating elements, lower and In testimony whereof, we have hereunto set intermediate headers to which said highly our signatures. heated tubes are connected, means to conduct HANS TREDE. 79 the condensate from said heating elements OTTO H. HARTMANN. Erst to said lower header and through said highly heated tubes to said intermediate header, connections from said intermediate l header to the less highly heated tubes, a downcomer connecting said headers, and means in said downcomer to permit flow of fluid therethrough from said intermediate header to said lower header only. 3.- In a steam generator in which steam is S0 generated by the indirect system by means of. a heating medium flowing in a closed circuit, said circuit including heat receiving tubes some of which are more highly heated than others and heating elements, lower and inter- 35 mediate headers to which said highly heated tubes are connected, other lower and intermediate headers to which said less highly heated tubes are connected, means connecting said first intermediate header to said second inter- 39 mediate header, means to conduct the condeni sate from said heating elements rst to said first lower header and through the highly heated tubes to said first intermediate header. 4:. In a. steam generator in which steam is liv generated by the indirect system by means of a heating medium flowing in a closed circuit, said circuit including heat receiving tubes some of which are more highly heated than others and heating elements, lower and intermediate headers to which said highly heated tubes are connected, other lower and intermediate headers to which said less highly heated tubes are connected, means connecting said first intermediate header to said second interv5 mediate header, means to conduct the condensate from said heating elements first to said first lower header and through the highly heated tubes to said first intermediate header, and downcomers connecting each intermedi- 313 ate header to the corresponding lower header. 5. Ina steam generator in which steam is generated by the indirect system by means of .a heating medium flowing in a closed circuit, said circuit including heat receiving tubes some of which are more highly heated than others and heating elements, a substantially horizontal header, an overflow wall in said header dividing the same into a plurality of 120 chambers, the highly heated tubes being connected to one of said chambers, the less highly heated tubes .being connected to the other of said chambers, a lower header to which the highly heated tubes are connected, a second 125 lower header to which the less highly heated tubes are connected, means to conduct the condensate from said heating elements to said first lower header, and downcomers connecting said first chamber to said flrst lower head- "-30
US581252A 1931-01-10 1931-12-15 Indirectly heated steam generator Expired - Lifetime US1883124A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2904016A (en) * 1955-11-15 1959-09-15 Babcock & Wilcox Co High temperature and pressure liquid heater
US3132472A (en) * 1959-09-08 1964-05-12 Crane Co Thermal actuator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2904016A (en) * 1955-11-15 1959-09-15 Babcock & Wilcox Co High temperature and pressure liquid heater
US3132472A (en) * 1959-09-08 1964-05-12 Crane Co Thermal actuator

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