US3254635A - Boiler for the heating or vaporization of a liquid medium - Google Patents

Boiler for the heating or vaporization of a liquid medium Download PDF

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Publication number
US3254635A
US3254635A US310939A US31093963A US3254635A US 3254635 A US3254635 A US 3254635A US 310939 A US310939 A US 310939A US 31093963 A US31093963 A US 31093963A US 3254635 A US3254635 A US 3254635A
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cells
boiler
radiation
walls
wall means
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US310939A
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Schoppe Fritz
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/22—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
    • F24H1/40—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00—Component parts or details of steam boilers
    • F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/40—Arrangements of partition walls in flues of steam boilers, e.g. built-up from baffles
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B9/00—Steam boilers of fire-tube type, i.e. the flue gas from a combustion chamber outside the boiler body flowing through tubes built-in in the boiler body
    • F22B9/02—Steam boilers of fire-tube type, i.e. the flue gas from a combustion chamber outside the boiler body flowing through tubes built-in in the boiler body the boiler body being disposed upright, e.g. above the combustion chamber
    • F22B9/04—Steam boilers of fire-tube type, i.e. the flue gas from a combustion chamber outside the boiler body flowing through tubes built-in in the boiler body the boiler body being disposed upright, e.g. above the combustion chamber the fire tubes being in upright arrangement

Definitions

  • Boilers of this kind known at the present time have a connected radiation chamber into which the flames are directed from one or more burners.
  • the radiation chamher into whose walls the heat is transferred mainly by radiation, is as a rule connected to a convection section in which heat transmission is effected by contact between the hot gases and the walls traversed by the medium to be heated.
  • the radiation chamber is made larger as the desired output of the boiler is increased. Since the rate of heat transfer is proportional to the transverse section, i.e. the second power of the dimensions of the chamber, while the space need increases in proportion to the third power of the dimensions of the chamber, the volume of a radiation chamber required for an increased output increases considerably more than the output itself does.
  • the present invention accomplishes this mainly by subdividing the radiation space into a number of radiation cells heated t individually, which are separated from each other by walls traversed by the medium.
  • the total of the volumes of the radiation cells is considerably smaller than the volume of a connected unified radiation space with equal boiler output.
  • the enclosed space of the boiler according to the present invention can therefore remain very small with a corresponding reduction in the costs of construction.
  • the boiler constructed according to the present invention can be regulated easily and particularly efiectively because heating of the individual radiation cells can be stopped or started as desired.
  • the radiation cells are preferably arranged horizontally and provided with upper and lower walls that are inclined with respect to the horizontal and are traversed by the medium to be heated.
  • the radiation cells preferably end at a distance from the vertical boiler casing with the remaining intermediate space forming combustion gas collecting passages. This means that the combustion gas coming out of the individual cells can be conducted away together, which fact also results in a reduction of the dimensions of the boiler.
  • the intermediate wall forms the boundary between adjacent radiation cells and acts simultaneously as the upper wall of the lower and the lower wall of the upper radiation cell.
  • the walls are usually constructed of pipes traversed by the medium, which walls are arranged parallel to the boiler casing with the walls either lying tightly side by side so that the heat radiation is effected from only one side, or else being arranged at intervals so that the boiler casing radiates back.
  • the latter method requires expensive casing material and does not use space efiiciently.
  • the radiation space of the high output boiler of the present invention can be connected to a convection section wherein heat transmission is effected by conduction, into which each combustion gas collecting passage extends.
  • the convection section is best formed by pipes traversed by the medium and arranged vertically or slanting upwards.
  • the convection section is best formed as a superheater where steam is being produced.
  • the medium and the combustion gases flow mainly in the same direction. This means that the drum is eliminated and thus a reduction in the size of the boiler is effected.
  • the boiler according to the present invention utilizes merely a level regulator which would be needed and used anyhow and which can also be used for controlling the temperature in the superheater.
  • An additional reduction of the boiler size with the same output is possible by providing burners of a known construction with a high flame gas velocity (impulse burners), and by working the boiler at a superatmospheric pressure in the firing space, preferably at a pressure of between 50 and mm. water column.
  • the high gas velocity improves the heat transmission so that the heating surface can be smaller.
  • the combustion gas which, because of its conduction in the same direction as the medium, is emitted at a relatively high temperature, is preferably supplied to a known air preheater whose preheating temperature is considerably higher than usual and perhaps runs between 350-450 C. This means, to be sure, that a larger air preheater is required.
  • the additional costs are proportional to its space requirements.
  • the flame temperature also rises. Its heat radiation is proportional to the fourth power of the temperature.
  • the space requirements of the convection section decrease proportionally to the supertemperature so that the boiler surfaces, which are more thick walled because of the steam pressure, are very considerably reduced. Taken as a whole the high temperature air preheating results in savings in the total surface and, thus, in a reduction of the cost of the boiler.
  • FIGURE 1 in the drawing shows a central vertical section through a high output boiler according to the invention.
  • FIGURE 2 shows a sectional view taken along the line IIlI in FIGURE 1.
  • FIGURE 3 shows a sectional view similar to FIGURE 2 of a modified boiler, this view being taken in a direction vertical to the lengthwise axis of the radiation cells.
  • FIGURE 4 shows a sectional view taken along the line IVIV in FIGURE 3.
  • FIGURE 5 is a view similar to FIGURE 3 showing another modification.
  • 1 indicates the casing of a high-output boiler which contains a radiation space 2 and a convection section 3.
  • the boiler illustrated is constructed as a water-steam boiler, but the invention could also be used in boilers for the production of warm water or for the heating or vaporization of any desired liquid medium.
  • radiation space 2 is subdivided into a number of radiation cells 4.
  • Each of these cells is individually heated, here by placing a burner 5 in association with each cell, which burner sends the flame into its associated radiation cell 4.
  • Cells 4 are separated from each other by walls traversed by water in a manner to be described in greater detail hereinafter.
  • Radiation cells 4 are delimited at their lateral ends by vertical walls 6 which are parallel to and spaced from each other.
  • An intermediate wall 7 extends between and is connected to the sidewalls 6.
  • the intermediate wall 7 begins at the foot of sidewalls 6 adjacent one edge thereof, and it comprises an upwardly inclined section 7a which extends close to the opposite edge of the sidewalls 6.
  • a short section 7b extends vertically upwardly from the upper end of section 7a.
  • Section 70 extends from the upper end of section 7b and it slants upward toward the opposite edge of the sidewalls 6.
  • Vertical section 7d extends upwardly from the upper end of section 70. From the upper end of vertical section 7d on, the described arrangement of the intermediate wall 7 is repeated until the desired number of radiation cells are formed. In the particular embodiment disclosed four radiation cells are provided. Because of the described shape of the intermediate wall 7 it rises between sidewalls 6 essentially in a substantially serpentine or sinuous form. In front of the open side of each of the cells is a burner 5.
  • the cells are essentially horizontally disposed and are arranged in a vertical stack.
  • the cells have upper and lower walls traversed by the medium, e.g., water, which walls are inclined horizontally in such a manner than the water can continuously rise at it moves through them.
  • Sections 7:: and 7c of intermediate wall 7 form in part common walls for two radiation cells lying above each other, which walls are exposed on both sides to the radiation of the flame gases emitted by burners 5.
  • the radiation cells 4 each have the form of a pocket of rectangular cross-section whose upper and lower walls converge toward a closed bottom.
  • the cells are arranged in a box form and with each cell being set at an angle of 180 with respect to the cells above and below it. As can easily be seen from FIGURE 1 this makes possible the best space utilization, so that radiation space 2 has a relatively small volume.
  • the vertical sections 7b and 7d of intermediate wall 7 are spaced from boiler casing 1 so that combustion gas collection channels 8 are formed. These channels can also be delimited toward their outsides by water-conducting walls 9.
  • the vertical sidewall 6, found at the right of the figure, can be joined by an additional intermediate wall 7 to another sidewall.
  • the boiler can be assembled from standardized parts so that it can easily be adapted to any desired output.
  • all walls traversed by the water consist of contiguous parallel pipes.
  • other wall-constructions of a known character could also be employed.
  • Flue gas collection channels 8 communicate with the convection section 3.
  • This section is equipped with vertically arranged pipes 10, which are contacted by the combustion gases as same are conducted back and forth by means of baffles 11.
  • the sidewalls 6 extend through convection section 3.
  • Convection section 3 can partly be constructed as a superheater for the production of steam.
  • FIGURE 1 shows and as can be derived from the description of the effect of the boiler below, the water and the gases move through the boiler mainly in the same direction. Thus, it is not necessary to provide a drum for the separation of the steam from the water.
  • An ordinary regulator sufiices to keep the water level constant at a suitable level such as that indicated by line A. This level regulator also permits control of the temperature in the heater part. Through the lowering of the level it is possible to increase the superheater temperature, and vice versa.
  • the stack gas leaves the boiler at 12.
  • the boiler is operated at a superatmospheric pressure of, say, 50-150 mm. water column.
  • the burners 5 shown in the boiler in the drawing show a burning space which expands conically beginning at the fuel and air supply end 5a and which is supplied with combustion air in a corkscrew manner.
  • the burning space communicates with an acceleration nozzle which in turn communicates with the radiation space of the boiler, which nozzle gives a high velocity to the flame gases.
  • the burners can use liquid, gaseous or solid fuels.
  • the apparatus shown has an air preheater 13 into which the stack gases enter directly from outlet 12.
  • the preheater 13 has two air inlets 14 and 15 through which, by means of blower 16, air can be fed into the preheater. It is of advantage to provide regulators by which the air admission can be controlled in such a manner that the stack gas temperature remains constant independent from the output of the boiler. Thus, the boiler will have maximum output, no matter what load, provided a regulator for the air flow is present.
  • the cold end 13a of the air preheater preferably is made of acid-resistant material.
  • the temperature of the stack-gas is determined by the control of air admission in such a manner that the stack-gas temperature falls below the dew point. This means that a considerable part of the sulphur in the fuel can be withdrawn from the stack-gas condensate and can be neutralized. An opening for the withdrawal of this condensate is shown at 17.
  • the stack-gas leaves the air preheater under pressure through outlet pipe 18 and reaches a flue which can be capped by an acceleration nozzle which ejects the stack-gases very high into the atmosphere so that they do not constitute a nuisance for the environment.
  • the boiler shown works as follows: Fresh water is admitted through conduit system 19 and reaches elastically suspended feed pipes 20, which are connected with pipes comprising the sidewalls 6 and the pipes comprising the intermediate wall 7. Burners 5 fire into the radiation cells bounded by these walls so that the water is heated by radiation and begins to boil.
  • the gas conduction in the radiation cells is arranged in such a manner that first of all the hot flame gas enters coaxially into the pocket-like radiation cells, is then reversed at the closed ends formed by wall section 7b, 7d, and finally flows back along sections 7a, 7c. Because of this flow-back a heat transference by radiation occurs in addition to the transference by contact. In the pipes the water is further heated because of contact with the hot gases and is perhaps even vaporized. Through additional heating in the upper part of pipes 10 it is possible to produce superheated steam. The steam collects in pipes 21 and is then conducted to a consumer (not shown here).
  • FIGURES 3 and 4 show a modified construction of radiation cells 4'.
  • Radiation cells 4' are constructed and arranged like honeycombs in which the cells are arranged in vertical adjacent rows, in which the cells in each row are vertically offset from and are sandwiched with the cells of the adjacent rows.
  • Cells 4 are here delimited by walls 23 which are common to several cells 4' lying above each other in a given row and said walls are wavy or sinuous corresponding to the crosscut of the honeycomb.
  • the walls are formed of pipes as before and are traversed by the medium and are fitted together with adjacent identical walls 23 being mirror images of each other with their maximum points and minimum points 23' being opposed to each other in the manner shown in FIGURE 3
  • the honeycomb-like radiation cells 4' can be open at both ends, in which case burners 5 fire into each of the pipe-like cells 4 from the two open ends thereof.
  • honeycomb-like cells can be formed in other ways.
  • the honeycomb cells as shown in FIGURE 5, can also be formed by zig-zag shaped walls 25.
  • said wall means inside of said casing dividing same into a plurality of separate cells, said wall means being hollow so that the medium to be heated can flow therethrough, said cells being of generally rectangular cross section and each having an upper and a lower wall inclined at substantially the same angle and in opposite directions relative to the horizontal, and in which the cells are arranged one above the other and are placed at an angle of 180 with respect to each other; and
  • any two adjacent cells having common intermediate wall means with one cell being on one side of said common wall means and the other cell being on the other side of said common wall means so that said common wall means are contacted on opposite sides thereof by the combustion gases supplied to the respective adjacent cells.
  • each burner is arranged on the outside of the boiler casing and wherein each burner is comprised of a combustion chamber of conically enlarging shape followed by a converging nozzle opening into the interior of the boiler casing.
  • a boiler according to claim 1 in which the cells include vertical side walls parallel to and spaced from each other and said upper and lower walls of each cell are formed by an intermediate transverse wall extending between and connected to said side walls, said intermediate wall being of serpentine shape to define a plurality of cells each of which is open at one end, and including a burner mounted in front of the open end of each cell.
  • a boiler according to claim 3 in which a plurality of substantially identical, spaced apart, parallel side walls are provided with substantially identical intermediate walls being provided between each pair of side walls.
  • a boiler according to claim 3 in which the intermediate wall is formed of tubes arranged closely adjacent each other and through which the medium flows, said tubes being arranged in vertical planes which are sub stantially parallel to the direction in which the combus-.
  • tion gases enter the cells.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Air Supply (AREA)
US310939A 1962-09-24 1963-09-23 Boiler for the heating or vaporization of a liquid medium Expired - Lifetime US3254635A (en)

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US508883A US3289642A (en) 1963-09-23 1965-10-18 Boiler for the heating or vaporization of a liquid medium

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AT (1) AT242713B (de)
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3375810A (en) * 1965-04-07 1968-04-02 Steinmueller Gmbh L & C Fire-box partition
US3391675A (en) * 1965-09-29 1968-07-09 Foster Wheeler Corp Burner arrangement
US4031860A (en) * 1975-02-03 1977-06-28 Deutsche Babcock & Wilcox Aktiengesellschaft Arrangement for reducing the nox content of fluid gases
US4180019A (en) * 1978-03-01 1979-12-25 The Lummus Company Process heater
ES2115461A1 (es) * 1994-08-04 1998-06-16 Roca Radiadores Perfeccionamientos en las calderas de calefaccion.
CN118998817A (zh) * 2024-10-23 2024-11-22 山西奥通环保自动锅炉有限公司 一种用于供热系统的供热装置

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2622298C3 (de) * 1976-05-19 1981-05-14 Centralnyj naučno-issledovatelskij i proektno-konstruktorskij kotloturbinnyj institut imeni I.I. Polsunova, Leningrad Dampferzeuger für eine Wärmekraftanlage
DE3328815C1 (de) * 1983-08-10 1984-10-11 Rolf 7770 Überlingen Bommer Feuerung für einen Heizkessel

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1801670A (en) * 1928-01-03 1931-04-21 Morgan Construction Co Recuperative-furnace control
DE746112C (de) * 1939-06-17 1944-06-10 Dr Georg Friedrich Stieger Wasserrohrkessel mit zwei oder mehr Brennkammern
US2491960A (en) * 1945-02-08 1949-12-20 Ehlinger Marcel Automatic feed regulator for boilers
US2582830A (en) * 1946-01-21 1952-01-15 Riley Stoker Corp Temperature regulation of air heaters
US2735660A (en) * 1956-02-21 Craig
FR1113705A (fr) * 1953-12-05 1956-04-03 Babcock & Wilcox France Foyer-cyclone
US2993480A (en) * 1957-07-31 1961-07-25 Huet Andre Tubular evaporator
US3043279A (en) * 1954-06-18 1962-07-10 Svenska Maskinverken Ab Steam boiler plant
US3117539A (en) * 1960-11-23 1964-01-14 Ind Cie Kleinewefers Konstrukt Heat exchange apparatus and method for operating same
US3160144A (en) * 1961-07-19 1964-12-08 Foster Wheeler Corp Fly ash entrapment wall

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2735660A (en) * 1956-02-21 Craig
US1801670A (en) * 1928-01-03 1931-04-21 Morgan Construction Co Recuperative-furnace control
DE746112C (de) * 1939-06-17 1944-06-10 Dr Georg Friedrich Stieger Wasserrohrkessel mit zwei oder mehr Brennkammern
US2491960A (en) * 1945-02-08 1949-12-20 Ehlinger Marcel Automatic feed regulator for boilers
US2582830A (en) * 1946-01-21 1952-01-15 Riley Stoker Corp Temperature regulation of air heaters
FR1113705A (fr) * 1953-12-05 1956-04-03 Babcock & Wilcox France Foyer-cyclone
US3043279A (en) * 1954-06-18 1962-07-10 Svenska Maskinverken Ab Steam boiler plant
US2993480A (en) * 1957-07-31 1961-07-25 Huet Andre Tubular evaporator
US3117539A (en) * 1960-11-23 1964-01-14 Ind Cie Kleinewefers Konstrukt Heat exchange apparatus and method for operating same
US3160144A (en) * 1961-07-19 1964-12-08 Foster Wheeler Corp Fly ash entrapment wall

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3375810A (en) * 1965-04-07 1968-04-02 Steinmueller Gmbh L & C Fire-box partition
US3391675A (en) * 1965-09-29 1968-07-09 Foster Wheeler Corp Burner arrangement
US4031860A (en) * 1975-02-03 1977-06-28 Deutsche Babcock & Wilcox Aktiengesellschaft Arrangement for reducing the nox content of fluid gases
US4180019A (en) * 1978-03-01 1979-12-25 The Lummus Company Process heater
ES2115461A1 (es) * 1994-08-04 1998-06-16 Roca Radiadores Perfeccionamientos en las calderas de calefaccion.
CN118998817A (zh) * 2024-10-23 2024-11-22 山西奥通环保自动锅炉有限公司 一种用于供热系统的供热装置

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CH425819A (de) 1966-12-15
AT242713B (de) 1965-10-11
GB1041838A (en) 1966-09-07

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