Furnace floor

Information

  • Patent Grant
  • 6205634
  • Patent Number
    6,205,634
  • Date Filed
    Thursday, March 30, 2000
    24 years ago
  • Date Issued
    Tuesday, March 27, 2001
    23 years ago
Abstract
An improved floor for a recovery boiler furnace having a flat floor has a number of tubes in the floor immediately adjacent each of the sidewalls of the furnace oriented at an oblique angle to horizontal. A method of replacing the floor is provided as well.
Description




FIELD OF THE INVENTION




The present invention relates generally to the field of industrial furnaces and boilers and, more particularly, to an improved decanting floor design for kraft recovery boilers.




BACKGROUND OF THE INVENTION




Kraft recovery boilers are used in the pulp and paper industry to recover usable energy from byproducts of the pulp making process. Kraft recovery boilers are similar to conventional fossil-fuel fired boilers. Black liquor fuel is introduced into the furnace along with combustion air. Inside the furnace, residual water is evaporated from the black liquor, and the organic material from the black liquor is combusted. The inorganic portions of the black liquor are recovered as sodium/sulfur compounds.




Gases generated by the black liquor combustion rise out of the furnace and flow across convection heat transfer surfaces. The vertical enclosure walls of the furnace are formed from heat transfer surfaces made of interconnected water tubes. Typically, feedwater enters the recovery boiler at the bottom of a first pass economizer, in which the water is heated as it flows to a steam drum. Saturated water is routed from the steam drum through pipe downcomers to lower furnace enclosure wall and floor inlet headers and a boiler bank. Natural circulation flow in the tubes is induced and driven by heat input to the vertical water cooled enclosure walls of the furnace from the combustion process.




Decanting floors in kraft recovery boilers are known for collecting and directing molten smelt from the black liquor combustion process to discharge openings in the boiler walls. The water tubes forming the floor are cooled by the circulation of water and/or a water/steam mixture through the tubes.




The floors of many known decanting recovery furnaces are essentially flat across the entire surface. Flat floors are subject to minor humping of the tubes, causing domes which form in the upper surfaces of the floor tubes. Steam can become trapped in these humps or domes (steam blanketing) which can cause the tubes to overheat and fail. More particularly, steam blanketing is where steam bubbles are not effectively entrained in the water moving through the tubes. In the flat floor tubes adjacent the furnace sidewalls, the heat input to the tubes may be lower. Since flow through the tubes is by natural circulation, the low heat input to these tubes results in lower fluid velocities and poor circulation in the tubes, which in turn causes steam blanketing.




Currently, the only known method for correcting this defect in flat floor furnaces is to replace the entire tube floor with a new floor. The new floor is sloped to increase the tolerance for heat absorption at lower fluid velocities and to permit venting of the minor humps which would otherwise trap steam and lead to tube overheat and failure. However, replacing the entire furnace floor is both time consuming and expensive, and a cost-effective solution would be welcomed by industry.




SUMMARY OF THE INVENTION




One aspect of the present invention is to provide a method for upgrading a recovery boiler furnace floor without replacing the entire floor.




Another aspect of the present invention is to provide a method and furnace floor for preventing burst tubes which can be implemented relatively inexpensively and efficiently as compared to known solutions.




Accordingly, an improved floor for a recovery boiler furnace having a flat floor has a number of replacement tubes in the floor immediately adjacent each of the sidewalls of the furnace oriented at an oblique angle to horizontal.




In a first embodiment of the invention, immediately adjacent each of the sidewalls, the ends of the replacement tubes at each of the front and back walls are above the remainder of the tubes forming the flat floor and angled to slope downwardly towards a center of the furnace to the level of the tubes forming the flat floor. At the center of the floor, the other ends of the tubes are joined to a central header below the tube floor. The sloped tubes may have a central flat portion adjacent the center of the floor. The radius of curvature of the connection between the flat tube section ends and the central header may be varied to improve fluid flow through the connection, and to join up with the existing flat floor tubes.




In a second embodiment, the ends of the replacement tubes at one of the furnace front and rear walls then are connected to a collection header and are lower than the remainder of the tubes forming the flat floor. The other ends of the replacement tubes at the opposite furnace wall are level with or higher than the remainder of the tubes in the floor. The replacement tubes may be substantially straight along their length. The collection header may be positioned below either the front or back wall of the furnace.




In a method of improving circulation in the floor tubes of a flat floor furnace, several floor tubes immediately adjacent the sidewalls in a flat floor furnace are removed. A series of curved replacement tubes adjacent to the side walls positioned such that the tubes are oriented at an oblique angle to horizontal are connected to the front and back walls of the furnace.




The improved floor design of the invention helps reduce the occurrence of steam bubbles being trapped in humped areas in the furnace floor tubes or forming a steam blanket by improving the fluid flow through the tubes adjacent the sidewalls of the recovery boiler furnace.




The various features of novelty which characterize the invention are pointed out with particularity in the claims annexed to and forming a part of this disclosure. For a better understanding of the invention, its operating advantages and specific benefits attained by its uses, reference is made to the accompanying drawings and descriptive matter in which a preferred embodiment of the invention is illustrated.











BRIEF DESCRIPTION OF THE DRAWINGS




In the drawings:





FIG. 1

is a side elevational view of a first embodiment of an improved replacement furnace floor of the invention;





FIG. 2

is an end elevational view of a floor tube arrangement for the furnace floor shown in

FIG. 1

, viewed in the direction of arrows


2





2


;





FIG. 3

is a top plan view of a portion of the furnace floor shown in

FIG. 1

;





FIG. 4

is a side elevational view of an alternate connection to a central headers for the floor tubes;





FIG. 5

is a side elevational view of a second embodiment of an improved replacement furnace floor;





FIG. 6

is a top plan view of a portion of the furnace floor shown in

FIG. 5

; and





FIG. 7

is an end elevational view of a floor tube arrangement for the furnace floor of FIG.


5


.











DESCRIPTION OF THE PREFERRED EMBODIMENTS




Referring now to the drawings, in which like reference numerals are used to refer to the same or functionally similar elements,

FIG. 1

shows the lower portion


10


of a recovery boiler furnace having front wall


12


, back wall


14


and flat floor


50


. Front and back walls


12


,


14


are water tube walls. Floor


50


is also comprised of a plurality of water tubes.




Adjacent the sidewalls on either side of flat floor


50


, a series of water tubes


30


are sloped downwardly from the front and back walls


12


,


14


toward the center of the furnace lower portion


10


. The sloped water tubes


30


are joined to central headers


40


. The upper ends of sloped water tubes


30


are connected to the front and back furnace walls at weld points


32


.




As seen in

FIGS. 2 and 3

, sloped tubes


30


and flat floor


50


form a continuous surface, with gaps between each tube sealed. Sloped tubes


30


are angled more relative to horizontal immediately adjacent a sidewall


20


and the angle gradually decreases the farther the tube


30


is located from the sidewall


20


until the tubes are consistent and level with the flat floor


50


. Between


3


and


9


water tubes


30


could be used for the sloped tubes


30


. Preferably, six water tubes


30


are used for the sloped tubes


30


, with the sixth tube


30


being relatively flat and unsloped. (See FIG.


2


). The angles which the tubes


30


make with the horizontal plane are between 0° and 10°.




The sloped water tubes


30


may be 2½ or 3 inch outer diameter, internally ribbed tubes, with Inconel® 625 outside cladding to enhance their resistance to the furnace environment.




By providing the sloped tubes


30


adjacent the sidewalls


20


, the path which the water and/or steam takes through these tubes


30


is more gradual and upwards adjacent the front and back walls


12


,


14


. The gradual, upward path improves the fluid flow through the sloped tubes


30


, which would otherwise be hampered by poor thermal conduction near the sidewalls


20


of the furnace


10


. As a result, the effect of humping and steam blanketing is greatly reduced.




The sloped tubes


30


are easily installed in existing flat floor recovery boiler furnaces, as only


12


tubes total need to be replaced and welded back to the flat floor


50


. Preferably, the existing tubes are removed adjacent each sidewall


20


between the front and back walls


12


,


14


. Then, the new sloped tube sections are connected to the front and back walls


12


,


14


with welds


32


at the appropriate heights on the front and back walls


12


,


14


for the desired angle the tube will make to horizontal, gradually decreasing to the level of the existing flat floor


50


. The other ends of the sloped tubes


30


are connected to the central headers


40


.




In the embodiment of

FIGS. 1-4

, the sloped tubes


30


have a flat portion, generally designated


35


, at the center of the lower portion


10


of the recovery boiler furnace. The flat portion


35


of the sloped tubes


30


from both the front wall


12


and back wall


14


meet at this location, and a seal must be provided at this point.





FIG. 4

shows an alternate configuration for the flat portion


35


connection to the central headers


40


which improves the seal between the sloped tube


30


, flat portion


35


and the floor


50


at the central header


40


. An elbow section


45


connects the flat portion


35


of section


30


to a bent tube


46


connected to the central headers


40


. The elbow section


45


bends about 90° and preferably has a radius of 5½ inches.




In a second embodiment of the improved furnace floor, shown in

FIGS. 5-7

, sloped tubes


60


adjacent the sidewalls


20


are only provided at one of the front or back walls


12


,


14


. A supply header


65


is provided at the end wall


12


or


14


where a lowest portion of the sloped tubes


60


are located.




As seen in

FIG. 5

, the sloped tubes


60


are provided at the back wall


14


. In this embodiment, the sloped tubes


60


are oriented at angles below the level of the flat floor


50


, as seen in FIG.


7


. Preferably six tubes


60


would be used; between


3


and


9


tubes


60


could be used as well. The tubes


60


are oriented at angles of between 0° and 10° below the horizontal, with the greatest slope being found in the tube


60


closest to the sidewall


20


and the angle each tube


60


makes decreasing to 0° where they are again even with the flat floor


50


. The ends of the sloped tubes


60


adjacent the front wall


12


are level with the flat floor


50


. The gaps between the tubes are sealed, membraned, as above to form a continuous floor


50


.




The floor of a flat floored furnace would be renovated according to this embodiment in a manner similar to that described above, except that a new header


65


must be installed at the end wall


12


or


14


where the sloped tubes


60


are located. Another new header


70


also is required. Header


70


feeds those rear wall tubes adjacent to the sidewall


20


that were previously fed with the floor.




While specific embodiments of the invention have been shown and described in detail to illustrate the application of the principles of the invention, those skilled in the art will appreciate that changes may be made in the form of the invention covered by the following claims without departing from such principles. For example, the present invention may be applied to new construction involving kraft recovery boilers, or to the replacement, repair, or reconstruction of existing kraft recovery boilers. In some embodiments of the invention, certain features of the invention may sometimes be used to advantage without a corresponding use of the other features. Accordingly, all such changes and embodiments properly fall within the scope and equivalents of the following claims.



Claims
  • 1. A method of improving the floor of a recovery boiler furnace having a horizontal water tube floor, a pair of sidewalls, a front wall, and a back wall to reduce steam blanketing and tube humping in the furnace floor, the method comprising the steps of:removing at least three water tubes of the water tube floor immediately adjacent to at least one of the sidewalls; and replacing the at least three water tubes of the water tube floor immediately adjacent to at least one of the sidewalls with at least three sloped water tubes, such that the angle each successive tube of the at least three sloped tubes after the first sloped tube nearest the sidewall forms with the horizontal tube floor decreases until the sloped tubes are horizontal, the at least three sloped tubes adjacent to at least one of the sidewalls and horizontal floor tubes forming a continuous furnace floor between the sidewalls and front and back tube walls.
  • 2. The method according to claim 1, wherein the at least three water tubes adjacent to at least one of the sidewalls comprises six water tubes adjacent to at least one of the sidewalls.
  • 3. The method according to claim 1, comprising the step of removing at least three water tubes of the water tube floor immediately adjacent to at least one of the sidewalls between one of the front and back walls and a header.
  • 4. The method according to claim 1, comprising the step of removing at least three water tubes of the water tube floor immediately adjacent to at least one of the sidewalls between one of the front and back walls and a header positioned near the center of the furnace floor between the front and back walls.
  • 5. The method according to claim 1, comprising the steps of removing at least three water tubes of the water tube floor immediately adjacent to at least one of the sidewalls and replacing the at least three water tubes of the water tube floor with at least three sloped tubes whose ends at said one of the front and back walls are level with or higher than a remainder of the horizontal floor tubes, and whose other ends at an opposite one of the front and back walls is lower than the remainder of the horizontal floor tubes.
  • 6. The method according to claim 5, comprising the step of providing a header at the ends of the replaced sloped tubes which are lower than the remainder of the horizontal floor tubes.
  • 7. A method of improving the floor of a recovery boiler furnace having a horizontal water tube floor, a pair of sidewalls, a front wall and a back wall to reduce steam blanketing and tube humping in the furnace floor, the method comprising the steps of:removing at least three water tubes of the water tube floor immediately adjacent each of the sidewalls; and replacing the at least three water tubes adjacent each sidewall with at least three sloped water tubes, such that the angle each successive tube of the at least three sloped tubes after the first sloped tube nearest the sidewall forms with the horizontal tube floor decreases until the sloped tubes are horizontal, the at least three sloped tubes adjacent each sidewall and horizontal floor tubes forming a continuous furnace floor between the sidewalls and front and back tube walls.
  • 8. The method according to claim 7, wherein the at least three water tubes adjacent each sidewall are connected between one of the front and back walls and a header.
  • 9. The method according to claim 8, wherein replacing the at least three water tubes adjacent each sidewall comprises welding each water tube between the header and one of the front and back walls.
  • 10. The method according to claim 9, wherein the at least three water tubes adjacent each sidewall comprises six water tubes adjacent each sidewall.
  • 11. The method according to claim 7, wherein the at least three water tubes adjacent each sidewall comprises six water tubes adjacent each sidewall.
Parent Case Info

This application is a Division of application Ser. No. 09/292,722 filed Apr. 15, 1999, now U.S. Pat. No. 6,067,944.