STEERING FUNNEL FOR BED MATERIAL IN FLUIDIZED BED BOILER, FLUlDIZED BED BOILER AND METHOD IN FLUIDIZED BED BOILER

TECHNICAL FIELD OF THE INVENTION The invention relates to a steering funnel for bed material in a fluidized bed boiler, a fluidized bed boiler and a method in a fluidized bed boiler in accordance with the preambles of the independent claims presented below. The invention especially relates to a new method for guiding flows of material to be removed from a fluidized bed boiler.

TECHNICAL BACKGROUND

An ordinary fluidized bed boiler essentially comprises a furnace limited by vertical walls, a bottom and a roof. A fluidized bed formed of solid matter particles like sand is maintained in the furnace. A typical fluidized bed boiler comprises feeding means for feeding fuel, fluidized bed material and air to the furnace. Flue gases are led away from the furnace to an exhaust duct for flue gases. At the bottom of the furnace there is a grate in which feeding elements of air, like air nozzles, are typically arranged. Air needed for burning of fuel and for fluidization of bed material is fed from air nozzles to the bottom of the furnace. Fluidization air is typically used as primary air of combustion process. On the grate are also arranged elements like openings or gaps for removing solid matter, i.e. bed material, ash, and impurities among them, to underside of the grate. Below the openings or gaps of the grate is typically arranged one or more channels or pockets, which are in this text called funnels, along which material to be removed from the furnace is led in a controlled manner from the furnace to the underside of the boiler. There usually are shutters on the bottom end of the funnels, by means of which the volume of the material to be removed from the furnace is controlled. Material to be removed from the funnels is usually led to a conveyor and onwards to further processing. Material is removed from the funnels at the need, typically periodically, for example a few times an hour in a normal operating situation.

On the underside of the grate there can be a windbox, inside which said funnels are at least partially arranged. Fluidization air is led to the windbox, i.e. around

funnels, and fluidization air is led from the windbox to the air feeding elements above of the grate. Typically air is heated in the windbox with the heat of bed material streaming downwards in the funnels. At the same time, bed material in the funnels is cooling.

One problem in a fluidized bed boiler is a high proportion of incombustible particles contained in some fuels, such as construction waste or logging waste, such as stumps: metals, stones, concrete, etc., that accumulate on the bottom of the furnace and interfere fluidization of sand. Above-mentioned problem has been solved by designing the bottom of the furnace to better remove bed material, for example by enlarging discharge openings of material that lead through the grate. In this manner, also impurities at the bottom of the furnace are removed from the furnace with the bed material.

Due to the downwards tapering form of one or more funnels below the grate, the flow in the funnel is not always steady. A so-called core flow usually tends to develop at the discharge opening in the bottom of the funnel or to the centre of the funnel. This means that material normally flows faster downwards at the centre of the funnel than at the edges of the funnel. Because in fluidized bed boilers the cross-sectional area of the bottom of the furnace, i.e. the bed, is typically considerably larger than the area of discharge openings at the bottom of the funnel or funnels, material is removed irregularly from the furnace. Sometimes material is removed in fluidized bed boilers only from said core flow area of the bottom of the furnace.

As a result of irregular discharge of material, unburnt material accumulates to piles in the bottom of the bed hindering fluidization, and it may cause a partial or total melting of bed material.

Because of an irregular flow of material, a part of the material may even be permanently stationary or move very slowly on the edges of the funnels. This disturbs heat transfer between air flowing in the windbox and bed material. In this case, the material to be removed from the funnels, having flown in the core flow,

does not have enough time to cool down as desired in the funnel. On the other hand, air blown to the furnace is not pre-heated in a desired manner in the wind box.

OBJECT AND BRIEF DESCRIPTION OF THE INVENTION

It is an object of the present invention to reduce or even eliminate the above- mentioned problems appearing in prior art.

The present invention has especially an object of providing a solution for achieving a discharge of material that is as regular as possible from the whole bottom area of the fluidized bed boiler.

An object of the present invention is to reduce so-called core flow which tends to develop to the centre of a steering funnel for bed material in a fluidized bed boiler.

An object of the present invention is to intensify the functioning of a fluidized bed boiler.

An object of the present invention is to intensify heat transfer between air of the windbox and material to be removed from a fluidized bed boiler.

Among others, in order to realize the objects mentioned above, a steering funnel for bed material in a fluidized bed boiler, a fluidized bed boiler, a method in a fluidized bed boiler, and other objects according to the invention are characterized by what is presented in the characterizing parts of the enclosed independent claims.

The embodiment examples and advantages mentioned in this text relate, where applicable, as well to a steering funnel, a fluidized bed boiler, a method, an inner funnel as to uses according to the invention, even though it is not always specifically mentioned.

The embodiments of the invention are suitable to be used in connection with boilers utilizing different fluidization techniques. In this text, the term fluidized bed boiler is used for all different boilers utilizing fluidized bed technique. Fluidized bed boilers are for example circulating fluidized bed boilers, i.e. circulating bed boilers (CFB boilers) or bubbling fluidized bed boilers, i.e. bubbling bed boilers (BFB boilers).

A typical fluidized bed boiler according to the invention comprises a furnace limited by walls, a grate and a roof. Below the grate in the connection with the furnace is arranged a steering funnel according to the invention, in which bed material removed from the furnace is led downwards. In this connection, for the sake of simplicity, only bed material is referred to, even though it is obvious that simultaneously also impurities are removed from the furnace.

A typical steering funnel according to the invention is mainly downwards tapering on its horizontal cross-section. This means that the upper edge of the funnel is larger by its surface area than its lower edge. In the steering funnel there may be vertical or even partly downwards expanding sections. The upper edge of the steering funnel comprises an inlet connection through which the bed material is led into the steering funnel. The lower edge comprises an outlet connection through which bed material is removed from the steering funnel. The outlet connection usually comprises a shutter, like a gate valve, by means of which a flow of the material to be removed from the steering funnel can be guided. In the typical steering funnel of the invention, bed material and elements flowing with it are thus are led along their path between an inlet and outlet connection. According to the invention, into the steering funnel, between its upper and lower edge, are arranged guide plates, which are substantially divergent from the surface of the steering funnel, for guiding the flow of the bed material inside the steering funnel. It is an aim of the guide plates to level the flow of material inside the steering funnel for example by preventing the development of a core flow between an inlet and outlet connection.

In an embodiment of the invention the guide plates are arranged so that the flow of bed material is maintained on mainly the whole cross-sectional area of the steering funnel. Thus, it is not an aim to totally prevent or stop the vertical flow of the bed material, but the flow is guided. The flow, which takes place on as large area as possible of the steering funnel, means that at least not big air pockets, i.e. points where there is no bed material, are formed to the steering funnel, nor at least large points, where bed material does not flow, are formed. This kind of air pockets or points without a flow may in some embodiments of the solution according to the invention cover for example less than 30 %, less than 20 %, less than 10 %, less than 5 %, less than 3 %, less than 2 % or less than 1 % of horizontal cross-sectional area in the steering funnel when bed material is removed in a normal operating situation of the invention.

In an embodiment of the invention guide plates slow down a downwards directed flow of bed material above the outlet connection of the steering funnel. Thus, the guide plates for example throttle the flow of the bed material at the centre of the steering funnel and facilitate flowing of the material near the edges of the steering funnel.

In an embodiment of the invention a free vertical path leads through the steering funnel from an inlet connection of the upper edge to an outlet connection of the lower edge in the steering funnel. In other words, if bed material has completely been removed from this kind of steering funnel, there is a visual contact along a vertical line from the inlet connection of the upper edge to the outlet connection of the lower edge of the steering funnel. Bed material can thus flow at least in theory also along a straight path through the steering funnel and between guide plates.

In an embodiment of the invention, below the grate of a fluidized bed boiler is arranged a windbox through which and thence onwards air needed for burning and fluidization of bed material is led through a grate to a furnace. Thus, a steering funnel according to the invention is typically arranged mainly inside the windbox of a fluidized bed boiler. A steady flow of bed material to be removed from the furnace on the whole cross-section of the steering funnel produces a

more regular retention of material in the steering funnel as compared with material flowing in a core flow according to prior art. The stabilization of the retention time results in more effective and more regular cooling of the material, which makes its later processing in conveyors and silos easier.

Now it has now been surprisingly found that by means of simple guide plates turning the flow and arranged inside the steering funnel, the removal of the material from the bottom of the fluidized bed boiler can be efficiently evened out. Furthermore, by means of the invention heat transfer between the air flowing in the windbox and the material travelling in the steering funnel can be simply increased.

In an embodiment of the invention, guide plates comprise several separate plates and bed material can flow in the spaces between the plates. Guide plates can be placed on various heights in the steering funnel or mainly to the same height with each other. Guide plates can be of different sizes or they can be equal in size with each other.

In an embodiment of the invention, guide plates are formed as an inner funnel into which leads an inlet opening and from which leads an outlet opening. Between the inlet and outlet opening, there are walls of the inner funnel. In an embodiment of the invention the walls are at least mainly closed so that bed material can reach inside the funnel only from the inlet opening and away from the funnel only from the outlet opening. In an embodiment of the invention, openings from which bed material can flow inside the funnel or out of it are formed on the walls.

In an embodiment of the invention, guide plates are formed inside the steering funnel as a substantially downwards tapering inner funnel. The inner funnel efficiently throttles the material flow leading through it and prevents the formation of a core flow by it.

The inner funnel has typically a conical shape, for example a truncated rectangular pyramid shape. Its size is adjusted to be suitable for each steering

funnel. A minimum inner diameter of the inner funnel, i.e. a minimum opening from which the material must flow when it travels through it, can be for example less than 2000 mm, 200 to 2000 mm, 200 to 1000 mm, 250 to 500 mm or 300 to 500 mm. One steering funnel can have one or more inner funnels, for example 1 , 2, 3, 4 or 5.

In an embodiment of the invention, a part of bed material is led along an inner path, i.e. through an inner funnel. Another part of the material is led along an outer path, i.e. between the inner funnel and the steering funnel. When the inner funnel is slowing down the flow inside it, material on the outer path can flow better.

In an embodiment of the invention guide plates, for example an inner funnel, are arranged to the centre part of a steering funnel. This is usually most efficient because usually the core flow of bed material tends to develop right to the centre of the steering funnel. For example, the inner funnel can be arranged straight above the outlet connection of the steering funnel. In an embodiment, the inner funnel is arranged symmetrically in relation to the steering funnel, when considering the horizontal cross-section of the steering funnel.

In an embodiment of the invention, an inner funnel is at a distance from all inner walls of the steering funnel. In this manner, bed material can be led from around the inner funnel on substantially all its sides.

In an embodiment of the invention, a steering funnel and an inner funnel have substantially the same or congruent shape in their horizontal cross-section. For example, both may have a cross-section with the shape of squares, circles or rectangles the length ratios of the sides of which are equal.

In an embodiment of the invention, a steering funnel and an inner funnel have substantially different shape in their horizontal cross-section. For example, one may have a circular horizontal cross-section and the other may be angular.

In an embodiment of the invention, guide plates are arranged between a steering funnel and an inner funnel. In this manner, a flow of bed material can be guided more efficiently also in the vicinity of the walls of the steering funnel.

In an embodiment of the invention, a steering funnel has a rectangular horizontal cross-section. Then, in an embodiment the aim is to intensify a flow of the material in the vicinity of the angles of the rectangle. This can be done, for example, by placing extra guide plates which turn the flow, between the inner funnel and the steering funnel, into the area between the angles of the rectangle. In an embodiment of the invention the inner funnel and said extra guide plates are one and the same piece. Then they can be for example retrofitted as one piece in an already existing steering funnel.

The invention also relates to an inner funnel as such, which funnel is intended inside a steering funnel in a fluidized bed boiler, as well as to the use of downwards tapering funnel and guide plates inside a steering funnel for preventing a core flow of bed material inside a steering funnel.

BRIEF DESCRIPTION OF THE FIGURES The invention is described in more detail below with reference to the enclosed schematic drawing, in which

Figure 1 shows a fluidized bed boiler according to the invention, Figure 2 shows a side-view of an inner funnel in a steering funnel according to the invention, and Figure 3 shows the inner funnel and the steering funnel of Figure 2 as seen from above.

DETAILED DESCRIPTION OF THE EXAMPLES OF THE FIGURES For the sake of clarity, the same reference numbers are used for corresponding parts in different embodiments.

Figure 1 shows a bubbling fluidized bed boiler, i.e. a bubbling bed boiler 1 according to the invention. The boiler comprises a furnace 5 limited by walls 2, a

grate 3 and a roof 4. Through the grate lead openings 6 from which material inside the furnace is guided below the grate into a steering funnel 7. Inside the steering funnel 7 bed material removed from the furnace and impurities among it are led further downwards. There is at the lower end of the steering funnel a damper 8 via which material is guided to a conveyor 9 and onwards to further processing.

Below the grate is arranged a windbox 10. The steering funnel 7 is mainly inside it. To the windbox 10 air needed for burning and fluidization of bed material is led from a connection 11. Air travels through the windbox 10 upwards via air nozzles 13 in a nozzle surface 12 formed onto the grate 3 to the lower part of the furnace 5.

Inside the steering funnel 7 are arranged guide plates 14 which form an inner funnel 15. A part of the material to be removed from the furnace 5 leads through the inner funnel 15. A part of the material flows between the inner funnel 15 and the steering funnel 7.

Figure 1 also shows other parts of a fluidized bed boiler, like different heat exchangers 20, beams 21 supporting the boiler, a steam drum 22, an outlet connection 23 of flue gas as well as an inlet assembly 26 for fuel and bed material which are not an aim of this invention as such and are not explained in further detail here.

Figures 2 and 3 show with broken lines a steering funnel 7 according to the invention, inside which there is an inner funnel 15. There is an inlet opening 24 for material on the upper edge of a steering funnel 7, which opening is intended against the grate 3, and on the lower edge there is an outlet opening 25 for material, in which opening a damper 8 is attached.

A rectangular inner funnel 15 has inclined side walls 16, and thus the funnel is downwards tapering on its horizontal cross-section. The upper edge of the inner funnel 15 comprises an inlet opening 17 for material and the lower edge comprises an outlet opening 18 which is smaller than the inlet opening. The inlet

opening 17 of the inner funnel is arranged approximately to the same height as the inlet opening 24 of the steering funnel. The outlet opening 18 of the inner funnel opens approximately to the middle of the height of the steering funnel 7, a little above the midpoint. The outlet opening 18 has a diameter somewhat smaller than the outlet opening 25. The funnel 15 throttles a material flow at the centre of the steering funnel, i.e. at the outlet opening 25, thus creating a condition for easier flowing of material between the inner funnel 15 and the outer funnel, i.e. the steering funnel 7. To the outer edges of the funnel 15 are attached extra guide plates 19. They throttle the flow of material outside the inner funnel 15 from the angles of the walls 16 towards the centre of the walls. From the Figure 3 it can be seen how a free path downwards for the material remains between the steering funnel 7 and the corners of the inner funnel 15.

Without the inner funnel 15 according to the invention, there would be a danger of forming a core flow for bed material at the centre of the steering funnel 7. Particularly, there would be a danger that at the corners of the steering funnel, i.e. also at the corners of the furnace, hardly any bed material could flow below the grate.

Even though guide plates arranged inside the steering funnel 7 are shown in the form of a funnel in the figures, it is obvious that also guide plates of other shapes can be arranged to guide the flows according to the invention.

The figures show only a few preferred embodiments according to the invention. Facts of secondary importance with regards to the main idea of the invention, facts known as such or evident for a person skilled in the art, such as power sources or support structures possibly required by the invention, are not separately shown in the figures. Fluidized bed technique is known as such, and the operation of boilers is not explained in further detail here. It is apparent to a person skilled in the art that the invention is not limited exclusively to the examples described above, but that the invention can vary within the scope of the claims presented below. The dependent claims present some possible embodiments of

the invention, and they are not to be considered to restrict the scope of protection of the invention as such.