• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a mobile solid fuel firing system (2) comprising a heat exchanger (6), a firing unit (4), a flue gas supply (26) from the firing unit (4) to a hot side of the heat exchanger (6), an ambient air duct (32) through a cold side the heat exchanger (6) and a fan (20) for driving ambient air through the cold side of the heat exchanger (6). A lightweight mobile solid fuel firing system may be achieved when the firing unit (4) comprises a horizontal burner (60) having a first combustion chamber (40) surrounding a firing tray (44) and having a side exit to a reheat chamber (46).
    公开号:AT15518U1
    申请号:TGM310/2015U
    申请日:2015-10-28
    公开日:2017-11-15
    发明作者:
    申请人:Lasco Heutechnik Gmbh；
    IPC主号:
    专利说明:

    Description: The invention relates to a mobile solid fuel combustion system comprising a heat exchanger, a combustion unit, a flue gas supply from the combustion unit to a hot side of the heat exchanger, an ambient air flow through a cold side of the heat exchanger and a blower for driving ambient air through the cold side of the heat exchanger.
    The weight of a mobile solid fuel firing system is an important criterion for the handling of a transport on the one hand and for their solidity, as occur at a very high weight by shaking and hitting during transport large forces within the system.
    It is an object of the present invention to provide a relatively lightweight mobile solid fuel burning plant.
    This object is achieved by a mobile solid fuel firing system of the type mentioned, in which the firing unit according to the invention comprises a horizontal burner with a Erstbrennraum, which surrounds a combustion bottom and has a side exit to a Nachbrennraum.
    The invention is based on the consideration that a compact firing can be achieved when the solid fuel lying on a firebox is over-blown with combustion air in the lateral direction and the flue gas is discharged in the lateral direction. It can be supplied with enough oxygen on a large firing surface much fuel at the same time flat combustion chamber. The compactness makes it possible to produce a high performance, low weight burning unit.
    The firing system is a mobile firing system, which is therefore intended to be transported by a vehicle to its place of use, operated there and later operated again at another site. For this purpose, the combustion plant expediently comprises a load-bearing construction and a lifting element, which is prepared to lift the entire furnace by means of a lifting device on the lifting element. The lifting element may be an insert for a forklift, an upper attachment for a cable suspension of a crane or the like, so that the furnace can be raised and parked, for example, on a loading area. In particular, inserts for standardized forks of a forklift are advantageous. The load-bearing construction expediently comprises a support frame with supports to which side walls are fixed in a housing-like manner. It is also possible that the carrier are formed by folds of housing-forming wall panels.
    In order to achieve a lighter movement of the firing system on site, it is advantageous if the firing system has its own drive unit with wheels. Practical are four wheels. For a safe stand during operation wheels are only on one side of the plant, e.g. two wheels, sufficient, connected to a non-rolling support unit, e.g. a wheelless support foot. With one or more handles, such as a grab bar on the ambient air inlet side, the furnace can easily be moved manually.
    The solid fuel burning plant is suitably prepared for the combustion of a biofuel furnace, ie a non-fossil fuel. Particularly advantageous is a wood-burning plant for use with, for example, wood chips or pellets. Accordingly, the solid fuel burner is made to burn solid, especially wood, and includes a fuel supply with an automatic feed unit for automatically feeding fuel into the firing unit, e.g. on the firebox. A feed motor of the feed unit can be controlled by a control unit, in particular depending on a combustion parameter, such as the combustion temperature, the exhaust gas temperature and / or the hot air temperature.
    The heat exchanger is suitably a gas-gas heat exchanger with a hot side through which during operation of the mobile solid fuel burning plant hot
    Flue gas is conducted from the combustion, and a cold side through which, for example, ambient air from the environment of the solid fuel combustion system is guided and heated there. Subsequently, the hot air from the furnace can be blown, for example, into the environment or an air hose.
    The ambient air duct can lead from an ambient air inlet in the outer casing of the firing system through an ambient air supply and further through the cold side of the heat exchanger, through an ambient air discharge to a hot air outlet in the outer casing of the firing system. In the ambient air inlet - or at a distance to a fan radius to - the ambient air blower is expediently arranged, which presses the ambient air into the housing of the furnace and back out of this. The ambient air duct runs through the heat exchanger and in particular also at least partially around the firing unit in order to cool it as well. The ambient air inlet and the warm air outlet are expediently arranged in opposite sides of the outer casing of the furnace.
    The firing unit comprises the Erstbrennraum and the Nachbrennraum. The horizontal burner comprises the Erstbrennraum and may - depending on the version - also include the afterburner. The horizontal burner is characterized by the side exit of the first combustion chamber, or the two laterally juxtaposed combustion chambers, so that in a combustion, the flames from the Erstbrennraum laterally out and hit the Nachbrennraum.
    The Erstbrennraum includes the firing floor, which is suitably arranged completely in Erstbrennraum. The firing floor is the area of the horizontal burner on which unburned solid fuel is located and continues to burn there, if necessary, except for glutters flying away, which further burn or anneal in the afterburner space.
    The boundary between the Erstbrennraum and the Nachbrennraum may be determined by the secondary air supply. Thus, the afterburner is expediently free of a combustion air supply from the outside. Thus, the boundary at the lateral end of the secondary air supply may be in the Erstbrennraum. Another criterion may be the hearth, ends at the lateral end of Erstbrennraum. A stage may also define the boundary between the first combustion chamber and the afterburner. This step or depression or opening expediently leads to an ash collecting unit in which the ashes formed by the combustion are collected. Such a step, opening or depression can thus form the boundary of the combustion region on which the combustion of the solid fuel takes place during operation of the solid fuel combustion system or which is provided for this purpose.
    In a compact horizontal burner, the problem of not sufficiently complete combustion may occur, so that the emission of pollutants, in particular carbon monoxide, is in an undesirably high range. Such a problem occurs in particular when the flames striking the first combustion chamber have too much opportunity to spread upwards and / or in their cross-section. The combustion cools down too much and does not occur in the desired completeness.
    To avoid this, it is advantageous if the extent of the afterburner remains limited upwards. Conveniently, the extent of the afterburner upwardly from the top of the first combustion chamber is less than the vertical height of the first combustion chamber. This is especially true for the distance from Erstbrennraum to the beginning of the hot side of the heat exchanger or up to a flue gas discharge from Nachbrennraum to the hot side of the heat exchanger out. The upper edge of the Erstbrennraums is suitably measured at the transition to Nachbrennraum or it is an average height of Erstbrennraums used as the top edge height. Further advantageous are smaller dimensions, in particular only up to a maximum of 2/3, 1/2, 1/3, or in particular to a maximum of 1/10 of the height of the Erstbrennraums. The height of the Erstbrennraums may be the cross-sectional height of the Erstbrennraums in the transition to Nachbrennraum or an average height of Erstbrennraums.
    In order to counteract an expansion of the flames after exiting the Erstbrennraum, it is advantageous if the flow cross section of the Nachbrennraums is less than three times, in particular less than twice, the flow cross section of the Erstbrennraums. The flow cross-section can be seen perpendicular to the main flow direction of the flue gas through the afterburner. Conveniently, the flow cross section of the Nachbrennraums is at most three times or twice the flow cross section of the Erstbrennraums over a distance that is equal to the horizontal extent of the Erstbrennraums, in particular from the transition of Erstbrennraums to Nachbrennraum. Of course, it is also possible that the flow cross section in the transition from Erstbrennraum to Nachbrennraum and within the entire Nachbrennraums remains the same or even decreases. Advantageously, the cross section of the afterburner is less than three times, in particular twice, the flow cross section of the first combustion chamber until the beginning of the hot side of the heat exchanger. The flow cross section of the first combustion chamber may be the flow cross section at the transition of the first combustion chamber to the afterburner or an average flow cross section may be measured over the entire first combustion chamber.
    In the heat exchanger, the hot flue gas is strongly cooled and its heat is transferred to the air flowing through the cold side of the heat exchanger ambient air. Until it enters the heat exchanger, the flue gas should therefore have passed through as complete a combustion as possible, since the further combustion is essentially prevented by the strong cooling in the heat exchanger. In order to achieve a good and complete combustion as possible before the entry of the flue gas into the heat exchanger, it is advantageous if a horizontal distance from Erstbrennraum to the beginning of the hot side of the heat exchanger is at least as long as the horizontal extent of Erstbrennraums in flame -direction.
    In order to achieve a sufficiently complete combustion of the flue gas in the afterburner, it may be sufficient that a smoke outlet of the afterburner is opposite the lateral exit of the first combustion chamber to Nachbrennraum. The flue gas must therefore at least substantially completely traverse the afterburner space, so that there is sufficient opportunity for hot afterburning.
    Good combustion or afterburning, it is beneficial if the afterburner is separated by a false ceiling in a subspace and an overlying upper space and the flue gas path from the subspace around the false ceiling around. Appropriately, the flue gas path in the upper space runs in the opposite direction as in the subspace.
    Particularly advantageous is a course of the flue gas path in the afterburner in an S-curve. An S-curve comprises at least two curves over a curve angle of at least 120 °, in particular at least 150 °. The S can be arranged lying or standing, so there may be at least two substantially horizontal separating elements for a stationary S or substantially vertical separating elements for a horizontal S in the afterburner.
    An expansion of the flue gas so that its excessive cooling can be avoided by a combustion chamber ceiling from Erstbrennraum in the Nachbrennraum inside, which runs continuously from the Erstbrennraum and expediently throughout the entire afterburner up and / or horizontally. Small steps up to approximately 20% of the vertical first combustion chamber diameter are irrelevant here.
    Advantageously, an ash bottom is arranged in the flue gas direction behind the firing floor. Between the hearth and the ash floor can be one step down, so that during operation the ash falls down over the step. The ashes may be pushed over the step by the pushing ash or blown down the step into the ash floor by another unit, such as a powerful blower. The ash bottom can be arranged in the afterburner or under the afterburner.
    In order to avoid an excessive expansion of the afterburner down, the ash bottom can be arranged on at least substantially the same height as the firing floor. Regardless of its arrangement, it is advantageous if it has openings that lead into an ash collection container. The ash can be discharged without having to open the afterburner too much downwards, so that its cross section is increased too much. The cross section of an ash collecting space is expediently not calculated to the cross section of the afterburner.
    A preparation of an effectively burning burning unit can be kept simple when the Erstbrennraum extends into the afterburner. The Erstbrennraum may be surrounded at the top and bottom of the afterburner, be suitably surrounded all around by Nachbrennraum, expediently, only the rear part of the Erstbrennraums is surrounded by Nachbrennraum. A good ash discharge, it is beneficial if the Erstbrennraum down openings in the Nachbrennraum inside and / or has an ash collection.
    In a malfunction, it may be advantageous to stop the combustion in the burning unit as quickly as possible. This can be achieved by tearing apart the burning solid fuel, for example by means of a pressure surge. For this purpose, the firing unit expediently comprises a quenching unit that is prepared to tear apart burning solid fuel lying on the firing floor. For this purpose, the extinguishing unit advantageously comprises a compressed air outlet in the first combustion chamber, which may be connected to a turbine, a compressor or the like.
    In order to keep the heat for the most complete combustion in the afterburner, it is advantageous if the afterburner is clad on at least one side wall with combustion stones. Suitable stones are, for example, firebricks.
    The invention is further directed to a method for producing hot air by means of a mobile solid fuel firing system in which solid fuel is burned in a firing unit, resulting from the combustion flue gas is passed through a flue gas supply from the firing unit to the hot side of a heat exchanger and the solid fuel firing system surrounding Air is blown through the cold side of the heat exchanger using a blower.
    Advantageously, the solid fuel is burned on a hearth in a Erstbrennraum a horizontal burner of the combustion unit, and the flue gas is passed through a lateral outlet of Erstbrennraums to a Nachbrennraum and fed from there expediently by a flue gas discharge to the heat exchanger.
    The previously given description of advantageous embodiments of the invention includes numerous features that are given in the individual subclaims partially summarized in several. However, these features may conveniently be considered individually and summarized to meaningful further combinations. In particular, these features can be combined individually and in any suitable combination with the device according to the invention.
    The above-described characteristics, features and advantages of this invention, as well as the manner in which they are achieved, will become clearer and more clearly understood in connection with the following description of an embodiment which will be explained in connection with the drawings. The embodiment is illustrative of the invention and does not limit the invention to the combination of features set forth therein, including functional features. In addition, suitable features of the embodiment may also be considered explicitly isolated and combined with any of the claims.
    In the drawings: FIG. 1 shows a schematic representation of a solid fuel firing plant with a
    Combustion unit, a heat exchanger and an outer housing around the combustion unit and heat exchanger around, Figure 2 shows a firing unit with a Erstbrennraum and a laterally therefrom
    Nachbrennraum and an overlying heat exchanger, 3 shows a further firing unit with a downwardly widening afterburning space with a lower ash collection area, FIG 4 a firing unit with an upwardly expanding afterburner with opposite output to the heat exchanger, [0036] 5 shows a firing unit with an S-shaped flue gas duct through the afterburner, FIG. 6 shows a firing unit with a flue gas duct in the form of a horizontal S, and FIG. 7 shows a firing unit with a first firebox which extends into a secondary firing chamber.
    1 shows a schematic representation of a mobile solid fuel burning plant 2, which is prepared for transport to several different locations. The solid fuel firing plant 2 comprises a firing unit 4 and a heat exchanger 6, which are mounted in a transport unit 8. The transport unit 8 comprises at its lower end insertion openings 10 for inserting the fork of a forklift. Laterally and above, the transport unit 8 is formed formed by folds of the respective side panels or the plant ceiling, which form a transport-stable and weatherproof outer housing 12 together with the ground. To ensure good on-site mobility, the solid fuel firing system 2 is equipped with a four wheel 14 wheel system, of which the two rear wheels 14 have a pivot mechanism 16 for rotating the wheels 14 about a vertical axis. For pushing or pulling the solid fuel combustion system 2, a handle 18 is provided above an ambient air blower 20, which preferably extends over the entire width of the rear wall of the outer housing 12.
    1 shows the solid fuel combustion system 2 in a highly simplified and schematic manner, with essential elements, which are immaterial to the explanation of the invention, has been omitted for clarity. The mobile solid fuel combustion system 2 has a nominal power of 50 kW in this embodiment and is fueled with solid fuel 22, in particular wood, such as wood pellets. For this purpose, a non-illustrated fuel storage can be connected to the solid fuel burning plant 2 via a fuel channel through which the solid fuel 22 reaches a fuel supply 24, which is shown only schematically in FIG. The fuel supply 24 comprises a screw conveyor through which the fuel 22 is conveyed-automatically controlled by an electrical control unit-into the firing unit 4.
    The resulting from the combustion of the solid fuel 22 hot flue gases are discharged upward from the firing unit 4 and fed by a flue gas supply 26 a hot side of the heat exchanger 6 from above or from below. The flue gas is passed vertically or horizontally through the hot side of the heat exchanger 6 and reaches a flue gas fan 28. The cooled in the heat exchanger 6 flue gas is blown out of this by a flue gas discharge 30 from the solid fuel burning plant 2.
    To remove the heat of combustion from the flue gas stream 32, a cooling air flow in an ambient air duct 34 is performed. The cooling air is sucked as outside air or ambient air through the ambient air blower 20 directly from the environment of the solid fuel combustion system 2 and blown into the outer housing 12 of the solid fuel combustion system 2. The ambient air blower 20 is disposed in an ambient air inlet 36 of the outer housing 12. Within the outer housing 12, therefore, there is an overpressure relative to the surroundings of the solid fuel firing system 2.
    The ambient air is blown in an ambient air supply from the ambient air inlet 36 to the cold side of the heat exchanger 6 and heated therein with heat from the hot side. Then it puts in an ambient air discharge the distance from the cold side of the heat exchanger 6 to a hot air outlet 38 of the outer housing 12 back and flows through this as warm air and is blown into the environment or a hose guide. The heated ambient air blown out of the hot air outlet 38 is available with a maximum rated output of 50 kW, for example for drying the building. The firing unit 4 is cooled by the cooling air flow, so that its outside temperature remains relatively cool and suitable for mobile use.
    2 shows a firing unit 4a, as it could be used in the solid fuel burning plant 2. 1, the firing units are provided with reference letters in the following figures: Each of the exemplary embodiments from FIGS. 2 to 7 can be used as firing unit 4 in the mobile firing installation 2 from FIG In the following embodiments, analogous units are provided with the same reference numbers and different reference letters.
    The firing unit 4a comprises a Erstbrennraum 40a, in one side of a För-dereinheit 42 of the fuel supply 24 opens with a screw conveyor. The auger pushes the solid fuel 22 in operation of the solid fuel combustion system 2 on a firing tray 44 which is disposed entirely within the Erstbrennraums 40 a. There burns the solid fuel 22, as indicated by the flames in FIG 2. The Erstbrennraum 40a expediently has a rectangular or polygonal cross-section with more than four sides or corners, for example, an octagonal cross-section.
    Opposite the fuel supply 42, the first combustion chamber 40a is open at the side and opens into a secondary combustion chamber 46a into which the flames from the first combustion chamber 40a project laterally. On its side opposite the first combustion chamber 40a, the afterburner 46a is open at the top and opens into the heat exchanger 6a. After passing through two trains up and down the cooled flue gas leaves the solid fuel combustion system 2 up through the flue gas discharge 30th
    The combustion air is supplied to the combustion taking place in the combustion unit 4a in two ways. Primary air is drawn in by a primary air blower 48 from the environment of the solid fuel combustion system 2 and blown laterally into the combustion via a primary air feed 50. Secondary combustion air is supplied via a secondary air supply 52, e.g. an opening to the outside, sucked and guided all around in the Erstbrennraum 40a. For this purpose, the secondary air around the Erstbrennraum 40a and then guided in a tubular guide 56 of the length and all around from radially outside to inside through a plurality of not shown opening into the Erstbrennraum 40a via a channel 54. A blower is not necessary for this, because the negative pressure generated by the flue gas fan 28 in the firing unit 4 a sucks in the ambient air through the opening 52. By the air supply and the suction of the flue gas blower 28, the flames are pushed or pulled laterally in a flame direction 58 from the first combustion chamber 40a into the afterburner 46a.
    In the afterburner 46a, the flames remain bundled, so that the combustion in the afterburner 46a remains hot and can be sufficiently complete. The proportion of unwanted combustion products, such as carbon monoxide, remains sufficiently low.
    By the laterally opened Erstbrennraum 40a, the flames are driven out substantially horizontally from the Erstbrennraum 40a. In this respect, the first combustion chamber 40a, the fuel supply 42 and the two air supply lines 50, 52 form a horizontal burner 60 with a horizontal flame orientation, at least at the end of the first combustion chamber 40a.
    The transition from Erstbrennraum 40a to Nachbrennraum 46a is formed in the embodiment shown in FIG 2 by the lateral end of the secondary air duct 56. In Figure 2, this transition is shown by a dashed line. Up to this line, secondary air is blown into the combustion from outside to radially inside. The afterburner 46a is free from a combustion air supply from the outside, so that the combustion taking place there is fed with combustion air from the first combustion chamber 40a.
    In the region of the transition from the first combustion chamber 40a to the afterburning chamber 46a, the combustion bottom 44 discharges into an ash bottom 62a, wherein the combustion bottom 44 and the ash bottom 62a, in particular the entire bottom of the afterburner 46a, are at the same height. The ceiling 64a of the afterburning space 46a is at the same height as the ceiling of the first combustion chamber 40a. In this respect, the vertical extent of the cross section of the flue gas stream 32 does not increase in the transition from the first combustion chamber 40a to the afterburner 46a. This expediently also applies to the horizontal extent of the flow cross section. The flow cross section can be seen perpendicular to the flame direction 58 and, for the sake of simplicity, can be regarded as vertical both in the first combustion chamber 40a and in the afterburner 46a, for the sake of simplicity over the entire length of the horizontal flame direction 58.
    3 shows another embodiment of a firing unit 4b. The descriptions of the following exemplary embodiments are essentially limited to the differences from the respective preceding exemplary embodiments, to which reference is made with regard to features and functions that remain the same. In order not to have to carry out several times already described, all the features of a preceding embodiment are generally taken over in the following embodiment, without being described again, unless features are described as differences from the preceding embodiments.
    In contrast to the embodiment of FIG 2, the firing unit 4b comprises a Nachbrennraum 46b, the ash bottom 62b is lower than the firing bottom 44 of the Erstbrennraums 40b. In the transition from Erstbrennraum 40b to Nachbrennraum 46b so far increases the flow cross-section of the flue gas. The magnification is about 200%, since the lateral extent of the afterburner 46b is greater than that of the first combustion chamber 40b. However, the extent of the combustion zone associated therewith is justifiable in terms of complete combustion since the flames can not escape upwards in the transition from the first combustion chamber 40b to the afterburning chamber 46b. The heat collects on the ceiling 64b, so there is enough heat for a good burn. Through the step 66b, the ash 68 collects in the recess of the Nachbrennraums 46b and can be particularly easily removed from there.
    The transition from Erstbrennraum 40b to Nachbrennraum 46b can - as indicated by the left of the two dashed lines in Figure 3 - again be seen at the lateral end of the secondary air supply. It is also possible to see the boundary - as indicated by the right-hand dot-dashed line in FIG. 3 - at the step 66b, ie at the transition at which the flow cross-section significantly increases.
    4 shows another example of a firing unit 4c, in which the afterburner 46c is extended up and down relative to the Erstbrennraum 40c. Here, the flames can extend upwards and also laterally, so that a cross-sectional enlargement of about 500% occurs in the transition between the Erstbrennraum 40 c and the Nachbrennraum 46 c. Although this causes a noticeable cooling of the combustion within the afterburner 46c. However, due to the wide horizontal distance of the outlet 70 of the afterburning chamber 46c to the hot side 72 of the heat exchanger 6b, there is sufficient distance available for sufficient afterburning before the hot flue gas in the hot side 72 is excessively cooled. The distance is about 120% of the length of Erstbrennraums 40c in horizontal
    Flame direction 58. The smoke outlet 70 of the afterburner 46c is so far compared to the side exit of Erstbrennraums 40c to the afterburner 46c.
    The afterburner 46c expands upwardly relative to the first combustion chamber 40c. This extent is about 30% of the vertical height of the first combustion chamber 40c. This expansion is relatively small, so that a too large expansion of the flames and thus a large cooling of the combustion in the afterburner is counteracted.
    To keep the heat in the afterburner 46c sufficiently large, it is lined on one or more sides with combustor bricks 74. In this case, the arrangement of the combustor bricks 74 on that wall of the afterburning chamber 46 c is advantageous, which is blown by the guided in the ambient air guide 34 ambient air. This is the right side in FIG. 4, as shown by the combustor bricks 74 shown there. The combustion stone stones 74 are expediently fireclay bricks, which are arranged in several rows on the corresponding wall.
    By the expansion of the Nachbrennraums 46c upwards is less space available, so that the heat exchanger 6b - in contrast to the heat exchanger 6a with vertically erected plates or tubes - is a plate heat exchanger with horizontal plates. Between the superimposed plates are air spaces between which the ambient air can flow through and heat up.
    The heat exchanger 6 is located above the Nachbrennraums 46, wherein for reasons of space, the heat exchanger 6 is not or only slightly, for example, after one or more pages by a maximum of 10% of its corresponding extent, laterally extends beyond the afterburner 46. The flue gas path leads through the heat exchanger 6 in an S-shape.
    In the embodiment shown in FIG 5, the afterburner 46d is substantially designed as in the previous embodiment, but it includes a false ceiling 76, which is shown in solid lines in Figure 5, the rear end is flowed around by the flames or the hot flue gas. The false ceiling 76 separates a lower subspace 78 from an overhead upper space 80 so that the flames or hot flue gas first pass through the subspace 78, then around the edge of the false ceiling 76 and then through the upper space 80. The flow direction in the upper space 80 is in the opposite direction to the flow in the subspace 78.
    In the embodiment shown in FIG 5, it is possible to provide a plurality of false ceilings 76 above each other, wherein the upper false ceilings 76 are optional, as indicated by the dashed representations. In the embodiment shown in FIG 5, the flue gas path is S-shaped with three opposing S-legs in the upper space and the lowest S-leg in the subspace 78th By this very long flow path of the flue gas or the flames from the first combustion chamber 40d to the hot side 72 of the heat exchanger 6b is a very complete combustion with low pollutants in the exhaust gas.
    A variation of the S-shaped flow guide of FIG. 5 is shown in FIG. The afterburner 46e shown there has two or more partitions 82, which are perpendicular in this embodiment. The first of the two partition walls 82, which faces the first combustion chamber 40e more, leaves a gap open up to the ceiling 64e for the passage of the flames or the flue gas. The subsequent partition wall 82 leaves a gap down to the bottom 62e, so that the hot flue gases can pass therethrough. In this way, an S-shaped flue gas flow is achieved with a horizontal "S." Also hereby - even if not quite as streamlined - a long flue gas path is achieved with sufficiently small flow cross-section, so that a sufficiently complete combustion takes place.
    7 shows a firing unit 4f, in which the first combustion chamber 40f - and also the secondary air supply 56, but only on the upper side of the first combustion chamber 40f - are led into the afterburning chamber 46f. As a result, the combustion is also oxygenated in the part of the first combustion chamber 40f extended into the afterburning chamber 46f, so that an oxygen-rich and therefore complete combustion is promoted.
    The hearth 44 merges into the ash bottom 62f, with a first opening 84 forming a boundary between the hearth 44 and the ash bottom 62f. The opening 84 permits passage of ash 68 from the first combustion chamber 40f into an ash chamber 86 from which the ash 68 can be easily removed. The ash bottom 62f includes a plurality of orifices such that the ash 68, which is pushed from the solid fuel 22 to the ash bottom 62f, gradually falls completely through the openings 84 down into the ash chamber 86, as always in FIG less expected ash 68 is indicated. The cross section of the first combustion chamber 40f is substantially maintained over its entire horizontal length, so that the combustion is concentrated and thus remains hot.
    During operation of the solid fuel combustion system 2, fuel 22 is pushed onto the combustion bottom 44 by the fuel supply 42. By means of an ignition unit, not shown, the fuel 22 is ignited and the combustion is started. By the two combustion air supply lines 50, 52, the combustion is fanned and the rated power of the solid fuel combustion system 2 is reached. The solid fuel 22 burns to ash 68 and is pushed by the advancing solid fuel 22, which is further inserted from the fuel supply 42 into the Erstbrennraum 40 in the direction of the Nachbrennraums 46. At the beginning or in the afterburning chamber 46, the ash falls, for example, via the step 66 or through the openings 84 onto the ash bottom 62 or into the ash chamber 86.
    The hot flue gases, and hereby means the combusting gases in the flames, flow out of the first combustion chamber 40 laterally and enter the afterburner 46. From this they flow through the flue gas outlet 70 in the hot side 72 of the heat exchanger 6. Im Afterburning 46 takes place afterburning of the combustion / flue gases, so that a sufficiently complete combustion of the combustion or flue gases is achieved. In the heat exchanger 6, the flue gases release most of their heat to the ambient air, which is blown through the fan 20 through the cold side of the heat exchanger 6.
    In the event of a malfunction, it may occur that the combustion in the first combustion chamber should be extinguished as quickly as possible. For this purpose, the primary air blower 48 is designed such that it can tear apart the burning solid fuel 22 in a pressure surge and expediently transported into the afterburner 46. There, the solid fuel 22 goes off relatively quickly. Alternatively or additionally, it is possible to connect a further air source in the primary air feed 50, for example a turbine, a compressor or a compressed-air tank. Instead of the primary air feed 50, another feed into the first combustion chamber 40 can also be selected. In this respect, such a compressed air supply, for example, the primary air blower 48 may be regarded as Löscheheit 88.
    REFERENCE LIST 2 Solid Fuel Firing Facility 4a-f Firing Unit 6a-b Heat Exchanger 8 Transport Unit 10 Injection Port 12 Outer Casing 14 Wheel 16 Swing Mechanism 18 Handle 20 Ambient Air Blower 22 Solid Fuel 24 Fuel Supply 26 Flue Gas Supply 28 Flue Gas Blower 30 Flue Gas Removal 32 Flue Gas Stream 34 Ambient Air Flow 36 Ambient Air Intake 38 Warm Air Outlet 40a-f First Burn Space 42 Feed Unit 44 Hearth 46a-f afterburner 48 primary air blower 50 primary air feed 52 secondary air feed 54 channel 56 guide 58 flame direction 60 horizontal burner 62a-f ash bottom 64a-e ceiling 66b-b step 68 ash 70 exit 72 hot side 74 combustor stone 76 false ceiling 78 subspace 80 upper space 82 divider 84 opening 86 Ash chamber 88 erase unit
    权利要求:
    Claims (15)
    [1]
    claims
    A mobile solid fuel firing system (2) comprising a heat exchanger (6), a firing unit (4), a flue gas supply (26) from the firing unit (4) to a hot side of the heat exchanger (6), an ambient air duct (32) through a cold side of the heat exchanger (6) and a fan (20) for driving ambient air through the cold side of the heat exchanger (6), characterized in that the firing unit (4) comprises a horizontal burner (60) with a Erstbrennraum (40) having a combustion bottom (44) surrounds and has a side exit to a Nachbrennraum (46).
    [2]
    2. Mobile solid fuel combustion system according to claim 1, characterized in that an extension of the Nachbrennraums (46) from the upper edge of Erstbrennraums (40) upwards within the distance from Erstbrennraum (40) to the beginning of the hot side of the heat exchanger (6) less than vertical height of Erstbrennraums (40).
    [3]
    3. Mobile solid fuel combustion system (2) according to claim 1 or 2, characterized in that the Erstbrennraum (40a) in the flame direction (58) has a flow cross-section and the flow cross-section of the Nachbrennraums (46a) from the transition of Erstbrennraums (40a) to Nachbrennraum (46a) is less than twice over a distance of at least the horizontal extent of Erstbrennraums (40a).
    [4]
    4. Mobile solid fuel burning plant (2) according to claim 3, characterized in that the cross section is less than twice until the beginning of the hot side of the heat exchanger (6).
    [5]
    5. Mobile solid fuel combustion system (2) according to any one of the preceding claims, characterized in that a horizontal distance from Erstbrennraum (40a-e) to the beginning of the hot side of the heat exchanger (6) is at least as long as the horizontal extent of Erstbrennraums (40a -e) in the direction of flame (58).
    [6]
    6. Mobile solid fuel combustion system (2) according to any one of the preceding claims, characterized in that a flue gas outlet (70) of the Nachbrennraums (46a, b, e, f) relative to the lateral output of Erstbrennraums (40a, b, e, f) to Nachbrennraum (46a, b, e, f) is located.
    [7]
    7. Mobile solid fuel combustion system (2) according to any one of the preceding claims, characterized in that the afterburner (46d) by a false ceiling (76) in a subspace (78) and an overlying and upper space (80) is separated and the flue gas path to the False ceiling (76) around and in the upper space (80) in the opposite direction as in the subspace (78) extends.
    [8]
    8. Mobile solid fuel firing system (2) according to any one of the preceding claims, characterized in that the flue gas path in the afterburner (46d) extends in an S-curve upwards.
    [9]
    9. Mobile solid fuel combustion system (2) according to any one of the preceding claims, characterized in that the combustion chamber ceiling (64a, b) from the first combustion chamber (40a, b) through the entire afterburner (46a, b) extends horizontally through.
    [10]
    10. Mobile solid fuel combustion system (2) according to any one of the preceding claims, characterized in that in the flue gas direction (58) behind the firing bottom (44) an ash bottom (62 b) is arranged, which has a step down, on the ashes in operation by nachdrängende Ash is pushed.
    [11]
    11. Mobile solid fuel combustion system (2) according to claim 10, characterized in that in the flue gas direction (58) behind the firing tray (44) an ash bottom (62f) is arranged, the openings (84) which lead into an ash collecting container (86).
    [12]
    12. Mobile solid fuel combustion system according to one of the preceding claims, characterized in that the Erstbrennraum (40f) in the Nachbrennraum (46f) extends into it.
    [13]
    13. Mobile solid fuel firing system (2) according to claim 12, characterized in that the first combustion chamber (40f) down openings (84) in the Nachbrennraum (46f).
    [14]
    14. Mobile solid fuel burning plant (2) according to one of the preceding claims, characterized in that the firing unit (4) has a quenching unit (88) which is prepared to tear apart burning solid fuel (22) lying on the firing floor (44) a compressed air outlet in the Erstbrennraum (40) which is connected to a turbine.
    [15]
    15. Mobile solid fuel firing system (2) according to claim 14, characterized in that the afterburner (46c-f) on at least one side wall with combustion chamber bricks (74) is covered. For this 3 sheets of drawings
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE1250586B|1964-04-14|1967-09-21|H R Hemicke GmbH, KoIn-SuIz|Furnace for incinerating waste materials|
    US3728976A|1971-07-13|1973-04-24|I Domnitch|Portable incinerator|
    DE2534092A1|1975-07-30|1977-02-17|Konus Kessel Waermetech|Solid fuel-fired horizontal boiler for heating oil - with complete combustion and higher flame temperature due to less excess air|
    KR100973342B1|2009-11-25|2010-07-30|윤학상|Cremation burner that have plural exhaust gas passage|
    WO2012026756A2|2010-08-26|2012-03-01|Song Bum-Hyun|Combustion device, and fan heater and heating apparatus having same|
    WO2016179824A1|2015-05-14|2016-11-17|Zheng Shi|A system for burning pulverized solid fuel and a method thereof|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE202014105238.0U|DE202014105238U1|2014-10-31|2014-10-31|Mobile solid fuel firing system|
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