WO2015131817A1 - Procédé de combustion et appareil de combustion pour combustible solide - Google Patents

Procédé de combustion et appareil de combustion pour combustible solide Download PDF

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Publication number
WO2015131817A1
WO2015131817A1 PCT/CN2015/073618 CN2015073618W WO2015131817A1 WO 2015131817 A1 WO2015131817 A1 WO 2015131817A1 CN 2015073618 W CN2015073618 W CN 2015073618W WO 2015131817 A1 WO2015131817 A1 WO 2015131817A1
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combustion
furnace
solid fuel
inlet
wall
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PCT/CN2015/073618
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English (en)
Chinese (zh)
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车战斌
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车战斌
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23B—METHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B50/00—Combustion apparatus in which the fuel is fed into or through the combustion zone by gravity, e.g. from a fuel storage situated above the combustion zone
    • F23B50/02—Combustion apparatus in which the fuel is fed into or through the combustion zone by gravity, e.g. from a fuel storage situated above the combustion zone the fuel forming a column, stack or thick layer with the combustion zone at its bottom
    • F23B50/04—Combustion apparatus in which the fuel is fed into or through the combustion zone by gravity, e.g. from a fuel storage situated above the combustion zone the fuel forming a column, stack or thick layer with the combustion zone at its bottom the movement of combustion air and flue gases being substantially transverse to the movement of the fuel

Definitions

  • the present invention relates to the field of solid fuel combustion, and in particular to a solid fuel combustion method and a combustion apparatus.
  • the inventors have found through careful study that the main difference between biomass burning materials and low-grade coal (such as lignite, peat, etc.) and high-grade coal is that high-grade coal has a high fixed carbon content (generally over 90%). Therefore, it is mainly fixed carbon combustion mode when burning; while biomass combustion materials and low-grade coal have relatively low fixed carbon content and relatively high volatile content (about 50%-70%).
  • the solid fuel with high volatile content mainly has two characteristics: 1) the volatile matter precipitation temperature is lower than the volatile ignition point; 2) the volatile matter has a higher ignition point than the ash melting point.
  • the current combustion furnaces are generally classified into two types: a forward combustion furnace and a reverse combustion furnace. Due to the above characteristics of biomass fuel and low-grade coal, continuous combustion can not be achieved by using these two combustion furnaces.
  • the existing combustion device generally enters the wind through the furnace, so that the solid fuel on the furnace is subjected to high-temperature combustion. Since the ash melting point is lower than the ignition point of the volatile matter and the fixed carbon, the combustion is performed in a high-temperature environment in which the carbon is burned on the furnace. After the ash is in a viscous molten state, it will paste on the furnace and cannot be normally discharged through the furnace or other ash-discharging mechanism (such as the ash stick), so that the viscous ash is mixed and burning. The fuel greatly affects the combustion efficiency of the fuel. Moreover, the viscous ash adheres to the furnace raft and blocks the air inlet passage on the furnace. After a period of time, the furnace is pasted, so that the furnace cannot continue to work.
  • the characteristic of the trans-burning furnace is that the fire outlet is lower than the furnace, so that the flame generated by the combustion passes through the furnace and then reaches the fire exit.
  • This type of combustion is compared with forward combustion, and the evolved volatiles can be ignited by the flame while passing through the furnace. Efficiency has improved.
  • the high temperature flame is located in the furnace position, this also makes the temperature of the furnace position very high. In the high temperature environment, the burnt ash is in a viscous molten state, which will paste on the furnace and block the furnace. The air flow passage will soon ruin the furnace, making the furnace unable to continue working.
  • the Chinese utility model patent No. 01220213695.8 proposes a hot blast stove 900 which can be used for full combustion of various solid combustibles and multi-point air distribution.
  • the hot blast stove includes a furnace body, and an upper combustion chamber 92 and a lower combustion chamber 93 are respectively disposed in the furnace body, and an upper furnace 94 and a lower furnace are respectively disposed at the bottoms of the upper combustion chamber 92 and the lower combustion chamber 93, respectively.
  • 95 below the lower furnace 95 is a ash removal chamber 96, and a burner outlet 98 is provided on the furnace body of the lower combustion chamber 93.
  • the upper combustion chamber 92 is provided with a funnel-shaped combustion chamber 910 whose upper portion is integrated with the inner wall of the furnace, and whose lower portion is reduced in diameter.
  • the lower port of the funnel-shaped fuel tank 910 is located on the upper furnace 94, and the center of the funnel-shaped fuel tank 910
  • a cylindrical pyrotechnic passage 911 having a lower end opening is formed in the longitudinal direction, and an annular upper air passage 912 is formed between the outer wall of the lower portion of the funnel-shaped fuel storage tank 910 and the inner wall of the furnace body 91, and the outer wall of the lower cylinder of the funnel-shaped fuel storage tank 910 is evenly opened.
  • the outer wall of the furnace body 91 is provided with two air inlets 914 communicating with the annular air duct, and the air inlet 914 is connected with the air duct 915.
  • the hot blast stove trial solves the problems of forward combustion and trans combustion through the combination of positive and negative combustion.
  • the hot blast stove 900 when used, it has the following defects and cannot be continuously used:
  • the hot air furnace has a large amount of air from the lower furnace 95 at the bottom of the lower combustion chamber 93, causing the temperature of the lower furnace 95 to be too high, and some solid biomass fuels (
  • the ash melting point of the straw is relatively low, so that the hot blast stove generates a ashing phenomenon when burning the solid biomass fuel, so that the ash produced by the combustion is in a viscous molten state and is bonded to the furnace 95.
  • the gap of the lower furnace 95 is melted and the ash is not effectively discharged, thereby causing the hot blast stove to be unable to continue working.
  • An object of the present invention is to provide a solid fuel combustion method and a combustion apparatus which can not only fully burn volatile matter in a solid fuel, but also solve the problem of melting, and achieve a natural matching of the burning speed in the combustion process. As the combustion proceeds in an orderly feed, continuous combustion of the fuel is ensured.
  • the present invention provides a method for burning a solid fuel, in which a feed port is provided at the top of the furnace, and a corresponding furnace inlet is provided with a furnace for receiving fuel entering from the feed port.
  • the fuel entering the feed port forms a pile layer on the furnace, the furnace is formed on the side of the pile layer as the inlet side, and the other side opposite to the inlet side is formed as the combustion side; the pile layer will enter
  • the wind side is separated from the combustion side, and the pile layer constitutes a separator separating the inlet side and the combustion side; on the combustion side of the furnace, a combustion chamber connected to the outlet of the exhaust gas is provided, and the volatile matter on the combustion side flows through the path a diversion wall is provided; wherein, during combustion, the stack layer is ignited, and air is introduced from the inlet side of the stack layer, and the wind passes transversely through the stack layer, and exits from the combustion side of the stack layer, and the combustion flame faces The combustion chamber burns, the fuel gradually moves down
  • the deflector wall guides through the combustion flame and enters the combustion chamber to burn
  • the combustion exhaust gas is discharged from the exhaust gas outlet; at the same time, the fixed carbon fuel after the volatile matter is ignited, and the fixed carbon combustion is performed to generate a new combustion flame, and the ash generated after the burnout is discharged through the furnace at the bottom of the pile layer, with the combustion In progress, the new fuel is continuously replenished on the pile layer to form a combustion cycle.
  • the invention also provides a solid fuel combustion device, comprising a furnace, the furnace is provided with an air inlet and a solid fuel feed port for supplying air into the furnace, the feed port is arranged at the top of the furnace, corresponding to the furnace
  • the feed port is provided with a furnace for receiving solid fuel entering from the feed port, and the solid fuel forms a pile layer between the feed port and the furnace, and the furnace above the furnace is formed on one side of the pile layer
  • the inlet side the other side opposite to the inlet side is formed as a combustion side; the pile layer constitutes a partition between the inlet side and the combustion side; and on the combustion side, a discharge to the exhaust outlet is formed
  • the combustion chamber is provided with a flow guiding wall for guiding the volatile gas flow to the lateral combustion flame on the volatile flow path on the combustion side, so that the main air flow generated by the wind entering the furnace is substantially transversely passed through the stack from the inlet side. After the material layer is guided through the diversion wall into the combustion chamber, and finally discharged from
  • the volatile matter is precipitated in the fuel and the fixed carbon combustion is carried out in the stacking layer during the combustion process, the volume of the fuel becomes smaller after the combustion proceeds, and the gravity is reduced. Under the action, it automatically moves downwards and is gradually ignited by the lower combustion flame. The new fuel is automatically replenished from the feed port to the pile layer, and the fixed carbon combustion of the lower layer fuel provides the heat required for the precipitation of the upper layer new fuel volatiles.
  • the replenishing speed of the new fuel depends on the burning speed of the lower layer fuel, thereby naturally achieving the matching of the upper layer volatiles precipitation and the fixed carbon fuel burning speed, and effectively solves the safety hazard problem existing in the existing hot blast stove due to the mismatch of the burning speed.
  • the volatiles precipitated by the upper layer of fuel are vented by the combustion flame and are ignited by the combustion flame by the lateral combustion flame generated by the combustion of the fixed carbon fuel under the guidance of the flow guiding wall.
  • the cavity is burned to achieve full combustion of the volatiles.
  • the combustion apparatus of the present invention can automatically and orderly feed by gravity with the progress of combustion, the combustion furnace can be placed in an unattended operation state, which not only saves labor, but also causes the pile layer to be in a dynamic equilibrium state.
  • the fixed carbon combustion and volatile matter precipitation have been in a continuous and stable combustion state, which effectively ensures the full combustion of the volatiles, improves the combustion efficiency, and realizes the orderly controllable combustion of the combustion furnace.
  • the present invention introduces air from one side of the stack layer, a combustion chamber is provided on the combustion side opposite to the inlet side of the stack layer.
  • a combustion chamber is provided on the combustion side opposite to the inlet side of the stack layer.
  • the fixed carbon fuel is located in the downward position, so that the lower the fixed carbon combustion layer is lower, the lower the temperature, the ash generated by the combustion is also moving down the fixed carbon fuel. In the middle, it is discharged into the lower ash chamber through the bottom furnace under the action of gravity, which effectively solves the problem of the ash existing in the existing combustion furnace and ensures the continuous and stable combustion of the combustion furnace.
  • the stack layer of the present invention constitutes a partition between the inlet side and the combustion side, the wind on the inlet side must pass through the pile layer to enter the combustion side, thereby achieving wind-to-fuel combustion and volatilization on the inlet side. An effective supply of combustion.
  • the stack layer is in contact with the inner wall of the furnace on opposite sides between the inlet side and the combustion side to isolate the inlet side from the combustion side.
  • the side walls of the two opposite side inner walls between the inlet side and the combustion side of the furnace above the furnace are formed on both sides between the inlet side and the combustion side of the stack.
  • the natural stacking slope is uniform or located on the inner side of the natural stacking slope, so that the two side wall faces of the stock layer between the inlet side and the burning side are in contact with the inner wall of the furnace.
  • the two opposite side inner walls of the furnace above the furnace above the inlet side and the combustion side are vertical side walls.
  • the two opposite side inner walls of the furnace above the furnace above the inlet side and the combustion side are inclined side walls.
  • the flow guiding wall is formed by a side wall of the deflector disposed in the furnace, and an air flow passage through which the airflow passes is formed at a lower end or a lower portion of the deflector.
  • the flow guiding wall may be formed by the inner wall of the furnace portion.
  • a heat exchange device is disposed within the combustion chamber, the flow guiding wall being formed by a portion of the side walls of the heat exchange device.
  • the stack layer may be formed on the outside of the side of the combustion side as an open structure that does not limit the side shape of the stack.
  • the stack layer may be formed with a sidewall having an open or apertured structure on the outside of the side of the combustion side.
  • the projected area of the feed port on a horizontal plane may be less than the projected area of the furnace stack region on a horizontal plane.
  • the feed port is positioned such that the stack layer forms a natural stacking slope on the inlet side.
  • the air inlet is higher than the upper surface of the natural stacking slope.
  • the edges of the grate may be connected to the inner wall of the grate.
  • the grate is spaced from the inner wall of the grate at one edge of the combustion chamber.
  • the combustion chamber may have two or more.
  • the combustion chamber can be coupled to a heat exchange device.
  • the combustion chamber is provided with one or more outlets for supplying heat to the heat exchange device.
  • combustion furnace of the present invention the volatile matter can be almost completely burned, the combustion efficiency of the combustion furnace is over 95%, and there is no black smoke emission, and the clean discharge of solid fuel combustion with high volatile content is realized.
  • the combustion furnace of the invention fully utilizes the characteristics of gravity and heat transfer, and can not only meet the requirements of the fuel principle, but also realize The automatic and orderly combustion of the fuel has the advantages of simple structure, low manufacturing cost and convenient use, thereby providing favorable conditions for the popularization and application of the solid fuel with high volatile content.
  • FIG. 1 is a schematic structural view of a conventional positive and negative hot air furnace
  • Figure 2 is a schematic view showing the combustion state of the combustion apparatus of the present invention.
  • Figure 3 is a side cross-sectional structural view showing the air inlet side of the combustion apparatus of the present invention and the side wall of the combustion side furnace being vertical side walls;
  • Figure 4 is a side cross-sectional structural view showing the side wall of the combustion device of the present invention and the side wall of the combustion side of the furnace being inclined side walls;
  • Figure 5 is a side view of the side of the inlet side of the combustion apparatus of the present invention and the side wall of the combustion side of the furnace being curved side walls;
  • Figure 6 is a schematic view showing the structure of the furnace casing of the present invention having a side edge of the furnace chamber spaced from the inner wall of the furnace;
  • Figure 7 is a schematic cross-sectional view taken along line A-A of Figure 6;
  • Figure 8 is a schematic structural view of the cross section taken along line B-B of Figure 6;
  • Figure 9 is a schematic view showing another structure of the cross section taken along line B-B of Figure 6;
  • Figure 10 is a schematic view showing the C-direction structure of the flow guiding wall of Figure 6;
  • Figure 11 is a schematic view showing another structure of the guide wall C
  • Figure 12 is a schematic view showing the structure of the side of the combustion structure of the combustion device of the present invention.
  • Figure 13 is a schematic view showing the structure of the combustion device of the present invention having an open side wall
  • Figure 14 is a schematic view showing the structure of the furnace casing of the present invention in contact with the inner wall of the furnace;
  • Figure 15 is a schematic view showing the structure of the combustion apparatus of the present invention having a tilting furnace
  • Figure 16 is a schematic view showing the structure of a combustion apparatus of the present invention having two combustion chambers;
  • Figure 17 is a schematic view showing the structure of the flow guiding wall formed by the inner wall of the furnace portion
  • Figure 18 is a schematic view showing the structure of the flow guiding wall formed by a part of the side wall of the heat exchange device
  • Figure 19 is a schematic view showing another structure of the flow guiding wall formed by a part of the side wall of the heat exchange device.
  • Combustion device 100 heat exchange device 200; exhaust gas discharge port 201;
  • Furnace 10 inlet side 101; combustion side 102; side wall faces 103, 104;
  • Stack layer 1 two opposite sides 161, 162; natural stacking slope 16; feed port 11; air inlet 12; side wall 13; pore structure 131; opening 132; furnace 14; feed hopper 15;
  • Combustion chamber 3 combustion chamber outlet 31;
  • Solid fuel 5 volatile matter 51; fixed carbon fuel 52 after volatilization; furnace ash 53.
  • the present invention provides a method for burning a solid fuel.
  • a feed port 11 is provided at the top of the furnace 10, and a corresponding feed port 11 is provided in the furnace 10 to receive from the feed port 11.
  • the solid fuel furnace 14, the fuel entering from the feed port 11 forms a pile layer 1 on the furnace 14, and the furnace 10 above the furnace 14 is formed on the side of the pile layer 1 as the inlet side 101,
  • the other side opposite the inlet side 101 is formed as a combustion side 102 which isolates the inlet side 101 from the combustion side 102, from which the stacking layer 1 constitutes the inlet side 101 above the furnace 14.
  • a separator with the combustion side 102; the combustion side 102 is provided with a combustion chamber 3 communicating with the exhaust gas outlet 201, and a flow guiding wall 2 is provided on the volatile flow path of the combustion side 102.
  • the pile layer 1 is ignited, and air is introduced from the inlet side 101 of the pile layer 1, the wind passes transversely through the pile layer 1, and exits from the combustion side 102 of the pile layer 1, the wind is directed toward the combustion flame
  • the combustion chamber 3 is burned, the fuel gradually moves down as the volume becomes smaller, and the new fuel is automatically replenished to the stack layer 1 under the action of gravity, and the volatiles 51 are heated to precipitate, and the volatiles 51 are deposited from the stack layer.
  • the combustion side 102 of 1 passes through and is guided through the combustion flame via the flow guiding wall 2, the volatile matter 51 is ignited by the combustion flame, enters the combustion chamber 3 for combustion, and the combustion exhaust gas is discharged from the exhaust gas outlet 201; at the same time, the fixation after the volatile matter 51 is precipitated
  • the carbon fuel 52 is ignited, carbon combustion is performed, and a new combustion flame is generated.
  • the ash 53 generated after the burnout is discharged through the furnace 14 at the bottom of the pile layer 1, and as the combustion progresses, the new fuel is continuously replenished. On, a combustion cycle is formed.
  • the present invention also provides a solid fuel combustion apparatus 100 using the above combustion method.
  • the combustion apparatus 100 includes a furnace 10 having an air inlet 12 for supplying air into the furnace, and a solid fuel feed port 11 at the top of the furnace 10, corresponding to the furnace 10
  • the feed port 11 is provided with a furnace 14 for receiving the solid fuel 5 entering from the feed port 11, and the solid fuel 5 forms a stack layer 1 between the feed port 11 and the furnace 14, and the furnace above the furnace 14 10 is formed on the one side of the pile layer 1 as the inlet side 101, and the other side opposite the inlet side 101 is formed as the combustion side 102, which separates the inlet side 101 from the combustion side 102.
  • the separator layer 1 constitutes a separator that isolates the inlet side 101 and the combustion side 102.
  • a combustion chamber 3 is formed on the combustion side 102 to be connected to the exhaust gas outlet 201, and a flow path 2 for guiding the volatile gas flow to the lateral combustion flame is provided on the flow path 51 of the combustion side 102 to enter the furnace.
  • the main airflow generated by the wind of 10 is generally transversely passed through the stacking layer 1 by the inlet side 101 and then guided into the combustion chamber 3 via the deflector wall 2 and finally discharged from the exhaust gas outlet.
  • the main air flow generated by the wind entering the furnace 10 of the present invention refers to the main air flow generated by the wind, which flows from the air inlet side 101 of the pile area 1 substantially transversely through the pile area 1 from the combustion side 102; during the combustion process
  • the wind entering the furnace 10 mainly produces airflow transversely through the stacking zone 1, and there is almost no airflow through the bottom furnace 14 of the stacking zone 1 or a weak airflow passes through the bottom furnace 14 as long as the weak
  • the airflow does not affect the main airflow direction, and does not affect the effect of the combustion device of the present invention, that is, the combustion device of the present invention can ensure the main airflow direction during the combustion process. It is within the scope of the invention to enter from the inlet side 101 of the stack layer 1 and to exit from the combustion side 102 substantially transversely through the stack layer 1 to form a lateral combustion mode.
  • the stock layer 1 in the present invention refers to a pile formed of a solid fuel between the feed port 11 and the furnace 14.
  • the newly introduced fuel in the upper layer is first heated to a temperature at which the volatile matter is precipitated to precipitate volatiles, and then ignited for fixed carbon combustion, and gradually decreases as the volume of the fuel becomes smaller as the combustion progresses.
  • the ash 53 generated after the burnout is discharged through the furnace 14; at the same time, the new fuel is automatically replenished to the pile layer 1 under the action of gravity, so that the pile layer 1 between the feed port 11 and the furnace 14 is burning.
  • the process is in a state of dynamic equilibrium, maintaining a stable stock shape.
  • the fuel is released from the volatile matter 51 and the fixed carbon combustion is in the furnace above the furnace 14, during the combustion, the fuel is released after the volatile matter 51 is released.
  • the volume becomes smaller, automatically moves downward under the action of gravity, and is gradually ignited by the lower combustion flame.
  • the new fuel is automatically replenished from the feed port 11 to the pile layer 1 under the action of gravity, and the fixed carbon combustion of the lower layer of fuel is
  • the evaporation of the upper fuel volatiles provides the required heat, and the replenishing speed of the new fuel depends on the burning speed of the lower fuel, thereby naturally achieving the natural matching of the upper volatiles precipitation and the burning speed of the fixed carbon fuel 52, effectively solving the existing hot air furnace.
  • the volatiles 51 which are heated and precipitated by the lower fixed carbon fuel 52 are flowed toward the combustion chamber 3, and the lower fixed carbon fuel 52 is burned to generate a flame which is also directed toward the air.
  • the combustion chamber 3 is burned, and when the volatile matter 51 passes through the combustion flame under the guidance of the flow guiding wall 2, it is ignited by the high temperature generated by the combustion flame, thereby achieving sufficient combustion of the volatile matter.
  • the combustion device can be placed in an unattended operating state, which not only saves manpower, but also because the stack layer 1 is in a state of dynamic equilibrium, the stack layer 1 Maintaining a stable stock shape during the combustion process, so that the fixed carbon combustion and volatile matter precipitation in the furnace 1 are always in a continuous stable combustion state, effectively ensuring full combustion of volatiles, improving combustion efficiency, and achieving combustion. Orderly controlled combustion of the device.
  • the present invention provides a combustion chamber 3 from the combustion side 102 of the side of the stack layer 1 and opposite the inlet side 101, the main gas stream is passed transversely through the stack layer 1 from the combustion side 102, A high temperature flame zone is formed on the combustion side 102 of the stock layer 1 to provide a high temperature environment for ignition of the volatiles to form a lateral combustion mode.
  • a feed hopper 15 may be disposed on the feed port 11 to facilitate feeding to the stacking zone 1.
  • the stock layer 1 of the present invention is formed on the outer side of the side of the combustion side 102 so as to be formed in an open structure in which the side shape of the stock layer 1 is not limited.
  • the combustion flame and volatiles which are blown from the side of the pile layer 1 of the combustion side 102 directly enter the combustion chamber 3 to be burned by the air flow, and the structure is simpler.
  • the stock layer 1 is located on the side of the combustion side 102.
  • a side wall 13 having an opening 132 or a pore structure 131 may be formed on the outer side of the face such that combustion flames and volatiles penetrating from the side of the pile layer 1 of the combustion side 102 enter the combustion chamber 3 through the opening 132 or the pore structure 131 for combustion.
  • the pore structure 131 of the side wall 13 may be a furnace structure, a fence structure, or a grid structure, or a perforated structure, etc., and the specific structure may be not limited as long as it has pores to allow the flame and volatiles to pass.
  • the opening 132 may be higher than the natural stacking slope setting formed on the combustion side to prevent solid fuel from falling directly from the opening 132.
  • the two opposite sides 161, 162 of the stack layer 1 between the inlet side 101 and the combustion side 102 are in contact with the inner wall of the furnace to place the furnace above the furnace 14
  • the space on the inlet side 101 is separated from the combustion side 102 by the stack layer 1.
  • the airflow generated by the wind entering the air inlet side 101 passes through the pile layer 1 to reach the combustion side 102, thereby preventing the wind from passing outside the pile layer 1 and doing useless work, thereby ensuring the effectiveness of the wind passing through the pile layer 1. supply.
  • the side walls 103, 104 of the two opposite side inner walls between the inlet side 101 and the combustion side 102 of the furnace 10 above the furnace 14 and the stack layer 1 on the inlet side 101 The natural stacking slopes 16 that may be formed by the two sides 161, 162 between the combustion sides 102 are coincident or located inside the natural stacking slope 16 such that the two side wall faces 103 of the stack layer 1 between the inlet side 101 and the combustion side 102 , 104 is connected to the inner wall of the furnace, as shown in Figures 3 to 5.
  • the shape of the side wall faces 103, 104 of the opposite side inner walls between the inlet side 101 and the combustion side 102 of the furnace 10 above the grate 14 can be set as needed, as long as the outer side of the natural stacking slope 16 is not exceeded, enabling the stacking
  • the two side wall faces 103, 104 of the layer 1 may be in contact with the furnace side wall faces 103, 104, and the specific shape thereof may not be limited.
  • 3 shows an example in which the two side wall faces 103, 104 of the two opposite side inner walls between the inlet side 101 and the combustion side 102 of the furnace above the furnace 14 are vertical side walls
  • FIG. 4 shows the furnace.
  • the two side wall faces 103, 104 of the two opposite side inner walls between the inlet side 101 and the combustion side 102 of the furnace above the crucible 14 are examples of inclined side walls, and FIG. 5 shows the furnace above the furnace 14 in the inlet air.
  • the two side wall faces 103, 104 of the opposite side inner walls between the side 101 and the combustion side 102 are examples of curved side walls.
  • the shape of the two side wall faces 103, 104 of the two opposite side inner walls between the inlet side 101 and the combustion side 102 of the furnace above the furnace 14 is not limited to the shape shown in the drawing. It can also be set to other various shapes, which will not be enumerated here.
  • the flow guiding wall 2 may be provided in various forms as long as the airflow with the volatile matter 51 can be guided to the position of the lateral combustion flame generated by the combustion of the lower layer fuel.
  • the flow guiding wall 2 may be formed by a side wall of the deflector 22 disposed in the furnace 10.
  • the baffle 22 can be integrally formed by a structure that blocks airflow.
  • an airflow passage 23 is formed at a lower end of the deflector 2, and a volatile gas flow passes through the airflow passage 2 to pass through the combustion.
  • the flame enters the combustion chamber 3 for combustion.
  • the baffle 22 is also configured to block the airflow at the upper portion, and the pore structure is formed at the lower portion, and the airflow enters the combustion chamber 3 through the airflow passage 23 at the lower portion of the deflector 22.
  • the flow guiding wall 2 may be formed by a portion of the inner wall of the furnace.
  • a heat exchange device 200 may be disposed in the combustion chamber 3, and the flow guide wall 2 may be formed by a portion of the side wall of the heat exchange device 200.
  • the projected area of the feed opening 11 in the horizontal plane may be less than the projected area of the bottom stack 14 in the horizontal plane.
  • a pile layer which is large and small can be formed in the pile area 1. This way of stacking can make the air flow of the upper fuel layer
  • the thickness is less than the thickness of the lower layer of the pile.
  • the lower layer of fixed carbon fuel has a larger area, which is beneficial to the full combustion of the fixed carbon fuel, and the thickness of the upper fuel layer is small, which facilitates the rapid passage of the airflow.
  • the volatile matter 51 is brought to the combustion chamber 3 of the combustion side 102 of the pile layer 1 for combustion.
  • the feed port 11 can be positioned such that the stack layer 1 forms a natural stacking slope on the inlet side 101 of the furnace 10.
  • the air inlet 12 may be higher than the upper surface of the natural stacking slope to supply air to the wind side 101 upon combustion.
  • the air inlet 12 may be provided on the side wall of the furnace 10 as shown in FIG. 2, or may be provided on the top of the furnace 10 as shown in FIG.
  • it is not limited to the illustrated manner, as long as it can supply air to the air inlet side 101 of the stacking area 1 and form a main airflow that passes substantially transversely through the stack layer, the specific arrangement position thereof can be omitted.
  • the edges of the furnace 14 can be joined to the inner wall of the furnace 14 to cover the entire area within the furnace.
  • the furnace 14 is spaced from the inner wall of the furnace 10 at one side edge of the combustion chamber 3.
  • the grate 14 may be horizontally disposed within the grate 10; as shown in FIG. 15, the grate 14 may be disposed obliquely within the grate 10.
  • the structure of the furnace 14 is not limited to the above, and the furnace 14 is disposed to form a pile layer 1 between the feed port 11 and the furnace 14 as long as it can receive the solid fuel, thereby avoiding the solid fuel of the pile layer 1. It can be dropped directly, and its specific form can be without limitation.
  • the combustion chamber 3 is connected to the heat exchange device 200 to utilize the heat generated by the combustion chamber 3.
  • the heat exchange device 200 may be a heat exchanger for heating, a crucible, a cooker, a water jacket, or the like.
  • 2 shows an example in which a heat exchanger is arranged in the combustion chamber 3;
  • FIG. 6 shows an example in which the combustion chamber 3 has an outlet 31 for supplying heat to the heat exchange device, on which the pot or other heat exchange device can be placed .
  • the outlet 31 can be provided in plurality, which can be used for anecdote, partly for heating, and partly for anecdote.
  • the combustion chamber 3 may have an outlet 32 for supplying heat to the fire, which is finally discharged through the exhaust outlet 201 after entering the heat exchange.
  • the combustion chamber 3 may be provided with two or more as needed to suit various actual heat exchange requirements.

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Abstract

L'invention concerne un procédé de combustion et un appareil de combustion (100) pour un combustible solide. L'appareil de combustion (100) comprend une chambre de four (10), une couche d'empilement de matériau (1) formée à l'intérieur de la chambre de four (10), un côté entrée d'air (101) formé d'un côté de la couche d'empilement de matériau (1) et un côté combustion (102) formé de l'autre côté à l'opposé du côté entrée d'air (101). La couche d'empilement de matériau (1) sépare le côté entrée d'air (101) du côté combustion (102). Une paroi de déviation (2) est disposée sur un trajet d'écoulement d'un flux d'air comprenant un composant volatil (51) du côté combustion (102).
PCT/CN2015/073618 2014-03-05 2015-03-04 Procédé de combustion et appareil de combustion pour combustible solide WO2015131817A1 (fr)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1643026A (en) * 1921-05-09 1927-09-20 Iron Products Corp Heater
US2695010A (en) * 1950-02-02 1954-11-23 Directie Staatsmijnen Nl Furnace for burning solid fuels
JPS5833004A (ja) * 1981-08-21 1983-02-26 Kobe Steel Ltd 固形燃料用燃焼装置
CN203731384U (zh) * 2014-03-05 2014-07-23 车战斌 固体燃料的燃烧装置
CN203731383U (zh) * 2014-03-05 2014-07-23 车战斌 固体燃料的燃烧装置

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1643026A (en) * 1921-05-09 1927-09-20 Iron Products Corp Heater
US2695010A (en) * 1950-02-02 1954-11-23 Directie Staatsmijnen Nl Furnace for burning solid fuels
JPS5833004A (ja) * 1981-08-21 1983-02-26 Kobe Steel Ltd 固形燃料用燃焼装置
CN203731384U (zh) * 2014-03-05 2014-07-23 车战斌 固体燃料的燃烧装置
CN203731383U (zh) * 2014-03-05 2014-07-23 车战斌 固体燃料的燃烧装置

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