• 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 method for drying bulk material (15), in particular for drying free-flowing wood in the form of sawdust or wood chips, or of fermentation and clarification residues. In this case, the bulk material (15) is guided successively through at least one pre-drying chamber (1) and at least one after-drying chamber (2). An air stream (3) in an after-drying chamber (2) comprises a circulating air (5) guided in the circuit via a heating coil (10), from which a partial air flow (6) is branched off and passed through a heat exchanger (7). After passing through the heat exchanger (7), the partial air flow (6) is completely returned to the circulating air flow (5). An air stream (3) through the at least one pre-drying chamber (1) is formed from a fresh air (8) sucked in via the heat exchanger (7). On the one hand, the fresh air (8) is preheated in the heat exchanger (7) by the partial air flow (6), and on the other hand a reduction of the water content in the partial air flow (6) takes place in the heat exchanger (7).
    公开号:AT515466A1
    申请号:T50142/2014
    申请日:2014-02-26
    公开日:2015-09-15
    发明作者:
    申请人:Mühlböck Kurt；
    IPC主号:
    专利说明:

    The invention relates to a method for drying bulk material, in particular for drying free-flowing wood in the form of sawdust or wood chips or sewage and fermentation residues, in which the bulk material is passed successively through at least one pre-drying chamber and at least one after-drying chamber, and the chambers at least a ventilation device is associated, wherein a stream of air for drying in the at least one after-drying chamber circulated via a heating coil circulating air comprises, from which circulating air diverted a partial air flow and passed through a heat exchanger, and wherein an air stream for drying in at least one pre-drying chamber a fresh air drawn in via this heat exchanger and optionally additionally heated by a heating register is formed.
    From WO 2012/075518 A1, which is based on the applicant, a generic method is known, which provides a drying of wood by means of air, in which a fresh air used for drying the wood in an air / air heat exchanger by a to the immediate Ambient exhaust air can be preheated. However, the measures taken here are only partially satisfactory in terms of the achievable energy efficiency or use of latent heat energy contained in this exhaust air.
    The invention has for its object to provide a method for drying bulk material, which is improved in terms of energy efficiency, and by which method also an increased burden on the ambient air is avoided or contamination of the system periphery is held back as possible.
    This object is achieved in that the diverted from the circulating air to at least one after-drying chamber partial air flow after passing through the heat exchanger and caused by condensation in the heat exchanger reduction in the amount of water contained in this partial air flow, is completely returned to the circulating air flow of at least one after-drying chamber ,
    By this measure, on the one hand achieved that not only a present between the partial air flow and the fresh air temperature difference, due to heat transfer from the partial air flow to fresh air, used for preheating the fresh air or used, but also in the warm partial air flow in the form of water inherently contained heat energy. This water was removed from the bulk material during the passage of the air flow to dry the bulk material. This heat energy is used in the generic method for bulk solids drying to a high proportion to heat or preheat the intake fresh air for a pre-drying and thus to increase the drying efficiency for a pre-drying chamber.
    In a synergetic manner, on the other hand, it is accomplished that a high amount of water is removed from the partial air flow in the heat exchanger, whereby the water absorption capacity of this partial air flow is improved. By returning the thus dewatered partial air flow into the recirculating air flow around a post-drying chamber, therefore, the drying capacity or the water absorption capacity of the drying air flow for a post-drying chamber can be significantly increased. In addition, by the described process management contained in the partial air flow, valuable heating or. Heat energy almost completely obtained in the process and used, so be used for drying the bulk material or wood.
    Another special advantage of the return or re-feeding of the partial air flow in the circulating air flow is the complete avoidance of pollution or pollution of the environment or immediate environment contained in the partial air flow solid, liquid or gaseous bulk or wood components or dust particles. In addition, the occurrence of a so-called steam swath can thereby be reduced or avoided. This advantage is particularly important in the drying of wood bulk material with an increased proportion of relatively small components to fruition. During the passage of the bulk material through a drying chamber, the bulk material is already at least partially dewatered or pre-dried by means of at least one pre-drying chamber, so that the mutual adhesion of the dusts or the components of the bulk material, which is caused by water contained, is already greatly reduced. Thus, the tendency that especially dust-like particles are entrained from the bulk material by the drying air flow, in a post-drying chamber compared to a pre-drying chamber significantly higher. After the drying circulating air flow is closed for the at least one after-drying chamber in itself and from this no exhaust air is discharged into the environment, the pollution load for the environment is very low. Any substances which can be dissolved out of the bulk material during the drying process in a post-drying chamber, thereby emerge from the drying plant predominantly or exclusively with the condensate water to be removed from the heat exchanger. This condensation can be cleaned or clarified in a simple manner, for example by means of a sewage treatment plant, relatively economical.
    In contrast, the probability is relatively low that dust-like wood particles are entrained in the course of a passage through a pre-drying chamber from the drying air stream, after the bulk material in a pre-drying chamber in relation to a final drying chamber is still relatively humid. For this reason, and due to the comparatively low temperature level of an air flow after passing through at least one pre-drying chamber, its discharge to the environment as exhaust air is unproblematic.
    In order to achieve the best possible use of the heat energy contained in the partial air flow, the partial air flow and the fresh air flow with respect to their flow rates and temperatures relative to each other when passing through the heat exchanger can be coordinated such that the largest possible part of the partial air flow surface facing the heat exchanger is cooled down by the fresh air so far that the dew point temperature for the partial air flow is below. This ensures that at least at these sections of the surface of the heat exchanger to a greater extent water is separated from the partial air flow.
    Due to the measures proposed in claims 2 and 3, on the one hand in terms of process engineering appropriate Teilstrommengen be adjusted so that both a sufficient drainage of the partial air flow can be achieved, as well as a sufficient preheating of the fresh air takes place. On the other hand, it is thus possible to ensure a practicable, structurally as simple as possible implementation. In particular, this allows the dimensions and associated costs of the heat exchanger to be used to be kept at a favorable cost-to-benefit ratio.
    The features according to claim 4 bring the advantage that thereby an efficient and reliable operation possibility for demand-oriented raising of the flow velocity of the partial air flow is created. In addition, this can ensure that a sufficient amount of the partial air flow is provided for preheating the fresh air by means of the heat exchanger.
    By the features specified in claim 5, the controllability of the flow velocities of all air streams can be drastically improved. Furthermore, this can be reacted quickly to parameter changes of the bulk material or wood to be dried or the drying air streams. In addition, it can be achieved that the respective drying climate can be adapted in a drying chamber with increased precision and reaction rate to desired or desired states.
    The procedure set forth in claim 6 provides a practical means of compensating for differences in the quality of the bulk material to be dried.
    Variations in the initial moisture in the bulk material to be delivered or to be dried can also be easily compensated by the measures according to claim 7.
    The measures specified in claim 8 represent a particularly energy-efficient or successful embodiment variant with regard to energy efficiency. The process described allows the bulk material to be dried to be dried stepwise or zone-wise to ever lower residual moisture. In particular, this ensures that each drying chamber can be charged with the specific, respectively optimized amount of air and / or air temperature. In addition, in the first pre-drying steps of the method, air streams with a relatively low temperature can be used, which makes further preheating by means of a heating register superfluous as a rule. Since the bulk material reaches a relatively low moisture content only in the last post-drying chambers, and no exhaust air is discharged from the after-drying chamber to the ambient air, it can also be advantageously prevented that the environment is polluted by wood dust or the like.
    In order to achieve the best possible flow through the bulk material with drying air, the measure specified in claim 9 is suitable. In particular, this avoids that a drying air stream flowing through a drying chamber merely flows around the bulk material located on the conveyor belt, and thus actually only the surface regions of the bulk material facing the air stream are dried sufficiently. In contrast, it is achieved by the claimed measures that as many subregions of the bulk material applied to the conveyor belt come into contact with the drying air, so that the achievable efficiency of the drying of the bulk material is drastically increased by means of an air flow. Furthermore, it is obstructed so that a large amount of the drying air passed through a drying chamber is not actively used for the drying process. This means that the amount of unused energy is reduced, and thus the drying process for bulk material or wood can be further increased in terms of energy efficiency. Finally, it is also achieved that the bulk material can pass through the entire drying process relatively quickly, so that shorter throughput times or higher throughputs can be achieved.
    The measures according to the wording of claim 10 provide the best possible utilization of the entire width of a drying chamber, since a stream of air flowing through a drying chamber in the vertical direction - related to the bearing surface of the conveyor belt - comes into contact with the bulk material to be dried at as many points as possible , Once again, this makes it possible to increase the percentage of subsets of the air stream passed through a drying chamber that are actively involved in the drying process.
    A method according to the features of claim 11 is another way to improve the efficiency of the bulk solids drying, as it can be responded to both fluctuations in the initial moisture content of the bulk material, as well as fluctuations in the drying energy provided.
    The measures specified in claim 12 ensure adequate drying for different types of wood bulk material. In particular, for a smaller piece or grain size of the bulk material, such as sawdust, the bulk material height can be reduced, and for a larger piece or grain size, for example for wood chips or the like, the bulk material height can be raised.
    The process step described in claim 13 minimizes the risk of a reduction in energy efficiency after a long-term operation, since it can be avoided that, for example introduced impurities gradually affect the course of the drying process negative. Such a method step is particularly advantageous when using an air-permeable conveyor belt, since the risk that air-permeable sections or through-flow openings of the conveyor belt are clogged or reduced, can be greatly reduced.
    Especially with prolonged operation and the measure according to claim 14 is appropriate. As a result, wood residues or soiling can be removed from the conveyor belt, whereby an improved Trocknungseffi efficiency and a long-term consistent drying quality or drying reliability can be achieved.
    Finally, the measure according to claim 15 are expedient, since thereby the formation of windrows is kept behind due to the low outlet temperature. As a result, optical impairments or impairments of adjacent road sections, in particular with regard to ice formation, can be avoided.
    For a better understanding of the invention, this will be explained in more detail with reference to the following figures.
    In each case, in a highly simplified, schematic representation:
    Fig. 1 is a block diagram of an embodiment of the inventive method for drying bulk material, in particular of wood bulk material;
    2 shows a schematic longitudinal section through a heat exchanger for heat recovery or dewatering of air streams.
    Fig. 3 sections of a device for drying bulk material in a schematic longitudinal section.
    By way of introduction, it should be noted that in the differently described embodiments, the same parts are provided with the same reference numerals or the same component names, wherein the disclosures contained in the entire description can be mutatis mutandis to the same parts with the same reference numerals or component names. Also, the location information chosen in the description, such as top, bottom, side, etc. related to the immediately described and illustrated figure and these position information in a change in position mutatis mutandis to transfer to the new location.
    In Fig. 1, a method for drying bulk material, in particular of wood in bulk form, shown schematically as a block diagram. The bulk material to be dried is first passed through at least one pre-drying chamber 1, and subsequently through at least one after-drying chamber 2. Of course, a plurality of pre-drying or after-drying chambers 1, 2 can also be arranged directly one after the other depending on the requirements and the size of the installation or the desired drying capacity and drying capacity. In principle, this opens up the possibility in each of these drying chambers 1, 2 of setting a drying climate, which is favorable for the process sequence, essentially independently of one another.
    The actual drying process for the bulk material in each chamber 1, 2 takes place by means of an air flow 3, which is passed through the respective drying chamber 1, 2. For this purpose, the drying chambers 1.2 are associated with ventilation devices 4, which, inter alia, pass the respective air stream 3 through the corresponding chamber 1, 2. In the exemplary embodiment shown in FIG. 1, each of the drying chambers 1, 2 has a corresponding ventilation device 4, wherein it would also be conceivable to associate a common ventilation device 4 with a plurality of drying chambers 1, 2. To improve a targeted or controlled adjustment of the respective climate in the drying chambers 1,2, it is advantageous, however, to associate each drying chamber 1, 2 with at least one separate ventilation device 4.
    An air flow 3 through an after-drying chamber 2 is in this case partially formed from a circulating air 5 guided via the ventilation device 4 in an air duct around the respective chamber 2. A partial flow of this guided around the after-drying chamber 2 circulating air 5 is diverted as a partial air stream 6 and fed to a heat exchanger 7. In addition, as is clear from Fig. 1, fresh air 8 is sucked through the heat exchanger 7, wherein the partial air flow 6 and the fresh air stream 8 are separated from each other by the heat exchanger 7. On the one hand, this allows the use of the heat energy contained in the partial air flow 6, on the other hand, a dehydration or a reduction of the water content of the partial air flow 6 takes place in the heat exchanger 7.
    The heat exchanger 7 is preferably formed by a so-called cross-flow heat exchanger 9, in which the partial air flow 6 and the fresh air flow 8 at the respective inlet sides 11, 12 enter the heat exchanger 7, and are guided at least predominantly at a right angle to each other through the heat exchanger, such as this is apparent from Fig. 2. In Fig. 2 is a schematic longitudinal section through such a heat exchanger 7 is shown, wherein the same reference numerals as in the preceding Fig. 1 are used for the same parts. In order to avoid unnecessary repetition, reference is made to the description in the preceding FIG. It should be noted at this point that the structural design of a heat exchanger 7 shown in FIG. 2 represents only one embodiment variant of the same. Alternatively, of course, other embodiments of the heat exchanger 7 deviating more or less from the embodiment shown in FIG. 2 are applicable.
    As shown in FIG. 1, the fresh air 8 preheated by energy transfer from the partial air stream 6 to the fresh air stream 8 in the heat exchanger 7 is used for predrying the bulk material 15 in a predrying chamber 1.
    The air flow 3 through an after-drying chamber 2 consists of the guided around the chamber 2 circulating air 5 and the diverted from the circulating air 5, and then guided through the heat exchanger 7 partial air flow 6, which partial air flow 6 after passing through the heat exchanger or after the moisture reduction in Heat exchanger 7 is thus supplied to the circulating air flow 5 in its entirety again. Before entering a post-drying chamber 2, it is necessary to heat this air stream 3. Therefore, the air flow 3 is guided before entering a post-drying chamber 2 via a heating coil 10, which can be fed with thermal energy.
    The air flow 3 through a pre-drying chamber 1, as shown in Fig. 1, formed by fresh air 8, which is sucked in via the ventilation device 4 and thereby passed through the at least one chamber. Before flowing through the pre-drying chamber 1, the fresh air 8 is passed through the heat exchanger 7 and thereby heated by means of the partial air flow 6. Depending on the availability of unused waste heat from peripheral installations, for example production plants, and / or to achieve a lower return temperature from the heating register 10 of the at least one after-drying chamber 2, the heating register 10 can also be used in front of the at least one pre-drying chamber 1. As a result, the drying capacity of the at least one pre-drying chamber 1 can be increased. Therefore, in the embodiment shown in Fig. 1 for the pre-drying chambers 1 also heating register 10 - shown in dashed lines - provided, which are arranged with respect to the flow direction of the fresh air 8 to the heat exchanger 7 and the pre-drying chamber 1. However, it is under favorable process conditions, and due to the use of the heat and condensation energy contained in the partial flow 6, usually not necessary to heat the fresh air 8 for a pre-drying chamber 1 by means of a heating register 10, or may possibly completely on such heating register 10 be waived.
    As a source of energy for heating the heater 10 is basically any known energy source in question. It is particularly advantageous if a waste heat arising in the course of an externally running process, for example a power generation process, can be used for this purpose.
    By the method of the invention, a particularly energy-efficient process is achieved, in which for heating the fresh air 8 in the heat exchanger 7 - in addition to the temperature difference between fresh air stream 8 and partial air flow 6 - the inherent contained in the partial air flow 6 condensation energy is used, so in the heat exchanger 7 as large as possible Amount of water is separated from the partial air flow 6 before the partial air flow 6 is returned to the recirculating air stream 5 again. Advantageously, this also reduces the absolute humidity of the partial air flow 6 at the same time before the partial air flow 6 is again supplied to the circulating air flow 5 in its entirety. The separated within the heat exchanger 7 from the partial air flow 6 condensate can be derived in a known manner from the heat exchanger 7.
    At least the flow velocities of the two air streams 6, 8 are matched to one another by the heat exchanger 7 such that at least partial sections of a surface 13 of the heat exchanger 7 facing the partial air flow 6, see FIG. 2, have a temperature which is below the dew point temperature of the partial air flow 6 lies.
    It may be useful to divert at least 10% of the circulating air 5 to a secondary drying chamber 2 as a partial air flow 6, and pass through the heat exchanger 7. After the partial dehydration in the heat exchanger 7, the partial air flow 6 is supplied to the circulating air stream 5 completely again.
    Preferably, based on the one after-drying chamber 2 total leaving air quantity - between 10% and 90% of the circulating air 5 is diverted as a partial air stream 6.
    Furthermore, it may be useful, for example, that the fresh air amount supplied to the heat exchanger 7 is selected such that it corresponds to at least twice the amount of the partial air flow 6 fed to the heat exchanger 7.
    Preferably, the amount of fresh air supplied to the heat exchanger 7 is selected or set such that it corresponds to 2 times to 20 times the amount of the partial air flow 6 fed to the heat exchanger 7.
    The flow velocities, and thus the respective amounts of air, which are passed through the heat exchanger 7 in a certain time interval, can be selected in a conventional manner depending on pipe cross sections, pipe lengths, etc. mainly by the air conveying performance of the ventilation devices 4 be set.
    It may be expedient if, for adjusting the flow rate of the guided through the heat exchanger 7 partial air flow 6 in addition to the ventilation devices 4 of the drying chambers 1.2, at least one additional exhaust fan 14 is provided.
    The efficiency of the process management with regard to the best possible use of latent heat energy contained in the partial air flow 6 can be further increased if the ventilation devices 4, 14 to control the temperature conditions and flow rates between the fresh air stream 8 and the partial air flow 6 are speed controlled by the heat exchanger 7. This ensures that the air delivery rates of the existing ventilation devices 4, 14, and thus in particular the flow rates of the air streams in the entire system, for example, depending on measured at different points temperature values can be set so that the best possible use of in the partial air flow 6 inherently contained heat energy is possible.
    FIG. 3 shows a further embodiment of the method for bulk material drying, which is possibly independent of itself, wherein the same reference numerals or component designations are again used for the same parts as in the preceding figures. To avoid unnecessary repetition, reference is made to the detailed description in the preceding figures.
    In Fig. 3 is a partial longitudinal sectional view of a device for bulk material or wood drying shown. In the exemplary embodiment shown, the bulk material 15 to be dried is first conveyed by means of a conveyor belt 16 of a belt conveyor 17 through at least one pre-drying chamber 1 and subsequently through at least one after-drying chamber 2. As can be seen from FIG. 3, the conveyor belt 16 forms an at least approximately horizontal conveying plane for the bulk material 15.
    The dosage of the applied to the conveyor belt 16 amount of bulk material 15 per unit time can be done in different ways. For example, a supply of the bulk material 15 by controlled irrigation of the activated conveyor belt 16 with bulk material 15 via a funnel-shaped feeding device 18 is conceivable, as indicated in Fig. 3. Alternatively or in combination, an active application of the bulk material 15 via a motor-driven application device, for example in the form of a screw or twin screw is possible.
    It may be useful to perform such application devices volume controlled, since regardless of the form and nature of the bulk material 15 contained in the bulk material to be dried 15 amount of water based on a unit mass or a unit weight of the bulk material 15 may vary. By means of this procedural measure, as can be seen from the embodiment shown in FIG. 3, depending on the initial water content of the bulk material 15 and / or depending on the available, external quantity of thermal energy, the bulk material height 19 on the conveyor belt 16 can be increased or decreased.
    Furthermore, it is expedient to adjust the bulk material height 19 to the type of bulk material 15 to be dried. In particular, the piece or grain size of the bulk material 15 is crucial for this. For a smaller piece or grain size of the bulk material 15, such as sawdust, the bulk material height 19 can be reduced expediently, and for a larger piece or grain size, for example Flackschnitzel or the like, the bulk material height 19 can be raised.
    In order to at least largely compensate for variations in the moisture content of the bulk material 15 in the continuous process, it may also be expedient to increase or decrease the conveying speed of the bulk material 15 or the transport speed of the conveyor belt 16 as a function of the initial water content of the bulk material 15.
    Alternatively or in combination with this, again depending on the initial water content of the bulk material 15, the flow velocities of the partial air stream 6 or the fresh air stream 8 separated from the circulating air 5 can be increased or decreased in order, for example, to achieve higher drying rates per unit time.
    In order generally to achieve higher drying rates per unit time in the drying chambers 1, 2, especially for wood in bulk form, it is expedient to guide the air flow 3 guided through the respective chamber 1, at least for the most part, through the conveyor belt 16. For this purpose, the conveyor belt 16 shown in Fig. 4 16, for example, sieve-like, fine mesh or other measures at least partially air permeable. As a result, for each
    Air flow in the drying chamber 1.2 predefined and specifically prepared airways directly through the conveyor belt 16 and therefore also by the bulk material 15 available. In this context, it is further expedient if the width of the conveyor belt approximately corresponds to the width of a drying chamber 1, 2, since the drying air 3 is thereby forced, as it were, to flow through the conveyor belt, and thus of the bulk material 15.
    In the embodiment shown in Fig. 3, both the fresh air stream 8 for a pre-drying chamber 1 and the circulating air 5 and the partial air stream 6 are sucked for an after-drying chamber 2 each of ventilation devices 4 and as drying air streams 3 through the respective chamber 1.2 and through the Conveyor belt 16 and 15 bulk material out. The respective pipes or air ducts for the exhaust air 25, which is discharged after passing through a pre-drying chamber 1 to the ambient air - see Fig. 1 - and for the circulating air 5 to a drying chamber 2 are located on the side facing away from the viewer side of FIG. 3 shown apparatus for bulk solids drying, and are not shown in Fig. 3. The discharged to the environment exhaust 25 comes exclusively from at least one pre-drying chamber 1, is highly saturated, and has a temperature of less than 25 ° C.
    In particular, to increase the drying performance or increase the drying quality, it may also be useful to provide a distribution device 20, with which the bulk material 15 is distributed over the entire width of the conveyor belt 16 as evenly as possible. Such a distribution device 20 can be realized for example by a limited pivoting distribution screw.
    Depending on the nature of the bulk material 15 to be dried, in particular as a function of its degree of soiling or as a function of the fines contained therein, at least one belt blow-off device 21 can be provided. Thus, the surface 22 of the conveyor belt 16 after passing through a discharge or discharge device 23 for the dried bulk material 15 of any adhering to the conveyor belt 16, solid or liquid residues of the bulk material 15 can be freed. For this purpose, one or more nozzles, possibly arranged at different angles to the surfaces 22 of the conveyor belt 16, through which nozzles, for example compressed air is blown by means of a compressor in the direction of the surfaces 22 of the conveyor belt 16.
    Furthermore, it may be helpful and / or necessary to clean or wash the surfaces 22 of the conveyor belt 16 after passing through the discharge or discharge device 23 for the dried bulk material 15 by means of a washing device 24. In this case, water is sprayed or sprayed against a surface 22 of the conveyor belt 16 under pressure.
    The Bandabblasungsvorrichtung 21 and / or washing device 24 shown in Fig. 3 is particularly useful when using the described air-permeable conveyor belt 16, since there is an increased probability that adhering to the conveyor belt 16 bulk or dirt residues affect the air permeability of the conveyor belt 16 gradually negative. When an air-permeable conveyor belt 16 is used, both at least one belt-blowing device 21 and at least one washing device 24 can be arranged, which can be directed to both surfaces 22 of the conveyor belt 16, as can be seen in FIG.
    The embodiments show possible embodiments of the method for drying bulk material 15 and the apparatus for bulk solids drying, it being noted at this point that the invention is not limited to the specifically illustrated embodiments thereof, but rather various combinations of the individual embodiments are possible with each other and this possibility of variation is due to the teaching of technical action by objective invention in the skill of those skilled in this technical field.
    Furthermore, individual features or combinations of features from the different exemplary embodiments shown and described can also represent independent, inventive or inventive solutions.
    The task underlying the independent inventive solutions can be taken from the description. All statements of value ranges in the present description should be understood to include any and all sub-ranges thereof, e.g. is the statement 1 to 10 to be understood that all sub-areas, starting from the lower limit 1 and the upper limit 10 are included, ie. all sub-areas begin with a lower limit of 1 or greater and end at an upper limit of 10 or less, e.g. 1 to 1.7, or 3.2 to 8.1, or 5.5 to 10.
    Above all, the individual embodiments shown in FIGS. 1 to 3 can form the subject of independent solutions according to the invention. The relevant objects and solutions according to the invention can be found in the detailed descriptions of these figures.
    For the sake of order, it should finally be pointed out that, for a better understanding of the drying process, this or the components required for carrying out the process have been shown partially unevenly and / or enlarged and / or reduced in size.
    LIST OF REFERENCES 1 pre-drying chamber 2 after-drying chamber 3 air flow 4 ventilation device 5 circulating air 6 partial air flow 7 heat exchanger 8 fresh air 9 cross flow heat exchanger 10 heating register 11 inlet side 12 inlet side 13 surface 14 exhaust fan 15 bulk material 16 conveyor belt 17 belt conveyor 18 feed device 19 bulk material height 20 distribution device 21 belt blow-off device 22 surface 23 discharge device 24 washing device 25 exhaust
    权利要求:
    Claims (15)
    [1]
    1. A method for drying bulk material (15), in particular for Trock- tion of free-flowing wood in the form of sawdust or wood chips or fermentation and Klärrückständen, in which the bulk material (15) successively by at least one pre-drying chamber (1) and at least one after-drying chamber (2) is guided, and at least one ventilation device (4) is assigned to the chambers (1, 2), an air stream (3) for drying bulk material in the at least one after-drying chamber (2) being circulated via a heating register (10 ) circulated air (5), from which circulating air (5) a partial air flow (6) is branched off and passed through a heat exchanger (7), and wherein an air stream (3) for drying bulk material in the at least one pre-drying chamber (1) from a via this heat exchanger (7) sucked and optionally via a heating coil (10) additionally heated fresh air (8) is formed, characterized in that the branched Tei lluftstrom (6) after passing through the heat exchanger (7) and caused by condensation in the heat exchanger (7) reduction in this partial air flow (6) amount of water, completely back into the circulating air stream (5) of at least one after-drying chamber (2) is returned.
    [2]
    2. The method according to claim 1, characterized in that at least 20% of the circulating air (5) of the at least one after-drying chamber (2) diverted as a partial air flow (6), and returned after passage through the heat exchanger (7) back into the recirculating air stream (5) becomes.
    [3]
    3. The method according to claim 2, characterized in that from the circulating air stream (5) branched off amount of partial air (6) based on the at least one after-drying chamber (2) total exiting air quantity is selected from a range between 20% and 60% ,
    [4]
    4. The method according to any one of the preceding claims, characterized in that at least one additional exhaust fan (14) is provided for adjusting the amount of air or the flow rate of the circulating air stream (5) and branched through the heat exchanger (7) partial air flow (6) ,
    [5]
    5. The method according to any one of the preceding claims, characterized in that the ventilation devices (4, 14) for influencing the temperature conditions and flow rates or air flow ratios between the fresh air stream (8) and the partial air flow (6) are speed controlled by the heat exchanger (7).
    [6]
    6. The method according to any one of the preceding claims, characterized in that depending on the initial water content of the bulk material (15), the conveying speed of the bulk material (15) is increased or decreased.
    [7]
    7. The method according to any one of the preceding claims, characterized in that, depending on the initial water content of the bulk material (15), the flow velocities of the recirculated air (5) separated partial air flow (6) and the fresh air flow (8) are increased or decreased.
    [8]
    8. The method according to any one of the preceding claims, characterized in that the bulk material (15) by means of a conveyor belt (16) of a belt conveyor (17) first by at least one pre-drying chamber (1) and subsequently by at least one after-drying chamber (2) is promoted.
    [9]
    9. The method according to claim 8, characterized in that the conveyor belt (16) is designed to be permeable to air, so that through the respective chamber (1,2) guided air flow (3) at least largely by the conveyor belt (16) or the bulk material (15). is directed.
    [10]
    10. The method according to claim 8 or 9, characterized in that a distribution device (20) is provided, with which the bulk material (15) over the entire width of the conveyor belt (16) is distributed as evenly as possible.
    [11]
    11. The method according to any one of claims 8 to 10, characterized in that depending on the initial water content of the bulk material (15) and / or depending on the available external heat energy quantity, the bulk material height (19) on the conveyor belt (16) increases or decreases becomes.
    [12]
    12. The method according to any one of claims 8 to 11, characterized in that, depending on the nature of the bulk material to be dried (15), in particular depending on the average grain size, the bulk material height (19) is increased or decreased.
    [13]
    13. The method according to any one of claims 8 to 12, characterized in that the surface (22) of the conveyor belt (16) after passing through a discharge or discharge device (23) for the dried bulk material (15) by means of at least one Bandabblasungsvorrichtung (21). is freed from adhering to the conveyor belt (16), solid or liquid residues of the bulk material (15).
    [14]
    14. The method according to any one of claims 8 to 13, characterized in that the surface (22) of the conveyor belt (16) after passing through a discharge or discharge device (23) for the dried bulk material (15) by means of a washing device (24) becomes.
    [15]
    15. The method according to any one of the preceding claims, characterized in that the exhaust air (25) discharged to the environment comes exclusively from at least one pre-drying chamber (1) is highly saturated and thereby has a temperature of less than 25 ° C.
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    同族专利:
    公开号 | 公开日
    EP3111148B1|2018-03-28|
    LT3111148T|2018-07-25|
    ES2671605T3|2018-06-07|
    EP3111148A1|2017-01-04|
    WO2015127490A1|2015-09-03|
    AT515466B1|2016-05-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE2941037A1|1978-10-13|1980-04-30|Svenska Traeforskningsinst|WARM AIR DRYING PROCESS|
    DE68924974T2|1988-09-27|1996-05-02|Valmet Paper Machinery Inc|METHOD FOR DRYING WOOD.|
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    AT510007A4|2010-12-07|2012-01-15|Muehlboeck Kurt|PROCESS FOR WOOD DRYING|DE102017108697A1|2017-04-24|2018-10-25|Stela Laxhuber Gmbh|Continuous dryer with an exhaust air return device|
    DE102016014643B4|2016-12-11|2021-05-27|Stela Laxhuber Gmbh|Continuous dryer for drying goods using warm air with at least two sections|DE506267C|1927-02-09|1930-09-01|Werner Brunnschweiler|Channel stage dryer|
    US2722752A|1953-05-04|1955-11-08|Morch Arne Soren|Drying plants for wooden sheet material|
    DE4234683A1|1992-10-14|1994-04-21|Brunner Reinhard|Device for drying wood or other solids|
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    AT510487B1|2010-10-07|2012-09-15|Mci Man Ct Innsbruck Internationale Hochschule Gmbh|DRYING PROCESS AND DRYING SYSTEM|
    EP2587203B1|2011-10-26|2015-09-23|Stela Laxhuber GmbH|Belt dryer|DE102015012848A1|2015-10-06|2017-04-06|Eisenmann Se|Device for controlling the temperature of objects and method for controlling a device for controlling the temperature of objects|
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    DE102017108699A1|2017-04-24|2018-10-25|Stela Laxhuber Gmbh|Continuous dryer with a heat exchanger|
    DE102017108695A1|2017-04-24|2018-10-25|Stela Laxhuber Gmbh|Continuous dryer with a first and a second section|
    AT520600B1|2017-10-19|2021-07-15|Muehlboeck Holztrocknungsanlagen Gmbh|Device and method for drying bulk material|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50142/2014A|AT515466B1|2014-02-26|2014-02-26|Process for drying bulk material|ATA50142/2014A| AT515466B1|2014-02-26|2014-02-26|Process for drying bulk material|
    ES15715125.9T| ES2671605T3|2014-02-26|2015-02-26|Procedure for drying bulk materials|
    PCT/AT2015/050053| WO2015127490A1|2014-02-26|2015-02-26|Method for drying bulk material|
    EP15715125.9A| EP3111148B1|2014-02-26|2015-02-26|Method for drying bulk material|
    LTEP15715125.9T| LT3111148T|2014-02-26|2015-02-26|Method for drying bulk material|
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