CN203586721U - Biomass wood chip drying system - Google Patents
Biomass wood chip drying system Download PDFInfo
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- CN203586721U CN203586721U CN201320775526.8U CN201320775526U CN203586721U CN 203586721 U CN203586721 U CN 203586721U CN 201320775526 U CN201320775526 U CN 201320775526U CN 203586721 U CN203586721 U CN 203586721U
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Abstract
The utility model discloses a biomass wood chip drying system, which comprises a hot air drying device, a feeding device, an airflow distributor, a rotational-jet flow drier, a collecting device and a tail gas filtering device, wherein the feeding device is connected to the lower part of the rotational-jet flow drier, the hot air drying device is connected with the airflow distributor through a pipeline, the airflow distributor is respectively connected with the bottom and the upper part of the rotational-jet flow drier through pipelines, the top of the rotational-jet flow drier is sequentially connected with the collecting device and the tail gas filtering device through pipelines. The biomass wood chip drying system is adopted for heating and drying biomass wood chips, the time and the labor can be saved, the biomass wood chip drying system can be used for drying different kinds of biomass wood chip particles, and the drying efficiency is improved. When the biomass wood chip drying system is adopted, the pollution caused by emissions to the air can also be reduced, the environment is protected, and the energy is saved.
Description
Technical field
The utility model relates to a kind of drying system, relates in particular to a kind of living beings wood chip drying system, belongs to materials processing technology field.
Background technology
Living beings wood pellet is a kind of regenerative resource of clean environmental protection, and dry technology is as one of important process flow process in its production process, can directly affect performance, quality, form and the energy consumption of converted products.Drying equipment will satisfied basic demand be to guarantee reach the quality index (as moisture content, structural behaviour, physics and chemistry character, nutritional labeling etc.) of desired dried material and guarantee best energy consumption index.By the drying equipment of present biological particles production base is on a large scale studied, discovery secondary cycle is dry, can save a large amount of room and times, can reduce the process of drying process, increase the time of material in hothouse, improved dry efficiency.For a long time, secondary cycle drying equipment for dried biomass wood pellet exists variety of issue in actual production process, its manpower consuming is large, the time is more of a specified duration, and drying efficiency is low, and with same fabric dryer, completes for dry being difficult to of different living beings wood pellets.
Notification number is CN 2369186 Y, publication date is the Chinese utility model patent on March 15th, 2000, a kind of Saw-dust drier is disclosed, comprise hot-blast stove, separator, air-introduced machine, wind sheltering machine, hot-blast stove connects primary separator by the pipeline that is provided with feed opening, through piping, connect the import of air-introduced machine, the outlet of air-introduced machine connects second-stage separator again, and second-stage separator communicates with wind sheltering device by pipeline.
Notification number is CN 102788488 A, publication date is the Chinese invention patent on November 21st, 2012, a kind of high speed centrifugation drying means is disclosed, comprise the following steps: a heated air drying device is set, a material to be dried conveying device and a tail gas filter, the work of heated air drying device, by air filtration, form high velocity air, and by duct injection, arrive in this drying tower after heating, form High Rotation Speed thermal current; The work of material to be dried conveying device, material to be dried is delivered to the centrifugal atomizer of being located at drier top after filtering, thereby forms toward the interior vaporific drop spraying of this hothouse; The dry finished product that forms after vaporific drop contacts with High Rotation Speed thermal current, finished product is through the outlet output of this drying tower bottom, enter the tail gas of tail gas filter successively by the separation of several cyclone separators, the finished product being mingled in tail gas is exported by the outlet of cyclone separator bottom, tail gas is discharged in air after further dust removal by filtration, completes high speed centrifugation dry run.This invention also discloses a kind of drying system corresponding with the method.
In above-mentioned patent documentation, all openly how to solve the technical scheme of above technical problem.
Utility model content
The utility model, for above technical problem, provides a kind of living beings wood chip drying system, and its energy in actual production process is time saving and energy saving and drying efficiency is high, can be used for dry different living beings wood pellets, environmental protection and energy saving.
For solving above technical problem, the technical scheme that the utility model is taked is: a kind of living beings wood chip drying system, comprise for generation of the dry heated air drying device with thermal current of wood chip, for delivery of the feed arrangement of processed wood chip, for controlling the air-flow distributor for primary drying hot blast and redrying hot blast distribution ratio, carry out the revolve-jetting type drier of dried wood chips operation, for collecting the gathering-device of qualified finished product and the tail gas filter for tail gas filtering dedusting, the bottom of revolve described in wherein said feed arrangement is connected to-jetting type drier, described heated air drying device is connected with described air-flow distributor by pipeline, described air-flow distributor is connected respectively with top with the bottom of described revolving-jetting type drier by pipeline, the top of described revolving-jetting type drier connects described gathering-device and described tail gas filter successively by pipeline.
Preferably, described revolving-jetting type drier comprises main unit for dryer, for delivery of warm-air pipe and the second heat airduct of hot blast, for screening the clasfficiator of wood pellet, collecting pipe and nozzle, described main unit for dryer comprises drier enclosure and for the Venturi tube of dried wood chips for the first time, described Venturi tube is arranged on described drier enclosure inside, between them, form annular space, the bottom of described drier enclosure has the charging aperture for charging, described nozzle is arranged on described main unit for dryer bottom, a described warm-air pipe is connected with described nozzle, the hot-air flow that the hot blast of coming in from warm-air pipe forms high velocity, low pressure after the nozzle ejection wood chip that will wet is sent to Venturi tube through charge door, described clasfficiator is arranged on the top of main unit for dryer, described collecting pipe is connected with clasfficiator, described second heat airduct is through described drier enclosure, one end is connected with pipeline in the outside of described drier enclosure, one end is in the inner annular space of described Venturi tube and the formation of described drier enclosure in addition.
Preferably, according to different processed wood chips, the lower end spacing of the jet hole of described nozzle and the reducing pipe of Venturi tube can be adjusted.
Preferably, described clasfficiator can be changed, the degree of drying of itself and described air-flow distributor co-controlling discharging wood chip, thus control different wood chips at dry later moisture content.
Preferably, described air-flow distributor comprises casing and is arranged on the case lid on described casing, described casing comprise into, the port of export and hot blast ratio regulate section, described enter, the port of export is distributed in described hot blast ratio and regulates section both sides, also comprise point fan blade bobbin being rotationally connected with described casing, described point of fan blade bobbin one end inserted in described casing and the other end passes the case lid on described casing, point air blade being fixedly connected with point fan blade bobbin being arranged in casing, it is two regions that described point of air blade regulates section by described hot blast ratio, thereby drive point air blade to rotate the air quantity ratio of adjusting two regions that are divided into by described point of air blade by described point of fan blade bobbin, to control and to adjust the hot blast ratio of the port of export.
Preferably, the cross section of described air-flow distributor is Y type, its vertical section is rectangle, one end of described air-flow distributor is entrance point, another divergent ends relative with entrance point is two ports of export, and the described point of longitudinal rotation of fan blade bobbin is arranged near the casing two port of export joints and described case lid is passed in its one end.
Preferably, described feed arrangement comprises two variable-pitch auger conveyers, for reinforced feeder and Blowing stopper, described Blowing stopper is arranged between two variable-pitch auger conveyers, feeder is connected with one of them variable-pitch auger conveyer, another one variable-pitch auger conveyer with described in the bottom of revolve-jetting type drier be connected.
Preferably, described variable-pitch auger conveyer adopts variable-pitch auger feeding structure, the pitch of feed end is little, discharge end pitch is large, conveyor screw can not be stopped up, described variable-pitch auger conveyer adopts variable-frequency motor speed governing, can control charging rate, adapts to different particle diameters and the wood chip of fibre length; The rotor of described Blowing stopper is provided with ring cutting blade, the wood fiber of Blowing stopper import can be cut off, and guarantees that charging is smooth.
Preferably, described gathering-device comprises the cyclone separator being connected with the collecting pipe of described revolving-jetting type drier and the Blowing stopper that is arranged on described cyclone separator bottom; Described tail gas filter comprises the cloth envelop collector being connected with described cyclone separator pipeline, is arranged on the Blowing stopper and the air-introduced machine being connected with described cloth envelop collector pipeline of described cloth envelop collector bottom.
The beneficial effects of the utility model are: adopt the utility model to carry out heat drying to living beings wood chip, can be time saving and energy saving and can be used for dry different types of living beings wood pellet, and improved drying efficiency; Adopt the utility model can also reduce the pollution of emission to air, environmental protection and energy saving.
Accompanying drawing explanation
Fig. 1 is the structural principle schematic diagram of living beings wood chip drying system in the utility model embodiment;
Fig. 2 is the partial structurtes schematic diagram at revolve described in the utility model embodiment-jetting type drier place;
Fig. 3 be in the utility model embodiment air-flow distributor face structural representation;
Fig. 4 is the plan structure schematic diagram of the casing of air-flow distributor in the utility model embodiment;
Fig. 5 is the structure for amplifying schematic diagram of A portion in Fig. 3;
Fig. 6 is the structure for amplifying schematic diagram of B portion in Fig. 3;
Fig. 7 is the structure for amplifying schematic diagram of C portion in Fig. 4;
Fig. 8 is the plan structure schematic diagram of the case lid of air-flow distributor in the utility model embodiment;
Fig. 9 is the sectional structure schematic diagram along D-D line in Fig. 8;
In figure: 1. air-flow distributor, 2. revolve-jetting type drier, 3. air blast, 4. heater, 5. a warm-air pipe, 6. second heat airduct, 7. clasfficiator, 8. collecting pipe, 9. nozzle, 10. drier enclosure, 11. Venturi tubes, 12. charge doors, 13. casings, 14. case lids, 15. entrance points, 16. ports of export, 17. hot blast ratios regulate section, 18. points of fan blade bobbins, 19. points of air blades, 20. turbine worm reducers, 21. shaft couplings, 22. upper shaft bearings, 23. bottom end bearing seats, 24. upper end bearings, 25. bottom end bearings, the logical lid of 26. upper bearing (metal)s, 27. lower bearing stifles, 28. O type rubber seal, 29. tuning drive gears, 30. dials, 31. through holes, 32. points of air blade asbestos pads, 33. points of air blade asbestos pad pressing plates, 34. points of fan blade bobbin asbestos pads, 35. points of fan blade bobbin asbestos pad press strips, 36. cambered surfaces, 37. variable-pitch auger conveyers, 38. feeders, 39. Blowing stoppers, 40. cyclone separators, 41. cloth envelop collectors, 42. air-introduced machines.
The specific embodiment
Below in conjunction with drawings and Examples, the technical solution of the utility model is done to further detailed elaboration.
Embodiment: as shown in Figure 1: a kind of living beings wood chip drying system, comprise for generation of the dry heated air drying device with thermal current of wood chip, for delivery of the feed arrangement of processed wood chip, for controlling the air-flow distributor 1 for primary drying hot blast and redrying hot blast distribution ratio, carry out the revolve-jetting type drier 2 of dried wood chips operation, for collecting the gathering-device of qualified finished product and the tail gas filter for tail gas filtering dedusting, the bottom of revolve described in wherein said feed arrangement is connected to-jetting type drier 2, described heated air drying device is connected with described air-flow distributor 1 by pipeline, described air-flow distributor 1 is connected respectively with top with the bottom of described revolving-jetting type drier 2 by pipeline, the top of described revolving-jetting type drier connects described gathering-device and described tail gas filter successively by pipeline.Described heated air drying device comprises air blast 3 and the heater 4 being connected with described air blast 3 pipelines; Described air-flow distributor 1 can be according to the wood chip kind being dried, specific heat capacity, density, relative moisture contents etc., regulate primary drying hot blast and redrying hot blast distribution ratio, for revolve-jetting type drier 2 provides satisfactory primary and secondary air, reach the different requirements that various wood chips will be dried, make like this this system can be used for dry different types of living beings wood pellet, improve drying efficiency, and it is easy to operate, practical.In revolve-jetting type drier 2, the time of staying of wood chip can be because of the size of wood pellet and " selection " to some extent of density size.Due to the difference of solid particle size, suffered gravity is also different, the length of the screw of answering in contrast difference to some extent, namely " selection " property of the so-called time of staying.Just due to the alternative of this time of staying, wood pellet is after overwinding-jetting type drier 2 dry, obtain all more uniform dry products of temperature, moisture content, both the phenomenon that there will not be the quality of physico-chemical property to decline, also there will not be the overheated or dry not saturating phenomenon of topical product, thereby obtained high-quality product.
As shown in Figure 2, described revolving-jetting type drier 2 comprises main unit for dryer, for delivery of warm-air pipe 5 and the second heat airduct 6 of hot blast, for screening the clasfficiator 7 of wood pellet, collecting pipe 8 and nozzle 9, described main unit for dryer comprises drier enclosure 10 and for the Venturi tube 11 of dried wood chips for the first time, described Venturi tube 11 is arranged on described drier enclosure 10 inside, between them, form annular space, the bottom of described drier enclosure 10 has the charging aperture for charging, described nozzle 9 is arranged on described main unit for dryer bottom, a described warm-air pipe 5 is connected with described nozzle 9, the hot-air flow that the hot blast of coming in from warm-air pipe forms high velocity, low pressure after the nozzle 9 ejections wood chip that will wet is sent to Venturi tube 11 through charge door 12, described clasfficiator 7 is arranged on the top of main unit for dryer, described collecting pipe 8 is connected with clasfficiator 7, described second heat airduct 6 is through described drier enclosure 10, one end is connected with pipeline in the outside of described drier enclosure 10, in the inner annular space that one end forms at described Venturi tube 11 and described drier enclosure 10 in addition.Described air-flow distributor 1 is connected with warm-air pipe 5 and second heat airduct 6.The hot-air flow of the high velocity, low pressure that the hot blast of a warm-air pipe 5 forms through nozzle 9 sprays in described Venturi tube 11, through the reducing of trunnion, the speed that makes air-flow increase rapidly, position after nozzle ejection air-flow has formed local negative pressure, and this just makes the wood chip of position nearby be inhaled in Venturi tube under the effect of negative pressure.Meanwhile, under the effect of high velocity air, the part of wood substance grain caking can be pulverized, and then can increase the contact surface area of wood substance grain and thermal current, thereby can improve dry efficiency.The second heat wind energy being provided by described secondary air channel 6 makes not reach the dry wood substance grain requiring, through the Action of Gravity Field of second heat wind action and particle self, in the inner annular space forming at described Venturi tube 11 and described drier enclosure 10, form top-down spiral flow, carry out redrying, can save the operation of a lot of filtrations, make the dry efficiency higher, saved again dry space.Described Venturi tube 11 comprises reducer, trunnion and increaser three parts, and during for dried biomass wood chip, reducer cone angle is 14 to 16 °, and the cone angle of increaser is 5 to 7 °.
According to different processed wood chips, the lower end spacing of the reducing pipe of the jet hole of described nozzle 9 and Venturi tube 11 can be adjusted, and to change the vacuum at Venturi tube reducing pipe place, adapts to the wood chip of different tree species and shape.A described warm-air pipe 5 is threaded connection with described nozzle 9, at the air outlet of a warm-air pipe 5, be provided with one and be with externally threaded straight tube, the air inlet place of nozzle 9 is provided with a tapped straight tube, by being with externally threaded straight tube to coordinate with tapped straight tube, a described warm-air pipe 5 is coupled together with described nozzle 9.Arrange like this, can pass through to adjust the position of nozzle 9, thereby change the lower end spacing of the jet hole of nozzle 9 and the reducing pipe of Venturi tube 11.
Described clasfficiator 7 can be changed, the degree of drying of itself and described air-flow distributor co-controlling discharging wood chip, thus control different wood chips at dry later moisture content.Thereby described clasfficiator 7 can make granularity is little after heated-air drying wood substance grain be smoothly through to be separated, the wood pellet that granularity is large is kept off back in hothouse, under the Action of Gravity Field of wood substance grain self, in conjunction with second heat wind action, impel the wet top-down rotary fluid of wood chip again, in making in inner annular space that wood substance grain forms at described Venturi tube and described drier enclosure, with certain radius, along helix, decline, re-start broken being dried, until reach clasfficiator, allow the granule size passing through.The size of clasfficiator 7 diameters has determined that wood chip is dried later moisture content, and therefore clasfficiator is arranged to removablely, just can, by changing clasfficiator, adapt to the different-grain diameter of different tree species and the wood raw material of different water cut dry.
As shown in Figures 3 to 5, described air-flow distributor 1 comprises casing 13 and is fixed by bolts to the case lid 14 on described casing 13, described casing 13 comprises entrance point 15, the port of export 16 and hot blast ratio regulate section 17, described entrance point 15, the port of export 16 is distributed in described hot blast ratio and regulates section 17 both sides, also comprise point fan blade bobbin 18 being rotationally connected with described casing 13, described point of fan blade bobbin 18 one end insert in described casing 13 and the other end through the case lid 14 on described casing, point air blade 19 being connected by welding manner with point fan blade bobbin 18 being arranged in casing, it is two regions that described point of air blade 19 regulates section 17 by described hot blast ratio, be respectively hot blast region and secondary hot-air region, thereby drive point air blades 19 to rotate to adjust hot blast region being divided into by described point of air blade and the air quantity ratio in secondary hot-air region by described point of fan blade bobbin 18, to control and to adjust the hot blast ratio of hot blast and secondary hot-air of the port of export 16.Also be provided with controller, described controller comprises turbine worm reducer 20 and shaft coupling 21, described turbine worm reducer 20 is connected through one end of described case lid with described point of fan blade bobbin 18 by shaft coupling 21, utilize the self-locking property of turbine and worm, can be by dividing air blade 19 accurately to locate, accurately to control hot blast distribution ratio.
As shown in Figure 4, the cross section of described air-flow distributor is Y type, its vertical section is rectangle, one end of described Y type air-flow distributor is entrance point 15, another divergent ends relative with entrance point is two ports of export 16, and wherein entrance point 15 connects blast pipe, and a port of export 16 connects warm-air pipe 5 one time, the another one port of export 16 connecting secondary warm-air pipes 6, the described point of longitudinal rotation of fan blade bobbin 18 is arranged near the casing two port of export joints and described case lid is passed in its one end.
As shown in Figure 5 and Figure 6, on near casing described two port of export joints, be respectively arranged with upper shaft bearing 22 and bottom end bearing seat 23, on described, on bottom end bearing seat, be respectively arranged with upper end bearing 24 and bottom end bearing 25, the bottom of the top of described upper shaft bearing 22 and bottom end bearing seat 23 is respectively arranged with that upper bearing (metal) is logical covers 26 and lower bearing stifle 27, described point of fan blade bobbin 18 with described on, bottom end bearing cooperation is rotationally connected, and the upper end of described point of fan blade bobbin 18 through described upper bearing (metal) logical cover 26 reach outside, point fan blade bobbin 18 and described on, between bottom end bearing seat, be also provided with O type rubber seal 28, described upper bearing (metal) is logical cover 26 and lower bearing stifle 27 by bolt be connected respectively to described on, on bottom end bearing seat.
As Fig. 5, shown in Fig. 8 and Fig. 9, the by-pass cock of described controller is designed to manually, at described point of fan blade bobbin 18, through on one end of casing, be provided with the tuning drive gear 29 being fixedly connected with it simultaneously, and the sensing of described tuning drive gear 29 is pointed to consistent with the longitudinal section of described point of air blade 19, on described case lid 14, be provided with dial 30 and through hole 31, thereby described dial 30 and described tuning drive gear 29 are used in conjunction with the allocation proportion that shows intuitively hot blast and secondary hot-air, so just can be easily point air blade be adjusted to needed position and controls the distribution ratio of the hot blast of air main and secondary wind inleting tube, described through hole 31 matches with described upper shaft bearing 22, make described upper shaft bearing 22 can pass the through hole 31 of described case lid.
As shown in Figure 5 and Figure 6, described point of air blade 19 upper and lower ends are respectively around being useful on point air blade asbestos pad 32 of two region hot blasts of isolation and being arranged on described point air blade asbestos pad 32, be used for fixing residence and state point air blade asbestos pad pressing plate 33 of point air blade asbestos pad 32, to divide air blade asbestos pad pressing plate 33 to be fixed on described point of air blade 19 with bolt, thereby described point of air blade asbestos pad 32 will be pressed abd fixed on to described air blade 19 upper and lower ends that divide.Described point of air blade asbestos pad 32 lived the gap in point air blade longitudinal section direction and between case lid and casing lower wall for barrier, isolates two region hot blasts, thereby further controls accurately the allocation proportion of hot blast and secondary hot-air.
As shown in Figure 7, on near the madial wall of the casing described two port of export joints, be provided with point fan blade bobbin asbestos pad 34 and be arranged on described point fan blade bobbin asbestos pad 34 one end, be used for fixing residence and state point fan blade bobbin asbestos pad press strip 35 of point fan blade bobbin asbestos pad 34, described point of fan blade bobbin asbestos pad press strip 35 is fixed near the madial wall of the casing described two port of export joints with screw, thereby described point of fan blade bobbin asbestos pad 34 one end are pressed abd fixed near the madial wall of the casing described two port of export joints, described point of other one end of fan blade bobbin asbestos pad 34 is cambered surface 36, the tangent laminating of cylindrical of described cambered surface 36 and described point of fan blade bobbin 18 cross sections, described point of fan blade bobbin asbestos pad 34 stated near the madial wall of two casings port of export joint and divides the gap between fan blade bobbin 18 for barrier residence, prevent two region hot blast exchanges, thereby further control accurately the allocation proportion of hot blast and secondary hot-air.
As shown in Figure 2, described feed arrangement comprises two variable-pitch auger conveyers 37, for reinforced feeder 38 and Blowing stopper 39, described Blowing stopper 39 is arranged between two variable-pitch auger conveyers 37, feeder 38 is connected with one of them variable-pitch auger conveyer 37, another one variable-pitch auger conveyer 37 with described in the charge door 12 of bottom of revolve-jetting type drier 2 be connected.
Described variable-pitch auger conveyer 37 adopts variable-pitch auger feeding structure, the pitch of feed end is little, discharge end pitch is large, conveyor screw can not be stopped up, described variable-pitch auger conveyer adopts variable-frequency motor speed governing, can control charging rate, adapt to different particle diameters and the wood chip of fibre length, the efficiency that has improved charging prevents again the problem of line clogging.The rotor of Blowing stopper 39 is provided with ring cutting blade, the wood fiber of Blowing stopper import can be cut off, and guarantees that charging is smooth.
As shown in Figure 1, described gathering-device comprises the cyclone separator 40 being connected with the collecting pipe 8 of described revolving-jetting type drier 2 and the Blowing stopper 39 that is arranged on described cyclone separator bottom; Described tail gas filter comprises the cloth envelop collector 41 being connected with described cyclone separator 40 pipelines, is arranged on the Blowing stopper 39 of described cloth envelop collector 41 bottoms and the air-introduced machine 42 being connected with described cloth envelop collector 41 pipelines.Described cyclone separator can be removed the solid particle polluter and the drop that in pumped (conveying) medium gas, carry to greatest extent, reaching gas-solid-liquid separates, to guarantee the normal operation of pipeline and equipment, utilize cyclone separator to carry out separation to dried wood substance grain with dust, both reached the requirement of work, can carry out collection and treatment to dust again, prevent from having caused air pollution, avoid human body to damage.Described cloth envelop collector can filter out the wooden granule in tail gas, and it can also serve as the materials of next step, so both can reduce the waste of resource, has also reduced the pollution of environment.Ring cutting blade is also installed on the rotor of described Blowing stopper 39.
Drying means of the present utility model, comprises the following steps:
(1), revolve-jetting type drier is set, for carrying out dried wood chips operation;
(2), feed arrangement is set, for delivery of processed wood chip, by this feed arrangement with described in the bottom of revolve-jetting type drier be connected;
(3), air-flow distributor is set, for controlling primary drying hot blast and redrying hot blast distribution ratio, this air-flow distributor is connected respectively with top with the bottom of described revolving-jetting type drier by pipeline;
(4), heated air drying device is set, dry with thermal current for generation of wood chip, this heated air drying device is connected with described air-flow distributor by pipeline;
(5), be provided for collecting the gathering-device of qualified finished product and the tail gas filter for tail gas filtering dedusting, the top of described revolving-jetting type drier is connected with tail gas filter with gathering-device successively by pipeline;
(6), described heated air drying device heats outside cold air suction to it, form hot blast, sends into described air-flow distributor;
(7), described air-flow distributor is according to the difference of wood chip kind that will be dry, regulates primary drying hot blast and redrying hot blast distribution ratio, bottom and the top of revolve-jetting type drier described in sending into respectively;
(8), hot blast forms the hot-air flow of high velocity, low pressure behind the bottom of described revolving-jetting type drier;
(9), described feed arrangement wet wood chip is sent into after treatment described in the bottom of revolve-jetting type drier;
(10) hot-air flow of the high velocity, low pressure that the bottom of revolve ,-jetting type drier forms and the wet wood chip granular finished product of the dry formation of Hybrid Heating in revolve-jetting type drier described in described;
(11), qualified product is collected through the gathering-device being connected with the top duct of described revolving-jetting type drier, described in underproof product quilt, the top of revolve-jetting type drier stops, the hot blast on the top of revolve-jetting type drier blows to the bottom of described revolving-jetting type drier described in send into, again dry with the hot-air flow Hybrid Heating of the high velocity, low pressure of bottom, so form circulation, until heated, be dried to qualified products, by the gathering-device being connected with the top duct of described revolving-jetting type drier, collected, tail gas is discharged in air through described tail gas filter after dust removal by filtration, complete dry run,
Wherein step (1) to (5) order in no particular order.
As depicted in figs. 1 and 2, when using the utility model drying system, air blast 3 is worked, first outside cold air is sent into heater 4, after cold air being heated to (being generally 130-230 ° of C) by heater 4, send into air-flow distributor 1, according to the difference of the wood chip kind being dried, by air-flow distributor 1, the hot blast rate of warm-air pipe 5 and second heat airduct 6 is distributed, through a warm-air pipe 5, hot-air is sent in the nozzle 9 of revolve-jetting type drier 2 bottoms, the air-flow of high velocity, low pressure is from nozzle 9 places ejection, the wood chip that will wet is sent in revolve-jetting type drier 2 through charge door 12, in the Venturi tube 11 of revolve-jetting type drier because the conversion of thermal current sound energy after heating makes hot blast contact fully with particle wood chip, heat and mass transfer process is carried out fully, when going out Venturi tube 11, reach the dry wood chip requiring and enter collecting pipe 8 from exporting classified device 7, from collecting pipe 8, send into cyclone separator 40 again, through Blowing stopper 39, discharge and carry out next link again, gas-solid two waste gas after being separated are discharged in air by air-introduced machine 42 after the dust removal and filtration of cloth envelop collector 41, simultaneously, after the particle wood chip that does not arrive requirement has gone out Venturi tube 11, stopping of classified device 7, by second heat airduct 6, be blown in the inner annular space that described Venturi tube 11 and described drier enclosure 10 form, do top-down rotation, the position of the charging aperture 12 of revolve-jetting type of arrival drier is again got back to Venturi tube 11 and is carried out redrying, until reach dry requirement after the suction of a hot blast mixes with new wet wood chip.Measure by experiment, adopt this drying system dried biomass wood chip, the box Air Dried System dried biomass energy wood chip efficiency that thermal efficiency ratio is traditional can improve nearly 10 ﹪, and under similarity condition, occupation area of equipment dwindles nearly 40 ﹪.
In sum, adopt the utility model to carry out heat drying to living beings wood chip, can be time saving and energy saving and can be used for dry different types of living beings wood pellet, improved drying efficiency; Adopt the utility model can also reduce the pollution of emission to air, environmental protection and energy saving.
Above embodiment is only for illustration of the utility model; but not to restriction of the present utility model; person skilled in the relevant technique is not in the situation that departing from spirit and scope of the present utility model; can also make a variety of changes or convert; therefore all technical schemes that are equal to also should belong to protection domain of the present utility model, and protection domain of the present utility model should be limited by each claim.
Claims (8)
1. a living beings wood chip drying system, it is characterized in that: comprise for generation of the dry heated air drying device with thermal current of wood chip, for delivery of the feed arrangement of processed wood chip, for controlling the air-flow distributor for primary drying hot blast and redrying hot blast distribution ratio, carry out the revolve-jetting type drier of dried wood chips operation, for collecting the gathering-device of qualified finished product and the tail gas filter for tail gas filtering dedusting, the bottom of revolve described in wherein said feed arrangement is connected to-jetting type drier, described heated air drying device is connected with described air-flow distributor by pipeline, described air-flow distributor is connected respectively with top with the bottom of described revolving-jetting type drier by pipeline, the top of described revolving-jetting type drier connects described gathering-device and described tail gas filter successively by pipeline.
2. living beings wood chip drying system according to claim 1, it is characterized in that: described in revolve-jetting type drier comprise main unit for dryer, for delivery of warm-air pipe and the second heat airduct of hot blast, for screening the clasfficiator of wood pellet, collecting pipe and nozzle, described main unit for dryer comprises drier enclosure and for the Venturi tube of dried wood chips for the first time, described Venturi tube is arranged on described drier enclosure inside, between them, form annular space, the bottom of described drier enclosure has the charging aperture for charging, described nozzle is arranged on described main unit for dryer bottom, a described warm-air pipe is connected with described nozzle, the hot-air flow that the hot blast of coming in from warm-air pipe forms high velocity, low pressure after the nozzle ejection wood chip that will wet is sent to Venturi tube through charge door, described clasfficiator is arranged on the top of main unit for dryer, described collecting pipe is connected with clasfficiator, described second heat airduct is through described drier enclosure, one end is connected with pipeline in the outside of described drier enclosure, one end is in the inner annular space of described Venturi tube and the formation of described drier enclosure in addition.
3. living beings wood chip drying system according to claim 2, it is characterized in that: at the air outlet of a described warm-air pipe, be provided with one and be with externally threaded straight tube, the air inlet place of described nozzle is provided with a tapped straight tube, by being with externally threaded straight tube to coordinate a described warm-air pipe and described nozzle are coupled together with tapped straight tube.
4. according to the living beings wood chip drying system described in any one claim in claims 1 to 3, it is characterized in that: described air-flow distributor comprises casing and is arranged on the case lid on described casing, described casing comprise into, the port of export and hot blast ratio regulate section, described enter, the port of export is distributed in described hot blast ratio and regulates section both sides, also comprise point fan blade bobbin being rotationally connected with described casing, described point of fan blade bobbin one end inserted in described casing and the other end passes the case lid on described casing, point air blade being fixedly connected with point fan blade bobbin being arranged in casing, it is two regions that described point of air blade regulates section by described hot blast ratio, thereby drive point air blade to rotate the air quantity ratio of adjusting two regions that are divided into by described point of air blade by described point of fan blade bobbin, to control and to adjust the hot blast ratio of the port of export.
5. living beings wood chip drying system according to claim 4, it is characterized in that: the cross section of described air-flow distributor is Y type, its vertical section is rectangle, one end of described air-flow distributor is entrance point, another divergent ends relative with entrance point is two ports of export, and the described point of longitudinal rotation of fan blade bobbin is arranged near the casing two port of export joints and described case lid is passed in its one end.
6. living beings wood chip drying system according to claim 5, it is characterized in that: described feed arrangement comprises two variable-pitch auger conveyers, for reinforced feeder and Blowing stopper, described Blowing stopper is arranged between two variable-pitch auger conveyers, feeder is connected with one of them variable-pitch auger conveyer, another one variable-pitch auger conveyer with described in the bottom of revolve-jetting type drier be connected.
7. living beings wood chip drying system according to claim 6, it is characterized in that: described variable-pitch auger conveyer adopts variable-pitch auger feeding structure, the pitch of feed end is little, and discharge end pitch is large, and described variable-pitch auger conveyer adopts variable-frequency motor speed governing; The rotor of described Blowing stopper is provided with ring cutting blade.
8. living beings wood chip drying system according to claim 7, is characterized in that: described gathering-device comprises the cyclone separator being connected with the collecting pipe of described revolving-jetting type drier and is arranged on the Blowing stopper of described cyclone separator bottom; Described tail gas filter comprises the cloth envelop collector being connected with described cyclone separator pipeline, is arranged on the Blowing stopper and the air-introduced machine being connected with described cloth envelop collector pipeline of described cloth envelop collector bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320775526.8U CN203586721U (en) | 2013-12-02 | 2013-12-02 | Biomass wood chip drying system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320775526.8U CN203586721U (en) | 2013-12-02 | 2013-12-02 | Biomass wood chip drying system |
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| CN203586721U true CN203586721U (en) | 2014-05-07 |
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| CN201320775526.8U Withdrawn - After Issue CN203586721U (en) | 2013-12-02 | 2013-12-02 | Biomass wood chip drying system |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103604285A (en) * | 2013-12-02 | 2014-02-26 | 中南林业科技大学 | Biomass wood bit drying system and biomass wood bit drying method |
| CN104315825A (en) * | 2014-11-10 | 2015-01-28 | 成都樵枫科技发展有限公司 | Air flow drying device with double helix structure |
| CN106172925A (en) * | 2016-07-28 | 2016-12-07 | 董超超 | One is applicable to large batch of tea processing device |
| CN106179809A (en) * | 2016-07-28 | 2016-12-07 | 董超超 | A kind of high-performance glass body processing means |
| CN106179679A (en) * | 2016-07-28 | 2016-12-07 | 董超超 | A kind of high-performance sewage-treating agent preparation system |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103604285A (en) * | 2013-12-02 | 2014-02-26 | 中南林业科技大学 | Biomass wood bit drying system and biomass wood bit drying method |
| CN104315825A (en) * | 2014-11-10 | 2015-01-28 | 成都樵枫科技发展有限公司 | Air flow drying device with double helix structure |
| CN104315825B (en) * | 2014-11-10 | 2016-08-24 | 成都樵枫科技发展有限公司 | There is double-stranded pneumatic conveying dryer |
| CN106172925A (en) * | 2016-07-28 | 2016-12-07 | 董超超 | One is applicable to large batch of tea processing device |
| CN106179809A (en) * | 2016-07-28 | 2016-12-07 | 董超超 | A kind of high-performance glass body processing means |
| CN106179679A (en) * | 2016-07-28 | 2016-12-07 | 董超超 | A kind of high-performance sewage-treating agent preparation system |
| CN106182412A (en) * | 2016-07-28 | 2016-12-07 | 董超超 | One not colour cast strong mixing Ceramic manufacturing system |
| CN106216061A (en) * | 2016-07-28 | 2016-12-14 | 董超超 | A kind of dyestuff body processing system utilizing ultrasound wave |
| CN106345537A (en) * | 2016-07-28 | 2017-01-25 | 董超超 | Mixed solid catalyst preparation system |
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