Summary of the invention
Therefore, the technical problem to be solved is in that to overcome in prior art that material handling system drying efficiency is low, drying effect is bad and baroque defect.
For this, the present invention provides a kind of material processing method, comprises the steps
The step that material is heated;
The step that material is stirred;
The step that material is dried;
The step of described heating, the step of stirring and dry step adopt same system to carry out simultaneously, and described system includes
Body of heater, horizontally disposed, there is cavity, for material addition, the charging aperture taken out, discharging opening; And for hot gas inflow, the first air inlet flowed out, the first gas outlet;
Charging gear, for adding material in described body of heater;
Material-receiving device, is used for the material after collecting described body of heater inner drying;
First rotating shaft, is located in the cavity of described body of heater, has installation cavity, and the inwall of described installation cavity is provided with some heating wire, the heating during energising of described heating wire, and described first rotating shaft is that Heat Conduction Material is made;
Second rotating shaft, it is set in described first rotating shaft, and and described first rotating shaft between formed venting cavity, described venting cavity is provided with several puff prots, the jet direction of described puff prot is misaligned not parallel with the mixing direction of the mixing direction of described shaft and described blade, it is not parallel misaligned that the jet direction of described puff prot and the axis of described charging aperture form 30-50 degree angle, the airintake direction of described first air inlet and the jet direction of described puff prot;
Connecting tube, described venting cavity is connected with described first gas outlet by connecting tube, and described first gas outlet is opened time different from described puff prot;
Shaft, is arranged on the outer wall of described second rotating shaft, and the radial direction towards described second rotating shaft extends, and multiple along the axial outer wall distribution of described second rotating shaft;
Blade, for multiple, is inclined on described shaft, and the distance between adjacent described blade is not more than 30mm.
Described blade is removably set on described shaft, and described mixing component also includes locking member, for described blade lock fixes on the desired location place on described shaft.
Multiple shafts are distributed on the multiple spaced periphery of described second rotating shaft, and on each periphery of described second rotating shaft, distribution has at least one shaft.
Shaft on adjacent circumferential face is positioned on different vertical planes.
Described shaft is at least four, four described shafts are separately positioned on four peripheries of described second rotating shaft, and four described shafts are successively set in the bottom outer wall on the rear portion outer wall on the anterior outer wall in the top exterior walls in the Z-direction of described second rotating shaft, in Y direction, in Y direction and in Z-direction respectively.
Described blade lean is arranged on the angle on described shaft more than 0 �� and less than or equal to 20 ��; Spacing between edge and the described inboard wall of furnace body of the close inboard wall of furnace body side of described blade is 0.5-10 centimetre.
Described is air stove to wind apparatus, and the gas outlet of described air stove is connected to described first air inlet by second pipe.
Also including air distribution device, the gas outlet of described air distribution device is connected to described second pipe, is used for introducing external air in described second pipe, mixes with the hot gas in described second pipe.
Also including dust arrester, described dust arrester includes cyclone cylinder, and described cyclone cylinder has the second air inlet, the second gas outlet and the 3rd gas outlet;
Described second air inlet is connected to described first gas outlet, for being introduced in described cyclone cylinder by the gas in body of heater, and to the dedusting introduced;
Described second gas outlet is in communication with the outside, for being discharged by the gas after dedusting;
Described 3rd gas outlet is connected to the cavity of wind apparatus with described by the first pipeline, for being mixed with to the hot gas in wind apparatus by the gas after dedusting, forms the hot gas of required moisture content.
The bore of described puff prot is not more than 3mm, and the jet velocity at described puff prot place is more than the rotary speed of described second rotating shaft.
Described material is mud.
Technical scheme provided by the invention, has the advantage that
1. material processing method provided by the invention, adopts a set of special process system so that heating, stirring and dry be integrated, and carries out simultaneously, and this process system includes body of heater, and body of heater has charging aperture, discharging opening, the first air inlet and the first gas outlet; For to the charging gear adding material in body of heater, for collecting the material-receiving device of the material after body of heater inner drying, agitating device, including the first rotating shaft, it is located in the cavity of described body of heater, there is installation cavity, the inwall of described installation cavity is provided with some heating wire, the heating during energising of described heating wire, described first rotating shaft is that Heat Conduction Material is made; Second rotating shaft, it is set in described first rotating shaft, and and described first rotating shaft between formed venting cavity, described venting cavity is provided with several puff prots, the jet direction of described puff prot is misaligned not parallel with the mixing direction of the mixing direction of described shaft and described blade, it is not parallel misaligned that the jet direction of described puff prot and the axis of described charging aperture form 30-50 degree angle, the airintake direction of described first air inlet and the jet direction of described puff prot; Shaft, is arranged on the outer wall of described second rotating shaft, and the radial direction towards described second rotating shaft extends, and multiple along the axial outer wall distribution of described second rotating shaft; Blade, for multiple, is inclined on described shaft, and the distance between adjacent described blade is not more than 30mm.
This processes system, when material is dried, material is added in the cavity of body of heater through charging aperture by charging gear, simultaneously, second axis of rotation drives the mixing component in the second rotating shaft along the radial and axial of the second rotating shaft, material constantly being stirred, mixing component includes the shaft being arranged on the second rotating shaft outer wall, and shaft extends towards the radial direction of the second rotating shaft, and multiple shafts are distributed along the axial outer wall of the second rotating shaft; And multiple blade, blade lean is arranged on shaft. Under the second axis of rotation, shaft and blade are all along with the second axis of rotation, multiple shafts and blade axially and radially material is stirred in the second rotating shaft simultaneously, and in whipping process, blade can comminuting matter, and material can be thrown in the cavity of body of heater, material is not only rolled in body of heater, can also moving in body of heater cavity, increasing material and the heat convection area of thermal current in cavity, thus improving heat exchange efficiency. Further, described venting cavity being provided with several puff prots, the jet direction of described puff prot is misaligned not parallel with the mixing direction of the mixing direction of described shaft and described blade; The airintake direction of described first air inlet is not parallel misaligned with the jet direction of described puff prot, thus adding the dimension of stirring, it is to avoid only stir material in one direction so that material is bonded together, and affects the loosening degree of material; Additionally, mixing component is while stirring material, additionally it is possible to by crushing material, form the material that granule is less, increase the area of material and hot gas heat convection further, improve the drying efficiency of material; After band material is dried, drops on material-receiving device under discharging opening, and be transferred away. Further, above-mentioned drying device also includes connecting tube, and described venting cavity is connected with described first gas outlet by connecting tube, and described first gas outlet is opened time different from described puff prot, so that the gas in body of heater can by further Collection utilization. Additionally, the axis of the jet direction of described puff prot and described charging aperture forms 30-50 degree angle, namely, the axis of the axis of puff prot and described air inlet forms 30-50 degree angle, this makes the material come in from charging aperture, eddy flow upset can be carried out for the gas of puff prot ejection, improve stirring and drying effect.
Additionally, first rotating shaft, is located in the cavity of described body of heater, has installation cavity, the inwall of described installation cavity is provided with some heating wire, the heating during energising of described heating wire, described first rotating shaft is that Heat Conduction Material is made, such that it is able to utilizing the heating wire being positioned at the first rotating shaft is the gas heating being positioned at described venting cavity, so that heating and dry integrate, first rotating shaft is arranged on inside the second rotating shaft, improves space availability ratio so that mechanism is simple.
2. material processing method provided by the invention, the blade of its system adopted is removably set on shaft, and mixing component also includes locking member, for blade lock fixes on the desired location place on shaft. Blade moves on shaft, adjusts the gap between blade and inboard wall of furnace body, to change blade to material stirring and crushing effect, and material is driven down by blade, kinestate in body of heater, so that it is determined that the time of staying that material is in body of heater, meets the dry demand of different material.
3. material processing method provided by the invention, multiple shafts of its system adopted are distributed on the multiple spaced periphery of the second rotating shaft, and on each periphery of the second rotating shaft, distribution has at least one shaft. When the second axis of rotation, second rotating shaft drives the shaft on multiple peripheries and blade thereon material is stirred and pulverizes, it is positioned at the material on the second rotating shaft axial direction to be stirred by the shaft on the periphery of corresponding position the second rotating shaft and blade and pulverize, guarantee that in body of heater, material all can be stirred by blade and pulverize, and the effect stirred and pulverize is evenly, improves the effect of dry materials.
Embodiment 1
Such as Fig. 1, the present embodiment provides a kind of material handling system to include
Body of heater 1, horizontally disposed, there is cavity, for material addition, the charging aperture 11 taken out, discharging opening 12;And first air inlet the 13, first gas outlet 14 flowing into for hot gas, flowing out;
Charging gear 2, for adding material in described body of heater 1;
Material-receiving device 3, is used for the material after collecting described body of heater 1 inner drying;
First rotating shaft 17, is located in the cavity of described body of heater 1, has installation cavity, and the inwall of described installation cavity is provided with some heating wire 19, the heating during energising of described heating wire, and described first rotating shaft is that Heat Conduction Material is made; As shown in Figure 4;
Second rotating shaft 5, it is set in described first rotating shaft, and and described first rotating shaft between formed venting cavity, described venting cavity is provided with several puff prots 18, the jet direction of described puff prot is misaligned not parallel with the mixing direction of the mixing direction of described shaft 6 and described blade 7, it is not parallel misaligned that the jet direction of described puff prot and the axis of described charging aperture 11 form 30-50 degree angle, the airintake direction of described first air inlet 13 and the jet direction of described puff prot;
Connecting tube, described venting cavity is connected with described first gas outlet 14 by connecting tube, and described first gas outlet 14 is opened time different from described puff prot;
Shaft 6, is arranged on the outer wall of described second rotating shaft 5, and the radial direction towards described second rotating shaft 5 extends, and multiple along the axial outer wall distribution of described second rotating shaft 5;
Blade 7, for multiple, is inclined on described shaft 6, and the distance between adjacent described blade 7 is not more than 30mm.
Material handling system provided by the invention, including body of heater, body of heater has charging aperture, discharging opening, the first air inlet and the first gas outlet; For to the charging gear adding material in body of heater, for collecting the material-receiving device of the material after body of heater inner drying, agitating device, including the second rotating shaft, it is located in the cavity of described body of heater, described second rotating shaft has venting cavity, and described venting cavity is provided with several puff prots, and the jet direction of described puff prot is misaligned not parallel with the mixing direction of the mixing direction of described shaft and described blade; Shaft, is arranged on the outer wall of described second rotating shaft, and the radial direction towards described second rotating shaft extends, and multiple along the axial outer wall distribution of described second rotating shaft; Blade, for multiple, is inclined on described shaft, and the distance between adjacent described blade is not more than 30mm.
This processes system, when material is dried, material is added in the cavity of body of heater through charging aperture by charging gear, simultaneously, second axis of rotation drives the mixing component in the second rotating shaft along the radial and axial of the second rotating shaft, material constantly being stirred, mixing component includes the shaft being arranged on the second rotating shaft outer wall, and shaft extends towards the radial direction of the second rotating shaft, and multiple shafts are distributed along the axial outer wall of the second rotating shaft; And multiple blade, blade lean is arranged on shaft. Under the second axis of rotation, shaft and blade are all along with the second axis of rotation, multiple shafts and blade axially and radially material is stirred in the second rotating shaft simultaneously, and in whipping process, blade can comminuting matter, and material can be thrown in the cavity of body of heater, material is not only rolled in body of heater, can also moving in body of heater cavity, increasing material and the heat convection area of thermal current in cavity, thus improving heat exchange efficiency. Further, described venting cavity being provided with several puff prots, the jet direction of described puff prot is misaligned not parallel with the mixing direction of the mixing direction of described shaft and described blade;The airintake direction of described first air inlet is not parallel misaligned with the jet direction of described puff prot, thus adding the dimension of stirring, it is to avoid only stir material in one direction so that material is bonded together, and affects the loosening degree of material; Additionally, mixing component is while stirring material, additionally it is possible to by crushing material, form the material that granule is less, increase the area of material and hot gas heat convection further, improve the drying efficiency of material; After band material is dried, drops on material-receiving device under discharging opening, and be transferred away. Further, above-mentioned drying device also includes connecting tube, and described venting cavity is connected with described first gas outlet by connecting tube, and described first gas outlet is opened time different from described puff prot, so that the gas in body of heater can by further Collection utilization. Additionally, the axis of the jet direction of described puff prot and described charging aperture forms 30-50 degree angle, namely, the axis of the axis of puff prot and described air inlet forms 30-50 degree angle, this makes the material come in from charging aperture, eddy flow upset can be carried out for the gas of puff prot ejection, improve stirring and drying effect.
As further preferred embodiment, blade 7 is inclined at the angle on shaft 6 outer wall for more than 0 �� and less than or equal to 20 ��. Such as, blade 7 is tilted 1 ��, 3 ��, 5 ��, 7 ��, 10 ��, 12 ��, 15 ��, 20 �� etc. and is equiangularly arranged on shaft 6, be inclined at the blade 7 on shaft 6 and do not only have stirring action and also have the effect of comminuting matter. Considering stirring and the pulverization of material, be arranged on shaft 6 it is further preferred that blade 7 tilts 5 ��-10 ��, blade 7 is usually no more than 20 �� in the angle of shaft 6 surface thereof, otherwise can weaken the blade 7 mixing effect to material.
As further preferred embodiment, blade 7 is removably set on shaft 6, and mixing component also includes locking member 8, for blade 7 is locked in the desired location place on shaft 6. Blade 7 moves on shaft 6, adjust the gap between blade 7 and body of heater 1 inwall, to change blade 7 to material stirring and crushing effect, and material is driven down by blade 7, kinestate in body of heater 1, so that it is determined that the time of staying that material is in body of heater 1, meet the dry demand of different material.
Such as, some material particles is less, in dry run, shaft 6 and blade 7 primarily serve stirring action, spacing between blade 7 and body of heater 1 inwall can be tuned up, make material by blade 7 drive process, more space is had to move in body of heater 1 and roll, with the hot gas heat exchange in body of heater 1 cavity. On the contrary, if some material particles is big, it is necessary to while stirring, material is pulverized, accelerate drying efficiency, reduce the material time of staying in body of heater 1, it is possible to the spacing between blade 7 and body of heater 1 inwall turned down, the crushing effect of reinforced blade 7.
As more preferably preferred embodiment, when the radius of body of heater 1 is 30-40 centimetre, spacing between the edge of the close body of heater 1 inwall side of blade 7 and body of heater 1 inwall is set to 0.5-10 cm range, such as 0.5 centimetre, 1 centimetre, 2 centimetres, 3 centimetres, 5 centimetres, 8 centimetres, 10 centimetres etc., so that forming headspace between the edge of blade 7 and body of heater 1 inwall. What be more highly preferred to ranges for 4-5 centimetre, but, actual must determine according to parameters such as the performance of material itself, dry requirements.
It is removably set on the preferred implementation on shaft 6 as blade 7, blade 7 is plate, shaft 6 in the axial direction on offer chute, blade 7 is inserted directly in chute, treat that blade 7 slides into desired location place, when tilting required angle, directly with locking member 8, blade 7 is locked on shaft 6, for instance nut or pin, plug-in unit. That is, blade 7 is inclined and mounted in the chute of shaft 6. As deformation, blade 7 can also be the plate with intermediate throughholes, and the outer wall of shaft 6 has external screw thread, and blade 7 is set on shaft 6, and fixes with locking member 8, for instance nut, pin etc. Further, it is also possible to other carriage or update device in employing prior art, make blade 7 move on shaft 6, and then the part 8 that is locked is fixed.
As preferred embodiment, multiple shafts 6 are distributed on the multiple spaced periphery of the second rotating shaft 5, and on each periphery of the second rotating shaft 5, distribution has at least one shaft 6. When the second rotating shaft 5 rotates, second rotating shaft 5 drives the shaft 6 on multiple periphery and blade thereon 7 material is stirred and pulverizes, it is positioned at the material on the second rotating shaft 5 axial direction to be stirred by the shaft 6 on the periphery of corresponding position the second rotating shaft 5 and blade 7 and pulverize, guarantee that in body of heater 1, material all can be stirred by blade 7 and pulverize, and the effect stirred and pulverize is evenly, improves the effect of dry materials.
For the number that shaft 6 is set on each periphery, the number arranging shaft 6 on preferred each periphery is four, four shafts 6 lay respectively at the fourth class branch place of this periphery, so that the material at co-located place, it is continuously agitated by four shafts 6 on the periphery of corresponding section and the blade 7 on shaft 6 and pulverizes, stirring interlude is shorter, increases the contact area of material and hot gas, improves the efficiency that material is dried further. Shaft 6 number on each periphery is except four, it is also possible to is five, six, seven, eight etc., best, several shafts 6 is evenly distributed on the Along ent place of this periphery.
As further preferred embodiment, multiple shafts 6 are distributed on the multiple spaced periphery of the second rotating shaft 5, the spacing of adjacent two periphery being provided with shaft 6 is preferably 5-15 centimetre, for instance 5 centimetres, 6 centimetres, 7 centimetres, 7.5 centimetres, 8 centimetres, 10 centimetres, 12 centimetres, 15 centimetres etc. Best spacing is 7.5-10 centimetre.
As further preferred embodiment, the shaft 6 on adjacent circumferential face is positioned on different vertical planes. Now, the material being in adjacent position is stirred by the shaft 6 on different vertical planes, blade 7 and pulverizes, the direction that adjacent material is stirred is inconsistent, the movement locus of adjacent material is also inconsistent, further such that material is in admixture in cavity, will not be bonded together, improve the loosening degree of material, it is easier to carry out heat convection with hot gas, improves heat exchange efficiency further.
As more preferably preferred embodiment, shaft 6 is four, four shafts 6 are separately positioned on four peripheries of the second rotating shaft 5, and four shafts 6 are successively set in the bottom outer wall on the rear portion outer wall on the anterior outer wall in the top exterior walls in the Z-direction of the second rotating shaft 5, in Y direction, in Y direction and in Z-direction respectively.Shaft 6 adopts this arrangement mode, in the second rotating shaft 5 rotation process, the moment that second rotating shaft 5 is produced by top exterior walls with two shafts 6 in bottom outer wall can balance mutually, the moment that second rotating shaft 5 is produced by adjacent anterior outer wall with two shafts 6 on the outer wall of rear portion balances mutually, make the more steady of the second rotating shaft 5, shaft 6 and blade 7 running, avoid the second rotating shaft 5 to vibrate, improve the service life of drying oven.
A variant embodiment as shaft 6 number, the number of shaft 6 can also be 8,12,16 etc., namely the quantity of shaft 6 is 4n, wherein n >=1, every four shafts 6 repeat above-mentioned arrangement mode and are arranged on the outer wall of the second rotating shaft 5.
Another variant embodiment as shaft 6 number, the number of shaft 6 can also be 5, 6, 7, 8 etc., multiple shafts 6 are separately positioned on the different peripheries of the second rotating shaft 5, and observe from the radial direction of the second rotating shaft 5, multiple shafts 6 are distributed on the radial circumference of the second rotating shaft 5, it is in the Along ent place of the second rotating shaft 5 radial circumference best, such as shaft 6 is six, six shafts 6 are distributed on six peripheries, and observe from the radial direction of the second rotating shaft 5, six shafts 6 are located just at six Along ent places of the periphery of the second rotating shaft 5, material it is stirred multi-facetedly and pulverizes.
In above-mentioned embodiment, the shape of blade 7 can be square, trapezoidal, fan-shaped, the Fructus Persicae heart etc. other shapes, and its shape is not especially limited, in addition, the surface of blade 7 can be smooth plane, it is also possible to be the curved surface with certain radian transition, or the surface of other moulding can.
Variant embodiment as mixing component, mixing component can also include the some connecting rods being arranged on the second axial outer wall of rotating shaft 5, and the some fins in connecting rod it are arranged on around connecting rod outer wall, fin arrangement mode in connecting rod can the arrangement mode of similar prior art wind fan leaf, fin can rotate around the axis direction of connecting rod, and then material is stirred and pulverizes. Additionally, mixing component can also be other agitating devices or the reducing mechanism that are capable of stirring and comminuting matter in prior art.
As preferred embodiment, also including to wind apparatus 4, be air stove to wind apparatus 4, the gas outlet of air stove is connected to the first air inlet 13 by second pipe 16, the hot gas of air stove is delivered in the cavity of body of heater 1, makes hot gas and material carry out direct heat convection. As deformation, can also be that hot gas can be delivered to the device in the cavity of body of heater 1 through the first air inlet 13 by prior art to wind apparatus 4, such as, extraneous air is thermally formed temperature required hot blast by heater, afterwards by the blower fan cavity by direct for hot blast suction body of heater 1.
As further preferred embodiment, also including air distribution device 15, the gas outlet of air distribution device 15 is connected to second pipe 16, is used for introducing external air in second pipe 16, mixes with the hot gas in second pipe 16. Now mainly prevent the hot gas temperature being delivered in body of heater 1 cavity to wind apparatus 4 too high, body of heater 1, shaft 6 and blade 7 are produced impact, reduce the hot gas of excessive temperature by introducing extraneous cold air in second pipe 16, form temperature required hot gas.
As preferably, air distribution device 15 can include blower fan, and blower fan is by the extraneous direct suction second pipe 16 of air according to demand;As long as or extraneous air can be delivered to the device in second pipe 16 by prior art or equipment can. Again, it is preferred to arrange the detector of a volume content that can detect in outside air entrance second pipe 16 in air distribution device 15, in time the gas flow entered in second pipe 16 is tested, it is simple to the need of opening air distribution device 15.
As more preferably preferred embodiment, also including dust arrester 9, dust arrester 9 includes cyclone cylinder, and cyclone cylinder has the second air inlet the 91, second gas outlet and the 3rd gas outlet 92. Wherein, second air inlet 91 is connected to the first gas outlet 14, and the second gas outlet is in communication with the outside, and the 3rd gas outlet 92 is connected with the cavity to wind apparatus 4 by the first pipeline 10, for being mixed with to the hot gas in wind apparatus 4 by the gas after dedusting, form the hot gas of required moisture content.
Specifically, after material is dried in body of heater 1, through the second air inlet 91, the gas in body of heater 1 and after material-heat-exchanging is introduced in cyclone cylinder; Under the effect of blower fan, gas spin in cyclone cylinder rise motion, in uphill process, the solid particle contained in gas and liquid are got rid of on the internal face of cyclone cylinder, under the effect of self gravitation, solid particle and liquid deposition are in the bottom of cyclone cylinder; And get rid of solid particle, liquid a part of gas through the second gas outlet directly discharged to outside air, another part gas is then transported in the cavity to wind apparatus 4 through the 3rd gas outlet 92, mix with to the hot gas in wind apparatus 4 cavity, portion gas after dedusting is recycled, reduces the heat required for heating hot gas.
In addition, in gas after dedusting, moisture content is typically in 20%-30%, and it is almost 0% to the moisture content of hot gas in wind apparatus 4, the dedusting gas that moisture content is 20%-30% is introduced in wind apparatus 4, mix with dry hot gas, to form the hot gas that moisture content is 6%-15%, this hot gas is introduced in body of heater 1 with the efficiency of material-heat-exchanging and effect, than the dry hot gas that moisture content is 0% introduced in body of heater 1 with the efficiency of material-heat-exchanging and better effects if. Because, containing a small amount of moisture in hot gas, under equivalent environment, specific heat of water holds the specific heat capacity more than air, and during dry same amount of material, the heat required for water is less, thus reducing the heat that dried material needs, improving drying efficiency, but the moisture content in hot gas is unsuitable too high, too high rear heat exchange efficiency can decline on the contrary, then, the optimum moisture content of hot gas controls at 6%-15%.
For the charging gear 2 in above-mentioned embodiment, material-receiving device 3. Wherein, charging gear 2 is preferably batcher of the prior art, for instance elevator, and is arranged on the hopper on charging aperture 11, and the feed opening of elevator faces toward or extend in hopper can. Material-receiving device 3 is preferably conveying worm, or belt conveyor and chain transfer, or is directly arranged below a discharging bin at discharging opening 12.
As the charging aperture 11 offered on body of heater 1, discharging opening the 12, first air inlet 13 and the first gas outlet 14 preferred embodiment, as shown in Figures 2 and 3, charging aperture 11 is opened on body of heater 1 sidewall radially, discharging opening 12 be opened in body of heater 1 in Z-direction bottom outer wall on, first air inlet 13 is opened in the top exterior walls in Z-direction of the body of heater 1 near charging aperture 11 place, first gas outlet 14 is opened in the body of heater 11 top exterior walls in Z-direction, and relative with the position of discharging opening 12.
In a word, the material handling system of the present embodiment, when to dry materials, first the performance according to material, the parameters such as such as moisture content, size, degree of drying, adjust the spacing between blade 7 and body of heater 1 inwall, the angle that blade 7 is arranged, and spacing between adjacent two peripheries in the second rotating shaft 5 in shaft 6 surface thereof; And the amount according to the hot gas added in the amount of material, introducing body of heater 1, calculate material in body of heater 1, stop the degree of drying that how long just can reach necessary requirement, and test repeatedly can be passed through, draw the optimized parameter that each material is dried, thus preparing the drying oven of relevant parameter and there is the material handling system of this drying oven.
Certainly, as deformation, it is also possible to omit the first air inlet 13, and only by puff prot air inlet.