Drying process and equipment suitable for materials with large particle size difference and high requirements on product moisture content uniformity
A technology of particle size and moisture content, which is applied in the directions of drying solid materials, drying gas layout, lighting and heating equipment, etc., can solve problems such as difficulty in discharging bulk materials, inconsistent drying degree, and product moisture content not meeting the requirements, etc. Achieve uniform moisture content, prolong drying time and save energy.
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Embodiment 1
[0068] In a horizontal multi-chamber fluidized bed dryer with a specification of 700×100mm, in the structure of a gas distribution plate, the included angles between the direction of the airflow blown out from the nail hole and the direction of material movement on the upper and lower sides are α and β respectively. , α=β=150°. The nail holes on the gas distribution plate are arranged in ABAB mode. When the opening rate is 3%, the average residence time of particles with a particle size of 0.5~1.0mm and 1.6~2.5mm is 20.2min and 27.6min, respectively.
[0069] Thermal model experiments were carried out with molecular sieves, the net bed height was 80mm, the inlet air temperature was 150°C, and the fluidization gas velocity was 1.16m / s. The initial moisture content of the wet material is 21.08%. After drying for 20.2 minutes, the moisture content of particles with a particle size of 0.5-1.0 mm is 5.63%, and after drying for 27.6 minutes, the moisture content of particles with a ...
Embodiment 2
[0071] In a horizontal multi-chamber fluidized bed dryer with a specification of 700×100mm, in the structure of a gas distribution plate, the included angles between the direction of the airflow blown out from the nail hole and the direction of material movement on the upper and lower sides are α and β respectively. , α=β=30°. The nail holes on the gas distribution plate are arranged in ABAB mode. When the opening rate is 3%, the average residence time of the particles with a particle size of 0.5~1.0mm and 1.6~2.5mm is 17.1min and 10.4min, respectively.
[0072] Thermal model experiments were carried out with molecular sieves, the net bed height was 80mm, the inlet air temperature was 150°C, and the fluidization gas velocity was 1.16m / s. The initial moisture content of the wet material is 21.08%, and the moisture content of the particles with a particle size of 1.6-2.5 mm measured after drying for 10.4 minutes is 12.32%; the moisture content of particles with a particle size o...
Embodiment 3
[0074] The process flow chart of the drying system for the initial heat softening and sticky materials, see Figure 7 .
[0075] The wet material is continuously fed into the first chamber of the horizontal multi-chamber fluidized bed dryer 02 through the screw feeder 01, and enters the primary drying section, drying section, and cooling section in turn under the action of the drying medium for fluidization, drying, and drying. After cooling, it enters the dust separation system 02-9 to separate the powder, and the dried product is discharged from the product outlet 02-11, discharged through the star discharger 03, screened by the sieving machine 04, and packaged for storage.
[0076] The drying medium is air, which enters the horizontal multi-chamber fluidized bed dryer 02 in five ways, one way is the air for the post-drying section; the second way is the air for the cooling section and the dust separation system; the third way is the air for the agglomerate crushing and sepa...
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