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DLG-B series inert particle fluidized bed drier
 
 

Features
◆Compact structure, occupied small area, high evaporated strength in unit area
◆Continuous operation, can meet large-scale production;
◆Wide suitable field, fine and uniform material of finished product.
Flow chart and its principle of work
A type flow chart(slurry material)
B type flow chart(liquid material)

Flow chart and its principle of work

A type chart(slurry material )

Technical Parameters

Item DLG-B -5 DLG-B -20 DLG-B -50 DLG-B -100 DLG-B -200 DLG-B -350 DLG-B -500
Evaporated amount of moisture kg/h 5-8 16-24 50-80 80-150 160-260 280-420 410-600

Temperature of air in °C

120-220 120-220 120-220 120-220 120-220 120-220 120-220

Temperature of air out°C

60-85 60-85 60-85 60-85 60-85 60-85 60-85

Evaporated amount of moisture kg/h

10-15 30-45 90-160 150-280 310-450 500-780 800-1000

Temperature of air in °C

300-500 300-500 300-500 300-500 300-500 300-500 300-500

Temperature of air out°C

85-185 85-185 85-185 85-185 85-185 85-185 85-185

equipped power kg/h

3.75 5.1 9 15 22 30 37

Application
◆This technology is suitable for: drying different solution, suspended liquid of dyestuff, pigment, agrochemicals, biochemical product, soybean milk(powder-
making), humic acid, immersed paste of Chinese traditional medicine, pesticide, lignin, pectase as well as paste material, thin slurry, filtered cake and
making it become powder.
◆Dust catcher: may choose pulse cloth bag dust catcher or damp spray dust catcher as secondary dust catcher in accordance with the feature of material.
◆Heating mode: it is considered to choose and use steam, electricity or hot air furnace as heat source in accordance with the condition possessed by the factory
and temperature undertaken by material.
◆Typical materials to be dried: iron oxide red, iron oxide black, yeast powder, kieselgur, titanium pigment, starch, calcium carbonate, sodium nitrite, humic
acid, barium sulfate, aluminum carbonate, immersed paste of Chine traditional medicine, water reducing agent of concrete, potato slurry, etc.

Comparison between inert particle fluidized bed and atomizing drier

Item inert particle fluidized bed atomizing drier
Volume of drying tower 0.05 1.0
Need air amount 0.6 1.0
Need heat amount 0.7 1.0
Need power 1.0 1.0
State of product decline powder grain
Supplying mode of material slurry Micro powder granule
Volume evaporation strength kg water m3.h 50-500 2.5
coefficient of the thermal capacity KJ/m3.h 8000-24000 200-400
 
 
 
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