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XSG series rotary flash dryer

Overview:Working principle The hot air enters the bottom of the dryer tangentially, and is driven by the agitator to form a powerful rotating wind field. The paste material enters the dryer from the screw feeder. Under the strong action of the high-speed rotat…

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Working principle

The hot air enters the bottom of the dryer tangentially, and is driven by the agitator to form a powerful rotating wind field. The paste material enters the dryer from the screw feeder. Under the strong action of the high-speed rotating stirring blade, the material is dispersed under the action of impact, friction and shearing force. The block material is quickly crushed, fully contacted with hot air, and heated ,dry. The dehydrated dry material rises with the hot air flow, and the grading ring traps large particles, and the small particles are discharged from the center of the ring to the outside of the dryer and recovered by the cyclone separator and dust collector. The incomplete or large materials are thrown to the wall by centrifugal force. , And fall to the bottom to be crushed and dried.


Schematic

Schematic diagram of flash dryer structure
Performance characteristics

◎The organic combination of swirling, fluidization, spouting and crushing classification technology.

◎Compact equipment, small size, high production efficiency, continuous production, realizing "small equipment, large production".

◎High drying strength, low energy consumption and high thermal efficiency.

◎The material residence time is short, the finished product is of good quality, and it can be used for drying heat sensitive materials.

◎Negative pressure or micro-negative pressure operation, good airtightness, high efficiency, eliminating environmental pollution.


Adapt to materials

Organic matter: Atrazine (pesticides), lauric acid, benzoic acid, benzoic acid, bactericide, sodium oxalate, cellulose acetate, organic pigments, etc.
Dyestuffs: anthraquinone, black iron oxide, indigo pigment, butyric acid, titanium hydroxide, zinc sulfide, various azo dye intermediates.


Inorganic substances: borax, calcium carbonate, hydroxide, copper sulfate, iron oxide, barium carbonate, antimony trioxide, various metal hydroxides, various heavy metal salts, synthetic cryolite, etc.


Food: soy protein, gelatinized starch, wine tank, wheat sugar, wheat starch, etc.


Technical specifications


Model XSG-2 XSG-4 XSG-6 XSG-8 XSG-10 XSG-12 XSG-16 XSG-20
Host inner diameter mm 200 400 600 800 1000 1200 1600 2000
Air volume M3/h 350-500 1150-2000 2450-4500 4450-7550 7000-12500 10000-20000 18000-36000 28200-56500
Evaporated water kg/h 12-17 40-70 80-150 150-250 230-450 300-600 600-1000 1000-1500
Installed capacity kw 10 20 40 65 85 105 150 230
Maximum height m 4.0 4.8 5.8 6.5 7.1 7.8 8.8 10.1
Area m2 15 20 28 35 40 52 80 150


Note: 1. The amount of water evaporation is the water evaporated per hour when the inlet air temperature is 180oC and the outlet air temperature is 80oC.


  2. In addition to the above models, special designs can be made for users,


  3. The above installed capacity is a standard package, and the power package can be significantly reduced according to different materials.

Processing materials and characteristics (based on type 6 flash evaporation)

Material name Stearic acid Aluminum hydroxide Zinc carbonate Insecticide list TMTD DSD acid Iron Oxide Red Antimony Dioxide Cuprous chloride White too black
Inlet air temperature oC 150 180 150 120 140 150 200 180 200 280
Initial moisture content % 80 55 80 30 65 60 60 45 30 85
Final moisture content % 0.5 1.5 1.0 1.0 0.5 0.5 0.5 1.0 3.0 5.0
Actual drying capacity kg/h 140-160 250-280 130-170 80-110 80-120 80-120 300-350 280-320 290-310 250-300

 

Material name Accelerator

Oil-soluble

ink

Manganese

zinc oxide

Phthalocyanine

Blue

Calcium

Citrate

Superfine

calcium

 carbonate

Mud treatment

agent

Sodium

Dioxyisocy-

anurate

Sodium

trioxyisocy-

anurate

Inlet air

temperature oC

150 150 120 150 140 160 200 180 150

Initial moisture

content %

60 45 30 55 40 70 75 25 30

Final moisture

content %

0.5 2.0 1.0 1.0 1.0 1.5 5.0 0.2-2 1.0

Actual drying

capacity kg/h

80-110 350-380 120-150 160-180 300-350 430-470 290-310 80-120 90-150
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