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IMPELLER TYPE ¼³Ä¡Á¶°Ç ¹× Ä¡¼ö FLOWÀÇ ÇüÅÂ
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PROPELLER

d/D=0.15¢¦0.4
H1/D=0.25¢¦0.35
H/D=0.8¢¦1.2
B/D=0.08¢¦0.12
Ne=0.35
∙ AXIAL
∙ 3¢¦4BAFFLE
∙ 1,000cp
∙ 2¢¦15m/sec
BLENDING
SUSPENSION
DISPERSION OF SOLID
CIRCULATION/PUMPING
DISSOLVING
PITCHED PADDLE

d/D=0.2¢¦0.5
H1/D=0.1¢¦0.3
H/D=0.8¢¦1.2
B/D=0.08¢¦0.12
Ne=0.5¢¦1.9
∙ AXIAL-RADIAL
∙ 2¢¦4BAFFLE
∙ 10,000cpÀÌÇÏ
∙ 3¢¦10m/sec
BLENDING
SUSPENSION
DISPERSION OF SOLID
HEAT TRANSFER
DISSOLVING
FLAT TURBIN

d/D=0.2¢¦0.5
H1/D=0.1¢¦0.4
H/D=0.8¢¦1.2
B/D=0.08¢¦0.12
Ne=4.6
∙ RADIAL
∙ 2¢¦4BAFFLE
∙ 10,000cpÀÌÇÏ
∙ 3¢¦7m/sec
DISPERSION-L/L
GASSING
(HIGH SHEAR RATES)
HEAT TRANSFER
DISSOLVING
PITCHED TURBIN

d/D=0.25¢¦0.5
H1/D=0.1¢¦0.3
H/D=0.8¢¦1.2
B/D=0.08¢¦0.12
Ne=1.5¢¦1.9
∙ AXIAL-RADIAL
∙ 2¢¦4BAFFLE
∙ 10,000cpÀÌÇÏ
∙ 2¢¦10m/sec
BLENDING
DISPERSION-L/L
DISPERSION-L/S
SUSPENSION
HEAT TRANSFER
DISSOLVING
DISPERSED TURBIN

d/D=0.1¢¦0.3
H1/D=0.3
H/D=0.8¢¦1.2
B/D=0.08¢¦0.12
Ne=0.65
∙ RADIAL
∙ 2¢¦4BAFFLE
∙ 10,000,000cpÀÌÇÏ
∙ 8¢¦10m/sec
DISPERSION-L/L
DISPERSION-L/S
(HIGH SHEAR RATES)
EMULSION
ANCHOR

d/D=0.7¢¦0.9
H1/D=0.8¢¦1.0
H/D=0.8~1.2
B/D=0.08¢¦10.12
Ne=50
∙ RADIAL
∙ 100,000cp
∙ 2m/sec ÀÌÇÏ
REACTION
BLENDING
(HIGHVISCOUS LIQUIDS)
HELICAL RIBBON

d/D=0.8¢¦0.95
S/d=0.5
H/D=0.85¢¦1.2
G/D=0.05¢¦0.1
Ne=440
∙ AXIAL FORCED
  CIRCULATION
∙ 500,000cp ÀÌÇÏ
∙ 8¢¦10m/sec
REACTION
BLENDING
(HIGHVISCOUS LIQUIDS)


 

 
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