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Extractor pressure(top), kgf/cm2 1.5
Extractor temperature, ℃
Bottom -18
Middle -20
Top -22
Solvent/feed ratio (vol./vol.) 1
Typical yield pattern
Product ATF Run Kerosene Run
Raffinate 58 63
Extract 41 36
Loss 1 1
Extractor pressure(top), kgf/cm2 8.4
Extractor temperature, ℃ 143
Solvent to Feed ratio (vol./vol.) 4.7
Solvent Composition
(a) % of triethylene glycol 92
(b) % of water 8
Typical yield pattern
Product Yield
Benzene 38
Toluene 14
Raffinate 47
C8 bottom + loss 1
SOLVENT EXTRATION PROCESSES
SOLVENT EXTRATION PROCESSES
SOLVENT EXTRATION PROCESSES

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SOLVENT EXTRATION PROCESSES

  • 1.
  • 2.
  • 3.
  • 4.
  • 5. Extractor pressure(top), kgf/cm2 1.5 Extractor temperature, ℃ Bottom -18 Middle -20 Top -22 Solvent/feed ratio (vol./vol.) 1 Typical yield pattern Product ATF Run Kerosene Run Raffinate 58 63 Extract 41 36 Loss 1 1
  • 6.
  • 7.
  • 8. Extractor pressure(top), kgf/cm2 8.4 Extractor temperature, ℃ 143 Solvent to Feed ratio (vol./vol.) 4.7 Solvent Composition (a) % of triethylene glycol 92 (b) % of water 8 Typical yield pattern Product Yield Benzene 38 Toluene 14 Raffinate 47 C8 bottom + loss 1

Editor's Notes

  1. Flash drum operate at 2 kgf/cm2 extractor pressure 8.4kgf/cm2