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Solvent production Process Flowsheets & Simulations

Explore 3 validated, solved Solvent production simulation flowsheets in MaximaLabs — real components: 2_butanol, methyl_ethyl_ketone, h2, isopropanol, acetone, water. Open any one directly in your browser.

Solved via: PENG-ROBINSON.

FEED
Dehydro
COOL
Flash
H2 Offgas
feed
dist
btms
COL
MEK Product
Butanol Bottoms
Solvents plant, Texas City, Texas, USA

Methyl ethyl ketone from 2-butanol dehydrogenation

Catalytic dehydrogenation of 2-butanol to methyl ethyl ketone (MEK) over an In/MgO catalyst, per DE2831465A1 (1978), followed by a flash to remove the H2 co-product and a distillation splitting MEK from unreacted 2-butanol.

8 unit ops • PENG-ROBINSON

17 0

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FEED
Dehydro
Scrub Water
liq
gas
gas
rich
ABS
H2 VENT
feed
dist
btms
COL
Acetone Product
Water Bottoms
Solvents plant, Texas City, Texas, USA

Acetone from isopropanol dehydrogenation

Endothermic gas-phase dehydrogenation of isopropanol (IPA) to acetone, after Luyben (Ind. Eng. Chem. Res. 2011, 50, 1206). The H2-rich reactor off-gas is scrubbed with water to recover the acetone before venting, then a column splits acetone from the water/unreacted-IPA absorbent.

8 unit ops • PENG-ROBINSON

16 0

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Meacfeed
Buohfeed
feed
dist
btms
RD
Methanol OUT
Butyl Acetate
Reference model (Luyben 2011)

Butyl acetate synthesis via reactive distillation

Methyl acetate transesterifies with n-butanol over the reactive stages of a column into butyl acetate (a common paint/coatings solvent) and methanol, which is pulled overhead as it forms while high-boiling butyl acetate collects in the bottoms. Luyben et al., Ind. Eng. Chem. Res. 2011, 50, 1247.

5 unit ops • PENG-ROBINSON

19 0

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