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Vacuum distillation Process Flowsheets & Simulations

Explore 2 validated, solved Vacuum distillation simulation flowsheets in MaximaLabs — real components: methyl_palmitate, methyl_stearate, methanol, water, lactic_acid, methyl_lactate. Open any one directly in your browser.

Solved via: PENG-ROBINSON, PSRK.

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Oleochemicals plant, Port Klang, Malaysia

Fatty-ester vacuum fractionation

Biodiesel methyl esters (C₁₆ / C₁₈) split at 0.05 bar — vacuum keeps the bottoms under 515 K; near-total C₁₆ recovery overhead and ~98% C₁₈ in the bottoms (the two components' relative volatility caps bottoms purity there — more stages/reflux do not push it further). From the ChemSep casebook (Fatty_Acids, as methyl esters).

4 unit ops • PENG-ROBINSON

221 0

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Methyl Lactate Product
Reference model (CN104628563A)

Patent benchmark: methyl lactate synthesis (CN104628563A)

Real patent replication, not an invented process: CN104628563A's acid-catalyzed lactate-ester route — lactic acid esterified with excess methanol, then purified by vacuum distillation — reproduced here as a continuous flowsheet. The patent's own worked methyl-lactate example reports 98.8% esterification conversion and 99.6% product purity at 120 degC/3h. This flowsheet's reactor conversion is set directly to the patent's reported 98.8% (not fitted); the vacuum column (0.2 atm, matching the patent's vacuum-distillation purification step) then splits the methanol and reaction water off the ester completely — zero methyl lactate leaves overhead — and delivers 97.8 mol% methyl lactate in the bottoms at 389.9 K. The property method is the whole story here, exactly as it was on the sulfolane extractive column. Written on Peng-Robinson, this example did not converge at all: every pair in a methanol / water / lactic-acid / methyl-lactate mixture is hydrogen-bonding, which van der Waals mixing cannot represent, and the column returned a partial profile carrying 2.60 mol/s of methyl lactate out of a column fed 1.98 — 32% more product than the reactor made, a 0.26 component-balance residual. (That wrong profile is where this example's previously-published 98.75% purity was read from; the number was retracted at the test level and is now corrected here.) A plain activity model cannot be used either, for a data reason rather than a physics one: neither lactic acid nor methyl lactate carries a regressed ideal-gas-Cp correlation, and the gamma-phi enthalpy path raises on that where a cubic quietly falls back to a corresponding-states estimate. PSRK is a cubic whose mixing is driven by UNIFAC, so it has both — and it converges to a 2.7e-06 component-balance residual, with methyl lactate and lactic acid each leaving in exactly the amount the reactor made.

5 unit ops • PSRK

223 0

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