Separate Penicillin G from Glucose

Separation strategy for Penicillin G (334 Da) from Glucose (180 Da) using Liquid-Liquid Extraction.

Recommended technique

Liquid-Liquid Extraction Best Match

Separation handle: Hydrophobic small molecule recovery.

Scope: Partition coefficient. CAPEX range: $200k-$1.5M.

Property comparison

PropertyPenicillin GGlucose
Molecular weight334.4 Da180.16 Da
Solubility (water)210 g/L909 g/L
Charge-10
Isoelectric point
pKa2.7612.28
Density1.41 g/cm³1.54 g/cm³
Diffusion coefficient4.80e-06 cm²/s6.73e-06 cm²/s
Log P1.83-3.24

Process design walkthrough

1

Define your feed stream

Set Penicillin G and Glucose as components with their concentrations and physical properties. Use the molecule database to auto-populate properties.

2

Drop in Liquid-Liquid Extraction

Connect the feed inlet, configure operating parameters (MWCO, pH, eluent, residence time as relevant), and connect the two outlets to product and waste streams.

3

Run the simulation

untangle.bio calculates outlet concentrations using mass balance and the separation function for this technique. Iterate on parameters to optimise yield vs purity.

4

Add polishing if needed

If the single step doesn't meet your purity spec, add a second separation with a complementary handle (e.g., size after charge, hydrophobicity after size).

Frequently Asked Questions

Why is Liquid-Liquid Extraction the right choice for this pair?

Liquid-Liquid Extraction exploits hydrophobic small molecule recovery as the separation handle. The property gap between Penicillin G and Glucose on this axis is large enough to give a clean separation in a single step at industrially relevant flow rates.

What yield and purity can I expect?

Typical single-step recovery is 85-99% depending on operating conditions. Purity from a single liquid-liquid extraction step is in the 90-99% range; polishing steps push above 99.5%.

What does this step cost to operate?

Capital cost for Liquid-Liquid Extraction at biotech scale is in the $200k-$1.5M range. Operating cost depends on scale, feed concentration, and product value. See the technique page for details.

How do I design this in untangle.bio?

Drop a liquid-liquid extraction unit operation into the flowsheet, connect the feed stream containing both Penicillin G and Glucose, and the simulator will calculate mass balance and expected outlet concentrations using the molecule database properties.

Design this separation in untangle.bio

Build a flowsheet, simulate yield and purity, and estimate CAPEX for separating Penicillin G from Glucose.

Open untangle.bio

Related pages

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