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πŸ§ͺ Extraction Equipment

Solvent Extraction Plant

Recover every last drop of oil from pre-pressed cake and oilseeds using food-grade hexane. Achieve residual oil below 0.5% in De-Oiled Cake β€” the most efficient extraction technology available for large-scale operations.

Hexane ExtractionDTDC System50–1000 TPDSolvent Recovery 99.9%
πŸ“‹ Request a QuoteView Specifications ↓
50–1000
TPD Capacity
<0.5%
Residual Oil
in DOC
99.9%
Solvent Recovery
50+
Years Exp.
TurnkeyATEX SafeSince 1972
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Capacity
50 – 1000 TPD
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Solvent Used
n-Hexane / HFHS
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Residual Oil in DOC
< 0.5%
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Solvent Recovery
99.9%+

Maximum Oil Recovery with Solvent Extraction

Mini Solvent Extraction Plant: Seed-cake, low oil content oil seeds and other low oil content materials are not preferable to process through mechanical pressing.

These oil bearing materials (OBM) can be processed in a Solvent Extraction Plant (SEP) to extract the remaining amount of oils efficiently. Our SEP setup is suitable to handle up to 20% oil content OBM and produce final materials called De-Oiled Cake (DOC) with less than 0.2% oil content. We can fabricate complete setups from 200 Tons per day to 1,000 Tons per day in OBM processing capacities.

SEP Setup β€” Four Sections

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1. Preparatory Section
OBM should be in smaller particle size which allows solvent to pass through and dissolve oil from the remaining materials. OBMs received from Oil Mill are in big chunks which need to be broken down into small pieces (3–5 mm) prior to extraction. This is done by passing OBM through a series of Spike and Fluted rolls of variable sizes and shapes.
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2. Extraction Section
Prepared OBM is fed into the extraction unit where a continuous moving belt carries the material while a constant flow of solvent is sprayed from the top of the material bed. Solvent percolates through the material bed, absorbing and dissolving oil, and leaves the extractor as an oil-solvent mixture called miscella.
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3. Distillation Section
Miscella is transferred to a distillation vessel which operates under vacuum at 90–110Β°C, creating conditions to evaporate hexane from the oil. The hexane vapour is condensed and recovered for reuse back in the Extraction Section, achieving over 99.9% solvent recovery.
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4. DOC Preparatory Section β€” De-Solventiser Toaster (DT)
Extracted De-Oiled Cake carries solvent and is typically wet when leaving the Extraction Section. DOC is fed into the DT vessel through a solvent-tight redler conveyor. The DT is essentially a vertical pan stack cooker with limpet coils having multiple stages. Certain OBM like Soya DOC requires a toasting humidifier to destroy urease activity. Finally, DOC passes through a dehumidifier to maintain the correct moisture content.

Why Add Solvent Extraction? For a 100 TPD groundnut pressing operation, an SEP can recover an additional 5–7 tonnes of oil per day β€” typically paying back the full SEP investment within 18–24 months.

Engineering Highlights

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Counter-Current Extraction Design
Fresh solvent always contacts near-exhausted meal β€” maximising oil recovery while minimising solvent usage.
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Closed-Loop Solvent Recovery System
Multi-stage condensation with chilled water cooling recovers 99.9% of hexane.
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Multi-Effect Evaporation with Heat Integration
Two-effect distillation design saves 20–25% steam over single-effect designs.
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ATEX-Compliant Explosion-Proof Design
All electrical equipment in solvent zones is ATEX Zone 1/Zone 2 rated with automatic hexane detection.

Detailed Specifications

ParameterSpecification
Capacity Range50 TPD – 1000 TPD OBM
Solvent Typen-Hexane (60–62Β°C BP) / HFHS
Extractor TypeLoop Belt / Rotocel (as per capacity)
Solvent-to-Meal Ratio1.2 – 1.5 : 1
Residual Oil in DOC< 0.5% (on dry basis)
Hexane in Extracted Oil< 50 ppm
Solvent Recovery> 99.9%

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Recover More Oil. Earn More Profit.

Every tonne of press cake you process through a Shradhha SEP recovers 4–7.5 kg of additional oil. Get your ROI analysis and free technical consultation today.

πŸ“‹ Get Free Proposal & ROI AnalysisπŸ“ž Call: +91 94274 23780