
Olive Pomace Hydroxytyrosol and Oil Extract

Olive Pomace Hydroxytyrosol and Oil Extract
Extraction Technologies
Mechotech designs and manufactures turnkey extraction plants that process olive pomace to recover hydroxytyrosol and olive oil. We supply the machinery for the route selected after screening — raw-material preparation, extraction, separation, concentration or recovery, and drying or collection — configured to the target specification. Mechotech's technology screening assigns routes by target — hydroxytyrosol: Counter-Current (CCE), Ultrasound (UAE), Hybrid and Microwave (MAE); olive oil: Supercritical CO₂ (SCFE); the best-ranked route overall is Supercritical CO₂ Extraction (SCFE) (high-priority screening, rank 1 of 100).
For olive pomace with hydroxytyrosol and olive oil as the target, there are 5 candidate technologies: Counter-Current Extraction (CCE), Supercritical CO₂ Extraction (SCFE), Ultrasound-Assisted Extraction (UAE), Hybrid Extraction and Microwave-Assisted Extraction (MAE). By route — Counter-Current (CCE) for hydroxytyrosol: high-priority screening, rank 3 of 100, ethanol/water or suitable food-grade solvent; Supercritical CO₂ (SCFE) for olive oil: high-priority screening, rank 1 of 100, CO₂; optional ethanol modifier; Ultrasound (UAE) for hydroxytyrosol: high-priority screening, rank 3 of 100, ethanol/water or water; Hybrid for hydroxytyrosol: high-priority screening, rank 3 of 100, sequence selected by target; Microwave (MAE) for hydroxytyrosol: high-priority screening, rank 3 of 100, ethanol/water or water. For the best-ranked route, Supercritical CO₂ (SCFE), the screening flags: nonpolar fraction preferred; polar targets may need modifier and separate validation. These are screening candidates rather than guarantees: the final technology, operating parameters and plant configuration are established during process development and pilot validation. Product-contact parts are built in SS 316L with CIP-cleanable design, and automation is configured to the project.
Technical Specifications
| Product | Olive Pomace Hydroxytyrosol and Oil Extract Plant |
|---|---|
| Feedstock | Olive pomace |
| Part / Feed Form | Pomace |
| Target Extract | Hydroxytyrosol and olive oil |
| Extraction Method | Counter-current, CO2, UAE, Hybrid, MAE |
| Technology Count | 5 |
| Product-contact Material | SS 316L, electropolished, CIP-cleanable |
| Automation | PLC-SCADA, configured to requirement |
Plant Capacities
| Plant Scale | Pomace Throughput | Typical Use |
|---|---|---|
| Pilot | Configured to your feedstock and trial plan | Product development, parameter validation |
| Semi-Commercial | Configured to raw-material supply and buyer volume | Contract manufacturing, scale-up trials |
| Commercial | Configured to raw-material supply and confirmed buyer volume | Commercial production at confirmed buyer volume |
Capacity is configured to raw-material supply and confirmed buyer volume; we recommend a pilot plant to validate process parameters before scaling. No fixed throughput is quoted for this product.
Manufacturing Process
Each extraction method follows a different process — pick a method to see its steps.
Raw-Material Preparation
Olive pomace is cleaned and size-reduced so hydroxytyrosol can be reached by the extraction medium; particle size and moisture are set during process development.
Counter-Current Loading
Prepared olive pomace is fed into a multi-stage solid–liquid counter-current extractor where fresh ethanol/water or a suitable food-grade solvent meets the most-depleted material.
Counter-Current Extraction
Solvent flows against the solids across stages to draw out hydroxytyrosol; bed flow and fines management are verified during pilot work.
Extract (Miscella) Collection
The hydroxytyrosol-bearing miscella is collected from the fresh-feed end while spent solids are discharged from the solvent-entry end.
Concentration & Solvent Recovery
Solvent is removed from the clarified hydroxytyrosol-bearing extract under vacuum and returned through a solvent-recovery loop; recovery performance is confirmed at pilot scale.
Standardisation & Drying
The hydroxytyrosol extract is assayed against the declared target specification and dried or supplied as a concentrate, according to the requirement.
Raw-Material Conditioning
Olive pomace is cleaned and conditioned so olive oil is accessible to supercritical CO₂; moisture and particle size are set during process development.
Extraction Vessel Loading
Conditioned olive pomace is charged into the high-pressure extraction vessel.
Supercritical CO₂ Extraction
Supercritical CO₂ passes through the charge and dissolves olive oil; an ethanol modifier can be evaluated where polar fractions are also required, and operating pressure and temperature are set in process development.
Separator Collection
Pressure is reduced in separator stages so the extracted olive oil drops out of the CO₂ and is collected.
CO₂ Recycle
Gaseous CO₂ is re-liquefied and recirculated to the extractor, limiting make-up gas demand.
Finishing & Packing
The collected olive oil is polished by filtration as needed and packed to the required specification.
Raw-Material Preparation
Olive pomace is cleaned and size-reduced so hydroxytyrosol can be reached by the extraction medium; particle size and moisture are set during process development.
Slurrying
Prepared olive pomace is slurried with ethanol/water or water in the extraction vessel.
Ultrasonic Cavitation
Ultrasound creates cavitation that disrupts the plant matrix and speeds release of hydroxytyrosol; probe intensity, temperature and filtration behaviour are piloted.
Separation
Spent solids are separated by filtration or centrifugation and the extract is clarified before concentration.
Concentration & Solvent Recovery
Solvent is removed from the clarified hydroxytyrosol-bearing extract under vacuum and returned through a solvent-recovery loop; recovery performance is confirmed at pilot scale.
Standardisation & Drying
The hydroxytyrosol extract is assayed against the declared target specification and dried or supplied as a concentrate, according to the requirement.
Raw-Material Preparation
Olive pomace is cleaned and size-reduced so hydroxytyrosol can be reached by the extraction medium; particle size and moisture are set during process development.
Stage Sequence Selection
A deliberate combined extraction train is used: the sequence of stages is selected for hydroxytyrosol in pilot screening and each stage is designed separately.
First Assisted Stage
The first stage releases hydroxytyrosol from the prepared feed under controlled conditions set for that stage.
Second / Combined Stage
The second stage completes recovery of hydroxytyrosol from the partially extracted material; stage conditions are optimised separately.
Separation & Concentration
Spent solids are removed and the combined extract is clarified and concentrated; solvent is recovered where a solvent is used.
Standardisation & Drying
The hydroxytyrosol extract is assayed against the declared target specification and dried or supplied as a concentrate, according to the requirement.
Raw-Material Preparation
Olive pomace is cleaned and size-reduced so hydroxytyrosol can be reached by the extraction medium; particle size and moisture are set during process development.
Medium Mixing
Prepared olive pomace is mixed with ethanol/water or water in the microwave extraction vessel.
Microwave Heating & Extraction
Controlled microwave heating drives hydroxytyrosol out of the prepared feed in a short cycle; heating, moisture, solvent safety and temperature-sensitive targets are controlled, with limits set during process development and pilot validation.
Separation
Spent solids are separated by filtration or centrifugation and the extract is clarified before concentration.
Concentration & Solvent Recovery
Solvent is removed from the clarified hydroxytyrosol-bearing extract under vacuum and returned through a solvent-recovery loop; recovery performance is confirmed at pilot scale.
Standardisation & Drying
The hydroxytyrosol extract is assayed against the declared target specification and dried or supplied as a concentrate, according to the requirement.
Major Plant Equipment
- Raw-material cleaning and size-reduction system
- Multi-stage counter-current extractor
- Solvent storage tanks and transfer pumps
- Ultrasonic extraction vessel with transducer system
- Combined extraction train (stage equipment per the sequence selected during process development)
- Microwave extraction vessel with temperature and safety controls
- Supercritical CO₂ extraction vessels
- CO₂ pump, heat exchangers and chiller
- Separator vessels
- CO₂ recovery / recycle system
- Optional ethanol-modifier dosing skid
- Filtration / centrifugation system
- Vacuum evaporator
- Solvent recovery system with condensers
- Dryer (where a dried form is specified)
- CIP (clean-in-place) system
- Storage and finished-product tanks
- PLC-SCADA control panel and instrumentation
Plant Output
Applications
- Pharmaceutical standardised ingredient supply — Olive Pomace Hydroxytyrosol and Oil Extract
- Nutraceutical capsule, tablet, and supplement manufacturing — Olive Pomace Hydroxytyrosol and Oil Extract
- Food and beverage applications — Olive Pomace Hydroxytyrosol and Oil Extract
- Cosmetic and personal care active ingredients — Olive Pomace Hydroxytyrosol and Oil Extract
- Export to regulated-market ingredient buyers — Olive Pomace Hydroxytyrosol and Oil Extract
Key Features
Supercritical CO₂ (SCFE) — High-Priority Screening Fit
Best-ranked route for olive pomace: rank 1 of 100 in Mechotech's supercritical CO₂ extraction screening, using CO₂; optional ethanol modifier. Ranks are directional screening priorities, not measured yield, ROI or plant guarantees.
Olive pomace — 5 Candidate Routes
Routes screened for olive pomace: Counter-Current (CCE) — high-priority, rank 3; Supercritical CO₂ (SCFE) — high-priority, rank 1; Ultrasound (UAE) — high-priority, rank 3; Hybrid — high-priority, rank 3; Microwave (MAE) — high-priority, rank 3. Each route has its own process tab above.
2-Target Scope
Targets are assigned to routes in the screening — hydroxytyrosol: Counter-Current (CCE), Ultrasound (UAE), Hybrid and Microwave (MAE); olive oil: Supercritical CO₂ (SCFE) — so each route’s steps name only the target it is screened for.
Parameters Fixed After Pilot Trials
Recovery of hydroxytyrosol and olive oil, selectivity, solvent or water duty, quality and cleaning are measured in pilot trials, starting with small-scale feed trials, before final plant parameters are fixed.
SS 316L Hygienic Construction
Product-contact surfaces are SS 316L and CIP-cleanable, in a hygienic design suited to food, nutraceutical and pharmaceutical supply chains; PLC-SCADA automation with recipe control can be configured to the project scope.
Frequently Asked Questions
What is an olive pomace extraction plant for hydroxytyrosol and olive oil?
Which plant part or feed form does the olive pomace plant process?
Which extraction technologies are suitable for olive pomace?
How does Mechotech's screening rank the candidate routes for olive pomace?
Which technologies are screened for each target of olive pomace?
How does the olive pomace extraction process work?
What equipment does the olive pomace extraction plant include?
What output and specification can the olive pomace plant deliver?
What application areas are listed for Olive Pomace Hydroxytyrosol and Oil Extract?
Which related Mechotech extraction pages cover the same material or target?
What capacity is available and is a pilot trial recommended?
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