
Advanced Botanical Extraction Systems
Advanced botanical extraction systems use a more selective technique than plain solvent soaking, such as supercritical carbon dioxide, ultrasound, microwave, enzyme, hot-water or counter-current extraction.
Product Categories
- Herbal, Botanical & Nutraceutical Extraction(9)
- Essential Oils, Spices & Oleoresins(6)
- Fruit & Vegetable Processing(8)
- Starch, Flour, Edible Oil & Food Processing(7)
- Drying & Dehydration Systems(5)
- Evaporation, Concentration & Solvent Recovery(4)
- Pharmaceutical & Industrial Process Equipment(4)
- Cocoa, Shea, Palm Oil & Oilseed Processing(6)
- Cereals, Tubers & Sugar Processing(6)
- Specialty African Botanical & Natural Ingredients(11)
- Specialty Food, Beverage & By-Product Processing(7)
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Advanced Botanical Extraction Systems
They are chosen for higher-value botanicals where selectivity, a solvent-free product or protection of heat-sensitive compounds earns more than the extra cost. The first thing to settle is the target: which compound or fraction, how sensitive it is to heat, oxygen and cavitation, and what the finished extract must contain, because the technology follows from that. The feed is normally a dried, milled plant part of known moisture. Volume matters as much, since supercritical systems in particular need more equipment and floor area, and give lower throughput, than simple soaking. The technology, the operating pressure, any co-solvent, batch or semi-continuous operation, and the safety classification of the area decide the design and the price. Pilot trials on the actual herb are the usual way to confirm the choice before a commercial plant is specified.
Each advanced technique changes one thing about conventional extraction. Supercritical carbon dioxide, held above its critical point, dissolves oil-soluble compounds at low temperature and separates from them as a gas when the pressure is dropped; a co-solvent such as ethanol widens the range to more polar compounds. It needs high-pressure vessels, a pump, separators and chilling. Ultrasound uses cavitation to break plant cells and shorten extraction at modest temperature, but cavitation also forms reactive oxygen species that can oxidise sensitive compounds. Microwave heating warms the moisture inside the plant tissue and ruptures it from within, but can cause oxidation or thermal decomposition of secondary metabolites, so power and exposure time must be limited. Enzyme-assisted extraction breaks down cell walls in water before extraction. Subcritical water, kept liquid above its normal boiling point under pressure, acts as a less polar solvent without any organic solvent. Counter-current extraction moves herb and solvent in opposite directions, so fresh solvent meets nearly spent herb. Whichever route is chosen, the composition of the extract follows the solvent, temperature, time and drying route, so the system is specified as controlled, recorded set points and not only as vessels.
Indicative Capacity Range
- 100–5,000 kg feed/day
Key Specification Inputs
Extraction solvent/water, extraction stages, batch time, filtration and recovery.
Technical Specifications
| Technology | One of supercritical carbon dioxide, ultrasound-assisted, microwave-assisted, enzyme-assisted, subcritical-water or counter-current extraction, chosen by trials |
|---|---|
| Working Principle | Controlled pressure, temperature, energy input or enzyme action frees the target compound from the plant cell into the carrier |
| Extraction Medium | Carbon dioxide with or without an ethanol co-solvent, water, or an ethanol-water mix, set by the polarity of the target |
| Operating Mode | Batch vessels, or semi-continuous and counter-current arrangements where throughput justifies them |
| Pressure Duty | High-pressure rated vessels, pipework and relief devices for supercritical and subcritical routes; ordinary pressure for ultrasound and microwave |
| Energy Input | Ultrasonic probes or microwave applicators, sized to the batch volume and the sensitivity of the compound |
| Separation | Depressurising separators for carbon dioxide routes; filtration or centrifugation for liquid routes |
| Contact Material | Stainless steel, in pressure-rated grades for high-pressure parts, matched to the solvent in use |
| Heating and Cooling | Chilling to liquefy carbon dioxide, steam or electric heating, and cooling water |
| Automation | PLC control with set-point and trend recording, and pressure and temperature interlocks |
| Safety Design | Classified area, ventilation and ignition control where a flammable solvent is used; carbon dioxide monitoring in enclosed rooms |
Typical Process Route
Define the target and run trials
A small-scale trial on the actual herb shows which technique extracts the target compound, at what temperature, pressure or power, and for how long. This step decides the technology, so skipping it risks specifying the wrong system.
Raw material preparation
The herb is dried to an even moisture and milled to the particle size the method needs. For supercritical extraction the bed must be dry and evenly sized, because excess fines pack the bed and let the gas channel through it, and water in the bed interferes with extraction.
Charging and conditioning
Herb goes into a sealed high-pressure vessel, or into a stirred tank fitted with ultrasonic probes, a microwave applicator or an enzyme-treatment hold. On pressure vessels, closure and seal checks come first.
Controlled extraction
Pressure, temperature, solvent or gas flow, power and time are held at the set points found in the trials and logged for each batch. Drifting set points change what the extract contains, so interlocks and alarms are part of the control system.
Separation of the extract
In a supercritical system the pressure is dropped across one or more separators so that the extract falls out and the carbon dioxide returns as gas, which also lets fractions be taken at different conditions. In liquid systems the extract is filtered or centrifuged from the spent herb.
Concentration and solvent removal
Where ethanol, water or another liquid carries the extract, it is concentrated under vacuum and the solvent is condensed and collected. Water-based extracts need more evaporation energy than alcohol-based ones, which matters for fuel cost.
Drying and finishing
Concentrates are dried to powder, or oils are filtered and packed, in a way that suits the sensitivity of the compound. Heat-sensitive extracts call for vacuum or low-temperature drying, and the drying route itself changes the final composition.
Gas and solvent recovery and cleaning
Carbon dioxide is recompressed or condensed for reuse, and solvents are recovered by distillation. Vessels, separators and lines are cleaned before the next herb, because oils and resins left in separators carry over.
Process & Equipment Modules
- Feed mill and sieve
- Extraction vessels, high-pressure rated for carbon dioxide routes
- High-pressure carbon dioxide pump and heat exchangers
- Ultrasonic or microwave module for assisted routes
- Co-solvent dosing set
- Fractional separators
- Chiller and condenser for gas recovery
- Filter or centrifuge for liquid routes
- Vacuum concentrator
- Dryer for powder extracts
- Relief devices and gas detection
- PLC panel with data recording
Plant Output
Applications
- Oils, resins and carotenoid-rich fractions made without organic solvent residue
- Heat-sensitive plant actives that degrade in conventional hot extraction
- Aroma and flavour extracts closer in character to the fresh herb
- Polyphenol and flavonoid extracts with shorter extraction times
- Higher-value extracts for supplement and cosmetic ingredients
- Pilot extractions to choose a technology before a full plant is sized
- Second extraction of spent plant material for a further product
Key Features
Technology Matched to the Target
Oil-soluble targets suit supercritical carbon dioxide, while polar targets suit water or ethanol routes with ultrasound, microwave or enzyme assistance. Trials decide between them.
Pressure Equipment Built for the Duty
Supercritical and subcritical systems need pressure-rated vessels, pipework, closures and relief devices. Ultrasound and microwave systems run at ordinary pressure.
Set Points Held and Recorded
Interlocks and logging keep pressure, temperature, power and time at the values found in the trials, so the extract composition repeats from lot to lot.
Safe-Area Design
A flammable co-solvent needs a classified area with ignition sources controlled, and carbon dioxide needs gas monitoring in enclosed rooms, where it can displace air.
Throughput Trade-Off Made Plain
More equipment and floor area and lower throughput than simple soaking are the price of selectivity, so the value of the extract per tonne must justify them.
Country Pages for Advanced Botanical Extraction Systems
This product is listed on the pages of the countries below, each with its own enquiry route. Where Kadali has no office in a country, enquiries are handled from the Accra office.
- Advanced Botanical Extraction Systems: Ghana
- Advanced Botanical Extraction Systems: Nigeria
- Advanced Botanical Extraction Systems: Kenya
- Advanced Botanical Extraction Systems: South Africa
- Advanced Botanical Extraction Systems: Lesotho
- Advanced Botanical Extraction Systems: Egypt
- Advanced Botanical Extraction Systems: Morocco
- Advanced Botanical Extraction Systems: Tunisia
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Frequently Asked Questions
What information is needed to size Advanced Botanical Extraction Systems?
What capacity range does Advanced Botanical Extraction Systems cover?
Does supercritical extraction replace conventional solvent extraction plants?
Can ultrasound or microwave heating damage the compounds being extracted?
Is the extract composition fixed once the extraction plant is installed?
How do I choose between these technologies?
What site and safety work do advanced systems need?
How do I request a proposal for Advanced Botanical Extraction Systems?
Enquire about Advanced Botanical Extraction Systems
Send your raw material, target product and capacity to Kadali Africa Ventures for a technical proposal.