Verified Material Grade
IS 2062 plate for structure and extractor body, SS 304 or SS 316 on miscella and oil contact parts, backed by mill test certificates in your company name.
Mecha Engineering designs, fabricates and commissions turnkey solvent extraction plants for the rice bran units of the Udham Singh Nagar Tarai belt, the mustard crushers of the plains and the herbal and aromatic extractors around Haridwar and Dehradun. Batch units from 10 TPD to continuous lines of 500 TPD.
Uttarakhand is the state closest to our works, and it happens to have two of the cleanest extraction opportunities in north India. The Tarai belt across Udham Singh Nagar, from Rudrapur and Kashipur through Kichha, Bazpur, Gadarpur and Sitarganj, is dense rice milling country, and the bran those mills generate is the natural feed for an extraction plant sitting alongside them. Haridwar and Roorkee add mustard and a steady flow of expeller cake.
The second opportunity is different in kind. Haridwar, Dehradun and Rishikesh form one of the largest ayurvedic and herbal manufacturing clusters in the country, where the requirement is not hexane at all but stainless steel batteries running ethanol or IPA for botanical and aromatic extracts. As a solvent extraction plant manufacturer in Uttarakhand, Mecha Engineering builds both, and our Saharanpur works is under an hour from Roorkee.
These are the points a Rudrapur, Kashipur or Haridwar processor checks before releasing a purchase order, so we put them in writing rather than in a brochure line.
IS 2062 plate for structure and extractor body, SS 304 or SS 316 on miscella and oil contact parts, backed by mill test certificates in your company name.
Extractor drive, conveyors and vessels trial assembled and run at our Saharanpur shop. Hydro and leak tests are recorded before anything is loaded on a trailer.
Civil and foundation drawings, structural erection, piping, insulation, utility tie-in, commissioning and operator training at your Uttarakhand site, covered in the scope.
You buy from the fabricator, not a trading house. No dealer margin, and every design change is quoted against actual material, machining and labour.
Every feature below protects one of three numbers your plant is judged on: oil recovered, solvent lost and steam burned per tonne.
Extractor bed depth, sprinkler layout and miscella stage count are matched to your feed so solvent washes the bed evenly. Residual oil in the meal is held to under one percent on a dry basis instead of drifting up with load.
Economiser, multi-stage evaporation and heat exchange between hot meal, vapour and incoming miscella cut live steam demand. Lower steam and power per tonne is where an extraction plant actually earns its payback.
Vapour recovery, nitrogen blanketing points, flameproof motors, starters and field instruments, bonded earthing and gas detection. The hexane section is treated as a hazardous area from the first drawing, not retrofitted later.
Layouts are drawn to your shed height, plot shape and boiler capacity. The structure and utility headers are sized so a second extraction line or a refinery block can be added later without rebuilding.
Shell and tube condensers, a solvent water separator and a mineral oil vent gas absorption column recover solvent that most plants send out of the vent. Hexane is a running cost, so every litre recovered is margin.
Controlled steam sparging and residence time in the desolventiser toaster strip solvent without scorching the meal, so protein and colour hold up and your de-oiled cake sells into the feed trade at the better rate.
Pick the line that matches your feed material, or send your material analysis and we will tell you which of these fits.
Built around stabilised and pelletised bran, with an expander section, gentle bed handling and a DT sized to protect meal quality. The standard choice for the Rudrapur, Kashipur and Kichha milling belt.
Cake breaking, sizing and conditioning to pull the remaining 8 to 12 percent oil out of expeller cake, for the Tarai and Haridwar expeller units.
Stainless steel batteries running ethanol, IPA, hexane or ethyl acetate for botanical, oleoresin and aromatic duty, with vacuum concentration, for the Haridwar and Dehradun ayurvedic cluster.
Batch percolation extractors for 10 to 30 TPD duty, lower capital and simpler operation. A practical first plant for a rice miller adding extraction behind existing capacity.
Decortication, drying and flaking for mahua, neem and karanja from the Bhabar belt, and small batch lines for walnut and apricot kernel from the hill districts.
Recovers the 20 to 30 percent oil held in refinery spent bleaching earth and residues, relevant to the food processing units across the SIDCUL estates.
Standard build for a continuous solvent extraction line. Every line below is changed to order, so treat this as the starting point for your enquiry rather than a fixed model list.
| Parameter | Standard offering | Options on request |
|---|---|---|
| Plant Capacity | 10, 20, 30, 50, 100, 150 and 200 TPD | Up to 500 TPD, and parallel lines for staged expansion |
| Plant Type | Continuous extractor for commercial oilseed duty | Batch percolation type for mini plants and herbal lines |
| Feed Material | Rice bran, mustard cake, herbal and aromatic material | Soyabean, mahua, neem, hill kernels, spent bleaching earth |
| Solvent Used | Commercial hexane to IS specification | Ethanol, IPA or ethyl acetate for herbal and oleoresin duty |
| Residual Oil in Meal | Under 1 percent on a dry basis | 0.5 to 0.7 percent with expander prepared feed |
| Hexane Consumption | Around 1.5 to 2.5 litres per tonne of material | Lower with vent gas absorption and mineral oil scrubber |
| Material of Construction | IS 2062 plate for structure and extractor body | SS 304 or SS 316 throughout for food, herbal and pharma duty |
| Preparatory Section | Cleaner, magnetic separator, cracking roll, conditioner, flaker | Expander, pelletiser, dehuller and cooker for higher bulk density |
| Extractor Type | Rotocel or shallow bed chain type with wedge wire screens | Loop type, sliding cell or basket type to suit the material |
| Desolventising | Desolventiser toaster with steam sparging trays | DTDC with dryer and cooler for finished feed grade meal |
| Miscella Distillation | Two stage evaporation with vacuum stripping column | Economiser plus rising film stages to hold FFA down |
| Solvent Recovery | Shell and tube condensers with solvent water separator | Vent gas absorption column with mineral oil circulation |
| Heating Utility | Low pressure steam from your boiler, at 3 to 10 kg per sq cm | Thermic fluid, waste heat recovery and economiser tie-in |
| Safety Fittings | Flameproof motors and panels, bonded earthing, purging points | Nitrogen blanketing, gas detectors, sprinkler and hydrant tie-in |
| Control System | Local panel with interlocks, level and temperature indication | PLC with HMI, SCADA link, batch reporting, flameproof instruments |
| Documentation | GA drawing, P and ID, MOC certificates, test report, manual | Third party inspection, statutory approval support, IQ and OQ protocols |
Scroll the table sideways on a mobile screen. Send your material, daily tonnage and available steam and we will fill this sheet in against your process.
The feed material decides the preparatory section and the extractor, not the other way around. This is the shortlist we work through with a Uttarakhand buyer on the first call.
| Feed material | Oil available | Preparation needed | Typical Uttarakhand location |
|---|---|---|---|
| Rice Bran | 14 to 20 percent | Stabilising, then pelletising or expander | Rudrapur, Kashipur, Kichha, Bazpur, Gadarpur, Sitarganj |
| Mustard and Rapeseed Cake | 8 to 12 percent residual | Cake breaking, sizing and conditioning | Haridwar, Roorkee, Laksar, Khatima |
| Soyabean | 18 to 20 percent | Cracking, dehulling, conditioning, flaking | Tarai belt and Haldwani area units |
| Herbal and Botanical Material | Varies by material | Drying and coarse milling | Haridwar, Dehradun, Rishikesh ayurvedic cluster |
| Aromatic and Essential Oil Crops | Varies by material | Drying and coarse milling | Dehradun, Pauri and the aromatic plant belt |
| Mahua and Neem Seed | 20 to 35 percent | Decortication, drying and flaking | Bhabar belt, Ramnagar and Kotdwar |
| Walnut and Apricot Kernel | 40 to 55 percent | Shelling, drying and gentle flaking | Pithoragarh, Chamoli, Almora, Uttarkashi |
| Spent Bleaching Earth | 20 to 30 percent held oil | Direct charging, no flaking needed | Food and oil units across SIDCUL estates |
Not sure which row you belong to? Share the material name and a recent oil content report and we will confirm the configuration along with an indicative recovery figure.
Six stages from raw cake to crude oil and de-oiled meal. The solvent runs in a closed loop throughout, which is what keeps hexane cost and fire risk under control.
Feed is cleaned, de-stoned and passed through cracking rolls, a conditioner and a flaker or expander so the oil bearing cells open and the bed drains freely.
Prepared material moves through the extractor while hexane is sprayed counter-current across the bed. Oil dissolves into the solvent and leaves as miscella.
Wet meal enters the desolventiser toaster, where steam sparging strips residual hexane and toasts the meal to stable moisture and temperature.
Miscella is heated through the economiser and evaporation stages, then vacuum stripped so the crude oil leaves free of solvent traces.
Vapour condenses in shell and tube condensers and passes to the solvent water separator. Vent gas goes to the absorption column so uncondensed hexane is recovered.
Crude oil is cooled and pumped to storage or onward to refining. De-oiled cake is dried, cooled and conveyed for bagging or bulk despatch.
Tarai milling groups converting bran they currently sell cheap into crude rice bran oil and de-oiled rice bran for the feed trade.
Haridwar and Dehradun units running stainless steel solvent batteries for standardised botanical extracts, where food grade build and clean changeover are required.
Expeller units recovering the oil that mechanical pressing leaves behind in cake, usually the fastest payback a small oil mill can make.
De-oiled cake producers judged on protein, colour and residual solvent, so the desolventiser toaster design matters as much as the extractor.
Units working with medicinal and aromatic crops, where solvent extraction sits alongside distillation rather than replacing it.
Industrial estate units at Haridwar, Pantnagar and Sitarganj adding extraction or recovery capacity within an existing process plant.
Dispatch, erection and site service run out of our Saharanpur works to every district of Uttarakhand. These are the locations we work in most often.
District not on the list? The list is only where we have worked most recently. Site visits, erection and after-sales service cover every district in Uttarakhand, and we supply across India and to export markets.
Straight answers to what Uttarakhand buyers ask before and after a site visit.
Mecha Engineering Pvt. Ltd. designs and fabricates solvent extraction plants at its own works at Village Meharbani on Behat Road, Saharanpur, Uttar Pradesh, and supplies them across Uttarakhand. The company was set up in 2022 and builds extraction, distillation, drying and process equipment for edible oil, agro-processing, feed, herbal and chemical units in Uttarakhand, the rest of India and export markets.
Batch type mini plants start at around 10 TPD, and continuous lines are built from 20 TPD up to 500 TPD. Tarai rice millers usually size against the bran their attached mills generate daily, while the herbal units at Haridwar and Dehradun work in far smaller stainless steel batteries measured in litres rather than tonnes. Tell us which of the two you are and the sizing conversation is quite different.
Rice bran, mustard and rapeseed cake, soyabean, mahua, neem and karanja seed, walnut and apricot kernel from the hills, and refinery spent bleaching earth. Stainless steel versions handle botanical, aromatic and oleoresin material for the ayurvedic cluster. The preparatory section changes with the material, which is why we ask for an oil content and moisture report before quoting.
A properly prepared and correctly loaded plant leaves under one percent oil in the meal on a dry basis, and 0.5 to 0.7 percent is achievable where the feed goes through an expander. Preparation matters more than the extractor here, which is why we quote the preparatory section and the extractor together rather than separately.
Typical consumption runs around 1.5 to 2.5 litres per tonne of material processed. Loss is controlled by condenser sizing, a properly working solvent water separator, sealed conveyors and a vent gas absorption column that scrubs uncondensed vapour with mineral oil before anything leaves the plant.
The hexane area is designed as a hazardous zone from the start. Flameproof motors, starters and field instruments, bonded earthing across the structure, nitrogen purging connections, gas detection points and a vapour recovery loop are part of the standard scope, and drawings are prepared in the form your statutory and insurance inspections in Uttarakhand ask for.
Yes. Common jobs are adding a preparatory or expander section ahead of an existing extractor, replacing a worn extractor chain and screen assembly, upgrading a DT to a DTDC, rebuilding the distillation and recovery block to cut steam, and adding a PLC panel to a manually run plant. Send photographs, your current layout and a nameplate reading to start.
Erection, piping tie-in, insulation, utility connection, water and solvent trials, first production run and operator training at your Uttarakhand site are part of the supply scope, along with foundation and civil drawings. Uttarakhand is our nearest market, and an engineer usually reaches a Roorkee, Haridwar or Dehradun site the same day.
Mini and batch plants are generally ready in 12 to 16 weeks. Continuous lines take 20 to 30 weeks depending on capacity and automation, with erection running alongside your civil work. Freight to Roorkee or Haridwar is a very short run, and to the Tarai belt still a single day movement, quoted at actual cost with trailer, route survey and unloading crane arranged for large vessels.
Call +91-9084351006 or +91-7500378000, send a WhatsApp message, or email info@mechaengg.com with four details: the material you will process, the tonnes per day you want to handle, the oil and moisture content of that material and the steam and power available at your site. A specification sheet, layout and price come back within one working day.
Share the material, the tonnes per day and the steam you have available. Our Saharanpur engineering team returns a specification sheet, plant layout and price so you can compare on paper rather than on promises.