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 sal seed, mahua, karanja and niger processors of the Jharkhand forest belt, alongside rice bran units at Ranchi, Palamu and Hazaribagh. Batch units from 10 TPD up to continuous lines of 500 TPD.
Jharkhand is the one state on this list where the most valuable extraction feed is not an oilseed crop at all. Sal seed collected across Saranda, West Singhbhum, Gumla, Simdega and Latehar yields sal fat, the raw material behind cocoa butter equivalents, and it commands a price no ordinary meal does. Mahua from Palamu, Latehar, Gumla and Khunti, along with karanja, kusum and neem, feeds the soap, oleochemical and biodiesel trade.
Forest produce also arrives very differently from a mandi crop. It is seasonal, collected rather than farmed, variable in moisture and often stored for months before it is processed. As a solvent extraction plant manufacturer in Jharkhand, Mecha Engineering designs for that reality, which usually means a batch or modest continuous plant with generous drying and storage ahead of it, rather than a large line that sits idle for half the year.
These are the points a Ranchi, Palamu or Singhbhum 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 Jharkhand 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.
Designed for sal seed and its fat, with decortication, drying and flaking ahead of the extractor, for collection centres across Saranda, Singhbhum, Gumla, Simdega and Latehar.
Decortication, drying and flaking for mahua, karanja, kusum and neem from Palamu, Latehar, Gumla and Khunti, feeding soap, oleochemical and biodiesel buyers.
Built around stabilised and pelletised bran, with an expander section and a DT sized to protect meal quality, for milling clusters at Ranchi, Palamu, Garhwa and Hazaribagh.
Batch percolation extractors for 10 to 30 TPD duty. For seasonal forest produce this is usually the right answer, since a batch plant idles cheaply between collection seasons.
Cleaning, conditioning and flaking for niger and linseed from the tribal upland belt, where lot sizes are small and changeover between materials has to be quick.
Recovers the 20 to 30 percent oil held in refinery spent bleaching earth and residues, turning a disposal problem into a recovered oil stream.
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 | Sal seed, mahua, karanja, niger and rice bran | Kusum, neem, linseed, mustard cake, 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 Jharkhand buyer on the first call.
| Feed material | Oil available | Preparation needed | Typical Jharkhand location |
|---|---|---|---|
| Sal Seed | 12 to 20 percent | Decortication, drying and flaking | Saranda, West Singhbhum, Gumla, Simdega, Latehar |
| Mahua Seed | 30 to 40 percent | Decortication, drying and flaking | Palamu, Latehar, Gumla, Khunti, Lohardaga |
| Karanja and Kusum Seed | 25 to 35 percent | Decortication, drying and flaking | Chaibasa, Saraikela, Khunti and the forest belt |
| Neem Seed | 20 to 30 percent | Decortication, drying and flaking | Across the central and eastern districts |
| Niger Seed | 30 to 40 percent | Cleaning, conditioning and flaking | Gumla, Simdega, Latehar tribal upland |
| Rice Bran | 14 to 20 percent | Stabilising, then pelletising or expander | Ranchi, Palamu, Garhwa, Hazaribagh, Deoghar |
| Linseed and Mustard Cake | 8 to 15 percent residual | Cake breaking, sizing and conditioning | Deoghar, Godda, Sahibganj and the Santhal belt |
| Spent Bleaching Earth | 20 to 30 percent held oil | Direct charging, no flaking needed | Refining and food units around Ranchi and Jamshedpur |
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.
Units extracting sal fat for the cocoa butter equivalent and confectionery trade, where the value of the product justifies careful, gentle processing.
Processors feeding soap, oleochemical and biodiesel buyers from mahua, karanja, kusum and neem collected across the forest districts.
Organisations handling seasonal minor forest produce that want processing capacity closer to collection rather than shipping seed out of the state.
Rice milling groups converting bran they currently sell cheap into crude rice bran oil and de-oiled rice bran for the feed trade.
De-oiled cake producers judged on protein, colour and residual solvent, so the desolventiser toaster design matters as much as the extractor.
Downstream units securing a captive supply of non-edible oil rather than buying it in from outside the state.
Dispatch, erection and site service run out of our Saharanpur works to every district of Jharkhand. 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 Jharkhand, and we supply across India and to export markets.
Straight answers to what Jharkhand 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 Jharkhand. 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 Jharkhand, 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. For sal seed and mahua the honest answer is usually a smaller plant than buyers first expect, because collection is seasonal and a large continuous line idling for months costs more than it earns. Tell us your collection volume and season length and we size against that.
Sal seed, mahua, karanja, kusum and neem seed, niger, linseed, rice bran, mustard cake and refinery spent bleaching earth. Stainless steel versions handle oleoresin and herbal material. Forest produce varies far more in moisture and quality than a mandi crop, so we ask for an oil content and moisture report on an actual stored lot 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 Jharkhand 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.
Yes, and the scope is the same as for a site next door. Foundation and civil drawings, structural erection, equipment installation, piping, insulation, utility tie-in, water and solvent trials, first production run and operator training at your Jharkhand site are included. Our erection team travels to site and stays until the plant is producing to specification.
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. Road freight from Saharanpur to Ranchi, Daltonganj or the Singhbhum belt is quoted at actual cost, and for large vessels we arrange the trailer, route survey and unloading crane.
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.