Bio Diesel Plants Dealers in Pune

We are offering biodiesel production plants. Biodiesel can be used in compression ignition engines without any modification. It is produced by continuous trans-esterification reaction of seed oils with methanol using caustic soda as catalyst. It is carried out in two or three stages with subsequent washing drying and polishing of the product. Nearly 100 percent conversion of the triglycerides in the oil or fat to biodiesel takes place. The excess methanol is recovered and the biodiesel is filtered to remove potential impurities. Glycerine is recovered as a valuable byproduct in the process. the trans-esterification process is most efficient when the feedstock quality is equivalent to refined and bleached oil (rb). Removing the phosphorus and fatty acids is critical to producing the best quality biodiesel at the lowest cost. consumption and yield per 1000 kg raw oil: (a) methanol consumed: 120 kg, (b) catalyst consumed: 10 kg, (c) glycerin recovered: 110 kg, (d) biodiesel produced: 950 kg. Quantity : 3 plants per month payment terms : negotiable, lc or 40% advance, balance on proforma invoice packaging : standard specifications : process performance guaranteed for 6 months quality : iso 9001:2008

• Application: Bio Diesel Processing
• Voltage: 220V
• Automatic Grade: Automatic
• Power: 10-20 Kw
• Driven Type: Electric
• Production Capacity: 1,000 to 50,000 LPD
• . Warranty: 2years

• Type: Biodiesel Production Plant
• Application: Producing Diesel
• Certification: CE Certified
• Automatic Grade: Semi Automatic
• Driven Type: Electric
• Warranty: 1year

Choosing the right technology partner for biodiesel processing is critical to meet the challenges of feedstock treatment, yields, quality and consumptions of chemicals & utilities. DVC Process Technologists offers the best solutions for commercial viability in the processing of the most challenging feedstocks, through both chemicals as well as enzymatic routes over various capacities.

• Application: Soya Oil, Sunflower Oil, Palm Oil, Corn Oil, Rice Bran Oil
• Type: Oil Refinery
• Usage/Application: Soybean Oil
• Automation Grade: Semi-Automatic
• Capacity: 25 to 500 ton / day

• Biodiesel: Processor
• 300 sq.ft.: 84"

We manufacture Biodiesel processing plant & machine. Our speciality is Multifeed Biodiesel processor with Chemical & process formulation is given by us alongwith biodiesel processor. 1)500 LPD Biodiesel processor - Amount- Rs.375000/- 2) 1000 LPD - Rs.725000/- 3) 2000 LPD- Rs.1400000/- 4) 3000 LPD -Rs.2075000/- Above 3000 LPD as per customers requirment please.

• Automatic Grade: Automatic
• Capacity: 30 Ton/day
• Types: BATCH AND CONTINUOUS TYPE

• Country of Origin: Made in India
• Voltage: 440 V
• Usage: Biodiesel electricity generator
• Capacity: 500 liters/day
• Automation Grade: Automatic
• Phase: 3
• Power Consumption: 25 kW
• Frequency: 60 Hz
• Body Material: SS

Unlike petroleum diesel, biodiesel is a renewable resource, and it creates less pollution than Petroleum Diesel. It can be used alone or in combination with petroleum diesel, or with heating oil. Generally, no expensive modifications to the engines are required. This makes it easier to integrate biodiesel into current systems than other alternative energy sources, which often require new equipment.

We provide Biodiesel Plants that are designed to use Multi feed Oils. Our Biodiesel Plant is manufactured as per the international standards, which raises its demand among clients. Based on that, we have carved a niche in the global markets as a trusted Manufacturer and Supplier of Biodiesel Plants. Specification : Capacity : 30 kl to 100 kl Feed Specifications before Trans-esterification : If these parameters are not met, then Pretreatment and Esterification have to be done FFA Content : 0.1%Phosphatide Content as phosphorus : 10 ppmSulphur Content : 5 ppmWater Content : 0.10%Impurities : 0.10%Temperature : 122oF (50oC) The Process : Trans-esterification of oil takes place when triglycerides react with methanol in the presence of an alkaline catalyst, resulting in the formation of methyl ester and glycerin. After this reaction occurs in the mixing section, the methyl esters are separated (as light phase) from glycerin water (as heavy phase) in the settling section. In the next step counter current washing of methylester removes it as a by-product to give bio-diesel. Rectification column removes excess methanol in the glycerin. Further purification takes place to convert industrial grade glycerin to pharma grade glycerin by distillation. Why Our Biodiesel Plant? Processes different types of oilLow oil lossCompletely AutomatedBiodiesel as Per ASME StandardsModular Plant with easy on-site assembly Suitable For Refining : Palm oilSunflower oilRapeseed oilSoybean oilVegetable fatsFatty acids

With the Group's Strong Background in Research and Long Experience in Designing of Equipments, We have Been Able to Evolve Technological Advancement in Biodiesel Processing. this Has Resulted in Making Our Plants Highly Efficient and Superior in Quality. innovative Process, Superior Results: principle of Process: the Process for Producing Biodiesel is Feed Dependent. Except Refined Oils, all other Feeds Require Pretreatment. for Feeds such as Palm or Tallow, Melting May Be Required. the Actual Process Starts with Acidulation of Feeds such as Soapstocks to Recover Acid Oil. Soapstocks Contain About 45% Oil and 45% Water. Acidulation with Appropriate Dose of Sulphuric Acid is Done to Recover Acid Oil. in Case of Oils such as Soybean, Degumming Process May Be Required. the Phosphatides are Removed from the Oil By Acid Degumming Process Employing Phosphoric Acid and Water. depending On Ffa Percentage, Two Stages Can Be Employed for Esterification Reaction.the Degumming Process is Followed By Acid Catalyzed Esterification Process. in this Process, the Free Fatty Acids React with Methanol in Presence of Sulphuric Acid as Catalyst. the Reaction is Followed By Settling and Phase Separation Under Gravity. the Acid Layer is Processed for Methanol Recovery and the Ester Layer is Further Processed for Transesterification. if the Free Fatty Acid Content is Less Than 3% of the Feed, Then One Can Directly Opt for the Transesterification Process. the Transesterification Process is the Reaction of Triglycerides and Methanol in Presence of Alkaline Catalyst. the Reaction Gives Glycerine as a By-product. the Layer Separation is Under Gravity. Washing of Biodiesel with Water Removes the Contaminants and Gives Clean and Clear Biodiesel. the Washed Biodiesel is Dried Under Vacuum and Filtered Through '1 Micron' Filters to Give 'ready for Use' Biodiesel. feed Based Plant Customization: feed_plantiespl Bio-diesel Processing Plants Can Be Customized to Suit Your Choice of Feed. Our Plant Design Already Supports a Variety of Feeds (details On Last Page). if You have a Different Feed, It Can Be Tested At Our Pilot Plant . the Pilot Plant and R&d Department Work On Optimizing the Process Quality and Efficiency for Producing Biodiesel from Different Feeds. casm Reactor (patent Applied) casm Uses Reaction Technology Based On Counter Atomized Spray Mixing and Circulation Through Eductors, Achieving Intimate Contact of the Reactants. this Results in Enhanced Reaction Rate with Reaction Reaching Completeness, and Surpasses the Efficiency Achieved By Conventional Process Technique Where the Mixing is Bulk Type and Results in Slower Reaction Rates. the Innovative Technology also Results in Lowering the Quantity of Methanol Added for Reaction. Conventionally the Methanol Added is 2.25 Times Ffa, Whereas the Casm Process, this is Drastically Reduced to 1.1 Times of Ffa in Case of Esterification Reaction. har Settlers (patent Applied) the Settling and Phase Separation, After Both Esterification and Transesterification, are Key to Successful Reactions and Quality of the Product. the Specially Designed Settlers Increase the Aspect Ratio, While Maintaining the L:d Ratio of 2.5:1of Settler. this Reduces the Settling Time Drastically as Compared to Conventional Settling. Moreover, in Conventional Settlers the Phase Separation is Done Under Gravity and Requires Orientation of Settlers At a Height, Whereas the Iespl Settlers Can Be Oriented At Ground Level. hphs Heat Exchanger (patent Applied) the Efficiency of Heat Exchanger Depends On the Design of the He.the Specially Designed Helicospiral Heat Exchangers Can Be Used for Multiple Duties such as Condensers, Heaters and Coolers. as Compared to the Conventional Shell and Tube Heat Exchangers,These Heat Exchangers Result in Higher Thermal Efficiency, Particularly for Vapour and Liquid Phases. sri Evaporator (patent Applied) the Methanol Added for Reactions of Both, Acid Catalysed Esterification and Base Catalysed Transesterification, is in Excess of What is Required for Consumption. Hence Methanol Recovery is of Prime Importance for the Economy of the Process. Iespl Provides Evaporator Under Atomized State, Resulting in Instant Evaporation of Volatile Matter; Whereas the Temperature of the Non-evaporables is Less Than Boiling Point of Mixture, Thus Saving Energy and Reducing the Steam Exchequer as Compared to Conventional Reboiler Type Evaporators. the System Imparts High Thermal Efficiency of 95 to 98% as Against Conventional System Where this Efficiency is 85 to 90%. the Spiral Column Results in Highly Improved Hetp (height to Equivalent Theoretical Plates) and Thus Recovery of Methanol with High Purity is Achieved as Against the Straight Path Column in Conventional Recovery Systems. special Features of Biodiesel Processing Technology: batch-continuous Plantflexibility of Feedno Limits of Ffa Contentreactions At Atmospheric Pressure and Low Temperatureefficient Processcompact Plantautomatic or Semi-automatic Plantinnovative Processesmethanol Recovery Achieved By Technological Advancementbiodiesel of High Qualitylow Maintenancesafe Operationsretrofitting of Existing Plants to Process High Ffa Feedsbio-diesel Meets Astm Standards flexibility of Feed plant Design Supports a Variety of Feeds. all These Feeds Can Be Used Without Any Modification in the Plant Operation if They Satisfy the Following Conditions: ffa : 0 to 100 %gums, Moisture, Impurities and Unsaponifiables 2 % feed Categories Supported plant Design Supports a Variety of Feeds. all These Feeds Can Be Used Without Any Modification in the Plant Operation if They Satisfy the Following Conditions: non-edible Oils like Pongamia, Jatrophaacid Oilsfatty Acid Distillatessoap Stocktallowtrap Greasefish Oilalgaerefined Oils

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