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Transesterification is a chemical reaction used for the conversion of triglycerides (fats) contained in oils, (Feedstocks) into usable biodiesel. The biodiesel production method  applied worldwide at industrial level is the alkoolysis (transesterification) of triglycerides which are the main component of vegetable oils and animal fats. Oil feedstocks containing more than 4% free fatty acids go through an acid esterification process to increase the yield of biodiesel. Oil feedstocks containing less than 4% free fatty acids are filtered and preprocessed to remove water and contaminants and then fed directly to the transesterification process along with any products of the acid esterification process.
The methanol is typically removed after the biodiesel and glycerin have been separated, to prevent the reaction from reversing itself. Once separated from the glycerin, the biodiesel goes through a clean-up or purification process to remove excess alcohol, residual catalyst and soaps. The glycerin by-product contains unreacted catalyst and soaps that are neutralized with an acid. Biodiesel produced by the process of transesterification has a much lower viscosity, making it capable of replacing petroleum diesel in diesel engines.
SRS' team of biodiesel engineers understands what it takes to run a profitable biodiesel plant, providing you with their proprietary FSP-Series pretreatment system which allows your plant to incorporate high FFA feedstock and maintain profitability. The transesterification process reacts an alcohol (like methanol) with the triglyceride oils contained in vegetable oils, animal fats, or recycled greases, forming fatty acid alkyl esters (biodiesel) and glycerin. Feedstocks with less than 4% free fatty acids, which include vegetable oils and some food-grade animal fats, do not require pretreatment. These feedstocks are filtered and preprocessed to remove water and contaminants, and then fed to the acid esterification process.
Feedstocks with more than 4% free fatty acids, which include inedible animal fats and recycled greases, must be pretreated in an acid esterification process.


The catalyst, sulfuric acid, is dissolved in methanol and then mixed with the pretreated oil. If an acid esterification process is used, then extra base catalyst must be added to neutralize the acid added in that step. The reaction is catalyzed by bases, acids and enzymes and can take place either at low or high temperatures. In this step, the feedstock is reacted with an alcohol (like methanol) in the presence of a strong acid catalyst (sulfuric acid), converting the free fatty acids into biodiesel. The mixture is heated and stirred, and the free fatty acids are converted to biodiesel. Once the reaction is complete, the major co-products, biodiesel and glycerin, are separated into two layers.
Sometimes the biodiesel goes through an additional distillation step to produce a colorless, odorless, zero-sulfur biodiesel. In large biodiesel plants, the glycerin can be further purified, to 99% or higher purity, for sale to the pharmaceutical and cosmetic industries.
The remaining triglycerides are converted to biodiesel in the transesterification reaction. Then, the reactor output stream is led to the removal of glycerin, before entering the remaining 20% of alcohol.After the reaction, the glycerol is separated from the methyl esters.
However, excess methanol is usually not removed from the reaction stream until a complete separation of glycerol and methyl esters has been achieved, because the direct reaction of transesterification of products (higher conversion). Moreover, it has been found that at high temperature and pressure (about 90bar, 240В°C, respectively) the transesterification of fats can take place without prior removal or conversion of free fatty acids.
Nevertheless, most biodiesel plants for financial and safety reasons still prefer to operate at low temperatures and atmospheric pressure retaining larger reaction times.Following the flowchart, after the glycerol separation, the mixture of the methyl esters is neutralized and then separated from impurities using vacuum distillation or evaporation, before washing with water.


For the neutralization of biodiesel an acid is added, which neutralizes the residues of the basic catalyst and separates any soap residue that can be produced during the reaction. The washing water is applied to remove any remaining catalyst, soap, salt, methanol and free glycerol from biodiesel. After washing, the water left in the biodiesel is distilled off under vacuum.The stream of glycerol is removed from the separator containing glycerol 50%. The first step to increase the purity of glycerol is the refinement where acid is introduced in the waste stream to convert soap into free fatty acids and salts. Free fatty acids are not soluble in glycerol and separated at the top of the mixture (upper layer) which can be removed and recycled. These fatty acids can be esterified and thus used as a biodiesel feedstock in the input stream of transesterification reaction.
When potassium hydroxide is used as a catalyst and phosphoric acid as a reagent for the neutralization reaction, then phosphates are produced and these can be used as fertilizer. After acidification and removal of free fatty acids, methanol impurities are also removed via an extraction process through vacuum or through another type evaporator. In this case a molecular sieve is required so as to remove water.Both of SRS’ Transesterification Processes convert ester oils to biodiesel efficiently.



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