Flow diagram

The technological scheme and the selected mechanisms are designed for maximum daily capacity of 50 cubic meters per day. The raw material which is plant, animal or waste fat of warehousing enter to the main reactor by pumps P1 and P2 (duplicate pump), which provides a continuous cycle of the project. The raw material is heated to a specified operating temperature with superheated steam, moving in a coil located in the middle of reactor. The condensate which is separated from the steam through the drainage line is collected in a buffer vessel in V4. Methyl catalyst is prepared in the reactor Rc3. The heat, which is released during the exothermic reaction in the preparation of the catalyst, uses for heating of the material, which contributes to reducing the cost of steam. This is one of the advantages of our reactor. By two overlapping pumps P3 and P4, the catalyst is submitted to the reactor to perform the basic process of transesterification.

The main reactors are equipped with stirrers, allowing homogenization of the whole volume. This contributes to the full operation of the process. Unbundled glycerol is collected in a buffer vessel V3, where through the pump R7 is transported to the storage farm. The recycling line over the reactor allows the excess of methanol to participate repeatedly in the process, which reduced its losses to a minimum. Contamination  biodiesel by pumps P5 and P6 is  filed in the column V1 for washing . Washing of biodiesel and separation of the  soap  is an essential process to improve the fuel quality. In the washing column offered by Kondakov Energy, the biodiesel and the wash water are moving in protivotok which ensures the complete separation of the soap. The wash water and the soap are passing through mazninoulovitel to separate of fuel particles carried away (this is a requirement of the provisions of the MOU). The water after the Mazninoulovitelya can be used to make liquid potassium fertilizer - a valuable resource in agriculture.

Washed biodiesel through pumps R8 and R9 (dubbing), passes through the gravitational separator for the separation of mechanical impurities and residual water. From buffer vessel V2 with pump R10 the biodiesel passes through a heat exchanger T1 where it cools and when the passage through the separator is repeated, there is a separation of heavy paraffin fraction. This ensures a reduction of the border temperature of  filtruemost  of the finished fuel. The finished product at the end of the technological process meets all the standards laid down in European standard EN14214.

• All devices are made from high quality stainless steel. Stopcocks have a special Teflon gaskets.
• Pumps and reducers are equipped with explosion-proof motors and this provides technical safety in the work process.