Home  >  Industrial Supplies  >  Energy Saving Equipment

1.Advanced,fatty acid can be decreased to 0.2, 2.Saving energy can be saving 40% at least, 3.Anti anticorrosion effect greatly - details see: https://www.machineto.com/biodiesel-production-energy-equipment-10213509

Specification of uco to biodiesel equipment

Technology program is thelow-temperatureaction programsusingacid-catalyzed esterification and alkali-catalyzed transesterification.The process is in the lowest energy consumption of biodiesel technology, which adopt gas esterification process, and it maximum resolve the problem of the reaction equilibrium and the mass transfer. In the case of no external kinetic energy within the circle, it can save electricity more than 60%. The independent design in return also can be a high degree of conservation of heat energy.Unique technology program solve the problem that the high acid value waste oil can not be divided in glycerol ester exchange, make the reaction rate arrive more than 97%.

The vegetable oil fatty acid methyl ester production process can use batch process ,semi-continuous process or continuous reaction process, the continuous process is in favor of energy utilization, can reduce production costs in a greater extent; the process solve the problem of raw materials corrosion for equipment, can effectively reduce the investment cost for the equipment; At the same time, the applicability of raw materials of the process is very extensive, which is adaped to all variety of oils and fats raw materials in current industrial market.

Production steps:

1. Preprocessing of raw oil: When it be heated to 65-70°c,the raw oil is leached to remove impurities.

2. Drying section: Raw oil without impurities is dehydrated and dried.

3. Esterification reaction:adding bio-oil dehydrated to methanol including 3% sulfuric acid,the esterification reaction starts, and it will take 1.5—2.5 hours.

4. Interesterification reaction: this reaction will take 9—12 hours.

5. Vacuum drying section: The interesterification reactants are dried with vacuum, removing moisture, reducing water content below 3%.

6. Distillation section: with vacuum state, interesterification reactants after vacuum drying section are heated to 220°C, biodiesel forms by steaming. Then cooling biodiesel to be liquid, the liquid biodiesel is just finished biodiesel.

7. Methanol fine-distillation: after biodiesel is isolated, the remaining methanol liquid is distilled to form methanol. Methanol cooled can be reused.

Advantage of our biodiesel plant

Patent 1 :

Reaction and separation integration :

(1.1) the energy can be saving 40% at least.

(1.2) improve the reaction rate

Patent 2 :

Tubular reactor :

(2.1) full-auto

(2.2) can be monitoring on-line

(2.3) more stable

(2.4) output can be expanded depend on your demand

Patent 3 :

Neutralizing tower :

(3.1) ensure equipment is not corrode

(3.2) extend the service life of the machine