Optimix Engineers

Sinhagad Road, Pune, Maharashtra

Material of Construction - All grades of Stainless Steel mainly SS304, SS316, SS316L etc. Finish Matt/ Mirror/ Electro polished depending on the application/ requirement. Special profiles & features can be manufactured based on requirements.

Features

• Impeller Diameters from - 1000 mm to 3000 mm
• Operating speed from - 10 to 3000 rpm
• Motor power from - 0.37 KW to 37 KW.
• Shaft Diameters from - 20mm to 150 mm.
• Viscosities from -1 cP to 2, 00, 000 cP.

Optimix Engineers is engaged in the manufacturing of agitators required for various process applications. We have over 17 years of experience in this field and a proven track record. We have state of the art machinery, and in-house expertise to handle all kinds of projects. We provide end to end solutions agitator solutions to our worldwide clients.

We use quality raw material that includes high quality stainless steel and adhere to CGMP norms. Our hallmark is quality workmanship, adherence to schedules and excellent after sales service

Material of Construction - All grades of Stainless Steel mainly: SS304, SS316, SS316L etc. Finish Matt/ Mirror/ Electro polished depending on the application/ requirement. Special profiles can be offered based on the requirements

Features

• Impeller Diameters from - 150 mm to 600 mm.
• Operating Speeds from - 100 to 500 rpm.
• Motor Power from - 0.37 KW to 5 KW.
• Viscosities from - 1 cP to 50 cP.

Material of Construction - All grades of Stainless Steel mainly SS304, SS316, SS316L etc. Finish Matt/ Mirror/ Electro polished depending on the application/ requirement.

Features

• Impeller Diameters from - 100 mm to 6500 mm.
• Operating Speeds from - 3 to 48 rpm.
• Motor Power from - 0.37 KW to 18 KW.
• Shaft Diameters from - 30mm to 120 mm.
• Viscosities from - 1 cP to 1000 cP.

Thus the shear stresses and strain rates vary greatly throughout an agitated liquid in a tank. As the viscosity of the fluids to be mixed increases, the physics fluid mechanics change from that of turbulent flow (like in liquid agitators) to that in which viscous drag forces dominate. Additionally, some fluids exhibit Non-Newtonian behavior their viscosity cannot be designated by a single coefficient. Mixing of such fluids requires special heavy duty agitators. As the dynamic viscosity of a Newtonian liquid is independent of shear at a given temperature, its viscosity will be the same at all points in the tank. In contrast the apparent viscosity of a non-Newtonian liquid varies throughout the tank. This in turn significantly influences the mixing process. For shear thinning liquids, the apparent viscosity is at a minimum in the immediate vicinity of the agitator. The progressive increase in the apparent viscosity of a shear thinning liquid with distance away from the agitator tends to dampen eddy currents in the mixing tank. In contrast, for shear thickening liquids, the apparent viscosity is at a maximum in the immediate vicinity of the agitator. In general shear thinning and shear thickening liquids should be mixed using high and low speed agitators respectively. Wherever possible, the movement of the entire contents of the agitator vessel should be avoided as rapid movement tends to segregate the components due to centrifugal forces.