chemi-eng

This sectionexplains the calculation formula for stirring power. We'll focus on the basics that users who use many stirr...

We will explain how to decide the shape of the powder storage hopper. When designing a hopper, volume calculations are t...

I will explain the utility of chemical plants. Although utilities are not a major concern for plant engineers, they are ...

I will introduce the knowledge about the flow pattern of the agitator. Mechanical and electrical engineers of chemical p...

U-factor. I explained how to collect on-site data for the overall heat transfer coefficient (U value) in a batch chemical plant.

I introduced the design of a plate heat exchanger as an example of using the calorific formula Q=mcΔt in a chemical plant.

Restricting orifice for head liquid transfer ・The orifice direction expands to the downstream side.The orifice direction expands to the downstream side.

pressure drop. In practice, a simple calculation that considers only the height and the pressure loss in areas where clogging is likely to occur is sufficient.

I explained the average flow rate in the pipes of a batch-type chemical plant. They are divided into liquids, gases, slurries, and entrained gases.