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Latexman, if we agitate faster, we will add more heat to the system right? Do you think it will solve this issue? Because the solution is anyway non viscous.

What do you mean by pumping upward?

How is the mixing looking like from the video?https://www.veed.io/view/59aeba8a-8a1d-4633-8916-5a877c39cabe?sharingWidget=true

Changes to equipment is not possible due to budget. And pilot plant test is coming up soon. That's why change needs to be in process conditions.

Based on the actual experimental data, U-value is at 41 W/m2 K. Is this reasonable for a cooling jacket?

This is the cooling rate profile. The duty decreases as temperature decreases and probably is due to loss of thermal coefficient on the wall. However, at over 0oC we can still see that the cooling duty is quite low compared to chiller duty of 10kW.

Compositepro, will this work also if the tank will be used for crystallization purposes?

The jacket is plain, there are no cooling tubes. Drawing of the jacket is not available.

LittleInch, My inlet and outlet temp of the cooling circuit is almost the same. No difference which I can't say a number due to error of instruments. I would like to keep the reaction below 5-6 oC with a coolant that will be at -20oC. The temperature outlet with content temperature has a...

Hello, I have a mixing tank 1.7 m3 half covered with plain cooling jacket (heat transfer area 2.44 m2). I tend to use the mixing tank for a reaction that is exothermic (ca -10kW), for that reason I want to check if cooling duty of chiller and jacket is sufficient. We carried out some tests...