Print page

Home » How do I select the optimal location for an impeller inside a tank?

Print page

How do I select the optimal location for an impeller inside a tank?

Q: I am new to tank mixing and I have a question about selecting the optimal location (and orientation) for an impeller inside a tank. I am dealing with a tank that contains very light materials (0.7 and 0.8 SG). The contents have been sitting in the tank and are stratified. Please let me know if there is some sort of general process for selecting the proper impeller position.

The tank is 120 ft. in diameter, 45 ft. high. It is allowed to only have one mixer. The first layer of material has a specific gravity of 0.75 is 32 ft. high. The second layer of the tank has a specific gravity of 0.67 and is 10 ft. high; making the total contents of the tank 42 ft. high. The purpose of the mixer is to have complete mixing within 6 hours.

A:

Based on the tank dimensions and liquid densities, this is a storage tank for hydrocarbon liquids.  Therefore, the logical mixer is a side-entering mixer, which is usually sized based on horsepower, with a practical gear reduction and impeller speed.  The impeller and corresponding pumping capacity is sized to utilize the available motor power.  For content uniformity, between 3 and 10 tank turnovers are typical for side-entering mixers.  This application would require a 30 hp to 50 hp side-entering mixer.

The answers by this expert are based on the best available interpretation of the information provided.  The consequences of the application of this information are the responsibility of the user.  If clarification is needed, please submit a further question.

Here are more of the latest questions on: Mixing

What is a good design for a stirred tank mixer?
We manufacture epoxy products with stirred tanks. We blend the resin and hardener separately. What is a good design for a stirred tank mixer and what are the power requirements? The viscosity is between 2,500-5,000 cp, the volume is 2,000 liters, the dimensions of the tank are 1.5 meters in diameter and the height is 2.5 meters.

What is your advice on a helical ribbon mixer/transport device?
We currently have some issues with a tank. From the top we continuously add powder while at the bottom we keep taking it away. The problem is that the powder dispensing results in a big cone-shaped pile in the center what results in an uneven powder dispending at the bottom. After some brainstorming we came up with the idea to add some sort of "screw" that spreads the power along the bin.

<--- flow --- Center of the bin --- flow--->
(existing heap of powder)

Since the powder is kind of sticky and cleaning of the entire equipment is scheduled to be less than 90 minutes, it should be an open screw so I was thinking in the direction of a double helical ribbon. Since this is mainly made for mixing I have a few questions:

Is it possible to use this principle as a semi-transport screw instead of a mixer?

It will be a double helical ribbon to prevent the powders from being pushed to the side of the bin. Which flight provides the most transportation, the inner or the outer one?

How fast should the agitator be in a mix tank?
I am putting together a mix tank that has an agitator in it and I need some help figuring out how fast it needs to rotate and how big of a motor I need.

The tank is round, 120 inches tall and 72 inches wide. The agitator shaft is 3.477 inches in diameter and 117 inches long. There are three impellers on the shaft one at 11 inches from the bottom, the next at 46.75 inches from the bottom and the last at 84.75 inches from the bottom. There are four blades on each impeller at a 45 degree angle; each blade is 27.5 inches long.

The solution I am mixing has a specific gravity of 1.45 and a viscosity of 6.2 cP.

This is far from my small area of knowledge and I would appreciate any help you could give me.

What is the required power for an anchor agitator?
I have a tank 22" ID x 36" straight shell with a conical bottom 20 degrees (41" total height). Inside will be 200 liters fluid with specific gravity 1.3 and viscosity 30,000 cP. We want to put an anchor agitator with scrapers (bottom and side scapers) at 16 -- 20 rpm speed. What is the required power for this agitator? How is the power calculated?

Can we use a formula like this:
P=Np*Sp.Gr*N3*D5
and for power number:
0.5 0.16 0.67
Np=113(D/(T+D)) (H/D)(W/D) (n/2)
Which are the units?
P - kW or HP
N3 - mm or in (what means N3)
D5 - mm or in (what means D5)
How is this formula taken into account the viscosity?

What is the suggested rpm and motor speed for an anchor impeller?
I am planning to have a mixer with an anchor impeller that has the following specifications for blending a viscous liquid (different lots of same material for the purpose of achieving homogeneity): Mixing vessel volume: 7000 liter; Batch volume of the liquid: 6660 liter (6 t); Tank diameter: 1500 mm; Density of the liquid: 900 kg/m3; viscosity of the liquid: 5000 - 7000 cp; liquid type: Viscous polymer

For the above application, kindly suggest the impeller rpm and motor power required. It would be of immense help to me if you can provide me the corresponding thumb rules. Also, what is the suitability of other impellers (helical, etc.) for the above application?

Back to Ask the Experts

More content on this topic:

Featured Sponsor