Problem with Weight Consistency

Posted in: , on 25. Oct. 2009 - 01:52

I am having problems with getting consistent weight results with my gross bag weigher. I have read most of the forums and believe that the problem lies in my hopper and how it feeds the trough conveyor.

The hopper is steep walled and vee shaped and I have placed an insert into it in order to approve mass flow. There is a vibrator attached to one side of the hopper, parallel to the 100 mm screw conveyor which extracts the Zinc Oxide Feed Grade material. The Zinc Oxide has a density of app. 2.2 and flows well. It is very aerated though. The screw conveyor is of trough design and of constant pitch throughout. The trough extends from the hopper app. 50 cm and feeds the weigher. The screw rotates at app. 100 rpm and I will reduce it's speed to app. 30 rpm with a frequency converter for the dribble stage.

Unfortunately the unit is not a feeder type but a conveyor but I thought that I could possibly make some physical and mechanical modifications in order to improve it's accuracy.

1) Would replacing the trough conveyor extension with a tube like enclosure increase the accuracy of the screw?

Any advice would be greatly appreciated as I must make do with existing equipment in the meantime,

Thank you for your help.

Alan

Weight Variations

Posted on 26. Oct. 2009 - 10:50

A fine, cohesive material like Zinc Oxide can vary considerably in density and flow condition when aerated, but be akward to flow when settled. The length of the outlet slot in the hopper is not clear, but a uniform pitch screw will only extract from over a short axial distance and a 100mm diameter screw is quite small, so the gravity flow potential of the system is very limited. If fully fluidised, the product can flush through a relatively long casing, particularly if a 'U' trough shape with clearance above the screw, so fitting a circular casing or 'choke' section in the machine will help to give better control.

If aeration pads are fitted, these are often connected to an air line supply at a set pressure. This can result in excess air injection to fluidise the powder, or at very least, an indeterminate state of flow and dilatation. You may try cutting down on the amount of air injected and supply a limited, controlled volume of air, rather than setting the pressure, as this will tend to secure a more consistent flow condition and more stable density.

Thank You For Your Prompt Reply-Weight Consistency Problem

Posted on 26. Oct. 2009 - 08:46

Thank you for your prompt reply. I mistakenly gave the inpression that I am using aeration pads in the hopper. I am not using these but have fitted a rotating electric vibrator welded to a cross beam running the length of the hopper parallel to the screw. The cross beam, to which the vibrator is attached, is app. 20 cm above the base of the hopper and screw trough. I don't believe that the material is flooding over the screw in the trough extension, as I am able to open the top cover of this part and observe the flow.

What I do indeed observe is that there is inconsistency in the amount of powder filling this trough section. As I stated, this trough extends from the hopper body by app. 50 cm.

I will indeed fit a choke section to the screw extension as you suggested.

I have also read about installing louvers or small flat sections of metal at the end of the "choke" tube? Can these louver pieces also increase the accuracy?

Can you comment about the speed of the dribble feed relative to the fast fill speed

( 100 rpm fast and 30 for dribble)?

Should I stop the vibrator before reducing to the dribble speed?

Thank you for your help.

Alan

Feed Fluctuation

Posted on 27. Oct. 2009 - 11:15

If the exiting screw has a variable fill level it shows that the flow from the hopper is not reliable or fast enough to fill the screw. This limited and erratic flow rate is probably due to 'air retarded' flow on the small span of opening. This behaviour occurs with fine powders that have difficulty expanding to flow because the void demand for air is inhibited by the low permeability of the mass and so develops a negative pressure differential to ambient above a collapsing arch. This partial vacuum holds up the material in the bin . Collapses through the outlet is then uneven as portions break away from the undersurface of the arch and 'flow' takes the form of failing dynamic arches. In some cases the surface 'rains' powder from an arch of increasing size until the span exceeds the critical arch size and it fails to fill the void in the hopper, and either starts the process again or flushes through, depending on the state of the bed. The dilated condition in the feed screw will give a misleading impression of the situation in the hopper as the looseness is caused by the material falling away from the bulk, whereas the bulk may be quite dense.

In this instance it is obviously not practical to enlarge the span of the outlet to overcome the flow reluctance so the best thing is to seek to satisfy the air demand of expansion by the controlled volume air supply method previously described. This should be entered centrally at each side, a little distance above the minimum span, say about 150mm. I suggest trying a total air injection rate of approx. 40 litres/min with the facility to increase or decrease the supply as the result indicate.

You will find that the screw will then deliver at a faster rate and it will be prudent to switch to dribble feed at 90% weight and slow down the dribble feed to about 10 or 15 rpm for better cut off accuracy. Please let me know if sucessful.

Lyn

Thank You Again.

Posted on 27. Oct. 2009 - 03:50

Lyn,

Thank you for your detailed explanation. I will install the pads and try your solution.

Please explain what you mean by "This should be entered centrally at each side, a little distance above the minimum span, say about 150mm" regarding position for installing the pads?

What or where is the "minimum span" in relation to the trough (screw)?

The hopper dimensions are 1450 mm long at top, 1000 mm wide at top,1000mm long at bottom (top of screw trough), 100 mm wide at bottom (screw trough width), and 800 mm high.

Thanks for your patience!

Alan

Erratic Flow

Posted on 27. Oct. 2009 - 04:11

From the dimensins given the side wall inclination is just over 60 degree to the horizontal and the end walls are at 74 degrees, giving a gully angle of around 58 degrees, which is also presumably square cornered rather than radiused. Also, the 1000 mm long outlet slot is four times the length of the pitch, so that the hopper will not mass flow and the screw will not extract from the full length of the slot with the uniform pitch screw. Accepting this poor design, it should be possible to fill screw much better by fitting the pads in the center of the outlet length, about 150 mm above the lower edge. The hopper width at that point is around 170mm.