Drop-through Metal Detector / Rejector

Posted in: , on 23. May. 2013 - 22:01

Hi everyone,

I'm involved in a project to install a drop-through metal detector c/w contaminant rejector diverter in our plant and I am wondering if anyone can share with me what equipment they have seen in use to feed such a detector. We're looking at a Thermo Scientific APEX model. All of Thermo's literature indicates that the product must be dropped from zero velocity through the detector from a point no more than about 19" above the opening of the detector. The purpose of this is so that all material is moving through the detector at a speed that is well known and accurately repeatable. This allows the reject diverter to be opened just in time to catch the contaminant but no longer than necessary to minimize the amount of good product that is rejected with the contaminant. This "zero velocity drop" is a concept that appears to be common among all drop-through metal detector manufacturers.

The problem that I'm facing is that a "zero velocity drop" seems to be something that works in theory but no one, including the manufacturer, can offer concrete advice on how to attain this. Certain other pieces of equipment (rotary valves, scalperators, screeners, etc.) drop the product nicely but none meet the letter of the law concerning the manufacturer's recommendation. Thermo has provided no assistance in this aspect of the design; they seem to be afraid of recommending anything other than this theoretical ideal.

The first problem is that the drop height is often much larger than the recommended 19". The concerns are that the product may be falling at a speed great enough that the diverter cannot open in time to catch the contaminant and that the dynamic impact of a faster falling product may damage the diverter or apply so much force to it that it's unable to close at all.

The second problem is that it's virtually impossible to match up the detector's inlet dimensions with a piece of equipment that has an outlet exactly the same size. This may be possible with a detector with a circular opening but we're looking at one with a long, narrow opening for better sensitivity. This requires some sort of funneling transition piece that results in some product sliding down the side of the funnel and therefore passing through the detector at a slower speed than the product falling through the centre of the detector.

I realize that we're going to have to compromise on our design but I'd like to draw on the experience of others who have similar systems installed in their plants. How have you fed your drop-through metal detector and how much leeway is there in varying from the manufacturer's recommendation?

Grant

Roland Heilmann
(not verified)

Friction In Several Places

Posted on 31. May. 2013 - 08:07

Hi Grant,

0 veloc. drop:

suppliers don't say so much in advance because it heavily depends on materials properties as density, size & shape of particles, moisture content, angles of friction, repose / friction coefficient to the chute surface etc. However once all those parameters clear, it's the supplier which must support you in designing, lest you pay their fee. Chute angles may be chosen that enable slow movement. Then there's the not uncommon approach of trial and error, there's people out there who do bulk material property analysis for a living.

My point: in project design stage i specify feasible limits for equipment operation, then the tenderer has to comply to that with his offer. How could that happen that after contract you are confronted to a seemingly no-go, again with no leverage upon the supplier?

adapter inlet:

If it is geometrically impossible i cannot judge without some sketch or so. A funneling adapter might however be achievable with some resources coming from good 3D - model engineering. Did you consider adapted flow improvement measures as pressurized air, vibros or so?

My point (without any disregard to your decision): You must somehow be very upset, clearnaming like that , but are you sure and how will this act on your second choice? If there's one at all... They might fear to get it alike. Perhaps the issue needs more engineering resources and less :-( ?

Regards

R.