Hi Mayo,
I don’t follow your reasoning entirely, but your experiments (and feedback) are very useful! We don’t have a vacuum table for our ShopBot, because we cannot decide what a multi-purpose system should look like – so my ramblings are based on theory and experience of “fluid transfer” in other applications.
Any extractor fan (shopvac) has a performance curve depending on the rate of air flow through the “turbine”. The highest pressure (vacuum) is attained at zero flow (left side of graph) and the highest flow rate is achieved with the lowest pressure (least resistance)(right side of graph)
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Okay, I stole this curve from a metric website, but let us imagine the vertical scale is “inches water” PRESSURE while the horizontal scale is “cubic feet per minute” FLOW RATE. So here we have a pump that can suck 210” or move free air (no resistance) at a rate of 80 CFM. But it cannot do both at the same time! Some unscrupulous suppliers will show you this curve and tell you that you have a 210” at 80CFM pump. Lies! In this case 150” @ 30CFM would be correct. (or 50” @ 60CFM, or 200” @ 15 CFM)
The two parameters of PRESSURE and FLOW RATE are important to us in the following way:
1. PRESSURE is going to give us our “clamping down force” if we multiply it with the area of the work-piece. So we want nice high pressures. (Okay, we are on the vacuum side of zero (negative pressure) , but we want to be as far away from zero pressure as possible – the terminology can be confusing)
2. FLOW RATE is caused by leakage, and we saw from the curve above that if we have a high flow rate then the pressure drops off. So we want to work at minimum flow rates, least leaks, to give nice holding pressures. (to the left side of the curve)
Generally a higher horsepower vac unit will have a curve lying above and to the right of low horsepower unit of similar construction. This means that a bigger vac unit will manage a higher flow rate while holding the same pressure. ie. More tolerant of leaks. Different types of pump (vane, turbine, piston, liquid ring) have different shapes of curves and you may find some curve crossovers if you compare them – vanes will be higher and to the left – turbines will be flatter and to the right . . . . .
The size of the canister (gallons) attached to the shopvac is not important at all!!! (Except in special cases where the canister can be pre-evacuated and special valving allows a quick suction on the workpiece to create the initial seal . . . . )
Now to come more directly to Mayo’s question (I hope), we must realise that the pressure inside the 8’x4’ box is the same everywhere in the box. Each peg-board hole has the same vacuum pressure at its bottom end as any other hole. The more air that leaks into the box causes us to move to the right on the curve and the pressure in the WHOLE box drops accordingly. Therefore as you cut through the sheet and introduce leaks, everything deteriorates rapidly, especially since the square inches per part also reduces quickly.
The only way I see around this is to go for big pumps (leak tolerant), seal obvious leaks and keep parts tabbed together (let the holding area of the scrap work to your advantage).
Good luck and keep us informed. (PS next week I am in Germany again, so if I go quiet, it is not because I have lost interest)