Paul, I think your idea of the 6x6 beams under the compressor is a good one. If I understand your planned arrangement correctly, I would pipe it up as shown here (pdf file). I have shown some 3/4" copper because your single stage compressor is operating at a lower pressure than a two stage and therefore you do not have the larger reserve margin for pressure drop between the storage tank and the stations. If you were starting out with a two stage machine running 145-175 psig, I'd stay with 1/2" all the way. I am sure 1/2" would work in your case also, but I think the 3/4" would be a more prudent choice in the area where I indicate. I also recommend a separate drop (in addition to the station drop) from the header in the ceiling area of the lower level for a dedicated water drip for the main header instead of combining it with the station drop. The valves shown for draining purposes don't have to be full sized valves. They only need to be "radiator style" petcocks. The isolation valves should be line-sized, preferably ball valves. You can add in the 8" riser sections at each station as shown on that TPTools diagram if you wish. That's a refinement that is probably not necessary but does no harm and could help some. If you have the fittings, go for it. Since you are using a single stage compressor, moisture issues will be a greator concern that they would be with a cooler- running two stage. For that reason you might want to consider using a 10' or so section of copper fin-tube in that 15' run along the lower level ceiling. That's the same stuff used for baseboard hot water heating systems and would help promote better heat transfer and condensation. The reason that I suggest this area for the fin-tube is that the fins are aluminim and are easily damaged. If you can protect the fins w/o obstructing them, locate any fin-tube in that riser section immediately after the compressor instead of in the overhead. The closer to the compressor, the better. Yes, I would stay with type L copper throughout with the possible exception of any fin-tube. I am not sure if that is available in L - maybe only M. If it's available in L use that, otherwise M is OK. The filter arrangement I show for my single station is likely overkill. I set it up conservatively for the most demanding use, which is painting, although it gets used for everything. Most would find a combination separator/filter/regulator unit, such as that sold by Sharp and others, quite satisfactory, even for painting. I strongly recommend locating separators, filters and regulators at each station and not trying to do those functions on a global basis by installing a single set back at the compressor. You want to run the header and distribution piping at the highest pressure available (tank pressure) for more efficient condensation of moisture. The line dewpoint increases with pressure and it is easier to condense out moisture if the line pressure is high. Pressure drops are also less for the same flow if the line pressure is higher. One thing to remember if you are going to purchase additional filters/separators/regulators. They do not have to be line-sized. It's probably better if they are not since line-sized equipment like that usually winds up to be significantly oversized in capacity, which is not always desirable. It's the rated capacity that counts, not the size of the connections. For a 1/2" nominal station, such connections may be 3/8" or even 1/4", depending on the equipment details concerning capacity (in cfm). Take this as suggestions for consideration. Modify as you wish. Good luck with it. Rod
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