The process for making Nylon polymer is like a solid rocket, once you hit start there is no pause button. We have about a thirty minute window if we loose any part of a polymer system. An overhaul cost five days of production and between $150,000 and $200,000, this is whether the line ran 1 hour or 1 year and we have 17 production lines.
Another reason for the 100% inspection was that two independent experts on explosions and detonations concluded that we sitting on a time bomb as the majority of our piping was in confined space. Therminol and Dowtherm will detonate at 927F and there is the big possibilty of BLEV. Then alone cam OSHA and lower the limit of Therminol vapor release to about 1 tablespoon full. Also during this peroid we have the big leak leak mention in the last post, Fortunately this was before the lowering release limits. Another problem we encounter was welder apathy, they either didn't like making socket welds or just couldn't.
Normally Leaks caused by porosity are small enough to be penned shut.
Our process areas are very confined spaces with very little room to manipulate pipe, 3/4" to 2", so the use of socket welds were deemed the most expedite way to accomplish the piping installation. A secondary factor not normally considered is that during the initial construction the majority of small CS pipe was welded by acetylene torch. It was a lot quicker to make a fillet weld on a socket than using the existing electrodes or acetylene torch of the day to make a butt weld.
We look at the gap. If the pipe was cut with a pipe cutter or portaband. The portaband cut are normally the ones that caused problems as a lot of cuts are biased by as much as 1/4" so one side has the proper insertion and the other is flush with the end of the fitting. We require that the inside edge of the fitting and the pipe be fused, no bridging of the fillet weld. No discernible porosity. Two passes on the fillet weld. Fitters using the fitting as a crutch, no insertion of the pipe in the fitting.
We have both a primary vapor heating system system, 70 psig and 650F, and a secondary system, 30 psig @ 600F. Each line has 6 reboilers that are feed primary system condensate and the primary vapor is used as the heating media to make the secondary vapor use to heat our process vesssels. We only use the latent heat of vaporization of the heating media.