Compressed air piping installation - design and assembly

    The pneumatic installation determines how much of the air generated in the compressor room actually reaches the machines, and at what pressure. Even a well-chosen compressor cannot fix a network with an undersized cross-section, full of restrictions and without drainage. We design and install compressed air pipework, starting with a demand survey, through material and diameter selection, to a pressure test and as-built documentation.

    What makes a good installation

    A good compressed air installation is invisible in operation: the pressure at the farthest point barely differs from the pressure in the compressor room, there is no standing water in the pipes, and expansion does not require rebuilding the main line. Four things settled at the design stage decide this.

    Ring or branch layout

    A ring (loop) installation feeds air to every point from two directions. Flow in a single section is lower, the pressure drop smaller, and cutting off part of the network for rework does not shut down the whole hall. A branch layout, where long spurs run off one main line, is cheaper to build, but the farthest receiver always operates at the lowest pressure. In larger halls we design a ring with sectioning options; in smaller plants we go with a branch layout and a generously sized main line.

    Pressure drop below 0.1 bar

    The design target for the entire distribution network is a pressure drop of no more than about 0.1 bar from the receiver to the farthest take-off point. That is achievable with the right diameters and a sensible number of fittings. Every tenth of a bar that has to be made up by raising the compressor setpoint costs roughly 0.7 percent more energy, and an old, narrowed network can accumulate well over 1 bar of unnecessary difference.

    Slopes and drainage

    Water still appears in the network even downstream of the dryer: at start-up, during a dryer fault, on hot days. That is why we run main lines with a slight slope in the direction of flow and fit drainage points with condensate drains at the lowest points. Take-offs to consumption points are led off the top of the pipe in a gooseneck shape, so water from the main line does not run straight into the machine.

    No restrictions or unnecessary bends

    The biggest losses in existing installations come from accidental restrictions: a reduced tee, an undersized ball valve, a quick coupler with a mismatched bore, a long hose coiled up. Every bend and every fitting adds equivalent length to the pipe run, so we route the shortest sensible path, use large-radius bends and never reduce the bore just before the receiver.

    Compressed air pipe materials

    We select the material based on operating conditions, required air purity, planned expansion and budget. The difference in material cost is often smaller than the difference in installation time, and in the long run what matters most is whether the pipe bore stays the same after ten-plus years of operation.

    Press-fit aluminium

    Today's standard material for new plant installations. Smooth bore, no corrosion, constant cross-section over years of use, light weight and very fast assembly with press-fit connectors, plus easy expansion and the ability to reuse components. The system is designed for compressed air and available in a wide range of diameters. Material cost is higher than steel, but shorter installation time and no loss of flow capacity over time usually make up for it.

    Galvanized steel

    A classic solution, cheap as a material and acceptable with wet air, but labour-intensive to install and vulnerable at cut and threaded areas where the coating is broken. Over time corrosion products and deposits build up on the inner wall, reducing the bore and contaminating the air. We use it where we need to match an existing network or where operating conditions rule out other materials.

    Stainless steel

    The most expensive option, chosen where air purity and full corrosion resistance matter: selected processes in food processing, pharmaceuticals, chemicals, and installations working in aggressive environments. Durability is very high, but the cost of material and joint fabrication clearly raises the budget, so it is usually used only in sections with the highest requirements.

    Plastics approved for compressed air

    Plastic systems intended for compressed air can be a good choice at lower pressures and smaller diameters, for example distribution at individual workstations. They resist corrosion and install quickly, but need attention to the air temperature after the compressor, contact with oil, and mechanical loads. We only ever use systems with the manufacturer's declaration for compressed air and for the given pressure.

    What we do not use

    We do not use plain black steel for compressed air, because in the presence of condensate it corrodes from the inside, and rust and scale travel to the receivers, clogging filters, valves and quick couplers. We also do not use PP water pipes or ordinary domestic water piping: they are not designed for hot, pulsating air combined with oil, their pressure ratings drop with temperature, and a leak in such a section under pressure is dangerous. The material must always carry the manufacturer's approval for compressed air.

    Diameter matters

    The most common mistake in compressed air installations is a bore sized by eye or copied from an old network built around a completely different machine fleet. The effects only show up after the plant expands, and are paid for in the energy bill.

    • Why the bore matters more than it seems

      Flow resistance rises very fast as the diameter shrinks, so one saving made during installation stays in the system for years as a fixed energy cost. An undersized bore shows up as a pressure drop under higher demand, weaker tool performance at the far end of the hall, and the need to raise the compressor setpoint just so the farthest receiver works correctly at all.

    • What it costs in energy

      Every 0.1 bar of drop that has to be made up with higher generation pressure means roughly 0.7 percent more energy used by the compressor. With a network suffering a real drop of 0.5 bar and a 37 kW compressor running multiple shifts, we are already talking about a clear line item on the bill that gets paid every month without ever showing up on any breakdown.

    • How we select the diameter

      We size the diameter for the flow in a given section and for the total route length, counting the equivalent length of bends, valves and tees, not just metres of pipe. On top of that we add a margin for plant growth, because expanding the network is much cheaper when the main line still has spare capacity. In practice we design the main line generously, size take-offs to the specific receiver, and when modernizing we check whether the old pipe's bore has not been narrowed by deposits.

    Take-off points and air preparation at the machine

    The last few metres of an installation can ruin the effect of a well-designed main line. This is where restrictions and leaks most often appear, so we treat take-offs and connections to machines as part of the design, not a minor installation detail.

    Take-off points

    We place take-offs where people and machines actually work, with spare outlets so shortages are not solved with hoses dragged across the hall. Every take-off is led off the top of the pipe and fitted with a shut-off valve, so replacing fittings does not require depressurizing the whole section.

    Air preparation at the machine

    Overall air quality is ensured globally by the dryer and filtration in the compressor room, but at the receiver it is worth having a local preparation unit: a filter, a pressure regulator with gauge if needed, and a lubricator for pneumatic hand tools. Local pressure reduction to the value the machine actually needs protects it and lowers air consumption.

    Flexible connections

    We connect to the machine with a flexible hose sized to the demand, as short as possible and not coiled up. The flexible section absorbs vibration and allows the machine to be repositioned, but it is also the most common leak point, so we use full-bore quick couplers and check these points during inspections.

    How we work

    We start with a measurement and a conversation about production: how much air the receivers use, which of them run at the same time, what the shift pattern is, and what pressure is actually needed at the most demanding point. This is the basis for the compressed air installation design: route layout, ring or branch configuration, section diameters, and the placement of take-off points, shut-off valves and drainage.

    We also carry out installation at a running plant, in stages. We build the new network alongside the existing one and switch receivers over during downtime windows, night shifts or weekends, so production does not stop because of installation work. After installation we run a leak test at working pressure and check the pressure at the take-off points under real demand.

    Finally we hand over as-built documentation: route layout, diameters, and the location of valves, drainage and take-off points. This document saves time on every future expansion and when diagnosing pressure drops.

    See also compressed air system modernization, compressed air energy audit, compressed air tanks and compressed air leak detection.

    Compressed air piping installation - FAQ

    The most common questions about materials, diameters and the installation process.

    For new plant installations we most often use press-fit aluminium: smooth bore, no corrosion, fast assembly and easy expansion. Galvanized steel can be justified when matching an existing network, and stainless steel where air purity matters. We do not use plain black steel or PP water pipes, because they are not designed to work with compressed air.

    A ring layout gives a smaller pressure drop, more even conditions across the whole hall, and the ability to cut off part of the network without stopping the rest, so in larger facilities it is worth the extra cost. In a small plant with a few receivers a branch layout with a generously sized main line is enough. We make the decision after inspecting the hall and the machine layout.

    The diameter is calculated for the flow in a given section and the total route length, including the equivalent length of bends, valves and tees, plus a margin for plant growth. The target is a network pressure drop below about 0.1 bar. A few extra centimetres of bore on the main line cost once, while an undersized bore is paid for on every energy bill.

    Yes, and it is the most common case in our work. We start by checking whether the existing main line still has spare capacity and what condition its interior is in. The expansion can be done in aluminium and tied into the old network, and it is usually worth removing the restrictions that were already hurting pressure before the expansion.

    Distribution for a few workstations usually takes one to two days. A main line with take-offs in a production hall most often takes a few days, and a large facility with a ring layout, sectioning and many take-off points is planned in stages over a longer period. We give timelines after inspecting the site, together with a breakdown of work into stages.

    Yes, we standardly work in stages at an operating plant: we build the new network alongside the existing one, and schedule switch-overs and any work requiring depressurizing for downtime, night shifts or weekends. After installation we run a leak test and hand over as-built documentation with route layout, diameters and fitting locations.

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