By Bob Shah and Jerry Lacatena
Compressed air systems are required in almost all industries such as oil and gas, chemical and petrochemical plants, agro-chem plants, power plants, nuclear facilities, pulp and paper, food, pharmaceuticals, automotive, aerospace, IT/PC industry, industrial manufacturing, large commercial buildings, hospitals, R&D facilities, and so on. The size and scope of the system depends on the type of facility. Hydrocarbon processing facilities have very large air systems with complex configurations.
Compressed air is used as motive force and for utility purposes. Dry air is required for operating control valves, on/off valves, and similar devices that cannot tolerate moisture. Air is typically dried by passing it over beds of silica gel or alumina. The beds are regenerated using source air, and moisture laden air is discharged to atmosphere. If the plant requires nitrogen, the compressed air system can provide the necessary air to separate nitrogen from the air. Some nitrogen generating systems have their own air compressors independent of the general compressed air system.
The main objective for a compressed air system is that it must continuously and reliably provide dry instrument air. While some units in the plant can be down for planned or unplanned reasons, the instrument air supply from the compressed air system must run all the time. If the instrument air system fails, the entire plant comes down. Although it is infrequent that someone worries about efficient operation of the air systems, one must remember that the air systems typically have big compressors running that use a considerable amount of power that can affect the plant economics. While not much can be done to improve the efficiency of the compressors, proper maintenance of the machines can save significant operating costs and prolong the machine life.
When a plant is built or when a major expansion is completed, the overall air system should work flawlessly. It will have a set of air compressors including one or more spares, air receiver(s), air dryer(s), dry air distribution system, and a “wet” air distribution system that includes main headers and laterals going to the units and users. The key element of the distribution scheme is, of course, the guarantee of instrument air (IA) supply. This is accomplished by a simple pressure control scheme which shuts off air supply to non-essential air users to ensure that the normal or unexpected high demand of IA is satisfied first.
In smaller applications and in many chemical plants, ALL of the air is dried and supplied to the users through two headers. Sometimes, only a single header supplies all the air needs.
A real air system, of course, may not come close to an ideal one. Air system problems can be attributed to insufficient pressure, insufficient flow, hydraulic bottlenecks, maldistribution, lack of proper control scheme, leakages to atmosphere, failure to maintain compressors, and dryers. As plants get expanded on a small or large scale, the air systems do not get adequately expanded. The older the plant is, the likelihood that it is more complex and less efficient increases. For illustration, here are some things that have gone wrong before:
Recently, three different reports were produced by a client in-house and by third parties on an air system failure. The air system failure had resulted in large quantities of expensive refrigerant being released to flare in an LNG plant. In addition, there was production loss. There was another unrelated air failure a few days later and the same losses were repeated. Such plants have emergency depressuring valves that open upon emergency situations. They first isolate affected systems and then immediately release pressure from the system to minimize damage from a fire or some other emergencies. These valves have to be FO (fail open upon loss of air). However, the valves need to stay closed and not open inadvertently. The valve actuators are provided with volume bottles or surge tanks with two dissimilar check valves in the inlet line. Should there be an air failure or leak elsewhere, the bottles will continue to maintain the air pressure and the depressuring valves will continue to maintain their intended closed position. All reports concluded that numerous check valves were missing. So when the small failure/leak occurred elsewhere, the bottles lost their air pressure to the leak resulting in the valves opening and discharging large quantities of refrigerant to flare and shutting down the LNG train on low pressure.
Why were so many of the check valves missing? The volume bottles, associated check valves, and piping were not shown on the project P&IDs. They were shown on instrument detail drawings. Here is the problem. When the plant is mechanically completed, a walk-down is performed by the contractor and/or the owner to ensure that everything is installed correctly as intended by the engineering team. Only then will the owner take care, custody, and control of the system/plant. If any component is not on the P&ID, its installation may not get verified and the owner may have accepted the plant with potential deficiencies.
We can survey your system, interview plant personnel, agree on a basis, and later develop a package with necessary documents and drawings that describe your system. Information from this package can be used by the plant personnel in daily operation and in the future. It can also be used by outside parties for future expansions or other air system related issues. With changes in plant ownerships being so common, it is good to have up-to-date and proper information about all systems.
If you are considering process expansion, air system addition needs to be evaluated. In the initial stages, you may need to estimate what that requirement will be. We can assist you, and propose how the new air system will integrate with your existing system.