Due to the need for several particular process loads — such as sterilization and kitchen/food prep — steam plants are typically found in hospitals. Steam plants are also found on university campuses. Typically, there is one or more (relatively old) central campus steam plant that delivers high-pressure steam throughout the campus. Regardless of their location and the types of loads they serve, these steam plants are typically 20 years old or older, though some may be more than 30 years old depending on the quality of the maintenance process and availability of funding. As such, steam plant replacement projects are often quite challenging, typically due to the age of the plants and the lack of complete design documents. Such a scenario, however, makes for a very exciting engineering project.

Once a design engineer is assigned on a steam replacement project, it is somewhat tempting to jump straight into the design phase (i.e., selecting/sizing equipment, system diagrams, etc.). However, we believe instead that a proper approach requires a series of steps preceding the design of what type of boiler or size one will specify. These phases should include, but are not limited to: 1) Obtaining as much information (e.g. drawings) associated with the original design intent; 2) Identifying the current loads served by the plant; 3) Asking what the owner desires of the new plant (i.e., redundancy, quality, etc.) and 4) Identifying the impact of the new code requirements on the design of the new steam plant.

Phase one typically involves a series of site visits and meetings with the facilities personnel that maintains the plant. As previously mentioned, the original design drawings are often incomplete. To make matters worse, the documentation for later projects (i.e additions to or alternations of the steam plant) is often also missing. As such, it may be required of the design engineer to spend time surveying the entire steam system and identifying what each line services.

One should not neglect the value that the local maintenance personnel can bring to these projects. In many scenarios, these individuals have been maintaining the plant from the moment it got started and could share valuable insight about the loads the plant is serving and its deficiencies (i.e short cycling of boilers, deficient condensate piping connections, corrosion/pitting). For a hospital, it’s critical that the design engineer analyzes the existing fuel system. This includes, but is not limited to, electrical power (i.e. is the fuel oil system on the life safety branch or on the optional standby branch?), controls, etc. The existing fuel oil system must be capable of supporting the new steam plant.

Once one has identified the loads/equipment served by the steam plant and its current deficiencies, the next step would be to identify the size of these loads. This step will inform the design engineer if the current plant is undersized, oversized, or sized accurately.

After the completion of phase one and two, it’s our recommendation that the design engineer sets at least one meeting with the owner to go over the findings. This approach will give an owner the opportunity to have a better understanding of the scope of the work and the existing conditions. It’s crucial for the owner to understand what items are not included in the original scope of work. For example, and in the case of a hospital, the outcome of phase one and two may be that the existing fuel oil system or boiler controls system is not connected to the emergency power system. This means that the owner must now find the funds to pay for the additional scope such that the new plant is code-compliant. Further, it’s important that the design engineer review the resiliency aspect of the fuel system to determine if it meets the joint commission and NFPA requirements for amount of run time, which is typically 96 hours. Lastly, but not less important, regardless of the building type we recommend, the design engineer must have a solid understanding of the existing chemical treatment system and its capabilities. Poor chemical treatment can have a significant impact on the condition of the existing piping and longevity of the steam system components.

Under phase four or earlier, the design engineer needs to identify and/or update the code requirements that are applicable to the project and to inform the owner of the impact these requirements will have on the design of the new steam plant. For example, and in the case of a hospital, due to various building additions, the existing steam plant could be at its maximum operational capacity, despite being designed with redundancy. However, the local Authority Having Jurisdiction (AHJ) may require the new plant to have N+1 operational redundancy. It’s worth noting the difference between operational capacity and design capacity. The operational capacity is used to describe the actual measured loads. The design capacity is the total connected load to the plant, which would be greater than the operational capacity.

As it relates to hospitals, FGI guidelines, and implicitly ASHRAE 170–2017, require these facilities to “provide heat sources and essential accessories in number and arrangement sufficient to accommodate the facility needs (reserve capacity) even when any of the heat sources or essential accessories is not operating due to a breakdown or routine maintenance.” Per the same document, one can take exception from this requirement,“… if the ASHRAE 99% design heating dry-bulb temperature is greater than or equal to 25^ºF…”

The efforts/processes described in the last two paragraphs above have a significant impact on the outcome of a steam plant replacement project. If a plant is at full operational capacity and there is a requirement (i.e either code or by the owner) to have N+1 operational redundancy, and if one cannot fit additional boilers within the footprint of the existing plant, then a building addition to the existing plant may be required. As such, the overall project may be delayed if the original scope of work and budget associated with the steam plant replacement did not include the addition and/or enlargement of the existing steam plant room to house more boilers.

After the completion of phase four and a clear scope of work has been defined, the design engineer has the minimum amount of information required to start the design of the new steam plant.

One of the main design items that needs to be clearly defined early in the design process is the design steam pressure of the boilers and the steam pressure that is to be delivered to the various loads throughout the building or throughout the campus. Depending on the requirements of the local AHJ and/or the owner’s design guidelines, steam pressures could be classified as follows: 1) low-pressure steam, 15 psig or less; 2) medium-pressure steam, between 15-45 psig; and 3) high-pressure steam, above 45 psig. Some jurisdictions only allow two pressure classifications: 1) low-pressure steam, 15 psig or less, and 2) high-pressure steam, above 15 psig. These pressure classifications play an important role in the design and selection of the various piping systems and their associated accessories.

> FIGURE 1. Proposed high-pressure steam header layout.

In the case of a steam plant that needs to deliver high-pressure steam (i.e 100 psig), it’s our recommendation to provide a main steam header (as shown in figure 1) downstream of the steam boiler and upstream of any loads and/or pressure-reducing stations. Further, double block and bleed isolation valves should be provided for each load.

 One of the most crucial elements associated with the success of the design and operation of a steam plant is the management of the condensate return systems. Typically, there are three pressure types of condensate return systems: low-pressure, high-pressure, and pumped condensate. If the design includes medium-pressure steam, then a fourth condensate system (i.e. medium-pressure condensate return) should be considered.

Even though some AHJs (see Department of Veterans Affairs, detail SD232111-09) do allow for the discharge from a high-pressure steam trap into a pumped condensate return line, it’s our recommendation not to combine the various condensate return systems upstream of the surge tank. Instead, with the exception of the pump condensate line, the main line from each condensate return system should be brought in the vicinity of the surge tank and discharged into a flash tank before discharging into the surge tank (see figure 2). As noted, there are many different solutions and processes to a steam plant design and design challenges.

> FIGURE 2. Proposed condensate return system approach.

There are many books and guidelines written about the design and operation of steam plants due to its complexity. As outlined throughout this article, there are many code requirements and factors that impact steam plant design. Despite the many challenges steam plants present, the design of a steam plant is not a lost art. It’s simply an art that requires the utmost attention to detail and engineering skills.