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Boiler Replacement and Existing Near-Boiler Piping

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Boiler Replacement and Existing Near-Boiler Piping

A 30-year-old cast-iron atmospheric boiler rated 150,000 Btu/h input is being replaced with a 120,000 Btu/h input condensing boiler in a basement mechanical room. The existing near-boiler piping is black steel with a single circulator on the supply, no primary/secondary separation, and a compression tank connected at the top of the boiler. The new boiler's instructions require primary/secondary piping and a minimum return water temperature of 130 degrees F to avoid flue-gas condensation. The existing system is a series loop of baseboard with a design supply of 180 degrees F and a 20-degree F temperature drop. The mechanical room has two combustion air openings to the exterior sized for the old boiler, and the new boiler is direct-vent capable. The gas line is 1/2-inch nominal at the boiler with a 10-foot developed length from the meter.

1. Identify the piping changes required and explain why the existing near-boiler arrangement is incompatible with the new boiler.

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The new condensing boiler requires primary/secondary piping per its instructions, and the existing single-circulator arrangement with the compression tank on the boiler does not provide hydraulic separation between the boiler loop and the system loop. Without primary/secondary separation, system flow and head interact directly with the boiler, causing flow through the boiler to vary with system conditions and potentially drop below the minimum required flow.

The minimum 130 degrees F return temperature is a corrosion and efficiency requirement: sustained return temperatures below the dew point of the flue gases cause condensation inside a boiler not designed for it, and the manufacturer's minimum must be maintained. With a 180/160 degree F series loop, the return is 160 degrees F at design, which is acceptable at design but may fall below 130 degrees F during shoulder-season part-load operation with a series loop. The fix is primary/secondary piping with a boiler circulator and a system circulator, plus a bypass or thermostatic mixing arrangement to maintain minimum return temperature during low-load periods.

The compression tank location must be reconsidered - with primary/secondary piping the point of no pressure change moves, and the tank and air elimination must be located at the correct point in the primary loop per the boiler instructions.

2. Assess the gas supply and combustion air provisions for the new boiler.

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Gas supply: the new boiler at 120,000 Btu/h input draws roughly 120 cubic feet per hour of natural gas. A 1/2-inch nominal line at 10 feet developed length may be adequate for that load depending on the table used and the allowable pressure drop, but it must be verified against the gas piping table for the actual length including fittings and the available pressure at the meter. The appliance's minimum inlet pressure and the manifold pressure must be confirmed, and the line must be sized for the specific gravity and heating value of the gas supplied. If the existing line was sized for 150,000 Btu/h it may be oversized in capacity terms but the connection size and the regulator must match the new appliance's requirements.

Combustion air: the existing two openings were sized for an atmospheric boiler drawing room air. If the new boiler is installed as a direct-vent appliance, room-air openings are no longer the combustion air source, but the openings may still be required for ventilation and dilution of other appliances in the room. If any other atmospheric appliance remains, the combustion air calculation must be redone for the remaining appliances. The direct-vent termination must also meet clearance requirements to openings, vents, and grade.