Temperature as a Design Input, not a Constraint

Q = m cp dT

Cast your mind back ten years. Gas boilers and combined heat and power (CHP) were the stars of any plant room: low CAPEX, low OPEX, easy to install, simple to run, and comfortable operating at high delta Ts between flow and return. The market had moved from a temperature set of 82/71 down to 70/40 […]

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