Have a steam boiler application where I am being asked to control blowdown water flow close to vessel nozzle with process conditions of 260 deg centigrade and 46 barg i.e. just below vapour point. Moving the flow measurement away from the nozzle to decrease temperature is not a viable option...
Have a steam boiler application where I am being asked to control blowdown water flow close to vessel nozzle with process conditions of 260 deg centigrade and 46 barg i.e. just below vapour point. Moving the flow measurement away from the nozzle to decrease temperature is not a viable option...