I would like to know what will be the pressure at the downstream of steam trap located in the Medium pressure(13 Kg/cm2, 230 Deg C)steam heater/exchanger condensate outlet. Is it possible to deliver that steam condensate downstream of steam trap to a deaerator or a condensate vessel having pressure of around 1.00 kg/cm2 . Steam used in the steam heater/exchanger will be at 13 Kg/cm2 pressure and 230 Deg C temperature. My assumption is that steam condensate at the exchanger outlet will be available at almost the same inlet steam pressure i.e. 13 kg/cm2 minus the pressure drop across the exchanger.we have steam trap located at the exchanger outlet for total condensation the exchanger outlet steam. What will be the condensate pressure still available at the downstream of steam trap ? Is it possible to deliver that condensate to a vessel having 1.00 kg/cm2 pressure? or do we need to put a condensate storage vessel and then pump it out to the pressure of 1.00kg/cm2?
Thanking you
Regards,
BJD