Evaporation dryer and method for operating same
View Patent ↗The invention relates to an evaporation dryer ( 1 ) for drying particles, having—a process chamber ( 10 ) with at least one product inlet ( 11 ) for supplying the particles to be dried into the process chamber ( 10 ) and a product outlet ( 12 ) for discharging dried particles from the process chamber ( 10 ), —a heat exchanger ( 20 ) arranged within the process chamber ( 10 ), —having at least one inlet ( 21, 211 ) into the heat exchanger ( 20 ) for pressurized steam as process steam and at least one condensate outlet ( 22, 222 ) from the heat exchanger ( 20 ), wherein—the at least one condensate outlet ( 22, 222 ) is connected to an expansion tank ( 30 ), wherein at least one pump ( 40 ) is connected to the expansion tank ( 30 ), and the expanding steam is pumped out of the expansion tank ( 30 ) and supplied to the process steam.
1. An evaporation dryer for the drying of particles, comprising:
a process chamber having at least one product inlet for feeding of particles to be dried into a process chamber space and having a product outlet for evacuation of dried particles from the process chamber;
a heat exchanger arranged within the process chamber, the heat exchanger comprising
at least one inlet for highly pressurized steam as heating steam and at least one condensate outlet connected to an expansion tank,
wherein the expansion tank is connected to at least one pump which pumps off flash steam from the expansion tank and supplies the flash steam to the heating steam,
wherein the heat exchanger is of multi-stage construction having at least a first stage and a second stage,
wherein to the first stage comprises a mixed steam of the heating steam and the flash steam, and
wherein the second stage is configured such that the heating steam is fed to the heat exchanger.
2. The evaporation dryer as claimed in claim 1 , wherein the first and second stages are assigned separate condensate tanks which are coupled to the expansion tank.
3. The evaporation dryer as claimed in claim 2 , wherein the separate condensate tanks are coupled to the expansion tank via a control valve.
4. The evaporation dryer as claimed in claim 2 , wherein the separate condensate tanks each have a pressure level equating to or below a pressure of the heating steam.
5. The evaporation dryer as claimed in claim 2 further comprising a connecting line from the expansion tank leads to a mixing point arranged downstream of a steam generating device, wherein the heating steam is mixed with condensate from the expansion tank and/or the separate condensate tanks in the mixing point.