valvepuke
Mechanical
- Jun 14, 2006
- 21
I have been reading many threads on the subject of handling condensate from a reboiler. We are in discussions with our client and can't seem to come to any agreement. The problem is that my client's condensate return header operates at 90 degC and 1 bara. The condensate from our reboiler is at 152 degC and 5 bar. Anything we do to drop the pressure into the condensate return piping will result in excess flashing. Also, my client is concerned with any two phase flow coming out of the reboiler due to process conditions. Here is what we want to propose to the client.
We will control steam into the reboiler with a CV. Condensate from the reboiler will flow to a condensate pot. Condensate pot will have a level transmitter. Condensate will flow to a cooler where it will be cooled to around 70 degC. A control valve downstream of the cooler, controlled by the condensate pot level, will control flow of the cool condensate into the atmospheric pressure return header.
Using a cooler seems like a lot of extra effort but cooling water is available and I just don't know what else to do with a lot (15750 kg/hr) of hot condensate and still satisfy my client. Would love to just dump it overboard!! Also, the client doesn't like steam traps.
Any thoughts would be very welcome.
We will control steam into the reboiler with a CV. Condensate from the reboiler will flow to a condensate pot. Condensate pot will have a level transmitter. Condensate will flow to a cooler where it will be cooled to around 70 degC. A control valve downstream of the cooler, controlled by the condensate pot level, will control flow of the cool condensate into the atmospheric pressure return header.
Using a cooler seems like a lot of extra effort but cooling water is available and I just don't know what else to do with a lot (15750 kg/hr) of hot condensate and still satisfy my client. Would love to just dump it overboard!! Also, the client doesn't like steam traps.
Any thoughts would be very welcome.