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Calculations related to condensate flash tanks

2016-01-26View Original

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I had never been exposed to flash tanks before; this time, I need to build one to recover 70 t/h of air-conditioning condensate and process condensate at 0.5 MPa. This water needs to have its iron removed before it can be sent to the deaerator for further use. How do I calculate it? Is there still pressure after coming out of the flash tank? Will steam be produced again as it enters the subsequent processing equipment?

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