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Heat exchanger selection problem

2020-08-05View Original

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There is a steam condensate tank from which steam constantly emerges at the top; it’s possible to recycle that steam. It is planned to add a heat exchanger to the top gas pipeline for cooling with circulating water. The temperature at the top of the tank is around 70°C, and it is planned to reduce this to 30°C. The gas flow rate is approximately 1400 Nm3/h, and the pipes have a diameter of around DN200. What size heat exchanger is required? It would be helpful to have an approximate calculation process. Thank you!
Reply #22020-08-06
It is recommended to get a copy of \"Principles of Chemical Engineering\" to read, or to contact a heat exchanger manufacturer – they will provide you with comprehensive guidance. It’s worth giving it a try.
Reply #32020-08-06
70C? It should just emit white smoke occasionally; can it produce a continuous flow?
Reply #42020-08-10
Do you intend to recycle the steam condensate? Using circulating water for cooling is not appropriate; as the temperature of the circulating water rises, it needs to be lowered again. It would be better to consider spraying deoxygenated water into the condensate tank.
Reply #52020-08-11
You’re trying to design a heat exchanger, right? It’s pretty similar to my graduation project; it took me several months to finish it – so how can you expect to figure this out so quickly?
Reply #62020-08-12
Cooling with an upper heat exchanger, taking condensation recovery into account – the cost-effectiveness is too low; it’s not worthwhile; It’s necessary to recalculate the thermal integration; determining where this amount of steam’s thermal energy can be utilized is what’s reasonable.
Reply #72020-08-13
Normally, it can be calculated using htri, but the following factors need to be taken into account: 1. Whether this steam at 70°C is saturated steam, or what the operating pressure is for the steam supply; 2. Circulating water conditions are provided; due to limitations imposed by the inlet water temperature, it is generally difficult for circulating water to cool or condense the steam to 30℃ ; 3. Does the steam have a stable flow rate? ; 4. If a cooler/condenser is to be used, please consider its cost-effectiveness ;

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