Floating-head graphite heat exchanger
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Flow rate: Shell side (housing) 100,000 kg/h, tube side (fluid) 3,000 kg/h. Design pressure: Shell side (housing) 0.5 MPa, tube side (fluid) 0.5 MPa. Design temperature: Shell side (housing) 150°C, tube side (fluid) 105°C. Working fluid: Shell side (housing) steam, tube side (fluid) phosphoric acid. How to make assumptions when the inlet and outlet temperatures are unknown? I’m a beginner in design – could the more experienced colleagues give me some advice? :lol
Knowing the medium, temperature, and pressure is enough. It’s okay to add the corresponding instruments and control valves to the design pipeline