Tube Length: In general, the greater the ratio of tube length to shell diameter, the more economical the exchanger. 1 inch tube are normally used when fouling is expected, or low ∆P is required. ![]() Shell Selection depends on available ∆P, the E-type is the least expensive shell.ģ/4 ~ 1 in are more compact and more economical. Design You define most exchanger geometry and enough process conditions for Xist to calculate the required heat duty. Simulation You define exchanger geometry and fewer process conditions for Xist to calculate the required heat duty. Rating (Default) You define exchanger geometry and enough process conditions for Xist to calculate the required heat duty. Setting Unit: select Edit > Data Units, or click button Create an empty case: select File > New Shell and Tube ExchangerĢ. Process Inlet/Outlet Fluid (Cold/Hot) PropertiesĮxample: Liquid-Liquid S&T Exchanger Standard Data Sheetġ. Jacket Pipe Plate-Frame Exchanger Exchanger How To Use HTRI For Shell & Tube Exchanger DesignĬontents What Can HTRI Do General Procedures Example: Liquid-Liquid Exchanger Design Result Evaluation
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