Anyoen who has used aspen plus or other software to design heat exchangers would have an output called TEMA sheet which gives the details of the exchanger design.
In that sheet the heat transfter coefficients are listed for 3 cases labelled as clean, service and dirty.
I would appreciate if someone explains
1.The PHYSICAL meaning of these 3 coefficients and not just the mathematical formula associated with it. I want to know the physical meaning of thes3 terms in order to have a feel
2. I want to know a broad approach of software like aspen plus in calculating these 3 coefficients. That is the sequence of steps that aspen plus follows to arrive at these 3 values. Assume user inputs= inlet/outlet properties of cold/hot streams and/or heat duty required.
I would think the sequence of steps is as follows but I could be wrong, pease correct:
1. Software gets inlet/outlet stream properties from user along with type of exchanger(whether BEM or BEU etc.) and M.O.C of shell/tube
2. Aspen calculates the missing parameter-either outlet property of oen of the streams or the heat load
3. software calculates U from first principles(using pressure drop limits set by user, flow limits in shell/tube side set by user, bulk properties of process fluids etc.)
This is clean.
4. Software applies user supplied fouling factors and calculates revised U-this is dirty
5. software uses dirty U tocalculate required area from Q=U.A.deltaT.
6. software from mechanical design(how?), calculates maximum available area, which excludes tubes extending outside tubesheets and so on. This is theoretical max. area available. Software plugs this area in Q=U.A.deltaT. and calculates U, which is the service U, or the U that corresponds to when thje heat exchanger is able to just meet the requirements of the duty, under maximum fouling conditions.
Please revise thanks.