ghamsa:
For a variety of reasons:
1) It was what the customer (client) specified;
2) It was what the engineering designer offered and was accepted;
3) No one cared about the units used and the computer simulation spit out lbmoles;
4) For convenience, if a gas process is involved; because the mole occupies a known quantity of gas (at "standard" conditions), it can be converted over to volumetric flow easily;
5) Because a chemist is involved and he/she wants molal relationships;
6) there are probably many other probabilities.
I have always constructed my PFDs in accordance with client wants or needs. It is no big deal to select either mass, volume, or molal and stick to the units. The biggest problem is usually getting a decision out of someone - especially business managers who are only versed in junk science and no engineering.
Art Montemayor
Spring, TX