samya
Chemical
- Oct 28, 2012
- 4
Recently, while doing simulation on hysys for a hydrocracker separation section, observed that feed stream composition (End Pont of ASTM D 2887) does not match end point in final product from recycle splitter bottoms (which is the heaviest product). i.e Feed End point is lower and post separation splitter bottoms end point is higher. Can anybody explain the reason behind this.
Technically, since there is no composition change in separaration process, end point in feed and product should be same.
Thanks in advance.
Technically, since there is no composition change in separaration process, end point in feed and product should be same.
Thanks in advance.