Milutin
Chemical
- Jul 7, 2006
- 152
Dear all
In our refinery as I suppose in many other refineries we are short for i-C4 as feed to alkilation unit. As I know for C4 alkylation unit, ratio of C4 olefins an i-C4 is about 1:1.2 respectively. And we run our alky unit in that manner, it is sulphuric acid alky unit.
During discussion with some of my colleagues they mentioned that is possible to run alky unit with ratio C4= to i-C4, 1 : 0.9 respectively. In my opinion it is not possible, because if we have ratio 1 : 0.9 we will consume i-C4 cooling media, and i-C4 recycle from disobutaniser column.
Is it possible to run alky unit with ratio 1:0.9?
Regards,
Milutin
In our refinery as I suppose in many other refineries we are short for i-C4 as feed to alkilation unit. As I know for C4 alkylation unit, ratio of C4 olefins an i-C4 is about 1:1.2 respectively. And we run our alky unit in that manner, it is sulphuric acid alky unit.
During discussion with some of my colleagues they mentioned that is possible to run alky unit with ratio C4= to i-C4, 1 : 0.9 respectively. In my opinion it is not possible, because if we have ratio 1 : 0.9 we will consume i-C4 cooling media, and i-C4 recycle from disobutaniser column.
Is it possible to run alky unit with ratio 1:0.9?
Regards,
Milutin