aquadigio
Chemical
- Aug 27, 2012
- 10
Dear All,
I am currently involved in a mega petrochemical complex project. The overall cooling water consumption is more than 130,000 m3/h (10& margin) and the initial design is to split to users into 2 main clusters, so end up with 2 block/cooling tower in two different locations within the complex.
There are 18 and 16 cells respectively for each cooling tower (one basin each) with 4000 m3/h per cell.
The issue is we are at the bottleneck on the cell arrangement. There are two options:
a) 9 x 2 (rows) and 8 x 2 (rows)
b) 6 x 3 (rows) and 5 x 3 (rows)
The above 2 options are being discussed between ourselves (project owner) and contractor. Contractor is preferring option 2 with the reason of easy maintenance and piping/nozzle layout
However, project owner side is in the opinion that by having three rows will not have maintenance issue.
By having 2 rows of cell arrangement(option a), the overall unit length will be too long compare to option b.
Appreciate your feedback. Thank you.
I am currently involved in a mega petrochemical complex project. The overall cooling water consumption is more than 130,000 m3/h (10& margin) and the initial design is to split to users into 2 main clusters, so end up with 2 block/cooling tower in two different locations within the complex.
There are 18 and 16 cells respectively for each cooling tower (one basin each) with 4000 m3/h per cell.
The issue is we are at the bottleneck on the cell arrangement. There are two options:
a) 9 x 2 (rows) and 8 x 2 (rows)
b) 6 x 3 (rows) and 5 x 3 (rows)
The above 2 options are being discussed between ourselves (project owner) and contractor. Contractor is preferring option 2 with the reason of easy maintenance and piping/nozzle layout
However, project owner side is in the opinion that by having three rows will not have maintenance issue.
By having 2 rows of cell arrangement(option a), the overall unit length will be too long compare to option b.
Appreciate your feedback. Thank you.