recharte
Chemical
- Jul 28, 2006
- 5
Hi, all
I have to relocate an existing air cooler propane condenser across an internal street of the plant. I got the isometric drawings from piping crew, and I realized that the return piping of liquid propane comes out from the condenser header, then goes up to cross the street on an existing bridge, and goes down to the normal level of pipe rack. The difference of levels is about 2.7 m for the up run and 1.4 m for the down run. Normally this type of pipe (condensed propane)are "slope - no pockets", so I suspect a serious operative problem of this line in the future.
Are my fears correct? Any help?
I have to relocate an existing air cooler propane condenser across an internal street of the plant. I got the isometric drawings from piping crew, and I realized that the return piping of liquid propane comes out from the condenser header, then goes up to cross the street on an existing bridge, and goes down to the normal level of pipe rack. The difference of levels is about 2.7 m for the up run and 1.4 m for the down run. Normally this type of pipe (condensed propane)are "slope - no pockets", so I suspect a serious operative problem of this line in the future.
Are my fears correct? Any help?