Venkatachalam Ponnusamy
Petroleum
- Dec 7, 2020
- 29
Good Day..
Refer to the subject we have a requirement for Supply of Shell & Tube Heat Exchanger to Liquid Handling Terminal at Port.
Type of Heat Exchanger is TEMA R - BEU (H) and ASME, Shell Sizes for various exchangers are 10",12" & 14". Design pressure is around 5.3 Kg/cm2 & Design Temperature 65 Deg C. MOC will be SS 304.
We have multiple no.of Heat Exhchangers, if we go Standard WNRF/SORF flanges instead of Girth Flanges, then we will be more competitive on price wise. Is there any restrictions to use WNRF/SORF flanges instead of Girth Flanges. Any code restrictions?.
Your valuable inputs will be appreciated...
Refer to the subject we have a requirement for Supply of Shell & Tube Heat Exchanger to Liquid Handling Terminal at Port.
Type of Heat Exchanger is TEMA R - BEU (H) and ASME, Shell Sizes for various exchangers are 10",12" & 14". Design pressure is around 5.3 Kg/cm2 & Design Temperature 65 Deg C. MOC will be SS 304.
We have multiple no.of Heat Exhchangers, if we go Standard WNRF/SORF flanges instead of Girth Flanges, then we will be more competitive on price wise. Is there any restrictions to use WNRF/SORF flanges instead of Girth Flanges. Any code restrictions?.
Your valuable inputs will be appreciated...