REP2
Mechanical
- Nov 8, 2010
- 8
Everytime I try to apply B31.1 Apprendix II Rules for PSV installation it always seems my f(Lmax/D) values are off the Chart II-1. I am looking for some discussions on this analysis. I do not have access to the original Keenan and Kaye 1948 Gas Tabels and do not know if values for f(Lmax/D) are available outside the area in the published Chart II-1. Due to the limitation of Chart II-1 I would interpret this as the B31.1 Apprendix II rules do not apply to long vent lines sizing that do not fall within the chart area. Anyone have the same experience and would my conclusion be accurate? Are the B31.1 Safety Valve rules for short pipe runs only?
Having said the above, I am looking method for calculating blowback on a long PSV for a saturated steam (35 psig) vent line 10" in diameter, 75 ft of horitontal straight pipe, 10 ft of vertical with (2)45ELbows and (5)90Elbows. To me this vent line is too long for the rules of B31.1 Appendix II. I also think that the use of drip pan elbow can not be used unless no blowback can be confirmed and I am afraid that there will be blowback. Any suggestions on a method for determining blowback?
An alternative is to hard pipe the outlet but condensate in the line would be hard to manage but could be desinged. Any one with this experience have any comments to add?
Having said the above, I am looking method for calculating blowback on a long PSV for a saturated steam (35 psig) vent line 10" in diameter, 75 ft of horitontal straight pipe, 10 ft of vertical with (2)45ELbows and (5)90Elbows. To me this vent line is too long for the rules of B31.1 Appendix II. I also think that the use of drip pan elbow can not be used unless no blowback can be confirmed and I am afraid that there will be blowback. Any suggestions on a method for determining blowback?
An alternative is to hard pipe the outlet but condensate in the line would be hard to manage but could be desinged. Any one with this experience have any comments to add?