PhilEduard
Mechanical
- Aug 24, 2004
- 36
Hi there guys,
I know this is the right forum for this question and I believe too mostly are working on process engineering. This question could be very simple for you but it took me a while to figure it out simply becuase of the metric unit I'm not use to. I have a system running on compressed nitrogen gas at 1650 psig and 150 deg F. Using ideal gas equation, density = p/RT where p is the operating pressure in lbm/cu. ft., R is specific gas constant equal to .2968 Kj/Kg-K from my research, and T is the temp at deg R. Since R has to be in consistent unit of ft-lbf/lbm-degR, I managed to convert the specific gas constant R in metric to customary english units and I am getting 3.8 lb/cu ft. To those who are more orineted in this kind of job, please correct me or kindly validate this calculation. Thanks a lot for all of your help or hints on this issue.
Regards,
I know this is the right forum for this question and I believe too mostly are working on process engineering. This question could be very simple for you but it took me a while to figure it out simply becuase of the metric unit I'm not use to. I have a system running on compressed nitrogen gas at 1650 psig and 150 deg F. Using ideal gas equation, density = p/RT where p is the operating pressure in lbm/cu. ft., R is specific gas constant equal to .2968 Kj/Kg-K from my research, and T is the temp at deg R. Since R has to be in consistent unit of ft-lbf/lbm-degR, I managed to convert the specific gas constant R in metric to customary english units and I am getting 3.8 lb/cu ft. To those who are more orineted in this kind of job, please correct me or kindly validate this calculation. Thanks a lot for all of your help or hints on this issue.
Regards,