acfm
Mechanical
- Apr 22, 2000
- 24
I deal mostly with liquid ring vacuum pumps and commpressors. I have an gas application in which the following conditions were supplied:
suction Pressure: 50 Torr
discharge pressure: 900 Torr
mw:50 (50% water)
inlet temp: 33 deg. C
volume: 3 MMACFH (I'm assuming this is actual cubic feet per hour?)
Here are the problems that I'm having and looking for assistance on:
1. (3 MMACFH?) Normally MSCFD is given and this form references the volume of gas under standard conditions. How do you convert this from MMACFH to SCFM? I now MSCFD is approximately 1000 SCFM.
Based on the pressure requirements I know That I could possibly use a liquid ring vacuum pump however, determining the actual capacity is proving rather difficult. I'm trying to determine the actual cubic feet per miniute (ACFM) required.
Any assistance would be greatly appreciated.
suction Pressure: 50 Torr
discharge pressure: 900 Torr
mw:50 (50% water)
inlet temp: 33 deg. C
volume: 3 MMACFH (I'm assuming this is actual cubic feet per hour?)
Here are the problems that I'm having and looking for assistance on:
1. (3 MMACFH?) Normally MSCFD is given and this form references the volume of gas under standard conditions. How do you convert this from MMACFH to SCFM? I now MSCFD is approximately 1000 SCFM.
Based on the pressure requirements I know That I could possibly use a liquid ring vacuum pump however, determining the actual capacity is proving rather difficult. I'm trying to determine the actual cubic feet per miniute (ACFM) required.
Any assistance would be greatly appreciated.