Bourbon103
Chemical
- Nov 30, 2005
- 32
We are going to use a 1500 gal. tank as a mineral oil hold tank; totes of mineral oil will be pumped into the tank and mineral oil will be metered from the tank for various uses. The only "process" in the tank will be to heat it to 100C while sparging N2 to drive off enough entrained water to meet spec.
The mineral oil has a flash point of greater than 370F (NFPA Class IIIB, combustible liquid). We will be using an appropriately sized demister to remove mineral oil mist with a pressure control valve and conservation vent to atmosphere on the vent side.
Is a flame arrestor also needed? Per NFPA 30 (2008), 21.4.3.6 & 7 there is only mention of arrestors needed for IA,B,&C services. Also, I am not sure if what we are doing is technically considered a "process", which would disqualify it from being a "storage tank", per NFPA.
Any ideas?
Thanks again.
The mineral oil has a flash point of greater than 370F (NFPA Class IIIB, combustible liquid). We will be using an appropriately sized demister to remove mineral oil mist with a pressure control valve and conservation vent to atmosphere on the vent side.
Is a flame arrestor also needed? Per NFPA 30 (2008), 21.4.3.6 & 7 there is only mention of arrestors needed for IA,B,&C services. Also, I am not sure if what we are doing is technically considered a "process", which would disqualify it from being a "storage tank", per NFPA.
Any ideas?
Thanks again.