V.     Flammability of Vapor-Air Mixtures      
The  flammability  of  a  hydrocarbon  vapor-air  mixture  depends  on  its  vapor  pressure,  flash  point  and  temperature.  These  properties  are  used  to  classify  petroleum  products  whose  electrical  resistivities  are  high  enough  to  enable  them  to  accumulate  significant  electrostatic  charges  under  certain  handling  conditions.  Following  are  the  three  petroleum  product Vapor Pressure Classifications, including common examples: 
Low – Those with a closed cup flash point above 100°F (38°C).      
These  products  do  not  develop  flammable  vapors  under  normal  handling  conditions.  However,  conditions  for  ignition  may  exist,  if  handled  at  temperatures  above  their  flash  points,  are  contaminated  with  higher  vapor-pressure  materials,  or  are  transferred  into  containers  where  vapors  are  at  concentrations  at  or  above  those  necessary  to  produce  a  flammable mixture. 
Examples:  #2  Fuel  Oil;  Kerosene,  Diesel,  Jet  Fuel  A  (commercial),  Motor  Oil,  Asphalt,  and  Safety Solvents Intermediate – Those with a closed-cup flash point below 100°F (38°C).   
Intermediate – Those with a closed-cup flash point below 100°F (38°C).  
 These  products  may  create  a  flammable  mixture  in  the  vapor  space  at  ambient  temperatures. 
Examples:  Xylene,  Benzene,  Toluene,  Jet  B  (commercial),  JP-4  (military),  and  Stoddard  Solvents   
High – Those with a Reid Vapor pressure above 4.5 psi absolute (31 kilopascals).      
These  products,  under  normal  handling  temperatures  in  a  closed  vapor  space,  will  rapidly produce a mixture too rich to be flammable. However, in some areas, a vapor space may pass through the flammable range before becoming too rich. 
Examples: Motor and Aviation Gasoline’s (sic), and high vapor pressure Naphtha’s (sic)