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ARID Technologies, Inc
323 S. Hale Street
Wheaton, IL 60187
tel:(630) 681-8500
fax:(630) 681-8505

Project No. 148
Test Report for the ARID Technologies Vapor Recovery Unit
installed in LANTANA, FL


Page 6

5.0 Calculations

The outlet hydrocarbon (HC) mass is calculated from the measured outlet volume corrected to standard conditions, the outlet HC concentration as propane and the density of propane. Standard conditions are 68 degrees F and 29.92 inches Hg.

The outlet volume during any one minute test interval is corrected to standard conditions using the formula:
Calculations Formula 1

Where:
17.65 = Standard Temperature / Standard Pressure
Vacf = Recorded meter volume in cubic feet
PA = Absolute pressure (barometric plus turbine meter) in inches of mercury
T = Temperature in volume meter in °F

The mass of hydrocarbons emitted from the outlet during any one minute test period is calculated from:
Calculations Formula 2

Where:
HC(out) = Hydrocarbon concentration at the outlet in %C3
Note: The density of propane is 51,950 mg/ft3

For recovery efficiency of the PERMEATOR®, the feed volume is calculated from the outlet volume, outlet hydrocarbon concentration, permeate hydrocarbon concentration and inlet hydrocarbon concentration. Calculations Formula 3

Where:
HC(in) = Hydrocarbon concentration at the inlet in %C3 HC(P) = Hydrocarbon concentration at the permeate in %C3

The inlet mass during any one minute test interval is: Calculations Formula 4

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Field Testing Summary
Table 1: Explanation of Terms
Table 1 - Field Test Data Summary
PERMEATOR On vs Off Graph
Actual independent third-party test results by Matus Technical Services, Inc.
ARID's Evaporative Loss Model
Average V over L Results
Gasoline RVP Samples
Notes Regarding Field Test Leak Results
Field Test Site Photos - Lantana, Florida
 
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