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Data yield heat and gas removal requirements to control the desired process chemistry
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Testing to support safe design of batteries and electrical power backup facilities particularly to satisfy UL9540a ed.4

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Evaluate your process to identify combustible dust hazards and perform dust explosion testing
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Deflagrations (Dust/Vapor/Gas)

Properly size pressure relief vents to protect your processes from dust, vapor, and gas explosions

Effluent Handling

Pressure relief sizing is just the first step and it is critical to safely handle the effluent discharge from an overpressure event

FATE™ & Facility Modeling

FATE (Facility Flow, Aerosol, Thermal, and Explosion) is a flexible, fast-running code developed and maintained by Fauske and Associates under an ASME NQA-1 compliant QA program.

Mechanical, Piping, and Electrical
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Low thermal inertial adiabatic calorimeters specially designed to provide directly scalable data that are critical to safe process design

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FERST

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Recent Posts

UN Test O.2 Oxidizing Liquids (Combustible Hazard)

Posted by Fauske & Associates on 10.06.15

 

Oxidizing substances cause or enhance the combustion of another material, generally by yielding oxygen.  For this reason, the classification of oxidizers for their relative oxidative strength is important for understanding the safety aspects of handling, storing, and shipping these oxidizers.  The UN Model Regulations assigns Division 5.1 for oxidizing substances.  Classification is assigned for liquid oxidizers by performing UN Test O.2, Test for Oxidizing Liquids, from the UN Manual of Tests and Criteria.  In this test, the oxidizing strength of the test sample is compared to 3 standard materials.  If the material is a Division 5.1 Oxidizer, it is then assigned a Packing Group relative to the 3 standard materials.

The test setup consists of a pressure vessel, pressure transducer, vent plug, igniter wire and firing plug.  At the start of the test, an igniter wire is wound and attached to the firing plug.  The setup is shown in Figure 1.Figure 1: Liquid oxidizer pressure vessel setup

Figure 1: Liquid oxidizer pressure vessel setup

The firing plug is attached to the vessel, along with the pressure transducer.  The vessel is charged with the substance to be tested – 5 grams of a 1:1 mixture by mass of the liquid to be tested and cellulose.  The vent plug is then attached to the pressure vessel, with a bursting disc with a bursting pressure of approximately 320 psi.  The assembled vessel is placed in a support stand at a 60° angle from the horizontal plane.  The igniter wire is energized for 60 seconds, or until the rupture disc bursts.  If the disc bursts, the time taken for the pressure rise from 100 psig to 300 psig is noted.  A shorter pressure rise time indicates a more energetic reaction and a stronger oxidizer.  Five trials are performed, and the mean time interval is used for the classification.  A graph of a sample trial is shown in Figure 2.

Figure 2: Oxidizing liquids pressure versus time displaying rise time from 100 psig to 300 psig

Figure 2: Oxidizing liquids pressure versus time displaying rise time from 100 psig to 300 psig

The results from the sample under test are compared with the standard reference liquid oxidizers of 50% perchloric acid, 40% aqueous sodium chlorate and 65% aqueous nitric acid.  The mean value from inter-laboratory comparative trials in the UN Manual of Tests and Criteria for 1:1 mixtures of the reference oxidizers are shown in Table 1.

Table 1: Mean rise time for reference oxidizers

Substance

Mean Pressure Rise Time for a 1:1 mixture with cellulose (s)

50% perchloric acid

0.121

40% aqueous sodium chlorate

2.555

65% aqueous nitric acid

4.767

Of the 3 standard oxidizers in Table 1, 50% perchloric acid is strongest oxidizer, and 65% aqueous nitric acid is the weakest oxidizer.  The Division 5.1 and Packing Group classifications are outlined in Table 2.          

Table 2: Packing Group Determination

Classification

Oxidizer Strength of Test Sample

Mean Pressure Rise Time (s)

Division 5.1, Packing Group I

Stronger oxidizer than 50% perchloric acid

MPRT < 0.121

Division 5.1, Packing Group II

Stronger oxidizer than 40% sodium chlorate,

but not PG I

0.121 < MPRT < 2.555

Division 5.1, Packing Group III

Stronger oxidizer than 65% nitric acid,

but not PG I or II

2.555 < MPRT < 4.767

Not Division 5.1

Weaker oxidizer than 65% nitric acid

MPRT > 4.767

aMean value from inter-laboratory comparative trials in UN Manual of Tests and Criteria

After determining the packing group for the oxidizer, this information can then be used to properly package and ship your oxidizer material.

For assistance or further discussion regarding combustible liquids, gases and vapors, please contact us at info@fauske.com

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