Combustible Dust Testing

Laboratory testing to quantify dust explosion and reactivity hazards

Safety Data Sheets

Develop critical safety data for inclusion in SDS documents

Gas and Vapor

Laboratory testing to quantify explosion hazards for vapor and gas mixtures

Classification of hazardous materials subject to shipping and storage regulations
Testing and consulting on the explosion risks associated with devices and processes which use or produce hydrogen
Safety Data Sheets

Develop critical safety data for inclusion in SDS documents

Thermal Stability

Safe storage or processing requires an understanding of the possible hazards associated with sensitivity to variations in temperature

Adiabatic Calorimetry
Data demonstrate the consequences of process upsets, such as failed equipment or improper procedures, and guide mitigation strategies including Emergency Relief System (ERS) design
Reaction Calorimetry
Data yield heat and gas removal requirements to control the desired process chemistry
Battery Safety

Testing to support safe design of batteries and electrical power backup facilities particularly to satisfy UL9540a ed.4

Safety Data Sheets

Develop critical safety data for inclusion in SDS documents

Cable Testing
Evaluate electrical cables to demonstrate reliability and identify defects or degradation
Equipment Qualification (EQ)
Testing and analysis to ensure that critical equipment will operate under adverse environmental conditions
Water Hammer
Analysis and testing to identify and prevent unwanted hydraulic pressure transients in process piping
Acoustic Vibration
Identify and eliminate potential sources of unwanted vibration in piping and structural systems
Gas & Air Intrusion
Analysis and testing to identify and prevent intrusion of gas or air in piping systems
ISO/IEC 17025:2017

Fauske & Associates fulfills the requirements of ISO/IEC 17025:2017 in the field of Testing

ISO 9001:2015
Fauske & Associates fulfills the requirements of ISO 9001:2015
Dust Hazards Analysis
Evaluate your process to identify combustible dust hazards and perform dust explosion testing
On-Site Risk Management
On-site safety studies can help identify explosibility and chemical reaction hazards so that appropriate testing, simulations, or calculations are identified to support safe scale up
DIERS Methodology
Design emergency pressure relief systems to mitigate the consequences of unwanted chemical reactivity and account for two-phase flow using the right tools and methods
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
Engineering and testing to support safe plant operations and develop solutions to problems in heat transfer, fluid, flow, and electric power systems
Hydrogen Safety
Testing and consulting on the explosion risks associated with devices and processes which use or produce hydrogen
Thermal Hydraulics
Testing and analysis to ensure that critical equipment will operate under adverse environmental conditions
Nuclear Safety
Our Nuclear Services Group is recognized for comprehensive evaluations to help commercial nuclear power plants operate efficiently and stay compliant
Radioactive Waste
Safety analysis to underpin decomissioning process at facilities which have produced or used radioactive nuclear materials
Adiabatic Safety Calorimeters (ARSST and VSP2)

Low thermal inertial adiabatic calorimeters specially designed to provide directly scalable data that are critical to safe process design

Other Lab Equipment and Parts for the DSC/ARC/ARSST/VSP2 Calorimeters

Products and equipment for the process safety or process development laboratory


Software for emergency relief system design to ensure safe processing of reactive chemicals, including consideration of two-phase flow and runaway chemical reactions


Facility modeling software mechanistically tracks transport of heat, gasses, vapors, and aerosols for safety analysis of multi-room facilities


Our highly experienced team keeps you up-to-date on the latest process safety developments.

Process Safety Newsletter

Stay informed with our quarterly Process Safety Newsletters sharing topical articles and practical advice.


With over 40 years of industry expertise, we have a wealth of process safety knowledge to share.

Recent Posts

Nuclear Waste Processing

Posted by Fauske & Associates on 09.14.18

Innovative Nuclear Waste Hydrogen Removal Design For Self-Shielded Containers

by Martin G. Plys, ScD, and James P. Burelbach, PhD, Fauske & Associates, LLC

Innovative Nuclear Waste Hydrogen Removal Design & Nuclear Waste Processing

A practical solution to the problem of hydrogen removal that permits the storage of spent metallic fuel and zeolytes in a shielded container with commercially available filters...


In partnership, Sellafield Ltd, Westinghouse Electric UK, and Fauske & Associates, LLC, considered design parameters and options for interim self-shielded storage of waste that contains metallic spent nuclear fuel pieces or zeolytes. It was found that this type of waste generates significant hydrogen as a product of chemical reactions and from radiolysis of water. Filtered vents need to be implemented on waste containers that hold this waste to prevent unwanted hydrogen accumulation. In order to attach the filters to the shielded containers, bore-holes must be drilled through the shielding to allow the hydrogen to reach the filters. The specific geometry of the bore-holes must be designed carefully to preserve shielding while minimizing resistance to hydrogen removal.

Filters for H2 Removal and Nuclear Waste Processing

Filters for H2 Removal

The rate of hydrogen removal through a filter varies with filter size and materials.

The key filter specification provided by the manufacturer is known as the filter coefficient, expressed in units of moles hydrogen per second per mole fraction difference across the filter.

Typical values range from 10-5 over 2x10-4 moles/s/mole fraction.

The filter design for a given application Is chosen based on the hydrogen generation rate and the target maximum hydrogen concentration:either the lower flammability limit (LFL) (4% hydrogen in air) or the stricter criterion of 25% of the LFL (1%hydrogen in alr).             

Experimental Setup

Lid & Pipe Configurations and Nuclear Waste Processing
Lid & Pipe Configurations
Modeling and experimental validation was completed on the four bore-hole geometries shown in the figure to the right. Configuration A (direct mounted filter) was tested in order to evaluate the manufacturer’s stated filter performance for the two types of commercial filters tested. Configuration D is the proposed innovative solution. 

Small and large scale testing was performed. Initially the tests were performed transiently by establishing an initial hydrogen concentration of about 4% and then allowing the concentration to decay as hydrogen was vented out the filter and was replaced by air coming in the filter. Later tests incorporated a steady-state methodology in which a constant hydrogen inflow was established.


Double Bore Hole Arrangement and Nuclear Waste Processing
Configuration D: Double bore-hole arrangement with single filter

Innovative Solution for Hydrogen Removal

Shielded Containers and Nuclear Waste Processing
Shielded Containers

The key to hydrogen removal from a shielded container is to reduce the flow  resistance such that the filter is the main resistance. Consider an arrangement to promote hydrogen circulation to the filter via a pair of bore-holes in the shielded container lid as shown in Configuration D. The hydrogen concentration in a plenum immediately on the inside of the filter is lower than the hydrogen concentration in the container, so the density difference induces circulation. 

Gas from the container flows up one of the bore-holes into the plenum beneath the filter and then down the other bore-hole, returning to the container. In Configuration D, the bore-holes are indicated on an angle for shielding purposes, and in practice a double-angle design would be used to prevent a  direct straight line path through the container lid.

Modeling demonstrated that Configuration D would be nearly as effective as Configuration A, providing a solution to hydrogen removal from a package with thick shielding.  In contrast, commonly employed Configurations B and C would have sufficiently low efficiency compared to Configuration A that these designs are impractical. 


The expected performance of the dual-bore design was confirmed through experiments for different filter types and variation in hydrogen concentration. An example comparison of a priori expectation versus actual system data is shown below. 

The efficiency of the double bore system can be in the range of 80% to 90%, depending upon the geometry and the hydrogen concentration in the container. Thus, the number of filters required for a given application may be, for practical purposes, unaffected by the extra resistance offered by the shielding, and at worst it is only weakly affected.

Experimental Results & Model Predictions
Experimental Results and Model Predictions



The dual-bore Configuration D achieves an effective filter performance which is comparable to that for a filter alone and is superior to any single bore design. This innovation minimizes the number of vents required for a given inventory of metallic fuel bearing waste.

Steady-state testing with a well-defined hydrogen source rate together with the corresponding steady-state hydrogen concentration results in an effective filter efficiency which is reproducible and independent of hydrogen concentration.

Large scale tests indicate that the integral performance of multiple filter assemblies is simply given by the product of the number of filter assemblies and the performance of an individual assembly as measured in small scale tests.

Chemical Technology and The First Generation Magnox Storage Pond at Sellafield
The First Generation Magnox Storage Pond at Sellafield


In partnership, Sellafield Ltd, Westinghouse Electric UK, and Fauske & Associates, LLC, have conceived, modeled and experimentally verified an innovative solution to the problem of hydrogen removal from shielded containers with significant hydrogen generation rates. This solution to the problem of hydrogen removal permits passive storage of spent metallic nuclear fuel and zeolytes in a shielded container that is vented by a practical number of commercially available filters.

For more information regarding nuclear waste technology, decommissioning, modeling and plant services in addition to chemical and industrial process safety and testing, please contact us.

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Topics: Nuclear


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