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

UN-DOT
Classification of hazardous materials subject to shipping and storage regulations
Hydrogen
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

FERST

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

FATE

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

Blog

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.

Resources

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

Recent Posts

VSP2 Pressure Transducer Calibration & Maintenance Guide

Posted by Fauske & Associates on 08.20.20

By Aaron Ruiz, Thermal Hazards Technician, Fauske & Associates LLC

The Vent Sizing Package 2, a bench-scale low thermal inertia adiabatic calorimeter, was developed as a result of a research project called the Design Institute for Emergency Relief Systems (DIERS). The VSP2™ utilizes established DIERS technology to identify and quantify process safety hazards so they can be prevented or accommodated by process design.  

 

Introduction

The key parameters measured during Vent Sizing Package 2 (VSP2) experiments are temperature and pressure. Temperature measurements are taken using K-type thermocouples connected to the VSP2 data collection system through a thermocouple gland.  Pressure measurements are made using pressure transducers.  These important parameters are used to make critical decisions related to safety. 

The key to collecting reliable and reproducible data is properly calibrating and maintaining the instrumentation used to collect it.  The pressure transducers used with the VSP2 are the DP15/ DP215 Variable Reluctance Pressure Sensors from Validyne Engineering Corporations.  These transducers were primarily selected because they are designed to withstand various corrosive liquids and gases, have replaceable diaphragms for various pressure ranges, and have high accuracy and precision. 

 

Calibration

The calibration system within the VSP2 control box requires the user to adjust a zero and gain reading based on a separate calibrated source.  In order to calibrate the VSP2 pressure transducer, perform the following steps:

1. Secure the pressure transducers that will be used for the experiment (with a diaphragm that will cover the pressure range of interest) to the calibration tree.  The calibration tree should be connected to a high-pressure inert gas (i.e. nitrogen) source, a vent line, and a calibrated source.  The FAI calibration kit comes with a pressure gauge that can be separately calibrated.  This gauge acts as the “calibrated source” that the transducers are calibrated against.  See Figure 1 for the FAI calibration tree with pressure gauge and transducers installed. Note; do not place the pressure transducers on the Super Magnetic Stirrer when it is enabled.

Figure 1: The FAI calibration tree with pressure gauge as the “calibrated source” for calibrating the pressure transducers.  The left-hand-side shows the “zero” point and the right-hand-side shows the “gain” measurement for a 2,000 psig transducer (i.e.. 847 psig)

Figure 1: The FAI calibration tree with pressure gauge as the “calibrated source” for calibrating the pressure transducers.  The left-hand-side shows the “zero” point and the right-hand-side shows the “gain” measurement for a 2,000 psig transducer (i.e.. 847 psig)

 

2. Within the VSP2 software, select the button that says “Calibrate Temperature and Pressure” to open up the calibration window (see Figure 2).

 

 

3. The full output of the transducers is 10V. In order for the VSP2 software to correlate the measured voltage from the deflection of the diaphragm to a pressure, the user must input the full range of the diaphragm divided by the total voltage (10V).  For example, if a 2,000 psi transducer is used, the VSP2 user should input 200 psi/V inside the “Pressure Sensitivities” window for each transducer that is used.  Figure 3 includes a table indicating the pressure range based on the number imprinted on the diaphragm used.  Figure 4 shows where the pressure range divided by the total voltage needs to be specified.

 

 

Figure 3: A table from the Validyne Pressure Transducer Manuel showing which dash number corresponds to what pressure range.

 

Figure 4: a screenshot from the VSP2 control software after the "Calibrate Temperature and Pressure" button is selected on the main page. The "Pressure Sensitivities" box is where the psi/volt needs to be input.

 

4. With the pressure transducers at atmospheric pressure, adjust the “zero” on the VSP2 potentiometer screw for each transducer (note, P1 measures the sample pressure and P2 typically measures the primary containment vessel pressure for pressure balancing), shown in Figure 5, until the display on the VSP2 screen (Figure 6) reads 0 psig. The manufacturer specification for accuracy of the pressure transducers is ±0.5% of the full scale for pressure ranges less than 2,000 psig.  For diaphragms 2,000 psi and above, the stated accuracy is ±1% of the full scale.  Note, adjusting the screws clockwise will increase the pressure reading on the VSP2 control box, and adjusting the screws counterclockwise will decrease the pressure reading.  Be careful not to apply pressure when adjusting the potentiometer screws as they can be pushed past the control box surface.

 
sd

Figure 5: VSP2 potentiometer screws where the user can adjust, the “zero” and “gain” for any pressure transducers that are being used to match the pressure reading from the gauge in Figure 1

Figure 6: The display from the VSP2 software.

 

5. adjust the “gain”, pressurize the transducers to near the peak pressure of interest (e.g. potentially 800 psig for a 2,000 psi transducer or 600 psig of an 800 psi transducer; these are recommended ranges, but it depends on the experiment and what pressure one expects). Be careful not to overpressurize the diaphragms above their measurement range, because this can permanently damage them.  Adjust the “gain” potentiometer screws until the pressure readings (Figure 6) matches the reading on the pressure gauge (Figure 1).

 

6. Depressurize the transducers back to 0 psig, check the reading, and adjust the “zero” potentiometer until the VSP2 screen reads zero.  Repeat with the “gain”.  This may take several iterations before the transducers have been fully calibrated.

 

7. When the calibration is complete, it is suggested to incrementally increase the pressure from 0 psig to the peak tested pressure and check that the pressure of all transducers are within the accuracy range for each increment.

 

 

MAINTENANCE

 

General Cleaning

The most important thing for properly maintaining the VSP2 pressure transducers is to promptly clean them after every experiment.  The simplest way to clean them is to remove the bleed screw and flush a suitable solvent through the channel.  To remove the bleed screw, use a small hex tool, and carefully twist to loosen it. Figure 7 shows where the bleed screw is located.

  • Be careful to not lose the orange washer inside the bleed screw port.

  • Flush the channel using a non-residue solvent from the negative side of the transducer, and out through the positive side to flush out any remnants of the sample.

  • Utilizing low pressure compressed air or other inert gas, dry out the channel.

  • Replace the bleed screw and tighten.

 

 

Thorough Cleaning

Periodically it is important to completely disassemble and clean the pressure transducer.  This can be for a few reasons:

 

A. It is expected that the transducer was exposed to a chemical that warrants a thorough cleaning (such as a sticky or viscous difficult to clean material or something that is toxic or severely corrosive).

 

B. The pressure range of the diaphragm needs to be changed.

 

C. The pressure transducer is not performing as it is expected, for example:

  • The pressure increments from full scale to zero are non-linear and deviate causing excessive hysteresis.

  • The zero reading shifts after being calibrated.

  • The outputs are not within the stated accuracy.

  • The outputs are not balanced despite after making multiple iterations from full scale to zero.

Figure 7:  The bleed port is located on the negative port side and shown by the arrow and can be removed by using a small hex tool as depicted. The circled area indicates that this is the negative port of the transducer by the (-) symbol.

Figure 7:  The bleed port is located on the negative port side and shown by the arrow and can be removed by using a small hex tool as depicted. The circled area indicates that this is the negative port of the transducer by the (-) symbol.

 

 

Disassembly

1. Carefully secure the pressure transducer within a vise (see Figure 7, note we have brass on the vise faces to prevent damage to the transducer body).

 

2. Using a hex or star key wrench (depending on the screws used), loosen the bolts, by slowly loosing and alternating the bolts incrementally until they are removed.

 

3. Gently pull open one side of the transducer. Be careful when opening the transducer because thin gauge wires are secured near the top of the transducer and can be snapped off. Now, the transducer is in a position that it can be cleaned with a suitable solvent, or parts can be replaced as needed. 

 

Figure 8: A vise clamp holding a transducer, so the user can unscrew the bolts to remove the diaphragms or the O‑rings.

Figure 8: A vise clamp holding a transducer, so the user can unscrew the bolts to remove the diaphragms or the O‑rings.

 

There are few key features of the transducer to note:

 

1. Diaphragms

The adaptability of the transducer is due to its economical feature allowing the user to replace the sensing diaphragms without purchasing multiple transducer bodies. This allows for numerous pressure ranges to be looked at accurately.  For example, closed cell VSP2 experiments can be performed to high pressures by implementing a high pressure diaphragm.  To run experiments in lower pressure ranges (like in an open cell orientation) with improved accuracy, lower range diaphragms can be implemented.  A benefit of this transducer and diaphragm type is they can withstand extreme shock, vibrations, and generally reasonable laboratory abuse from the stainless steel construction. Further, the stainless steel construction is ideal for use with the VSP2 due to the protection against corrosion and oxidation.  Some notes on the transducer diaphragms (shown in Figure 9):

  • Check for signs of warping or damage to the diaphragms, and periodically replace the them. They can become damaged over time from overpressure, or long exposure to numerous chemicals without prompt cleanup. 
  • Make sure to utilize the correct diaphragm that correlates with the desired testing range (see Figure 3). The accuracy of the transducers is based on the full scale, and thus the lower the pressure range, the more accurate the pressure readings will be.
  • Tip: label what diaphragm is being used on the outside of transducer, so it is clear what the range is without disassembling it.

Figure 9: Each diaphragm has a dash number and this case, the diaphragm being cleaned has a dash number of 60, indicating that this diaphragm has a maximum pressure limit of 1250 psig. The diaphragms are compressed by the coiled pads inside of the transducer bodies where the applied pressure compresses internal coils.

Figure 9: Each diaphragm has a dash number and this case, the diaphragm being cleaned has a dash number of 60, indicating that this diaphragm has a maximum pressure limit of 1250 psig. The diaphragms are compressed by the coiled pads inside of the transducer bodies where the applied pressure compresses internal coils.

2. O-rings

Besides the diaphragm, there is also an o-ring on either side of the body of the transducers between the diaphragm and transducer body (Figure 10):

  • Replace the o-rings when they swell-up, appear damaged, or have been inside the transducer of a long period of time, they do not have to be replaced every time the transducer is opened.

  • Ensure the o-rings are compressed securely in their grooves.

  • Avoid pinching the o-rings (this can damage them).

  • It is suggested to use Teflon o-rings instead of Viton-A, which are the default for when purchasing a pressure transducer. Teflon can resist corrosives better than Viton-A.

 

Figure 10: Close-up of Teflon o-rings inside the pressure transducer. This is an example of o-rings that are ready to be changed. 

Figure 10: Close-up of Teflon o-rings inside the pressure transducer. This is an example of o-rings that are ready to be changed. 

Reassembly

After the required cleaning or replacing of parts, the transducer can be reassembled for use, by retightening the bolts:

  • Apply anti-seize as a sealer on the bolts to prevent any potential leaks from the transducer, protects them during the metal-to-metal contact, and helps prevent the bolts degrading from corrosion.
  • Replace any bolts that are damaged.
  • Align the bolts carefully with the diaphragm holes.
  • Tighten the bolts snug and uniformly applying equal torque throughout. The threads from the bolts should never catch the holes of the diaphragms.

 

For any further assistance or questions, feel free to contact us at parts@fauske.com.

 
 

Topics: Flammability, Emergency Relief System Design

cta-bg.jpg

Is My Dust Combustible?

A Flowchart To Help You Decide
Download Now