We are currently conducting research and development and testing on Fluidized Electrode Capacitive Deionization (Feci) devices for water treatment applications. To validate the preliminary fluid simulation model, we need to in situ measure the flow rate differences in different regions within the device chamber and the pressure difference between the inlet and outlet.
After research, I plan to use multi-point Capillary Fiber Bragg Gratings (CapillaryFBG) to pass through the flowing brine chamber for stress/strain detection. Since our working conditions involve micro-pressure differences and low flow rates, I would like to consult your company’s technical experts to see if the current customized FBG products and supporting demodulators can meet the following measurement requirements:
Operating Conditions and Fluid Parameters
Fluid Chamber Dimensions: 40502mm
Fluid Medium: Low-concentration brine (1000mg/L NaCl) or a mixed liquid containing carbon particles (fluidized electrode slurry).
Flow Rate Range: Simulation results show that the high flow rate region is approximately 0.3m/s, and the low flow rate region (including dead zones) is approximately 0.05m/s.
Pressure Characteristics: The pressure gradually decreases from the inlet to the outlet. The total pressure difference between the inlet and outlet measured by simulation is only about 600Pa. (The pressure distribution is not completely consistent with the flow rate distribution; for example, the flow rate at the outlet may be high, but the pressure is the lowest in the chamber).
Preliminary Proposed Installation and Testing Plan
Fiber Arrangement: A multi-point customized CapillaryFBG will pass through the entire flowing fluid chamber horizontally or vertically.
Measurement Point Distribution: 3 measurement points (Gratings) will be arranged on one fiber, with a spacing of 15mm between adjacent points.
Measurement Logic: Measure flow rate difference: Rely on the different shear stress exerted by the fluid on the fiber surface in different regions (e.g., main channel and dead zone) to cause different center wavelength shifts in the FBGs at different positions, thereby inferring the flow rate distribution.
Measure overall pressure difference: Monitor the trend of internal stress changes in the device as the inlet flow rate/pressure increases.
Stress Measurement Sensitivity: For the flushing of liquids (even slurries containing carbon particles) in the low flow rate range of 0.05m/s to 0.3m/s, is the deformation caused by the force on the CapillaryFBG sufficient to cause a wavelength shift that can be effectively captured? Can the signal-to-noise ratio meet the requirements for distinguishing different flow rate regions?
Micro-pressure Difference Resolution: The maximum pressure difference between the inlet and outlet is only 600Pa. Can the customized fiber combined with the demodulator achieve precise demodulation of such small pressure changes?
Encapsulation and Interference: When FBG is subjected to lateral force, is there a problem of excessive attenuation in stress transmission? For the friction/flushing of carbon particles, what special coating treatment is required for the fiber surface?
Demodulator Recommendation: For the dynamic monitoring of the aforementioned micro-strain, what resolution (pm level) and sampling frequency demodulator are needed? Are there any recommended models?
We look forward to the answers and selection advice from the technical experts. If this plan is theoretically feasible, I would like to discuss customization details further. Thank you very much!





