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Compact Lab-Scale Testing System for Filtration Membrane Evaluation (MF, NF, UF, RO), CFMECLSTS

Compact Lab-Scale Testing System for Filtration Membrane Evaluation (MF, NF, UF, RO), CFMECLSTS

$499.00 USD
In Stock SKU: CFMECLSTS
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A Lab-Scale Membrane Testing System is a benchtop apparatus used to evaluate flat-sheet membrane coupons or small hollow-fiber modules. It determines core transport and separation properties—such as pure water permeability (PWP), solute/salt rejection, molecular weight cut-off (MWCO), and fouling resistance—across Microfiltration (MF), Ultrafiltration (UF), Nanofiltration (NF), and Reverse Osmosis (RO) regime.

There are two main configuration systems: (1) Cross-Flow (Tangential Flow) System: Feed solution flows tangentially across the membrane active layer at a controlled cross-flow velocity, continuously sweeping away accumulated foulants. High-pressure feed pump (diaphragm or gear pump), backpressure regulator valve, cross-flow cell with feed spacers, heat-exchange cooling coil, and automated permeate mass balance. It is best for NF, RO, Forward Osmosis (FO), and long-term anti-fouling evaluations. (2) Dead-End Stirred Cell (e.g., Amicon-type): Feed is pushed perpendicular to the membrane surface using pressurized gas (N2 or compressed air) while an internal magnetic stir bar minimizes concentration polarization. It is best for rapid screening of MF/UF membranes, MWCO determination (using dextran/PEG standards), and protein concentration.

Part Number
  • CFMECLSTS (C-FME-CLSTS)
Power
  • AC110V-220V±10% (DC24V adaptor), single phase, 50/60Hz, ~50 W
General Features
  • Pressure gauge is installed for pressure monitoring
  • Automatic pressure adjustment with intelligent pressure increment pump 
  • Water and electricity sections are well separated for improving safety
Operation Procedures
  • Before incorporating the membrane core into the testing system, use tap water (>10 L) to flush the filtration tester.
  • If the sourcing water has a TDS value >1000, a pre-filtration pressurization unit should be used to avoid block of membrane
  • Rotate the ball valve of concentrated water to adjust the water flow and pressure. UF: 1-3 kg/cm2; NF and RO: 4-8 kg/cm2
Testing System Structures
  • Front View: The testing system was mainly composed of membrane core chamber, intelligent pressurization system (100G pump) and pressure gauge. 

       

  • Back View: The power plug port and on/off button, water inlet/outlet ports, and concentrated water outlet are presented at the backside. 

       

Membrane Core Options
  • UF2012-0% 1.8L/min (External Pressure PES membrane), filtration >100 kDa organic substance; D=56 mm, L=230 mm, working pressure=30 psi
  • UF2012-0% 1.8L/min (External Pressure PVDF membrane), filtration >100 kDa organic substance; D=56 mm, L=230 mm, working pressure=30 psi
  • 2012UF300-0% 1.8L/min (Internal Pressure PES membrane), filtration >8 kDa organic substance; D=60 mm, L=300 mm, working pressure=30 psi
  • 2012UF320-0% 1.8L/min (Internal Pressure PAN membrane), filtration >50 kDa organic substance; D=75mm, L=320 mm, working pressure=30 psi
  • NF2012-30% 1.1 L/min, filtration >600 Da organic substance; D=47 mm, L=298 mm, working pressure=65 psi
  • NF2012-60% 1.1 L/min, filtration >300 Da organic substance; D=47 mm, L=298 mm, working pressure=65 psi
  • NF2012-90% 1.1 L/min, filtration >100 Da organic substance; D=47 mm, L=298 mm, working pressure=65 psi
  • RO2012-95% 1.1 L/min, filtration >50 Da organic substance; D=47 mm, L=298 mm, working pressure=80 psi

       

All the retention rates mentioned above refers to the +1 salt concentration.

Dimension L380 mm * D140 mm * H230mm
Weight ~10 kg

References:

1. F. J. Benítez, et al., The use of ultrafiltration and nanofiltration membranes for the purification of cork processing wastewater, Journal of Hazardous Materials, 2009, 162, 1438-1445. 

2. S Benfer, et al. Development and characterization of ceramic nanofiltration membranes, Separation and Purification Technology, 2001, 22, 231-237. 

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