Principal Applications

  • Eliminarea materiei organice

Advantages

  • stabilitate termică bună
  • Rezistență excelentă la șocul osmotic
  • Capacitate de sorbtie reversibila inalta

Regulatory Approvals

  • Certificat Halal IFANCA
  • Certificat de WQA conform standardului NSF ANSI 61

Typical Packaging

  • sac 1 ft³
  • 25 L sac
  • Butoi (Fibră) de 5 CF
  • 1 M³ supersac
  • supersac de 42 CF

Typical Physical & Chemical Characteristics:

Polymer Structure polimer polistiren macroporos reticulat cu DVB
Appearance Perle sferice
Functional Group Grupari quaternare de amoniu tip I
Ionic Form forma Cl-
Capacitatea totală 0.85 eq/L (18.6 Kgr/ft³) ( forma Cl- )
reținerea umidității 66 - 72 % ( forma Cl- )
Distribuția granulometrică 300 - 1200 µm
< 300 µm (max.) 1 %
coeficient de uniformitate (max.) 1.7
Dilatare reversibilă, Cl- → OH- (max.) 20 %
densitate specifică 1.04
Greutate de transport (aprox.) 640 - 690 g/L (40.0 - 43.1 lb/ft³)
Limita de temperatură 100 °C (212.0 °F) ( forma Cl- )

Caracteristici hidraulice

Pressure Drop

The pressure drop across a bed of ion exchange resin depends on the particle size distribution, bed depth, and voids volume of the exchange material, as well as on the flow rate and viscosity of the influent solution. Factors affecting any of these parameters— such as the presence of particulate matter filtered out by the bed, abnormal compressibility of the resin, or the incomplete classification of the bed—will have an adverse effect, and result in an increased head loss. Depending on the quality of the influent water, the application and the design of the plant, service flow rates may vary from 10 to 40 BV/h.

Pressure Drop Across Resin Bed

Backwash

During up-flow backwash, the resin bed should be expanded in volume between 50 and 70% for at least 10 to 15 minutes. This operation will free particulate matter, clear the bed of bubbles and voids, and reclassify the resin particles ensuring minimum resistance to flow. When first putting into service, approximately 30 minutes of expansion is usually sufficient to properly classify the bed. It is important to note that bed expansion increases with flow rate and decreases with influent fluid temperature. Caution must be taken to avoid loss of resin through the top of the vessel by over expansion of the bed.

Backwash Expansion of Resin Bed