Principalele Aplicatii

sorbție
Separarea speciilor organice hidrofobe
decolorare-indulcitori
decolorare - bere
decolorare - soluții zaharoase
Indepartarea patulinei

Avantaje

Rezistență mecanică ridicată
Suprafata specifica mai mare in comparatie cu un adsorbant standard
Sistem dual: IEX (schimb ionic)/interactiune hidrofoba

Aprobari de reglementare

Certificat Halal IFANCA
OK Kosher Certified
În conformitate cu Regulamentul FDA 21 CFR 173.25 pentru tratarea alimentelor, rășini schimbătoare de ioni
în conformitate cu Rezoluția europeană ResAP 2004 3
Liber de GMO/TSE/BSE

Ambalaje tipice

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

APPLICATION GUIDE

Polymeric Adsorbent Resins for Industrial Applications

APPLICATIONS GUIDE

Macronet Adsorbents Carbonless Corn Sweetener Refining

COLOR REMOVAL IN PROCESS STREAMS

Caracteristici tipice fizice si chimice

Structura polimerica	polimer polistiren macroporos reticulat cu DVB
Aspect	Perle sferice
Grupari functionale	Amina tertiara
Forma ionica	FB (baza libera)
Total Capacity	0.1 - 0.3 eq/L ( forma FB )
reținerea umidității	50 - 60 % ( forma FB )
Distribuția granulometrică	300 - 1200 µm
Dilatare reversibilă, FB → Cl- (max.)	5 %
Typical Pore Diameter by nitrogen adsorption (Meso/Macro/ Transport Pores)	350 Å
Typical Pore Diameter by nitrogen adsorption (Micropores)	15 Å
Typical Pore Volume by nitrogen adsorption	0.4 mL/g
Typical Surface Area by nitrogen adsorption	800 m²/g
densitate specifică	1.07
Greutate de transport (aprox.)	610 - 640 g/L (38.1 - 40.0 lb/ft³)
limite de pH, stabilitate	0 - 14
Limita de temperatură	60 °C (140.0 °F) ( forma FB )

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

Macronet™ MN102

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Overview

Literature

Resources