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MK3miniHT

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E-Cell StackTM  Modello MK-3miniHT

E-Cell StackTM Modello MK-3miniHT

MK3miniHT

The MK-3miniHT module is an EDI cell capable of producing very high-purity, demineralised water for pharmaceutical use. The ions are removed by means of an ion-exchange resin, which in turn is regenerated on a continuous basis by means of electric current. Interruptions of the process and regenerating chemicals are thus not necessary to restore functionality.


In addition, the module can be heat-sanitized (160 cycles at T <85 º C - P <2.1 bar). In this way it is possible to optimize the quality of the water produced also from the microbiological point of view.

Technical data:

Design pressure of the E-CellTM module 6.2 Bar
Working pressure 3.1-6.2 Bar
Pressure drop 1.4-2.4 Bar
Operating temperature 4.4-40 ºC
Membrane Asahi Glass Corporation (AGC)
Ion-exchange resin Mitsubishi Chemical
Anode materila IrOx/TiO2 su Ti
Cathode material stainless steel
Dimensions 300 x 280 x h 610 (H) mm
Weight 49 kg
Connections TC (1" for feed - 3/4" for concentrate)
Performance:
Minimu flow rate 0.57 m3 / h
Maximun flow rate 1.52 m3 / h
Normal flow 1 m3/h
Recovery 90-95%
Supply Voltage 150 VDC (maximum)
Current 0.5 - 4.5 A
Produced water quality resistivity >10 MΩ-cm

The water supplied must meet the following requirements:


Constituent Unit Power supply
TEA * ppm CaCO 3 <25@1 m 3 / h
Conductivity uS/cm <43
pH from 5 to 9
Hardness ppm CaCO 3 <1
Silica (reactive) ppm <1
TOC ppm <0.5
Total chlorine ppm <0.05
Fe, Mn, H2S ppm <0.01
SDI 15 min. <1.0
Turbidity NTU <1.0
Oil and fats Not detectable
Oxidizing agents Not detectable
Colour APHA <5


* TEA represents the total anionic load, thus including CO2

In all cases the module must be protected from components which might damage the resin or the membranes. The module must also be protected against excess pressure and water-hammer phenomena.

Note: the feed to the module must be a reverse-osmosis permeate or water presenting equivalent characteristics. In any case, the parameters indicated above are to be considered maximum values for each individual contaminant and the quality of the inlet water compatible with a specific application must be determined on a case by case basis.


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