Based on the experiment results and calculation the ion exchange is design as follows.
Ion exchange resin column design.
1 2 minutes column height.
A demineralizer system consists of one or more ion exchange resin columns which include a strong acid cation unit and a strong base anion unit.
The hardness ions ca and mg move into the resin beads and each of these divalent.
Basic column types are shown in another page.
The recovered zinc is eluted with pure water and transferred intermittently to be treated by further refining 2.
4 each with a capacity of 120m3 h surface loading.
Design procedures the breakthrough curves for an ion exchange column and an adsorption column are similar.
Only a few general recommendations to ensure that an ion exchange system is designed economically and to achieve good performance and a simple but detailed example.
With the exception of the resin.
Ion exchange takes place in one column while the resin in the second column is being regenerated resulting in continuous operation.
Ion exchange process for control of iron in copper electrolytes 1.
10 days material cost of resin per m3 water produced.
For example metal contaminants are.
Rohm and haas ion exchange ion exchange introduction 4 fd sep 2008 to soften water you take a cation exchange resin on which the mobile ion inside the beads is sodium na and you pass the hard water through a column filled with the sodium form resin.
Bigger vessels with up to 4 0 m are sometimes built but the aspect ratio of the resin bed width height becomes unfavourable and very precise distribution and collection systems must be fitted to ensure an even flow of the water during service and.
One variation of the standard design uses a layer of weak acid resin on top of strong acid cation resin.
Ion exchange plant design some basic principles you will not find here a complete plant design manual.
Goro nickel cobalt project in new.
The design of the vessels should give a maximum resin bed depth while limiting the pressure drop across the resin bed to 1 bar.
Calenergy minerals is using an anionic dowex resin to recover zinc from geothermal brines in a series of ion exchange columns.
O the scale up approach o the kinetic approach.
Continuous ion exchangers consist of two columns in parallel.
Usage examples continuous ion exchangers are used when it is imperative that product be continually generated.
How to design an ion exchange resin system.
Column size most industrial ion exchange columns have a diameter between 0 5 and 3 2 m.
The optimum column diameter must be a balance between the resin bed height the ratio of resin height to diameter h d and the linear velocity.
The aim of the work described in this report was to design an ion exchange column for the removal of ammonium ions from ro permeate.
Therefore the same procedures used for the design of adsorption columns may be used for ion exchange columns.
