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Regenerative adsorption | |
| The process exists from a bed of adsorbents (active carbon, zeolite, polymer or a combination), on what the fragrance or solvents is firstly adsorbed and desorbert again whereupon the cycle again can start. Generally 5-tal cycles are necessaryto get a stable adsorption and desorption quantity. The desorbering can happen by means of pressure lowering, temperature increase or a combination. Generally the desorption happens with steam, hot air or hot inert gas. The time of regeneration can be set up or is possible detected with means of a sensor. If one has a constant emission average has u can be work with fixed times. The gases which are released at the desorption must be treated further. In the case of steam or vacuum regeneration the solvent can be recovered easily using a condenser from the desorption gasses. |
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There is only a then a very small flow non condensable components that possibly sent back to the adsorption circle. At desorption with hot air or is hot inert gas an accumulation of the concentration can be obtained of 10 - 15 time. The desorption gasses to be in this case is less suitable for solvent recuperation but well for afterburning. At the design of the installation the work capacity must be known. The required bed size can be namely twice the size of the calculated fresh adsorbents. This way the work capacity has a large impact on the size of the installation and on the investment - and functioning costs.
There three different implementation forms of adsorption- desorption installations exist:
At thermal regeneration the installation exists from 2 or more adsorbentbeds. One bed is regenerated, the other bed remains active for adsorption. The possible third bed is dried , cooled and stand-by stand after regeneration. Regeneration is carried out by blowing steam through the bed so that the bed warms up and the VOC desorbs. This happens at temperatures between 80 and 200 °C. After the desorbing cooling air us blown through the bed so that it cools down and dries. This is done till the desired temperature and humidity of the bed has been reached. Thermal regeneration is most suitable for volatile VOC.
The disadvantages are:
At spray cabins of enamel, glue regenerative adsorption are especially used to reduce the flow Click here for overview about air purification technologies For more books and reading information see our website: | |
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