Page 279 - Gas Purification 5E
P. 279

Mechanical Design and Operation of Alkanolarnine Plants   263
        A schematic flow  diagram of the unit  is shown in Figure 3-33. A  solution  of 48 wt%
      potassium hydroxide is added to the contaminated diethanolamine before it enters the top of
      a packed tower where it is contacted with superheated steam rising from the reboiler. Essen-
      tially all of the amine and water is vaporized, and the product is withdrawn at a point below
      the packed section into a condenser, which is held at a slightly lower pressure than that pre-
      vailing in the reboiler. A steam jet is used to maintain the required pressure. The salts drop
      into the reboiler and melt at 420 to 440"F, and any residual  diethanolamine  is flashed  off.
      The temperature of the diethanolamine-water vapor withdrawn is 300 to 375°F. The temper-
      atures in the column and reboiler are sufficient to vaporize practically all the amine without
      decomposition. Heat  is supplied by  circulating oil at 600°F through the reboiler tubes.
      Recovery of 90% of reusable diethanolamine is claimed.
         Another proposed thermal reclaiming method consists of withdrawing a small sidestream
      of the ethanolamine solution, adding  sodium or potassium  hydroxide, and then  removing
       most of the water by distillation. After this, the solution, containing 5% to 10% of water, is
       mixed  with  an alcohol-preferably   isopropyl  alcohol-which  causes  precipitation  of  the
       sodium or potassium salts of volatile organic  and inorganic  acids. After filtration  of these
       salts, the alcohol is removed from the mixture by distillation, and the amine is returned to the
       main solution stream (Paulsen et al., 1955).
        Thomason  (1985) described  tests of  a novel reclaiming  technique  in which  DEA was
      reclaimed by sparging both C02 and low pressure steam into a reclaimer kettle that contains
      DEA. At 280°F and atmospheric pressure, reclaiming  was successful, but part of the DEA
      was converted to TEA.









                             WATER SPRAY
                                                 ,-DEMISTING  PA0
                   CONTAMINATED
                                                      ,P--  CONDENSER





                                                  WATER VAPOR












                Figure 3-33. Diethanolamine reclaimer using molten salt bath.
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