Page 287 - Adsorption Technology & Design, Elsevier (1998)
P. 287

262  Index


              sugar refining 2, 3,14, 21,214, 223,   Bed draining 246
               224, 226                      Bed filling 107,108, 246
              sweetening of natural gas 187,   Bed lifting 246
               204-207                       Beds in cascade 114-119
              taste removal 14               Bentonite 3
              treatment of hazardous industrial   Benzene 22, 52, 53
               wastes 243,250                Bergbau-Forschung process 201
              treatment of pesticides 243    Binder 9,14, 27, 79, 205
              VOC control 15, 27, 204,213, 21.4   Biological activated carbon 246
              water treatment 3, 4,14,15,18, 21,   Biot number 83
               26,100,106,107,121.,  136-142,   Bleaching of oils 3
               166-172,182, 214, 241,243,246   Blowdown 191,192,193,196
              xylene separation 26           Bone char 2, 21,241
            Argon 23, 29, 41,201             Boundary layers 66, 68
            Aromatics 23, 29,118             Boron-fluorine compounds 28
            Aromax process 1.18              Breakthrough 97, 98,102,119,145,151,
            Arosorb process 11.8                 165,170,182, 209, 234, 242
            Arrhenius equation 74            Breakthrough concentration 169,170
            Attrition 27, 96, 99,105,106,109,111,   Breakthrough curve 103,104,  145,
               114,177                           154-157, 165-169, 248, 250
            Axial conduction of heat 157, 158   Breakthrough time 151
            Axial dispersion 69, 92, 93,146-152,   Breakthrough volume 169
               158,162,166,1.74,178-180,228,   Brunauer-Emmett-Teller (BET) equa-
               229                               tion 10, 42-44, 241
            Axial dispersion coefficient 148, 222   Bulk separation 8
                                             Butane 29, 54, 62, 89, 92, 93, 109
            Axially dispersed plug flow 148,149,
                                             Butene 54
                154-156, 178, 221
                                             Buoyancy forces 106
            Azeotropes 29, 61, 62, 132, 205,209
            Backwashing 106,107              Cage 24, 50, 51, 63, 67
            Ballast 105                      Capacity at breakpoint 164,173,174
            Batch processes 2, 20, 75, 82, 99-102,   Caprolactam 28
                                             Carbon 2, 4, 8, 29, 32, 39, 42, 46, 47,183,
                106,136-142,182, 244, 246, 251
              countercurrent 101,102,141,142     241,243,246, 250
              cross flow 100, 102,138-141    Carbon dioxide 26, 27, 29, 46, 52, 61,86,
              optimum number of stages 102       91,199, 204, 205
              minimum amount of adsorbent 102   Carbon monoxide 29, 52
              multiple stages 100-102        Carbon tetrafluoride 92, 93
                                             Catalysis 241,242
              number of stages 102
                                             Cavity 25, 79
              single stage 99,136-138
                                             Cetane 196
            Bauxite 2, 3
            Bead activated carbon 112        Chabazite 24
                                             Channel 24, 50, 67, 79
            Bed crushing 178, 246
                                             Channeling 102, 146,176,181
            Bed depth service time (BDST) 164,
                                             Chapman-Enskog equation 71
                170-173
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