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