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260 L.K. Wang et al. Fig. 6.18. Separation of cyclodextrin from liquefied starch by UF and NF. Cheese Whey Pretreatment Ultrafiltration Permeate Sterilization Feed Storage (Balance) Tank Retentate Nutrient Gas Temperature used for fermentation of biomass to ethanol, saccharification of liquefied starch, processing of soybean for producing protein hydrolyzates (Table 6.5) and processing of biomass for the production of biochemicals. pH Fermentation Vessel Bleed Circuit Cells MF Microbial Cells Liquid Product Fig. 6.19. Continuous membrane reactor for fermentation process. Membrane Module
Treatment of Food Industry Foods and Wastes by Membrane Filtration 261 Fig. 6.20. Cross-flow pervaporation system for VOC separation. Waste Solution Waste Acids Metallic Salts A A A Acids Acids Metallic Salts CMR proved to be a feasible process for the treatment of liquefied starch (Table 6.5 and Fig. 6.18). Cyclodextrin (CD) can be produced from starch in the presence of CD-forming enzyme in a fermentation reactor (Fig. 6.18). To enhance the CD productivity, UF membrane is used in conjunction with the fermentation reactor forming a CMR in which an enzyme is continuously separated by UF and recycled to the fermentation reactor for CD production. The fermentation reactor is usually a stirred-tank. The UF membrane separates CD and recycles the enzyme. The functions of the NF membrane shown in Fig. 6.18 are twofold: Water Recovered Acids Fig. 6.21. Diffusion dialysis system using anion-exchange membrane. A: Anion Exchange Membrane.
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Membrane and Desalination Technolog
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Editors Dr. Lawrence K. Wang Zorex
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vi Preface Our treatment of polluti
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Contents Preface . ................
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Contents xi 3.4. Considering Existi
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Contents xiii 7. Membrane Separatio
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Contents xv 6. Design for Large Com
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Contents xvii 13. Desalination of S
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Contributors JIRAPAT ANANPATTARACHA
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CONTENTS 1 Membrane Technology: Pas
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Membrane Technology: Past, Present
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48 J. Ren and R. Wang Key Words Pol
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50 J. Ren and R. Wang Nonporous den
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52 J. Ren and R. Wang pervaporation
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54 J. Ren and R. Wang HO HO OH O OH
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56 J. Ren and R. Wang Fig. 2.7 Chem
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58 J. Ren and R. Wang N O O 3.10. P
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60 J. Ren and R. Wang inversion, th
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62 J. Ren and R. Wang where Dm i an
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64 J. Ren and R. Wang as nucleation
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66 J. Ren and R. Wang and no polyme
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68 J. Ren and R. Wang where b ¼ v1
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70 J. Ren and R. Wang S gelation ti
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72 J. Ren and R. Wang structure wil
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74 J. Ren and R. Wang Viscous finge
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76 J. Ren and R. Wang nonsolvent so
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78 J. Ren and R. Wang Thickness of
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80 J. Ren and R. Wang 5.1.1. Rheolo
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82 J. Ren and R. Wang the spinneret
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84 J. Ren and R. Wang Dynamic visco
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86 J. Ren and R. Wang where A is th
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88 J. Ren and R. Wang In the spinni
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90 J. Ren and R. Wang stress, espec
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92 J. Ren and R. Wang solution at t
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94 J. Ren and R. Wang TIPS ¼ Therm
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96 J. Ren and R. Wang 5. Kesting RE
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98 J. Ren and R. Wang 51. Matsuyama
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100 J. Ren and R. Wang 92. Ren J, C
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102 L. Song and K.Guan Tay Key Word
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104 L. Song and K.Guan Tay Flux A A
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106 L. Song and K.Guan Tay increase
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108 L. Song and K.Guan Tay Table 3.
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110 L. Song and K.Guan Tay • A fe
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112 L. Song and K.Guan Tay Feed wat
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114 L. Song and K.Guan Tay Fouling
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116 L. Song and K.Guan Tay Fouling
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118 L. Song and K.Guan Tay The symb
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120 L. Song and K.Guan Tay Table 3.
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122 L. Song and K.Guan Tay Permeate
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124 L. Song and K.Guan Tay Average
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128 L. Song and K.Guan Tay generati
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132 L. Song and K.Guan Tay flux. Un
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134 L. Song and K.Guan Tay 14. Kaak
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136 N.K. Shammas and L.K. Wang remo
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138 N.K. Shammas and L.K. Wang The
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140 N.K. Shammas and L.K. Wang excu
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142 N.K. Shammas and L.K. Wang dire
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144 N.K. Shammas and L.K. Wang broa
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146 N.K. Shammas and L.K. Wang remo
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148 N.K. Shammas and L.K. Wang 4. T
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150 N.K. Shammas and L.K. Wang 8. S
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152 N.K. Shammas and L.K. Wang 4.5.
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154 N.K. Shammas and L.K. Wang Tabl
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156 N.K. Shammas and L.K. Wang phys
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158 N.K. Shammas and L.K. Wang mono
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164 N.K. Shammas and L.K. Wang Fig.
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170 N.K. Shammas and L.K. Wang CSTR
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172 N.K. Shammas and L.K. Wang chec
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174 N.K. Shammas and L.K. Wang due
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178 N.K. Shammas and L.K. Wang 4. C
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182 N.K. Shammas and L.K. Wang Sens
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186 N.K. Shammas and L.K. Wang Maxi
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188 N.K. Shammas and L.K. Wang 2. 2
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196 N.K. Shammas and L.K. Wang PFR
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198 N.K. Shammas and L.K. Wang 16.
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5 Treatment of Industrial Effluents
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Treatment of Industrial Effluents,
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312 J. Paul Chen et al. To calculat
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314 J. Paul Chen et al. biofilm for
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316 J. Paul Chen et al. magnesium,
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318 J. Paul Chen et al. reduction o
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320 J. Paul Chen et al. Table 7.6 C
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322 J. Paul Chen et al. many factor
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324 J. Paul Chen et al. 9.2. Gas Se
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326 J. Paul Chen et al. c w2 ¼ Con
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328 J. Paul Chen et al. 14. Economi
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330 J. Paul Chen et al. 55. Basu OD
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332 J. Paul Chen et al. 99. Teodosi
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334 N.K. Shammas and L.K. Wang 1. I
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336 N.K. Shammas and L.K. Wang dete
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338 N.K. Shammas and L.K. Wang for
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342 N.K. Shammas and L.K. Wang impo
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346 N.K. Shammas and L.K. Wang prio
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348 N.K. Shammas and L.K. Wang 5-20
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354 N.K. Shammas and L.K. Wang cour
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358 N.K. Shammas and L.K. Wang wher
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360 N.K. Shammas and L.K. Wang and
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362 N.K. Shammas and L.K. Wang syst
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364 N.K. Shammas and L.K. Wang blee
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370 N.K. Shammas and L.K. Wang oxid
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372 N.K. Shammas and L.K. Wang memb
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376 N.K. Shammas and L.K. Wang capa
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378 N.K. Shammas and L.K. Wang Disp
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380 N.K. Shammas and L.K. Wang sali
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384 N.K. Shammas and L.K. Wang the
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386 N.K. Shammas and L.K. Wang 9. N
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388 N.K. Shammas and L.K. Wang 16.
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CONTENTS 9 Adsorption Desalination:
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Adsorption Desalination: A Novel Me
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434 J. Qin and K.A. Kekre 1. INTROD
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436 J. Qin and K.A. Kekre utilized
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438 J. Qin and K.A. Kekre 3.2. Desc
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440 J. Qin and K.A. Kekre Table 10.
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442 J. Qin and K.A. Kekre Fig. 10.4
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446 J. Qin and K.A. Kekre different
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448 J. Qin and K.A. Kekre protectin
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462 J. Qin and K.A. Kekre 7.2. Desc
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468 J. Qin and K.A. Kekre and anion
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470 J. Qin and K.A. Kekre become on
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472 J. Qin and K.A. Kekre COD ¼ Ch
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474 J. Qin and K.A. Kekre 25. Parso
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476 J. Qin and K.A. Kekre technique
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478 P. Kajitvichyanukul et al. 1. I
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480 P. Kajitvichyanukul et al. of 5
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482 P. Kajitvichyanukul et al. well
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484 P. Kajitvichyanukul et al. The
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486 P. Kajitvichyanukul et al. 3.3.
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488 P. Kajitvichyanukul et al. 4. C
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490 P. Kajitvichyanukul et al. nonp
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492 P. Kajitvichyanukul et al. rDNA
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494 P. Kajitvichyanukul et al. 3. E
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496 P. Kajitvichyanukul et al. Form
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500 P. Kajitvichyanukul et al. do n
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502 P. Kajitvichyanukul et al. Wate
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504 P. Kajitvichyanukul et al. Tabl
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506 P. Kajitvichyanukul et al. Fig.
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508 P. Kajitvichyanukul et al. Tabl
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512 P. Kajitvichyanukul et al. solu
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516 P. Kajitvichyanukul et al. (b)
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518 P. Kajitvichyanukul et al. 8. A
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520 P. Kajitvichyanukul et al. 52.
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12 Desalination of Seawater by Ther
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Desalination of Seawater by Thermal
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CONTENTS 13 Desalination of Seawate
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Desalination of Seawater by Reverse
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604 P. Kajitvichyanukul et al. wate
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606 P. Kajitvichyanukul et al. hydr
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608 P. Kajitvichyanukul et al. it i
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610 P. Kajitvichyanukul et al. UV i
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612 P. Kajitvichyanukul et al. The
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614 P. Kajitvichyanukul et al. abov
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618 P. Kajitvichyanukul et al. larg
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620 P. Kajitvichyanukul et al. insi
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624 P. Kajitvichyanukul et al. wate
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628 P. Kajitvichyanukul et al. Adju
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630 P. Kajitvichyanukul et al. 4. D
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632 P. Kajitvichyanukul et al. For
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634 P. Kajitvichyanukul et al. Cc
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640 P. Kajitvichyanukul et al. grea
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642 P. Kajitvichyanukul et al. 2. F
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644 P. Kajitvichyanukul et al. cond
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648 P. Kajitvichyanukul et al. l En
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652 P. Kajitvichyanukul et al. Feed
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658 P. Kajitvichyanukul et al. holl
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660 P. Kajitvichyanukul et al. wher
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662 P. Kajitvichyanukul et al. 10 L
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670 K. Mohanty and R. Ghosh 1. INTR
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672 K. Mohanty and R. Ghosh municip
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674 K. Mohanty and R. Ghosh 3.2. Tw
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676 K. Mohanty and R. Ghosh Fig. 16
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680 K. Mohanty and R. Ghosh Cabassu
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682 K. Mohanty and R. Ghosh 4.3. Ga
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684 K. Mohanty and R. Ghosh Membran
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688 K. Mohanty and R. Ghosh MBRs ca
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690 K. Mohanty and R. Ghosh two pro
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692 K. Mohanty and R. Ghosh can be
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694 K. Mohanty and R. Ghosh 27. Bel
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696 K. Mohanty and R. Ghosh 70. Fut
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Acceptance testing, 384-385 ACF. Se
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Index 701 Challenge test solution d
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Index 703 Disinfection by-products
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Index 705 Hemodialysis, 2, 6, 281 H
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Index 707 Membrane bioreactor-rever
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Index 709 Microfiltration-reverse o
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Index 711 Physical cleaning, 322-32
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Index 713 Reynolds number, 676, 679
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Index 715 Thermal concentration, 25
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