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20231120010610.0 |
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|a 1280047136
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|z 9780128196267
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|z 0128196262
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|a (OCoLC)1277275016
|z (OCoLC)1280047136
|z (OCoLC)1280103504
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|a TP248.25.M46
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4 |
|a 660.28424
|2 23
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1 |
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|a Ismail, Ahmad Fauzi.
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1 |
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|a Membrane separation processes :
|b theories, problems and solutions /
|c Ahmad Fauzi Ismail and Takeshi Matsuura.
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| 260 |
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|a Amsterdam :
|b Elsevier,
|c [2022]
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| 300 |
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|a 1 online resource
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| 336 |
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|a text
|b txt
|2 rdacontent
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| 337 |
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|a computer
|b c
|2 rdamedia
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| 338 |
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|a online resource
|b cr
|2 rdacarrier
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| 500 |
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|a Includes index.
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| 588 |
0 |
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|a Print version record.
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|a Front Cover -- Membrane Separation Processes -- Copyright Page -- Contents -- Preface -- 1 Solubility parameter -- 1.1 Why is the solubility parameter necessary? -- 1.2 Theory -- 1.3 Examples of the solubility parameter -- Nomenclature -- References -- 2 Triangular phase diagram -- 2.1 Principles -- 2.1.1 Thermodynamics of polymer solution -- 2.1.2 Solutions for the ternary system using Flory-Huggins equations -- Nomenclature -- References -- 3 Reverse osmosis, forward osmosis, and pressure-retarded osmosis -- 3.1 Reverse osmosis -- 3.1.1 Reverse osmosis performance -- 3.2 Concentration polarization -- 3.3 Prediction of RO performance considering concentration polarization -- 3.4 Pore models -- 3.4.1 Preferential sorption-capillary flow model -- 3.4.2 Gl|ckauf model -- 3.5 Forward osmosis and pressure-retarded osmosis -- 3.5.1 Principles of forward osmosis, reverse osmosis, and pressure-retarded osmosis -- 3.5.2 Applications of forward osmosis -- 3.5.3 Concentration polarization in forward osmosis -- 3.5.4 Forward osmosis transport -- Nomenclature -- References -- 4 Nanofiltration -- 4.1 Solution in general -- 4.2 Solution for mono-monovalent electrolytes -- 4.3 Solution method -- Nomenclature -- References -- 5 Ultrafiltration and microfiltration -- 5.1 Ultrafiltration: gel model -- 5.2 Microfiltration: Brownian diffusion, shear-induced diffusion, inertia lift -- 5.2.1 Brownian diffusion -- 5.2.2 Shear-induced diffusion -- 5.2.3 Inertial lift -- Nomenclature -- References -- 6 Membrane gas separation -- 6.1 Solution-diffusion model -- 6.1.1 Steady-state transport -- 6.1.2 Unsteady-state evaluation of S and D by the time-lag method -- 6.1.3 Separation of binary gas mixture -- 6.1.4 Resistance model -- 6.2 Gas transport in porous membrane -- 6.2.1 Transport mechanism -- 6.2.2 Separation of gas mixture by the porous membrane.
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|a 6.2.3 Measurement of pore size and pore size distribution -- 6.3 Mixed matrix membrane -- Nomenclature -- References -- 7 Pervaporation -- 7.1 Pervaporation transport -- 7.2 Pervaporation transport model by Greenlaw and coworkers -- 7.3 A new model for pervaporation transport -- Nomenclature -- References -- 8 Membrane distillation -- 8.1 About membrane distillation -- 8.1.1 Process principles -- 8.1.2 Different membrane distillation configurations -- 8.1.2.1 Direct contact membrane distillation -- 8.1.2.2 Air gap membrane distillation -- 8.1.2.3 Vacuum membrane distillation -- 8.1.2.4 Sweep gas membrane distillation -- 8.2 Transport in direct contact membrane distillation -- 8.2.1 Heat transfer -- 8.2.2 Mass transfer -- Nomenclature -- References -- 9 Membrane contactor (membrane absorption) and membrane adsorption -- 9.1 Membrane contactor -- 9.1.1 Transport in membrane contactor -- 9.1.2 Wilson plot -- 9.2 Membrane adsorption -- 9.2.1 Membrane adsorption process outline -- 9.2.2 Carman-Kozeny equation for flux calculation -- 9.2.3 Mass balance in membrane adsorption -- Nomenclature -- References -- 10 Membrane module -- 10.1 Reverse osmosis -- 10.1.1 Reverse osmosis hollow fiber module -- 10.1.2 Reverse osmosis flat-sheet membrane -- 10.2 Gas separation -- Nomenclature -- References -- 11 Membrane system -- 11.1 Two flow types -- 11.1.1 Cross-flow types -- 11.1.2 Cascade and recycle -- 11.1.3 Hybrid systems -- 11.2 Reverse osmosis systems -- 11.2.1 Reverse osmosis-nanofiltration cascade -- 11.2.2 Reverse osmosis recycle -- 11.3 Gas separator systems -- 11.3.1 Gas separator cascade -- 11.3.2 Gas separator recycle -- 11.4 Forward osmosis-reverse osmosis hybrid system -- 11.5 Membrane reactor -- 11.5.1 Description of the membrane bioreactor -- 11.5.2 Bioreactor modeling -- Nomenclature -- References -- 12 Cost of water.
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| 505 |
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|a 12.1 Calculation of water production cost by Desalination Economic Evaluation Program 2000 -- 12.1.1 Case identification and site characteristics box -- 12.1.2 Technical parameter input data -- 12.1.3 Membrane water performance data -- 12.1.4 Economic parameters input data -- 12.1.5 Reverse osmosis plant cost input data -- 12.1.6 Single-purpose plant performance -- 12.1.7 Stand-alone reverse osmosis water plant performance -- 12.1.8 Stand-alone reverse osmosis water plant costs -- 12.1.9 Power plant -- 12.1.10 Stand-alone reverse osmosis plant -- References -- Appendix -- Index -- Back Cover.
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| 650 |
|
0 |
|a Membrane separation.
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| 650 |
|
6 |
|a S�eparation par membranes.
|0 (CaQQLa)201-0147649
|
| 650 |
|
7 |
|a Membrane separation
|2 fast
|0 (OCoLC)fst01015857
|
| 700 |
1 |
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|a Matsuura, Takeshi,
|d 1936-
|
| 776 |
0 |
8 |
|i Print version:
|z 0128196262
|z 9780128196267
|w (OCoLC)1240773582
|
| 776 |
0 |
8 |
|i Print version:
|a ISMAIL, AHMAD FAUZI. MATSUURA, TAKESHI.
|t MEMBRANE SEPARATION PROCESSES.
|d [S.l.] : ELSEVIER, 2021
|z 0128196262
|w (OCoLC)1240773582
|
| 856 |
4 |
0 |
|u https://sciencedirect.uam.elogim.com/science/book/9780128196267
|z Texto completo
|
