Microstructured Devices for Chemical Processing. (Record no. 40403)
[ view plain ]
| 000 -LEADER | |
|---|---|
| fixed length control field | 11187nam a22005173i 4500 |
| 001 - CONTROL NUMBER | |
| control field | EBC1775476 |
| 003 - CONTROL NUMBER IDENTIFIER | |
| control field | MiAaPQ |
| 005 - DATE AND TIME OF LATEST TRANSACTION | |
| control field | 20240729123029.0 |
| 006 - FIXED-LENGTH DATA ELEMENTS--ADDITIONAL MATERIAL CHARACTERISTICS | |
| fixed length control field | m o d | |
| 007 - PHYSICAL DESCRIPTION FIXED FIELD--GENERAL INFORMATION | |
| fixed length control field | cr cnu|||||||| |
| 008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION | |
| fixed length control field | 240724s2014 xx o ||||0 eng d |
| 020 ## - INTERNATIONAL STANDARD BOOK NUMBER | |
| International Standard Book Number | 9783527685196 |
| Qualifying information | (electronic bk.) |
| 020 ## - INTERNATIONAL STANDARD BOOK NUMBER | |
| Canceled/invalid ISBN | 9783527331284 |
| 035 ## - SYSTEM CONTROL NUMBER | |
| System control number | (MiAaPQ)EBC1775476 |
| 035 ## - SYSTEM CONTROL NUMBER | |
| System control number | (Au-PeEL)EBL1775476 |
| 035 ## - SYSTEM CONTROL NUMBER | |
| System control number | (CaPaEBR)ebr10921707 |
| 035 ## - SYSTEM CONTROL NUMBER | |
| System control number | (CaONFJC)MIL640755 |
| 035 ## - SYSTEM CONTROL NUMBER | |
| System control number | (OCoLC)891386196 |
| 040 ## - CATALOGING SOURCE | |
| Original cataloging agency | MiAaPQ |
| Language of cataloging | eng |
| Description conventions | rda |
| -- | pn |
| Transcribing agency | MiAaPQ |
| Modifying agency | MiAaPQ |
| 050 #4 - LIBRARY OF CONGRESS CALL NUMBER | |
| Classification number | TP155.7 -- .K374 2014eb |
| 082 0# - DEWEY DECIMAL CLASSIFICATION NUMBER | |
| Classification number | 660.283 |
| 100 1# - MAIN ENTRY--PERSONAL NAME | |
| Personal name | Kashid, Madhvanand N. |
| 245 10 - TITLE STATEMENT | |
| Title | Microstructured Devices for Chemical Processing. |
| 250 ## - EDITION STATEMENT | |
| Edition statement | 1st ed. |
| 264 #1 - PRODUCTION, PUBLICATION, DISTRIBUTION, MANUFACTURE, AND COPYRIGHT NOTICE | |
| Place of production, publication, distribution, manufacture | Newark : |
| Name of producer, publisher, distributor, manufacturer | John Wiley & Sons, Incorporated, |
| Date of production, publication, distribution, manufacture, or copyright notice | 2014. |
| 264 #4 - PRODUCTION, PUBLICATION, DISTRIBUTION, MANUFACTURE, AND COPYRIGHT NOTICE | |
| Date of production, publication, distribution, manufacture, or copyright notice | ©2015. |
| 300 ## - PHYSICAL DESCRIPTION | |
| Extent | 1 online resource (381 pages) |
| 336 ## - CONTENT TYPE | |
| Content type term | text |
| Content type code | txt |
| Source | rdacontent |
| 337 ## - MEDIA TYPE | |
| Media type term | computer |
| Media type code | c |
| Source | rdamedia |
| 338 ## - CARRIER TYPE | |
| Carrier type term | online resource |
| Carrier type code | cr |
| Source | rdacarrier |
| 505 0# - FORMATTED CONTENTS NOTE | |
| Formatted contents note | Intro -- Microstructured Devices for Chemical Processing -- Contents -- Preface -- List of Symbols -- Chapter 1 Overview of Micro Reaction Engineering -- 1.1 Introduction -- 1.2 What are Microstructured Devices? -- 1.3 Advantages of Microstructured Devices -- 1.3.1 Enhancement of Transfer Rates -- 1.3.2 Enhanced Process Safety -- 1.3.3 Novel Operating Window -- 1.3.4 Numbering-Up Instead of Scale-Up -- 1.4 Materials and Methods for Fabrication of Microstructured Devices -- 1.5 Applications of Microstructured Devices -- 1.5.1 Microstructured Reactors as Research Tool -- 1.5.2 Industrial/Commercial Applications -- 1.6 Structure of the Book -- 1.7 Summary -- References -- Chapter 2 Basis of Chemical Reactor Design and Engineering -- 2.1 Mass and Energy Balance -- 2.2 Formal Kinetics of Homogenous Reactions -- 2.2.1 Formal Kinetics of Single Homogenous Reactions -- 2.2.2 Formal Kinetics of Multiple Homogenous Reactions -- 2.2.3 Reaction Mechanism -- 2.2.4 Homogenous Catalytic Reactions -- 2.3 Ideal Reactors and Their Design Equations -- 2.3.1 Performance Parameters -- 2.3.2 Batch Wise-Operated Stirred Tank Reactor (BSTR) -- 2.3.3 Continuous Stirred Tank Reactor (CSTR) -- 2.3.4 Plug Flow or Ideal Tubular Reactor (PFR) -- 2.4 Homogenous Catalytic Reactions in Biphasic Systems -- 2.5 Heterogenous Catalytic Reactions -- 2.5.1 Rate Equations for Intrinsic Surface Reactions -- 2.5.1.1 The Langmuir Adsorption Isotherms -- 2.5.1.2 Basic Kinetic Models of Catalytic Heterogenous Reactions -- 2.5.2 Deactivation of Heterogenous Catalysts -- 2.6 Mass and Heat Transfer Effects on Heterogenous Catalytic Reactions -- 2.6.1 External Mass and Heat Transfer -- 2.6.1.1 Isothermal Pellet -- 2.6.2 Internal Mass and Heat Transfer -- 2.6.2.1 Isothermal Pellet -- 2.6.2.2 Nonisothermal Pellet -- 2.6.2.3 Combination of External and Internal Transfer Resistances. |
| 505 8# - FORMATTED CONTENTS NOTE | |
| Formatted contents note | 2.6.2.4 Internal and External Mass Transport in Isothermal Pellets -- 2.6.2.5 The Temperature Dependence of the Effective Reaction Rate -- 2.6.2.6 External and Internal Temperature Gradient -- 2.6.3 Criteria for the Estimation of Transport Effects -- 2.7 Summary -- 2.8 List of Symbols -- References -- Chapter 3 Real Reactors and Residence Time Distribution (RTD) -- 3.1 Nonideal Flow Pattern and Definition of RTD -- 3.2 Experimental Determination of RTD in Flow Reactors -- 3.2.1 Step Function Stimulus-Response Method -- 3.2.2 Pulse Function Stimulus-Response Method -- 3.3 RTD in Ideal Homogenous Reactors -- 3.3.1 Ideal Plug Flow Reactor -- 3.3.2 Ideal Continuously Operated Stirred Tank Reactor (CSTR) -- 3.3.3 Cascade of Ideal CSTR -- 3.4 RTD in Nonideal Homogeneous Reactors -- 3.4.1 Laminar Flow Tubular Reactors -- 3.4.2 RTD Models for Real Reactors -- 3.4.2.1 Tanks in Series Model -- 3.4.2.2 Dispersion Model -- 3.4.3 Estimation of RTD in Tubular Reactors -- 3.5 Influence of RTD on the Reactor Performance -- 3.5.1 Performance Estimation Based on Measured RTD -- 3.5.2 Performance Estimation Based on RTD Models -- 3.5.2.1 Dispersion Model -- 3.5.2.2 Tanks in Series Model -- 3.6 RTD in Microchannel Reactors -- 3.6.1 RTD of Gas Flow in Microchannels -- 3.6.2 RTD of Liquid Flow in Microchannels -- 3.6.3 RTD of Multiphase Flow in Microchannels -- 3.7 List of Symbols -- References -- Chapter 4 Micromixing Devices -- 4.1 Role of Mixing for the Performance of Chemical Reactors -- 4.2 Flow Pattern and Mixing in Microchannel Reactors -- 4.3 Theory of Mixing in Microchannels with Laminar Flow -- 4.4 Types of Micromixers and Mixing Principles -- 4.4.1 Passive Micromixer -- 4.4.1.1 Single-Channel Micromixers -- 4.4.1.2 Multilamination Mixers -- 4.4.1.3 Split-and-Recombine (SAR) Flow Configurations -- 4.4.1.4 Mixers with Structured Internals. |
| 505 8# - FORMATTED CONTENTS NOTE | |
| Formatted contents note | 4.4.1.5 Chaotic Mixing -- 4.4.1.6 Colliding Jet Configurations -- 4.4.1.7 Moving Droplet Mixers -- 4.4.1.8 Miscellaneous Flow Configurations -- 4.4.2 Active Micromixers -- 4.4.2.1 Pressure Induced Disturbances -- 4.4.2.2 Elektrokinetic Instability -- 4.4.2.3 Electrowetting-Induced Droplet Shaking -- 4.4.2.4 Ultrasound/Piezoelectric Membrane Action -- 4.4.2.5 Acoustic Fluid Shaking -- 4.4.2.6 Microstirrers -- 4.4.2.7 Miscellaneous Active Micromixers -- 4.5 Experimental Characterization of Mixing Efficiency -- 4.5.1 Physical Methods -- 4.5.2 Chemical Methods -- 4.5.2.1 Competitive Chemical Reactions -- 4.6 Mixer Efficiency and Energy Consumption -- 4.7 Summary -- 4.8 List of Symbols -- References -- Chapter 5 Heat Management by Microdevices -- 5.1 Introduction -- 5.2 Heat Transfer in Microstructured Devices -- 5.2.1 Straight Microchannels -- 5.2.2 Curved Channel Geometry -- 5.2.3 Complex Channel Geometries -- 5.2.4 Multichannel Micro Heat Exchanger -- 5.2.5 Microchannels with Two Phase Flow -- 5.3 Temperature Control in Chemical Microstructured Reactors -- 5.3.1 Axial Temperature Profiles in Microchannel Reactors -- 5.3.2 Parametric Sensitivity -- 5.3.3 Multi-injection Microstructured Reactors -- 5.3.3.1 Mass and Energy Balance in Multi-injection Microstructured Reactors -- 5.3.3.2 Reduction of Hot Spot in Multi-injection Reactors -- 5.4 Case Studies -- 5.4.1 Synthesis of 1,3-Dimethylimidazolium-Triflate -- 5.4.2 Nitration of Dialkyl-Substituted Thioureas -- 5.4.3 Reduction of Methyl Butyrate -- 5.4.4 Reactions with Grignard Reagent in Multi-injection Reactor -- 5.5 Summary -- 5.6 List of Symbols -- References -- Chapter 6 Microstructured Reactors for Fluid-Solid Systems -- 6.1 Introduction -- 6.2 Microstructured Reactors for Fluid-Solid Reactions -- 6.3 Microstructured Reactors for Catalytic Gas-Phase Reactions -- 6.3.1 Randomly Micro Packed Beds. |
| 505 8# - FORMATTED CONTENTS NOTE | |
| Formatted contents note | 6.3.2 Structured Catalytic Micro-Beds -- 6.3.3 Catalytic Wall Microstructured Reactors -- 6.4 Hydrodynamics in Fluid-Solid Microstructured Reactors -- 6.5 Mass Transfer in Catalytic Microstructured Reactors -- 6.5.1 Randomly Packed Bed Catalytic Microstructured Reactors -- 6.5.2 Catalytic Foam Microstructured Reactors -- 6.5.3 Catalytic Wall Microstructured Reactors -- 6.5.4 Choice of Catalytic Microstructured Reactors -- 6.6 Case Studies -- 6.6.1 Catalytic Partial Oxidations -- 6.6.2 Selective (De)Hydrogenations -- 6.6.3 Catalytic Dehydration -- 6.6.4 Ethylene Oxide Synthesis -- 6.6.5 Steam Reforming -- 6.6.6 Fischer-Tropsch Synthesis -- 6.7 Summary -- 6.8 List of Symbols -- References -- Chapter 7 Microstructured Reactors for Fluid-Fluid Reactions -- 7.1 Conventional Equipment for Fluid-Fluid Systems -- 7.2 Microstructured Devices for Fluid-Fluid Systems -- 7.2.1 Micromixers -- 7.2.2 Microchannels -- 7.2.2.1 Microchannels with Inlet T, Y, and Concentric Contactor -- 7.2.2.2 Microchannels with Partial Two-Fluid Contact -- 7.2.2.3 Microchannels with Mesh or Sieve-Like Interfacial Support Contactors -- 7.2.2.4 Microchannels with Static Mixers -- 7.2.2.5 Parallel Microchannels with Internal Redispersion Units -- 7.2.3 Microstructured Falling Film Reactor for Gas-Liquid Reactions -- 7.3 Flow Patterns in Fluid-Fluid Systems -- 7.3.1 Gas-Liquid Flow Patterns -- 7.3.1.1 Bubbly Flow -- 7.3.1.2 Taylor Flow -- 7.3.1.3 Slug Bubbly Flow -- 7.3.1.4 Churn Flow -- 7.3.1.5 Annular and Parallel Flow -- 7.3.2 Liquid-Liquid Flow Patterns -- 7.3.2.1 Drop Flow -- 7.3.2.2 Slug Flow -- 7.3.2.3 Slug-Drop Flow -- 7.3.2.4 Deformed Interface Flow -- 7.3.2.5 Annular and Parallel Flow -- 7.3.2.6 Slug-Dispersed Flow -- 7.3.2.7 Dispersed Flow -- 7.4 Mass Transfer -- 7.4.1 Mass Transfer Models -- 7.4.2 Characterization of Mass Transfer in Fluid-Fluid Systems. |
| 505 8# - FORMATTED CONTENTS NOTE | |
| Formatted contents note | 7.4.3 Mass Transfer in Gas-Liquid Microstructured Devices -- 7.4.3.1 Mass Transfer in Taylor Flow -- 7.4.3.2 Mass Transfer in Slug Annular and Churn Flow Regime -- 7.4.3.3 Mass Transfer in Microstructured Falling Film Reactors -- 7.4.4 Mass Transfer in Liquid-Liquid Microstructured Devices -- 7.4.4.1 Slug Flow (Taylor Flow) -- 7.4.4.2 Slug-Drop and Deformed Interface Flow -- 7.4.4.3 Annular and Parallel Flow -- 7.4.4.4 Slug-Dispersed and Dispersed Flow -- 7.4.5 Comparison with Conventional Contactors -- 7.5 Pressure Drop in Fluid-Fluid Microstructured Channels -- 7.5.1 Pressure Drop in Gas-Liquid Flow -- 7.5.2 Pressure Drop in Liquid-Liquid Flow -- 7.5.2.1 Pressure Drop - Without Film -- 7.5.2.2 Pressure Drop - With Film -- 7.5.2.3 Power Dissipation in Liquid/Liquid Reactors -- 7.6 Flow Separation in Liquid-Liquid Microstructured Reactors -- 7.6.1 Conventional Separators -- 7.6.2 Types of Microstructured Separators -- 7.6.2.1 Geometrical Modifications -- 7.6.2.2 Wettability Based Flow Splitters -- 7.6.3 Conventional Separator Adapted for Microstructured Devices -- 7.7 Fluid-Fluid Reactions in Microstructured Devices -- 7.7.1 Examples of Gas-Liquid Reactions -- 7.7.1.1 Halogenation -- 7.7.1.2 Nitration, Oxidations, Sulfonation, and Hydrogenation -- 7.7.2 Examples of Liquid-Liquid Reactions -- 7.7.2.1 Nitration Reaction -- 7.7.2.2 Transesterification: Biodiesel Production -- 7.7.2.3 Vitamin Precursor Synthesis -- 7.7.2.4 Phase Transfer Catalysis (PTC) -- 7.7.2.5 Enzymatic Reactions -- 7.8 Summary -- 7.9 List of Symbols -- References -- Chapter 8 Three-Phase Systems -- 8.1 Introduction -- 8.2 Gas-Liquid-Solid Systems -- 8.2.1 Conventional Gas-Liquid-Solid Reactors -- 8.2.2 Microstructured Gas-Liquid-Solid Reactors -- 8.2.2.1 Continuous Phase Microstructured Reactors -- 8.2.2.2 Dispersed Phase Microstructured Reactors. |
| 505 8# - FORMATTED CONTENTS NOTE | |
| Formatted contents note | 8.2.2.3 Mass Transfer and Chemical Reaction. |
| 588 ## - SOURCE OF DESCRIPTION NOTE | |
| Source of description note | Description based on publisher supplied metadata and other sources. |
| 590 ## - LOCAL NOTE (RLIN) | |
| Local note | Electronic reproduction. Ann Arbor, Michigan : ProQuest Ebook Central, 2024. Available via World Wide Web. Access may be limited to ProQuest Ebook Central affiliated libraries. |
| 650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM | |
| Topical term or geographic name entry element | Chemical processes -- Study and teaching. |
| 655 #4 - INDEX TERM--GENRE/FORM | |
| Genre/form data or focus term | Electronic books. |
| 700 1# - ADDED ENTRY--PERSONAL NAME | |
| Personal name | Renken, Albert. |
| 700 1# - ADDED ENTRY--PERSONAL NAME | |
| Personal name | Kiwi-Minsker, Lioubov. |
| 776 08 - ADDITIONAL PHYSICAL FORM ENTRY | |
| Relationship information | Print version: |
| Main entry heading | Kashid, Madhvanand N. |
| Title | Microstructured Devices for Chemical Processing |
| Place, publisher, and date of publication | Newark : John Wiley & Sons, Incorporated,c2014 |
| International Standard Book Number | 9783527331284 |
| 797 2# - LOCAL ADDED ENTRY--CORPORATE NAME (RLIN) | |
| Corporate name or jurisdiction name as entry element | ProQuest (Firm) |
| 856 40 - ELECTRONIC LOCATION AND ACCESS | |
| Uniform Resource Identifier | <a href="https://ebookcentral.proquest.com/lib/orpp/detail.action?docID=1775476">https://ebookcentral.proquest.com/lib/orpp/detail.action?docID=1775476</a> |
| Public note | Click to View |
No items available.