LEADER 05476nam 2200697 450 001 9910808632903321 005 20210209143938.0 010 $a1-118-44937-1 010 $a1-118-44939-8 035 $a(CKB)2670000000616821 035 $a(EBL)2038559 035 $a(OCoLC)906172180 035 $a(SSID)ssj0001482657 035 $a(PQKBManifestationID)12627793 035 $a(PQKBTitleCode)TC0001482657 035 $a(PQKBWorkID)11412884 035 $a(PQKB)10402630 035 $a(PQKBManifestationID)16037043 035 $a(PQKB)22906423 035 $a(MiAaPQ)EBC4035471 035 $a(DLC) 2015013228 035 $a(MiAaPQ)EBC2038559 035 $a(PPN)190654589 035 $a(EXLCZ)992670000000616821 100 $a20151109h20152015 uy 0 101 0 $aeng 135 $aur|n|---||||| 181 $ctxt 182 $cc 183 $acr 200 00$aProcess intensification for sustainable energy conversion /$fedited by Fausto Gallucci and Martin van Sint Annaland 210 1$aChichester, England :$cWiley,$d2015. 210 4$dİ2015 215 $a1 online resource (408 p.) 300 $aDescription based upon print version of record. 311 $a1-118-44938-X 311 $a1-118-44935-5 320 $aIncludes bibliographical references at the end of each chapters and index. 327 $aCover; Title Page; Copyright; Contents; Preface; List of Contributors; Chapter 1 Introduction; References; Chapter 2 Cryogenic CO2 Capture; 2.1 Introduction-CCS and Cryogenic Systems; 2.1.1 Carbon Capture and Storage; 2.1.2 Cryogenic separation; 2.2 Cryogenic Packed Bed Process Concept; 2.2.1 Capture Step; 2.2.2 CO2 Recovery Step; 2.2.3 H2O Recovery and Cooling Step; 2.3 Detailed Numerical Model; 2.3.1 Model Description; 2.3.2 Simulation Results; 2.3.3 Simplified Model: Sharp Front Approach; 2.3.4 Model Description; 2.3.5 Process Analysis; 2.3.6 Initial Bed Temperature 327 $a2.3.7 CO2 Inlet Concentration2.3.8 Inlet Temperature; 2.3.9 Bed Properties; 2.4 Small-Scale Demonstration (Proof of Principle); 2.4.1 Results of the Proof of Principle; 2.5 Experimental Demonstration of the Novel Process Concept in a Pilot-Scale Set-Up; 2.5.1 Experimental Procedure; 2.5.2 Experimental Results; 2.5.3 Simulations for the Proof of Concept; 2.5.4 Radial Temperature Profiles; 2.5.5 Influence of the Wall; 2.6 Techno-Economic Evaluation; 2.6.1 Process Evaluation; 2.6.2 Parametric Study; 2.6.3 Comparison with Absorption and Membrane Technology; 2.7 Conclusions 327 $a2.8 Note for the ReaderList of symbols; Greek letters; Subscripts; References; Chapter 3 Novel Pre-Combustion Power Production: Membrane Reactors; 3.1 Introduction; 3.2 The Membrane Reactor Concept; 3.3 Types of Reactors; 3.3.1 Packed Bed Membrane Reactors; 3.3.2 Fluidized Bed Membrane Reactors; 3.3.3 Membrane Micro-Reactors; 3.4 Conclusions; 3.5 Note for the reader; References; Chapter 4 Oxy Fuel Combustion Power Production Using High Temperature O2 Membranes; 4.1 Introduction; 4.2 MIEC Perovskites as Oxygen Separation Membrane Materials for the Oxy-fuel Combustion Power Production 327 $a4.3 MIEC Membrane Fabrication4.4 High-temperature ceramic oxygen separation membrane system on laboratory scale; 4.4.1 Oxygen permeation measurements and sealing dense MIEC ceramic membranes; 4.4.2 BaxSr1-xCo1-xFeyO3-? and LaxSr1-xCo1-yFeyO3-? Membranes; 4.4.3 Chemical Stability of Perovskite Membranes Under Flue-Gas Conditions; 4.4.4 CO2-Tolerant MIEC Membranes; 4.5 Integration of High-Temperature O2 Transport Membranes into Oxy-Fuel Process: Real World and Economic Feasibility; 4.5.1 Four-End and Three-End Integration Modes; 4.5.2 Pilot-Scale Membrane Systems 327 $a4.5.3 Further Scale-Up of O2 Production SystemsReferences; Chapter 5 Chemical Looping Combustion for Power Production; 5.1 Introduction; 5.2 Oxygen carriers; 5.2.1 Nickel-based OCs; 5.2.2 Iron-based OCs; 5.2.3 Copper-based OCs; 5.2.4 Manganese-based OCs; 5.2.5 Other Oxygen Carriers; 5.2.6 Sulfur Tolerance; 5.3 Reactor Concepts; 5.3.1 Interconnected Fluidized Bed Reactors; 5.3.2 Packed Bed Reactors; 5.3.3 Rotating Reactor; 5.4 The Integration of CLC Reactor in Power Plant; 5.4.1 Natural Gas Power Plant with CLC; 5.4.2 Coal-Based Power Plant with CLC 327 $a5.4.3 Comparison between CLC in packed beds and circulated fluidized beds 330 $aThis book addresses the application of process intensification to sustainable energy production, combining two very topical subject areas. Due to the increasing process of petroleum, sustainable energy production technologies must be developed, for example bioenergy, blue energy, chemical looping combustion, concepts for CO2 capture etc. Process intensification offers significant competitive advantages, because it provides more efficient processes, leading to outstanding cost reduction, increased productivity and more environment-friendly processes. 606 $aChemical processes 606 $aRenewable energy sources 606 $aGreen chemistry 615 0$aChemical processes. 615 0$aRenewable energy sources. 615 0$aGreen chemistry. 676 $a660/.28 702 $aGallucci$b Fausto 702 $aSint Annaland$b Martin van 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910808632903321 996 $aProcess intensification for sustainable energy conversion$93982775 997 $aUNINA