LEADER 06199nam 22007812 450 001 9910786725903321 005 20151005020622.0 010 $a1-107-35736-5 010 $a1-107-23478-6 010 $a1-107-34399-2 010 $a1-107-34885-4 010 $a1-107-34774-2 010 $a0-511-99784-1 010 $a1-107-34524-3 010 $a1-107-34149-3 035 $a(CKB)2670000000353227 035 $a(EBL)1139672 035 $a(SSID)ssj0000871891 035 $a(PQKBManifestationID)11536642 035 $a(PQKBTitleCode)TC0000871891 035 $a(PQKBWorkID)10822528 035 $a(PQKB)11203858 035 $a(UkCbUP)CR9780511997846 035 $a(MiAaPQ)EBC1139672 035 $a(Au-PeEL)EBL1139672 035 $a(CaPaEBR)ebr10695348 035 $a(CaONFJC)MIL494730 035 $a(OCoLC)842929899 035 $a(PPN)261317709 035 $a(EXLCZ)992670000000353227 100 $a20110112d2013|||| uy| 0 101 0 $aeng 135 $aur||||||||||| 181 $ctxt$2rdacontent 182 $cc$2rdamedia 183 $acr$2rdacarrier 200 10$aModelling drying processes $ea reaction engineering approach /$fXiao Dong Chen, Monash University, Australia, Aditya Putranto, Monash University, Australia$b[electronic resource] 210 1$aCambridge :$cCambridge University Press,$d2013. 215 $a1 online resource (xxxvii, 214 pages) $cdigital, PDF file(s) 300 $aTitle from publisher's bibliographic system (viewed on 05 Oct 2015). 311 $a1-107-01210-4 320 $aIncludes bibliographical references and index. 327 $aContents; Figures; Tables; Preface; Historical background; 1 Introduction; 1.1 Practical background; 1.2 A 'microstructural' discussion of the phenomena of drying moist, porous materials; 1.3 The REA to modelling drying; 1.3.1 The relevant classical knowledge of physical chemistry; 1.3.2 General modelling approaches; 1.3.3 Outline of REA; 1.4 Summary; References; 2 Reaction engineering approach I; 2.1 The REA formulation; 2.2 Determination of REA model parameters; 2.3 Coupling the momentum, heat and mass balances; 2.4 Mass or heat transfer limiting; 2.4.1 Biot number analysis 327 $a2.4.2 Lewis number analysis2.4.3 Combination of Biot and Lewis numbers; 2.5 Convective drying of particulates or thin layer products modelled using the L-REA; 2.5.1 Mathematical modelling of convective drying of droplets of whey protein concentrate (WPC) using the L-REA; 2.5.2 Mathematical modelling of convective drying of a mixture of polymer solutions using the L-REA; 2.5.3 Results of modelling convective drying of droplets of WPC using the L-REA; 2.5.4 Results of modelling convective drying of a thin layer of a mixture of polymer solutions using the L-REA 327 $a2.6 Convective drying of thick samples modelled using the L-REA2.6.1 Formulation of the L-REA for convective drying of thick samples; 2.6.2 Prediction of surface sample temperature; 2.6.3 Modelling convective drying thick samples of mango tissues using the L-REA; 2.6.4 Results of convective drying thick samples of mango tissues using the L-REA; 2.7 The intermittent drying of food materials modelled using the L-REA; 2.7.1 Mathematical modelling of intermittent drying of food materials using the L-REA; 2.7.2 The results of modelling of intermittent drying of food materials using the L-REA 327 $a2.7.3 Analysis of surface temperature, surface relative humidity, saturated and surface vapour concentration during intermittent drying2.8 The intermittent drying of non-food materials under time-varying temperature and humidity modelled using the L-REA; 2.8.1 Mathematical modelling using the L-REA; 2.8.2 Results of intermittent drying under time-varying temperature and humidity modelled using the L-REA; 2.9 The heating of wood under linearly increased gas temperature modelled using the L-REA; 2.9.1 Mathematical modelling using the L-REA 327 $a2.9.2 Results of modelling wood heating under linearly increased gas temperatures using the L-REA2.10 The baking of cake modelled using the L-REA; 2.10.1 Mathematical modelling of the baking of cake using the L-REA; 2.10.2 Results of modelling of the baking of cake using the L-REA; 2.11 The infrared-heat drying of a mixture of polymer solutions modelled using the L-REA; 2.11.1 Mathematical modelling of the infrared-heat drying of a mixture of polymer solutions using the L-REA 327 $a2.11.2 The results of mathematical modelling of infrared-heat drying of a mixture of polymer solutions using the L-REA 330 $aThis comprehensive summary of the state of the art and the ideas behind the reaction engineering approach (REA) to drying processes is an ideal resource for researchers, academics and industry practitioners. Starting with the formulation, modelling and applications of the lumped-REA, it goes on to detail the use of the REA to describe local evaporation and condensation, and its coupling with equations of conservation of heat and mass transfer, called the spatial-REA, to model non-equilibrium multiphase drying. Finally, it summarises other established drying models, discussing their features, limitations and comparisons with the REA. Application examples featured throughout help fine-tune the models and implement them for process design and the evaluation of existing drying processes and product quality during drying. Further uses of the principles of REA are demonstrated, including computational fluid dynamics-based modelling, and further expanded to model other simultaneous heat and mass transfer processes. 606 $aDrying 606 $aFood$xDrying 606 $aPorous materials$xDrying 606 $aPolymers$xCuring 606 $aLumber$xDrying 615 0$aDrying. 615 0$aFood$xDrying. 615 0$aPorous materials$xDrying. 615 0$aPolymers$xCuring. 615 0$aLumber$xDrying. 676 $a664/.0284 700 $aChen$b Xiao Dong$01545210 702 $aPutranto$b Aditya 801 0$bUkCbUP 801 1$bUkCbUP 906 $aBOOK 912 $a9910786725903321 996 $aModelling drying processes$93800028 997 $aUNINA