LEADER 01572nam0 2200325 i 450 001 SUN0010832 005 20110128084526.174 010 $a88-243-1042-7 100 $a20021128d1993 |0itac50 ba 101 $aita 102 $aIT 105 $a|||| ||||| 200 1 $aDall'ente pubblico creditizio alla societą per azioni$ecommento sistematico alla L. 218/90$fa cura di Marilena Rispoli Farina$gcon i contributi di Franco Belli ... [et al.] 205 $aNapoli : Jovene$b1993 210 $aXV$d466 p. ; 24 cm 215 $aSegue: Appendice legislativa. 606 $aBanche di diritto pubblico$xLegislazione$xRiforma$2FI$3SUNC005937 620 $dNapoli$3SUNL000005 676 $a346.45082$v21 702 1$aBelli$b, Franco$3SUNV006460 702 1$aRispoli Farina$b, Marilena$3SUNV008200 712 $aJovene$3SUNV000014$4650 790 1$aFarina Rispoli, Marilena$zRispoli Farina, Marilena$3SUNV091426 801 $aIT$bSOL$c20181224$gRICA 912 $aSUN0010832 950 $aUFFICIO DI BIBLIOTECA DEL DIPARTIMENTO DI ECONOMIA$d03PREST IVCd36 $e03 31556 20140326 950 $aUFFICIO DI BIBLIOTECA DEL DIPARTIMENTO DI ECONOMIA$d03PREST IVCd36bis $e03 31557 20140326 950 $aUFFICIO DI BIBLIOTECA DEL DIPARTIMENTO DI GIURISPRUDENZA$d00CONS VI.Eg.44 $e00 6786 20021129 996 $aDall'ente pubblico creditizio alla societą per azioni$9688523 997 $aUNICAMPANIA LEADER 01361nam 2200349 n 450 001 996391824503316 005 20221108080841.0 035 $a(CKB)1000000000674373 035 $a(EEBO)2240873524 035 $a(UnM)99842511 035 $a(EXLCZ)991000000000674373 100 $a19910513d1546 uy | 101 0 $alat 135 $aurbn||||a|bb| 200 00$aRichardi Sampsonis nuper Cicestrię, nunc vero Lichfeldię Episcopi, in D. Pauli epistolam ad Romanos$b[electronic resource] $eatq[ue] in priorem ad Corinthios breuissima explanatio 210 $a[Londini $cIn ędibus Ioannis Herfordię]$d1546 215 $a[6], ccxxxv [i.e. ccxxix], [1] leaves 300 $aPlace of publication and printer from colophon. 300 $aWith a final colophon leaf. 300 $aNumerous errors in foliation; actual foliation deduced from signature collation. 300 $aSignatures: Aā¶ B-Z a-f gā¶. 300 $aReproduction of the original in the Cambridge University Library. 330 $aeebo-0021 700 $aSampson$b Richard$fd. 1554.$01007566 801 0$bCu-RivES 801 1$bCu-RivES 801 2$bCStRLIN 801 2$bWaOLN 906 $aBOOK 912 $a996391824503316 996 $aRichardi Sampsonis nuper Cicestrię, nunc vero Lichfeldię Episcopi, in D. Pauli epistolam ad Romanos$92412673 997 $aUNISA LEADER 05019nam 2200685 a 450 001 9910814983903321 005 20240516092004.0 010 $a9786613620606 010 $a9781523109869 010 $a1523109866 010 $a9781118259696 010 $a1118259696 010 $a9781118260050 010 $a1118260058 010 $a9781280590771 010 $a1280590777 010 $a9781118259689 010 $a1118259688 035 $a(CKB)2670000000174732 035 $a(StDuBDS)AH21630584 035 $a(SSID)ssj0000634295 035 $a(PQKBManifestationID)11382907 035 $a(PQKBTitleCode)TC0000634295 035 $a(PQKBWorkID)10640604 035 $a(PQKB)11494991 035 $a(MiAaPQ)EBC827145 035 $a(Au-PeEL)EBL827145 035 $a(CaPaEBR)ebr10558104 035 $a(CaONFJC)MIL362060 035 $a(OCoLC)784136711 035 $a(Perlego)1001670 035 $a(EXLCZ)992670000000174732 100 $a20111007d2012 uy 0 101 0 $aeng 135 $aurcn||||||||| 181 $ctxt 182 $cc 183 $acr 200 10$aDistillation control $ean engineering perspective /$fCecil L. Smith 205 $a1st ed. 210 $aHoboken, N.J. $cJohn Wiley & Sons$dc2012 215 $a1 online resource (xi, 332 p. )$cill 300 $aFormerly CIP.$5Uk 311 08$a9780470381946 311 08$a0470381949 320 $aIncludes bibliographical references and index. 327 $aMachine generated contents note: Chapter 1. Principles 1.1 Separation Processes 1.2 Total Material Balance 1.3 Reflux and Boilup Ratios 1.4 Total Material Balance Around Condenser 1.5 Total Material Balance Around Reboiler 1.6 Component Material Balances 1.7 Energy and the Separation Factor 1.8 Multicomponent Distillation 1.9 Stage-by-Stage Separation Model 1.10 Formulation of the Control Problem 1.11 Tower Internals 1.12 Flooding 1.13 Tray Hydraulics 1.14 Inverse Response in Bottoms Level 1.15 Composition Dynamics Chapter 2. Composition Control 2.1 Product Specifications 2.2 Columns in Series 2.3 Composition Analyzers 2.4 Temperature 2.5 Distillate Composition Control, Constant Boilup 2.6 Distillate Composition Control, Constant Bottoms Flow 2.7 Operating Lines 2.8 Temperature Profiles 2.9 Feed Composition Disturbances 2.10 Bottoms Composition Control 2.11 Propagation of Variance in Level Control Configurations 2.12 Level Control in Direct Material Balance Configurations Chapter 3. Pressure Control and Condensers 3.1 Pressure Control 3.2 Once-Through Heat Transfer Processes 3.3 Water-Cooled Condensers 3.4 Flooded Condensers 3.5 Air-Cooled Condensers 3.6 Partial Condensers 3.7 Atmospheric Towers 3.8 Vacuum Towers 3.9 Floating Pressure / Pressure Minimization Chapter 4. Reboilers and Feed Preheaters 4.1 Types of Reboilers 4.2 Steam-Heated Reboilers 4.3 Hot Oil 4.4 Fired Heaters 4.5 Feed Preheater 4.6 Economizer Chapter 5. Applying Feedforward 5.1 Feed Flow and Composition 5.2 Internal Reflux Control 5.3 Extreme Feedforward 5.4 Feedforward for Bottoms Level 5.5 Feedforward for Column Pressure 5.6 Product Compositions Chapter 6. Unit Optimization 6.1 Energy and Separation 6.2 Optimization of a Column 6.3 Constraints in Distillation Columns 6.4 Control Configurations for Single Constraint 6.5 Control Configurations for Multiple Constraints Chapter 7. Double-End Composition Control 7.1 Defining the Problem. 7.2 Options for Composition Control 7.3 Relative Gain 7.4 Relative Gains from Open Loop Sensitivities 7.5 Relative Gains for Other Configurations 7.6 Ratios for Manipulated Variables 7.7 Effect of Operating Objectives 7.8 Model Predictive Control Chapter 8. Complex Towers 8.1 Heat Integration 8.2 Side Heater / Side Cooler 8.3 Sidestreams 8.4 Withdrawing a Liquid Sidestream 8.5 Withdrawing a vapor sidestream 8.6 Composition Control in Sidestream Towers. 330 $a"This book approaches the subject from a process engineering perspective, specifically, to use the steady-state simulation of the column as the primary source of the parameters required to develop, to analyze, and to troubleshoot a column control configuration. For an operating column, the first action must be to confirm that the separation currently provided by the column is consistent with design expectations (using control sophistication to solve process problems is a loser). The objective is to choose the control configuration that properly reflects the column design parameters (number of stages; feed stage location, etc), the materials being separated (relative volatility), the operating requirements for the column (reflux ratios, product purities, etc)"--$cProvided by publisher. 606 $aDistillation 615 0$aDistillation. 676 $a660/.28425 686 $aTEC009010$2bisacsh 700 $aSmith$b Cecil L$0209864 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910814983903321 996 $aDistillation control$94019309 997 $aUNINA