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Reactive distillation [[electronic resource] ] : status and future directions / / Kai Sundmacher and Achim Kienle (eds.)
| Reactive distillation [[electronic resource] ] : status and future directions / / Kai Sundmacher and Achim Kienle (eds.) |
| Pubbl/distr/stampa | Weinheim, : Wiley-VCH, c2003 |
| Descrizione fisica | 1 online resource (309 p.) |
| Disciplina |
660
660.28425 660/.28425 |
| Altri autori (Persone) |
SundmacherKai
KienleAchim |
| Soggetto topico |
Distillation
Distillation apparatus - Design and construction Reactivity (Chemistry) - Industrial applications |
| ISBN |
1-280-55826-1
9786610558261 3-527-60626-2 3-527-60052-3 |
| Formato | Materiale a stampa  |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Nota di contenuto |
Reactive Distillation Status and Future Directions; Contents; Preface; List of Contributors; Part I Industrial Applications; 1 Industrial Applications of Reactive Distillation; 1.1 Introduction; 1.2 Etherification: MTBE, ETBE, and TAME; 1.3 Dimerization, Oligomerization, and Condensation; 1.4 Esterification: Methyl Acetate and Other Esters; 1.5 Hydrolysis of Esters; 1.6 Hydration; 1.7 Hydrogenation/Hydrodesulfurization/Hydrocracking; 1.7.1 Benzene to Cyclohexane; 1.7.2 Selective Hydrogenation of C(4) Stream; 1.7.3 Hydrogenation of Pentadiene; 1.7.4 C(4) Acetylene Conversion
1.7.5 Hydrodesulfurization, Hydrodenitrogenation, and Hydrocracking1.7.6 Miscellaneous Hydrogenations; 1.8 Chlorination; 1.9 Acetalization/Ketalization; 1.10 Recovery and Purification of Chemicals; 1.11 Difficult Separations; 1.12 Chemical Heat Pumps; 1.13 RD with Supercritical Fluids; 1.14 Conclusions; 2 Reactive Distillation Process Development in the Chemical Process Industries; 2.1 Introduction; 2.2 Process Synthesis; 2.3 Process Design and Optimization; 2.4 Limitations of the Methods for Synthesis and Design: the Scale-Up Problem; 2.5 Choice of Equipment 2.6 Some Remarks on the Role of Catalysis2.7 Conclusions; 2.8 Acknowledgments; 2.9 Notation; 3 Application of Reactive Distillation and Strategies in Process Design; 3.1 Introduction; 3.2 Challenges in Process Design for Reactive Distillation; 3.2.1 Feasibility Analysis; 3.2.2 Catalyst and Hardware Selection; 3.2.3 Column Scale-Up; 3.3 MTBE Decomposition via Reactive Distillation; 3.3.1 Conceptual Design; 3.3.2 Model Development; 3.3.2.1 Catalyst Selection and Reaction Kinetics; 3.3.2.2 Phase Equilibrium Model; 3.3.2.3 Steady-State Simulation; 3.3.3 Lab-Scale Experiments 3.3.4 Pilot-Plant Experiments3.4 Conclusions; Part II Physicochemical Fundamentals; 4 Thermodynamics of Reactive Separations; 4.1 Introduction; 4.2 Process Models for Reactive Distillation; 4.2.1 Outline; 4.2.2 Case Study: Methyl Acetate; 4.3 Equilibrium Thermodynamics of Reacting Multiphase Mixtures; 4.4 Fluid Property Models for Reactive Distillation; 4.4.1 Outline; 4.4.2 Examples; 4.4.2.1 Hexyl Acetate: Sensitivity Analysis; 4.4.2.2 Methyl Acetate: Prediction of Polynary Vapor-Liquid Equilibria; 4.4.2.3 Butyl Acetate: Thermodynamic Consistency 4.4.2.4 Ethyl Acetate: Consequences of Inconsistency4.4.2.5 Formaldehyde + Water + Methanol: Intrinsically Reactive Complex Mixture; 4.5 Experimental Studies of Phase Equilibria in Reacting Systems; 4.5.1 Outline; 4.5.2 Reactive Vapor-Liquid Equilibria; 4.5.2.1 Batch Experiments; 4.5.2.2 Flow Experiments; 4.5.2.3 Recirculation Experiments; 4.6 Conclusions; 4.7 Acknowledgments; 4.8 Notation; 5 Importance of Reaction Kinetics for Catalytic Distillation Processes; 5.1 Introduction; 5.2 Reactive Ideal Binary Mixtures; 5.2.1 Reaction-Distillation Process with External Recycling 5.2.1.1 (,)-Analysis |
| Record Nr. | UNINA-9910830995803321 |
| Weinheim, : Wiley-VCH, c2003 | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. Federico II | ||
| ||
Reactive distillation design and control [[electronic resource] /] / William L. Luyben, Cheng-Ching Yu
| Reactive distillation design and control [[electronic resource] /] / William L. Luyben, Cheng-Ching Yu |
| Autore | Luyben William L |
| Pubbl/distr/stampa | Hoboken, NJ, : John Wiley, c2008 |
| Descrizione fisica | 1 online resource (598 p.) |
| Disciplina |
660
660.28425 660/.28425 |
| Altri autori (Persone) | YuCheng-Ching <1956-> |
| Soggetto topico |
Distillation apparatus - Design and construction
Chemical process control Distillation Reactivity (Chemistry) |
| ISBN |
1-282-11265-1
9786612112652 0-470-37774-7 0-470-37779-8 |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Nota di contenuto |
REACTIVE DISTILLATION DESIGN AND CONTROL; CONTENTS; PREFACE; 1 INTRODUCTION; 1.1 History; 1.2 Basics of Reactive Distillation; 1.3 Neat Operation Versus Excess Reactant; 1.4 Limitations; 1.4.1 Temperature Mismatch; 1.4.2 Unfavorable Volatilities; 1.4.3 Slow Reaction Rates; 1.4.4 Other Restrictions; 1.5 Scope; 1.6 Computational Methods; 1.6.1 Matlab Programs for Steady-State Design; 1.6.2 Aspen Simulations; 1.7 Reference Materials; PART I STEADY-STATE DESIGN OF IDEAL QUATERNARY SYSTEM; 2 PARAMETER EFFECTS; 2.1 Effect of Holdup on Reactive Trays; 2.2 Effect of Number of Reactive Trays
2.3 Effect of Pressure2.4 Effect of Chemical Equilibrium Constant; 2.5 Effect of Relative Volatilities; 2.5.1 Constant Relative Volatilities; 2.5.2 Temperature-Dependent Relative Volatilities; 2.6 Effect of Number of Stripping and Rectifying Trays; 2.7 Effect of Reactant Feed Location; 2.7.1 Reactant A Feed Location (N(FA)); 2.7.2 Reactant B Feed Location (N(FB)); 2.8 Conclusion; 3 ECONOMIC COMPARISON OF REACTIVE DISTILLATION WITH A CONVENTIONAL PROCESS; 3.1 Conventional Multiunit Process; 3.1.1 Assumptions and Specifications; 3.1.2 Steady-State Design Procedure 3.1.3 Sizing and Economic Equations3.2 Reactive Distillation Design; 3.2.1 Assumptions and Specifications; 3.2.2 Steady-State Design Procedure; 3.3 Results for Different Chemical Equilibrium Constants; 3.3.1 Conventional Process; 3.3.2 Reactive Distillation Process; 3.3.3 Comparisons; 3.4 Results for Temperature-Dependent Relative Volatilities; 3.4.1 Relative Volatilities; 3.4.2 Optimum Steady-State Designs; 3.4.3 Real Chemical Systems; 3.5 Conclusion; 4 NEAT OPERATION VERSUS USING EXCESS REACTANT; 4.1 Introduction; 4.2 Neat Reactive Column; 4.3 Two-Column System with Excess B 4.3.1 20% Excess B Case4.3.2 10% Excess B Case; 4.4 Two-Column System with 20% Excess of A; 4.5 Economic Comparison; 4.6 Conclusion; PART II STEADY-STATE DESIGN OF OTHER IDEAL SYSTEMS; 5 TERNARY REACTIVE DISTILLATION SYSTEMS; 5.1 Ternary System Without Inerts; 5.1.1 Column Configuration; 5.1.2 Chemistry and Phase Equilibrium Parameters; 5.1.3 Design Parameters and Procedure; 5.1.4 Effect of Pressure; 5.1.5 Holdup on Reactive Trays; 5.1.6 Number of Reactive Trays; 5.1.7 Number of Stripping Trays; 5.2 Ternary System With Inerts; 5.2.1 Column Configuration 5.2.2 Chemistry and Phase Equilibrium Parameters5.2.3 Design Parameters and Procedure; 5.2.4 Effect of Pressure; 5.2.5 Control Tray Composition; 5.2.6 Reactive Tray Holdup; 5.2.7 Effect of Reflux; 5.2.8 Chemical Equilibrium Constant; 5.2.9 Feed Composition; 5.2.10 Number of Reactive Trays; 5.2.11 Number of Rectifying and Stripping Trays; 5.3 Conclusion; 6 TERNARY DECOMPOSITION REACTION; 6.1 Ternary Decomposition Reaction: Intermediate-Boiling Reactant; 6.1.1 Column Configuration; 6.1.2 Chemistry and Phase Equilibrium Parameters; 6.1.3 Design Parameters and Procedure 6.1.4 Holdup on Reactive Trays |
| Record Nr. | UNINA-9910145955003321 |
Luyben William L
|
||
| Hoboken, NJ, : John Wiley, c2008 | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. Federico II | ||
| ||
Reactive distillation design and control [[electronic resource] /] / William L. Luyben, Cheng-Ching Yu
| Reactive distillation design and control [[electronic resource] /] / William L. Luyben, Cheng-Ching Yu |
| Autore | Luyben William L |
| Pubbl/distr/stampa | Hoboken, NJ, : John Wiley, c2008 |
| Descrizione fisica | 1 online resource (598 p.) |
| Disciplina |
660
660.28425 660/.28425 |
| Altri autori (Persone) | YuCheng-Ching <1956-> |
| Soggetto topico |
Distillation apparatus - Design and construction
Chemical process control Distillation Reactivity (Chemistry) |
| ISBN |
1-282-11265-1
9786612112652 0-470-37774-7 0-470-37779-8 |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Nota di contenuto |
REACTIVE DISTILLATION DESIGN AND CONTROL; CONTENTS; PREFACE; 1 INTRODUCTION; 1.1 History; 1.2 Basics of Reactive Distillation; 1.3 Neat Operation Versus Excess Reactant; 1.4 Limitations; 1.4.1 Temperature Mismatch; 1.4.2 Unfavorable Volatilities; 1.4.3 Slow Reaction Rates; 1.4.4 Other Restrictions; 1.5 Scope; 1.6 Computational Methods; 1.6.1 Matlab Programs for Steady-State Design; 1.6.2 Aspen Simulations; 1.7 Reference Materials; PART I STEADY-STATE DESIGN OF IDEAL QUATERNARY SYSTEM; 2 PARAMETER EFFECTS; 2.1 Effect of Holdup on Reactive Trays; 2.2 Effect of Number of Reactive Trays
2.3 Effect of Pressure2.4 Effect of Chemical Equilibrium Constant; 2.5 Effect of Relative Volatilities; 2.5.1 Constant Relative Volatilities; 2.5.2 Temperature-Dependent Relative Volatilities; 2.6 Effect of Number of Stripping and Rectifying Trays; 2.7 Effect of Reactant Feed Location; 2.7.1 Reactant A Feed Location (N(FA)); 2.7.2 Reactant B Feed Location (N(FB)); 2.8 Conclusion; 3 ECONOMIC COMPARISON OF REACTIVE DISTILLATION WITH A CONVENTIONAL PROCESS; 3.1 Conventional Multiunit Process; 3.1.1 Assumptions and Specifications; 3.1.2 Steady-State Design Procedure 3.1.3 Sizing and Economic Equations3.2 Reactive Distillation Design; 3.2.1 Assumptions and Specifications; 3.2.2 Steady-State Design Procedure; 3.3 Results for Different Chemical Equilibrium Constants; 3.3.1 Conventional Process; 3.3.2 Reactive Distillation Process; 3.3.3 Comparisons; 3.4 Results for Temperature-Dependent Relative Volatilities; 3.4.1 Relative Volatilities; 3.4.2 Optimum Steady-State Designs; 3.4.3 Real Chemical Systems; 3.5 Conclusion; 4 NEAT OPERATION VERSUS USING EXCESS REACTANT; 4.1 Introduction; 4.2 Neat Reactive Column; 4.3 Two-Column System with Excess B 4.3.1 20% Excess B Case4.3.2 10% Excess B Case; 4.4 Two-Column System with 20% Excess of A; 4.5 Economic Comparison; 4.6 Conclusion; PART II STEADY-STATE DESIGN OF OTHER IDEAL SYSTEMS; 5 TERNARY REACTIVE DISTILLATION SYSTEMS; 5.1 Ternary System Without Inerts; 5.1.1 Column Configuration; 5.1.2 Chemistry and Phase Equilibrium Parameters; 5.1.3 Design Parameters and Procedure; 5.1.4 Effect of Pressure; 5.1.5 Holdup on Reactive Trays; 5.1.6 Number of Reactive Trays; 5.1.7 Number of Stripping Trays; 5.2 Ternary System With Inerts; 5.2.1 Column Configuration 5.2.2 Chemistry and Phase Equilibrium Parameters5.2.3 Design Parameters and Procedure; 5.2.4 Effect of Pressure; 5.2.5 Control Tray Composition; 5.2.6 Reactive Tray Holdup; 5.2.7 Effect of Reflux; 5.2.8 Chemical Equilibrium Constant; 5.2.9 Feed Composition; 5.2.10 Number of Reactive Trays; 5.2.11 Number of Rectifying and Stripping Trays; 5.3 Conclusion; 6 TERNARY DECOMPOSITION REACTION; 6.1 Ternary Decomposition Reaction: Intermediate-Boiling Reactant; 6.1.1 Column Configuration; 6.1.2 Chemistry and Phase Equilibrium Parameters; 6.1.3 Design Parameters and Procedure 6.1.4 Holdup on Reactive Trays |
| Record Nr. | UNINA-9910830370703321 |
|
Luyben William L
|
||
| Hoboken, NJ, : John Wiley, c2008 | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. Federico II | ||
| ||
A real-time approach to distillation process control / / Brent R. Young, Michael A. Taube, Isuru A. Udugama
| A real-time approach to distillation process control / / Brent R. Young, Michael A. Taube, Isuru A. Udugama |
| Autore | Young Brent R. |
| Pubbl/distr/stampa | Hoboken, New Jersey : , : Wiley, , [2023] |
| Descrizione fisica | 1 online resource (258 pages) |
| Disciplina | 663.506 |
| Soggetto topico |
Distillation
Chemical process control |
| ISBN |
1-394-18594-4
1-119-66924-3 |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Nota di contenuto |
Cover -- Title Page -- Copyright Page -- Contents -- Preface -- About the Companion Website -- Chapter 1 Introduction -- 1.1 The Purpose of Process Control -- 1.2 Introduction to Distillation -- 1.3 Distillation Process Control -- 1.4 A Real-Time Approach to Distillation Process Control Education -- Tutorial and Self Study Questions -- References -- Chapter 2 Fundamentals of Distillation Control -- 2.1 Mass and Energy Balance: The Only Means to Affect Distillation Tower's Behavior -- 2.2 Control Design Procedure -- 2.3 Degrees of Freedom -- 2.4 Pairing -- 2.5 Gain Analysis -- 2.6 Common Control Configuration -- 2.7 Screening Control Strategies via Steady-State Simulation -- Tutorial and Self-Study Questions -- References -- Chapter 3 Control Hardware -- 3.1 Introduction -- 3.2 Control Hardware Overview -- 3.3 Sensors -- 3.3.1 Process Considerations -- 3.3.2 Flow Measurement Devices -- 3.3.3 Pressure Measurement Devices -- 3.3.4 Level Measurement Devices -- 3.3.5 Temperature Measurement Devices -- 3.3.6 Direct Composition Measurements -- 3.3.7 Maintenance -- 3.4 Final Control Elements -- 3.4.1 Linearity -- 3.4.2 Time Constant and Failure Mode -- 3.4.3 Mechanical Design Considerations -- 3.5 Controllers/CPU -- 3.5.1 Level 0 -- 3.5.2 Level 1 -- 3.5.3 Levels 2 and 3 -- 3.5.4 General Set Up and Considerations -- 3.6 Modern Trends -- 3.6.1 Wireless Communication and Smart Devices -- 3.6.2 Smart CPUs -- 3.6.3 Digital Twins -- Tutorial and Self-Study Questions -- References -- Chapter 4 Inventory Control -- 4.1 Pressure Control -- 4.1.1 Total Condenser -- 4.1.2 Flooded Condensers -- 4.1.3 Sub-Cooled Reflux -- 4.1.4 Partial Condenser -- 4.2 Level Control -- 4.2.1 Surge Capacity Control -- 4.2.2 Open-Loop Stable versus Integrating Processes -- 4.2.3 Calculating the Process Gain for Vessel Levels.
4.2.4 Relative Gain Analysis, aka Closing the Loop in Plant Design -- Tutorial and Self-Study Questions -- References -- Chapter 5 Distillation Composition Control -- 5.1 Temperature Control -- 5.1.1 Setting Up a Single Temperature-Based Composition Controller -- 5.1.2 When Temperature Is Like an Integrating Process -- 5.1.3 Reboiler Outlet Temperature Controls -- 5.2 Actual Composition Control -- 5.3 More Complex Control Configurations -- 5.3.1 Ryskamp's Scheme -- 5.3.2 Dual Composition Control -- 5.4 Distillation Control Scheme Design Using Steady-State Models -- 5.5 Performance Analysis Using Steady-State Data for an Existing Distillation Tower -- 5.6 Distillation Control Scheme Design Using Dynamic Models -- Tutorial and Self-Study Questions -- References -- Chapter 6 Refinery Versus Chemical Plant Distillation Operations -- 6.1 New Generation of Refinery Controls -- 6.1.1 Atmospheric and Vacuum Refining Columns -- 6.2 Improving Thermodynamic Efficiency Through Control -- 6.3 Blending and Its Implications on Control -- Tutorial and Self-Study Questions -- References -- Chapter 7 Distillation Controller Tuning -- 7.1 Model Identification: Step Testing -- 7.2 Typical Process Responses -- 7.3 Engineering Units Versus Percent-of-Scale -- 7.4 Basics in PID Tuning -- 7.5 Tuning in Distillation Control -- 7.6 The Role of Tuning in a "Value Engineering" Era -- Tutorial and Self-Study Questions -- References -- Chapter 8 Fine and Specialty Chemicals Distillation Control -- 8.1 Key Features -- 8.2 Measurement and Control Challenges -- 8.3 Nuances of Fine Chemicals Distillation -- 8.4 Side-Draw Distillation -- 8.5 Composition Control in High-Purity Side-Draw Distillation -- 8.6 Advanced Distillation Column Configurations -- 8.7 Petlyuk and Divided Wall Columns -- 8.8 Optimal Design Versus Optimal Operations -- 8.9 Conclusions. Tutorial and Self-Study Questions -- References -- Chapter 9 Advanced Regulatory Control -- 9.1 Introduction -- 9.2 Cascade Control -- 9.2.1 Cascade Control in Distillation -- 9.2.2 Inferential Cascade Control -- 9.3 Ratio Control -- 9.3.1 Ratio Control in Distillation -- 9.4 Feedforward Control -- 9.5 Constraint/Override Control -- 9.6 Decoupling -- Tutorial and Self-Study Questions -- References -- Chapter 10 Model Predictive Control -- 10.1 Introduction to MPC -- 10.2 To MPC or not to MPC -- 10.3 MPC Fundamentals -- 10.4 Dynamic Matrix Control -- 10.5 Setting Up a MPC in Distillation -- 10.5.1 Model Setup -- 10.5.2 Objective Function -- 10.5.3 Tuning -- 10.6 Digitalization and MPC -- Tutorial and Self-Study Questions -- References -- Chapter 11 Plant-Wide Control in Distillation -- 11.1 Distillation Column Trains -- 11.1.1 Average Flow Control -- 11.1.2 Alternatives to Average-Level Control -- 11.2 Heat Integration (Energy Recycle) -- 11.2.1 Auxiliary Steam Boilers -- 11.2.2 Feed Preheating -- 11.2.3 High-pressure/Low-pressure Columns -- 11.2.4 Mechanical Vapor Recompression -- 11.3 Materials Recycling -- Tutorial and Self-Study Questions -- References -- Workshop 1 Hands-on Learning By Doing -- Workshop 2 Fundamental Distillation Column Control -- Workshop 3 Distillation Column Model Predictive Control -- Workshop 4 Distillation Column Control in a Plant-Wide Setting -- Appendix A P& -- ID Symbols -- Index -- EULA. |
| Record Nr. | UNINA-9910830783203321 |
|
Young Brent R.
|
||
| Hoboken, New Jersey : , : Wiley, , [2023] | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. Federico II | ||
| ||
Several reasons most humbly offered to the Honourable House of Commons [[electronic resource] ] : for passing the bill for prohibiting the distilling of brandy from malt or corn, in behalf of the poor of this nation, that they may have bread to eat and beer to drink
| Several reasons most humbly offered to the Honourable House of Commons [[electronic resource] ] : for passing the bill for prohibiting the distilling of brandy from malt or corn, in behalf of the poor of this nation, that they may have bread to eat and beer to drink |
| Pubbl/distr/stampa | [London?, : s.n., 1699?] |
| Descrizione fisica | 1 sheet ([1] p.) |
| Soggetto topico |
Alcoholic beverages
Brandy industry - England Distillation |
| Soggetto non controllato | News books |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Record Nr. | UNISA-996409028403316 |
| [London?, : s.n., 1699?] | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. di Salerno | ||
| ||
To the honourable House of Commons, reasons humbly offered by the farmers and malsters of the counties of Middlesex, Surrey, Essex, Kent, Sussex, Suffolk and Norffolk, against the bill for prohibiting the distilling of spirits and low wines from corn [[electronic resource]]
| To the honourable House of Commons, reasons humbly offered by the farmers and malsters of the counties of Middlesex, Surrey, Essex, Kent, Sussex, Suffolk and Norffolk, against the bill for prohibiting the distilling of spirits and low wines from corn [[electronic resource]] |
| Pubbl/distr/stampa | [London, : s.n., 1702?] |
| Descrizione fisica | 1 sheet ([1] p.) |
| Soggetto topico |
Alcoholic beverages - Law and legislation - England
Distillation |
| Soggetto genere / forma | Broadsides |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Record Nr. | UNISA-996391506403316 |
| [London, : s.n., 1702?] | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. di Salerno | ||
| ||
The treasure of Euonymus [[electronic resource] ] : conteyninge the vvonderfull hid secretes of nature, touchinge the most apte formes to prepare and destyl medicines, for the conseruation of helth: as quintesse[n]ce, aurum potabile, hippocras, aromatical wynes, balmes, oyles perfumes, garnishyng waters, and other manifold excellent confections. Wherunto are ioyned the formes of sondry apt fornaces, and vessels, required in this art. Translated (with great diligence, et laboure) out of Latin, by Peter Morvvying felow of Magdaline Colleadge in Oxford
| The treasure of Euonymus [[electronic resource] ] : conteyninge the vvonderfull hid secretes of nature, touchinge the most apte formes to prepare and destyl medicines, for the conseruation of helth: as quintesse[n]ce, aurum potabile, hippocras, aromatical wynes, balmes, oyles perfumes, garnishyng waters, and other manifold excellent confections. Wherunto are ioyned the formes of sondry apt fornaces, and vessels, required in this art. Translated (with great diligence, et laboure) out of Latin, by Peter Morvvying felow of Magdaline Colleadge in Oxford |
| Autore | Gesner Konrad <1516-1565.> |
| Pubbl/distr/stampa | Imprinted at London, : By Iohn Daie, dvvelling ouer Aldersgate, beneath Saint Martines. Cum priuilegio ad imprimendum solum, [1559] |
| Descrizione fisica | [20], 408 p. : ill |
| Altri autori (Persone) | MorwenPeter |
| Soggetto topico |
Medicine
Medicine - Formulae, receipts, prescriptions Distillation |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Record Nr. | UNISA-996390366103316 |
|
Gesner Konrad <1516-1565.>
|
||
| Imprinted at London, : By Iohn Daie, dvvelling ouer Aldersgate, beneath Saint Martines. Cum priuilegio ad imprimendum solum, [1559] | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. di Salerno | ||
| ||
The vertuose boke of distyllacyon of the waters of all maner of herbes [[electronic resource] ] : with the fygures of the styllatoryes, fyrst made and compyled by the thyrte yeres study and labour of the moste co[n]nynge and famous master of phisyke, Maister Iherom bruynswyke. And now newly translate out of Duyche into Englysshe, nat only to the synguler helpe and profyte of the surgyens, phisycyens, and pothecaryes, but also of all maner of people, parfytely and in dewe tyme and ordre to lerne to dystyll all maner of herbes, to the profyte, cure, [and] remedy of all maner dysseases and infirmytees apparant and nat apparant. And ye shall vndersta[n]de that the waters be better than the herbes, as Auicenna testefyeth in his fourth canon saynge that all maner medicynes vsed with theyr substance, febleth and maketh aged, and weke. Cum gratia et priuilegio regali
| The vertuose boke of distyllacyon of the waters of all maner of herbes [[electronic resource] ] : with the fygures of the styllatoryes, fyrst made and compyled by the thyrte yeres study and labour of the moste co[n]nynge and famous master of phisyke, Maister Iherom bruynswyke. And now newly translate out of Duyche into Englysshe, nat only to the synguler helpe and profyte of the surgyens, phisycyens, and pothecaryes, but also of all maner of people, parfytely and in dewe tyme and ordre to lerne to dystyll all maner of herbes, to the profyte, cure, [and] remedy of all maner dysseases and infirmytees apparant and nat apparant. And ye shall vndersta[n]de that the waters be better than the herbes, as Auicenna testefyeth in his fourth canon saynge that all maner medicynes vsed with theyr substance, febleth and maketh aged, and weke. Cum gratia et priuilegio regali |
| Autore | Brunschwig Hieronymus <ca. 1450-ca. 1512.> |
| Pubbl/distr/stampa | [Imprynted at London, : In the flete strete by me Laurens Andrewe, in the sygne of the golden Crosse, In the yere of our lorde. M.ccccc.xxvii. [1527] the xviii daye of Apryll] |
| Descrizione fisica | [276] p. : ill |
| Altri autori (Persone) |
AndrewLaurence |
| Soggetto topico |
Distillation
Medicine - Formulae, receipts, prescriptions |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Record Nr. | UNISA-996390560003316 |
The vertuose boke of distyllacyon of the waters of all maner of herbes [[electronic resource] ] : with the fygures of the styllatoryes, fyrst made and compyled by the thyrte yeres study and labour of the moste co[n]nynge and famous mayster of phisyke, Master Iherom bruynswyke. And now newly translate[d] out of Duyche into Englysshe Nat only to the synguler helpe and profyte of the surgyens, phisycyens, and pothecaryes, but also of all maner of people, parfytely and in dewe tyme and ordre to lerne to dystyll all maner of herbes, to the profyte, cure, and remedy of all maner dysseases and infirmytees apparant and nat apparant. And ye shall vnderstande that the waters be better than the herbes, as Auicenna testefyeth in his fourthe conon saynge that all maner medicynes vsed with theyr substance, febleth and maketh aged, and weke. Cum gratia et preuilegio regali
| The vertuose boke of distyllacyon of the waters of all maner of herbes [[electronic resource] ] : with the fygures of the styllatoryes, fyrst made and compyled by the thyrte yeres study and labour of the moste co[n]nynge and famous mayster of phisyke, Master Iherom bruynswyke. And now newly translate[d] out of Duyche into Englysshe Nat only to the synguler helpe and profyte of the surgyens, phisycyens, and pothecaryes, but also of all maner of people, parfytely and in dewe tyme and ordre to lerne to dystyll all maner of herbes, to the profyte, cure, and remedy of all maner dysseases and infirmytees apparant and nat apparant. And ye shall vnderstande that the waters be better than the herbes, as Auicenna testefyeth in his fourthe conon saynge that all maner medicynes vsed with theyr substance, febleth and maketh aged, and weke. Cum gratia et preuilegio regali |
| Autore | Brunschwig Hieronymus <ca. 1450-ca. 1512.> |
| Pubbl/distr/stampa | [Imprynted at London, : In the flete strete by me Laurens Andrewe, in the sygne of the golden Crosse, In the yere of our lorde. M.ccccc.xxvii. the xviii daye of Apryll. [1527] [i.e. 1528?]] |
| Descrizione fisica | [278] p. : ill |
| Altri autori (Persone) |
AndrewLaurence |
| Soggetto topico |
Distillation
Medicine - Formulae, receipts, prescriptions |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Record Nr. | UNISA-996390528503316 |
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Brunschwig Hieronymus <ca. 1450-ca. 1512.>
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| [Imprynted at London, : In the flete strete by me Laurens Andrewe, in the sygne of the golden Crosse, In the yere of our lorde. M.ccccc.xxvii. the xviii daye of Apryll. [1527] [i.e. 1528?]] | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. di Salerno | ||
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