Chemical process design and integration:
"Written by a highly regarded author with industrial and academic experience, this new edition of an established bestselling book provides practical guidance for students, researchers, and those in chemical engineering. The book includes a new section on sustainable energy, with sections on car...
Gespeichert in:
1. Verfasser: | |
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Format: | Buch |
Sprache: | English |
Veröffentlicht: |
Chichester, West Sussex, United Kingdom
Wiley
2016
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Ausgabe: | Second edition |
Schlagworte: | |
Online-Zugang: | Cover image Inhaltsverzeichnis Klappentext |
Zusammenfassung: | "Written by a highly regarded author with industrial and academic experience, this new edition of an established bestselling book provides practical guidance for students, researchers, and those in chemical engineering. The book includes a new section on sustainable energy, with sections on carbon capture and sequestration, as a result of increasing environmental awareness; and a companion website that includes problems, worked solutions, and Excel spreadsheets to enable students to carry out complex calculations".. |
Beschreibung: | Includes index |
Beschreibung: | xxiii, 896 Seiten Illustrationen, Diagramme |
ISBN: | 9781119990147 9781119990130 |
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245 | 1 | 0 | |a Chemical process design and integration |c Robin Smith (School of Chemical Engineering and Analytical Science, The University of Manchester, UK) |
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Datensatz im Suchindex
_version_ | 1804176441946931200 |
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adam_text | Contents
Preface xiii
Acknowledgements xv
Nomenclature xvii
1 The Nature of Chemical Process Design and
Integration 1
1.1 Chemical Products 1
1.2 Formulation of Design Problems 3
1.3 Synthesis and Simulation 4
1.4 The Hierarchy of Chemical Process Design and
Integration 6
1.5 Continuous and Batch Processes 8
1.6 New Design and Retrofit 11
1.7 Reliability, Availability and Maintainability 11
1.8 Process Control 12
1.9 Approaches to Chemical Process Design and
Integration 13
1.10 The Nature of Chemical Process Design and
Integration - Summary 16
References 17
2 Process Economics 19
2.1 The Role of Process Economics 19
2.2 Capital Cost for New Design 19
2.3 Capital Cost for Retrofit 25
2.4 Annualized Capital Cost 26
2.5 Operating Cost 27
2.6 Simple Economic Criteria 30
2.7 Project Cash Flow and Economic Evaluation 31
2.8 Investment Criteria 33
2.9 Process Economics-Summary 34
2.10 Exercises 34
References 36
3 Optimization 37
3.1 Objective Functions 37
3.2 Single-Variable Optimization 40
3.3 Multivariable Optimization 42
3.4 Constrained Optimization 45
3.5 Linear Programming 47
3.6 Nonlinear Programming 49
3.7 Structural Optimization 50
3.8 Solution of Equations Using Optimization 54
3.9 The Search for Global Optimality 55
9
3.10 Optimization - Summary 56
3.11 Exercises 56
References 58
4 Chemical Reactors I - Reactor
Performance 59
4.1 Reaction Path 59
4.2 Types of Reaction Systems 61
4.3 Measures of Reactor Performance 63
4.4 Rate of Reaction 64
4.5 Idealized Reactor Models 65
4.6 Choice of Idealized Reactor Model 73
4.7 Choice of Reactor Performance 76
4.8 Reactor Performance - Summary 77
4.9 Exercises 78
References 79
5 Chemical Reactors II - Reactor Conditions 81
5.1 Reaction Equilibrium 81
5.2 Reactor Temperature 85
5.3 Reactor Pressure 92
5.4 Reactor Phase 93
5.5 Reactor Concentration 94
5.6 Biochemical Reactions 99
5.7 Catalysts 99
5.8 Reactor Conditions - Summary 102
5.9 Exercises 103
References 105
6 Chemical Reactors III - Reactor
Configuration 107
6.1 Temperature Control 107
6.2 Catalyst Degradation 111
6.3 Gas-Liquid and Liquid-Liquid Reactors 112
6.4 Reactor Configuration 116
6.5 Reactor Configuration For Heterogeneous
Solid-Catalyzed Reactions 121
6.6 Reactor Configuration - Summary 122
6.7 Exercises 122
References 123
7 Separation of Heterogeneous Mixtures 125
7.1 Homogeneous and Heterogeneous
Separation 125
7.2 Settling and Sedimentation 126
7.3 Inertial and Centrifugal Separation 130
7.4 Electrostatic Precipitation 131
7.5 Filtration 133
7.6 Scrubbing 134
7.7 Flotation 135
7.8 Drying 136
7.9 Separation of Heterogeneous
Mixtures - Summary 137
7.10 Exercises 137
References 138
8 Separation of Homogeneous Fluid
Mixtures I - Distillation 139
8.1 Vapor-Liquid Equilibrium 139
8.2 Calculation of Vapor-Liquid Equilibrium 141
8.3 Single-Stage Separation 146
8.4 Distillation 146
8.5 Binary Distillation 150
8.6 Total and Minimum Reflux Conditions for
Multicomponent Mixtures 155
8.7 Finite Reflux Conditions for Multicomponent
Mixtures 162
8.8 Column Dimensions 164
8.9 Conceptual Design of Distillation 174
8.10 Detailed Design of Distillation 176
8.11 Limitations of Distillation 179
8.12 Separation of Homogeneous Fluid Mixtures by
Distillation - Summary 180
8.13 Exercises 180
References 183 9 10
9 Separation of Homogeneous Fluid Mixtures H - Other
Methods 185
9.1 Absorption and Stripping 185
9.2 Liquid-Liquid Extraction 189
9.3 Adsorption 196
9.4 Membranes 199
9.5 Crystallization 211
9.6 Evaporation 215
9.7 Separation of Homogeneous Fluid Mixtures by
Other Methods - Summary 217
9.8 Exercises 217
References 219
10 Distillation Sequencing 221
10.1 Distillation Sequencing using Simple
Columns 221
10.2 Practical Constraints Restricting Options 221
10.3 Choice of Sequence for Simple Nonintegrated
Distillation Columns 222
10.4 Distillation Sequencing using Columns With
More Than Two Products 229
10.5 Distillation Sequencing using Thermal
Coupling 231
10.6 Retrofit of Distillation Sequences 236
10.7 Crude Oil Distillation 237
10.8 Structural Optimization of Distillation
Sequences 239
10.9 Distillation Sequencing - Summary 242
10.10 Exercises 242
References 245
11 Distillation Sequencing for Azeotropic
Distillation 247
11.1 Azeotropic Systems 247
11.2 Change in Pressure 247
11.3 Representation of Azeotropic Distillation 248
11.4 Distillation at Total Reflux Conditions 250
11.5 Distillation at Minimum Reflux Conditions 255
11.6 Distillation at Finite Reflux Conditions 256
11.7 Distillation Sequencing Using an Entraîner 259
11.8 Heterogeneous Azeotropic Distillation 264
11.9 Entraîner Selection 267
11.10 Multicomponent Systems 270
11.11 Trade-Offs in Azeotropic Distillation 270
11.12 Membrane Separation 270
11.13 Distillation Sequencing for Azeotropic
Distillation - Summary 271
11.14 Exercises 272
References 273
12 Heat Exchange 275
12.1 Overall Heat Transfer Coefficients 275
12.2 Heat Exchanger Fouling 279
12.3 Temperature Differences in Shell-and-Tube Heat
Exchangers 281
12.4 Heat Exchanger Geometry 288
12.5 Allocation of Fluids in Shell-and-Tube Heat
Exchangers 294
12.6 Heat Transfer Coefficients and Pressure Drops in
Shell-and-Tube Heat Exchangers 294
12.7 Rating and Simulation of Heat Exchangers 301
12.8 Heat Transfer Enhancement 307
12.9 Retrofit of Heat Exchangers 313
12.10 Condensers 316
12.11 Reboilers and Vaporizers 321
12.12 Other Types of Heat Exchangers 326
12.13 Fired Heaters 328
12.14 Heat Exchange - Summary 345
12.15 Exercises 346
References 348
13 Pumping and Compression 349
13.1 Pressure Drops in Process Operations 349
13.2 Pressure Drops in Piping Systems 349
13.3 Pump Types 355
13.4 Centrifugal Pump Performance 356
13.5 Compressor Types 363
13.6 Reciprocating Compressors 366
13.7 Dynamic Compressors 367
13.8 Staged Compression 369
13.9 Compressor Performance 370
13.10 Process Expanders 372
13.11 Pumping and Compression -
Summary 374
13.12 Exercises 374
References 375
14 Continuous Process Recycle Structure 377
14.1 The Function of Process Recycles 377
14.2 Recycles with Purges 382
14.3 Hybrid Reaction and Separation 385
14.4 The Process Yield 386
14.5 Feed, Product and Intermediate Storage 388
14.6 Continuous Process Recycle
Structure - Summary 389
14.7 Exercises 389
References 391
15 Continuous Process Simulation and
Optimization 393
15.1 Physical Property Models for Process
Simulation 393
15.2 Unit Models for Process Simulation 394
15.3 Flowsheet Models 400
15.4 Simulation of Recycles 400
15.5 Convergence of Recycles 402
15.6 Design Specifications 408
15.7 Flowsheet Sequencing 408
15.8 Model Validation 408
15.9 Process Optimization 408
15.10 Continuous Process Simulation and
Optimization - Summary 413
15.11 Exercises 413
References 416
16 Batch Processes 417
16.1 Characteristics of B atch Processes 417
16.2 Batch Reactors 417
16.3 Batch Distillation 420
16.4 Batch Crystallization 431
16.5 Batch Filtration 432
16.6 Batch Heating and Cooling 433
16.7 Optimization of Batch Operations 436
16.8 Gantt Charts 442
16.9 Production Schedules for Single Products 442
16.10 Production Schedules for Multiple Products 444
16.11 Equipment Cleaning and Material Transfer 445
16.12 Synthesis of Reaction and Separation Systems for
Batch Processes 446
16.13 Storage in Batch Processes 452
16.14 Batch Processes - Summary 452
16.15 Exercises 452
References 455
17 Heat Exchanger Networks I - Network
Targets 457
17.1 Composite Curves 457
17.2 The Heat Recovery Pinch 461
17.3 Threshold Problems 464
17.4 The Problem Table Algorithm 466
17.5 Non-global Minimum Temperature
Differences 472
17.6 Process Constraints 473
17.7 Utility Selection 475
17.8 Furnaces 477
17.9 Cogeneration (Combined Heat and Power
Generation) 480
17.10 Integration of Heat Pumps 485
17.11 Number of Heat Exchange Units 486
17.12 Heat Exchange Area Targets 489
17.13 Sensitivity of Targets 493
17.14 Capital and Total Cost Targets 493
17.15 Heat Exchanger Network Targets -
Summary 496
17.16 Exercises 496
References 499
18 Heat Exchanger Networks II - Network
Design 501
18.1 The Pinch Design Method 501
18.2 Design for Threshold Problems 507
18.3 Stream Splitting 507
18.4 Design for Multiple Pinches 511
18.5 Remaining Problem Analysis 516
18.6 Simulation of Heat Exchanger Networks 518
18.7 Optimization of a Fixed Network Structure 520
18.8 Automated Methods of Heat Exchanger Network
Design 523
18.9 Heat Exchanger Network Retrofit with a Fixed
Network Structure 525
18.10 Heat Exchanger Network Retrofit through
Structural Changes 530
18.11 Automated Methods of Heat Exchanger Network
Retrofit 536
18.12 Heat Exchanger Network Design -
Summary 538
18.13 Exercises 539
References 542
19 Heat Exchanger Networks III - Stream
Data 543
19.1 Process Changes for Heat Integration 543
19.2 The Trade-Offs Between Process Changes, Utility
Selection, Energy Cost and Capital Cost 543
19.3 Data Extraction 544
19.4 Heat Exchanger Network Stream
Data - Summary 551
19.5 Exercises 551
References 553
20 Heat Integration of Reactors 555
20.1 The Heat Integration Characteristics of
Reactors 555
20.2 Appropriate Placement of Reactors 557
20.3 Use of the Grand Composite Curve for Heat
Integration of Reactors 558
20.4 Evolving Reactor Design to Improve Heat
Integration 560
20.5 Heat Integration of Reactors - Summary 561
20.6 Exercises 561
Reference 561
21 Heat Integration of Distillation 563
21.1 The Heat Integration Characteristics of
Distillation 563
21.2 The Appropriate Placement of Distillation 563
21.3 Use of the Grand Composite Curve for Heat
Integration of Distillation 564
21.4 Evolving the Design of Simple Distillation
Columns to Improve Heat Integration 564
21.5 Heat Pumping in Distillation 567
21.6 Capital Cost Considerations for the Integration of
Distillation 567
21.7 Heat Integration Characteristics of Distillation
Sequences 568
21.8 Design of Heat Integrated Distillation
Sequences 571
21.9 Heat Integration of Distillation - Summary 572
21.10 Exercises 572
References 575
22 Heat Integration of Evaporators and
Dryers 577
22.1 The Heat Integration Characteristics of
Evaporators 577
22.2 Appropriate Placement of Evaporators 577
22.3 Evolving Evaporator Design to Improve Heat
Integration 577
22.4 The Heat Integration Characteristics of Dryers 579
22.5 Evolving Dryer Design to Improve Heat
Integration 579
22.6 A Case Study 581
22.7 Heat Integration of Evaporators and
Dryers - Summary 581
22.8 Exercises 582
References 582 23
23 Steam Systems and Cogeneration 583
23.1 Boiler Feedwater Treatment 585
23.2 Steam Boilers 589
23.3 Gas Turbines 595
23.4 Steam Turbines 602
23.5 Steam Distrubution 609
23.6 Site Composite Curves 612
23.7 Cogeneration Targets 623
23.8 Power Generation and Machine Drives 627
23.9 Utility Simulation 631
23.10 Optimizing Steam Systems 633
23.11 Steam Costs 638
23.12 Steam Systems and Cogeneration - Summary 641
23.13 Exercises 642
References 645
24 Cooling and Refrigeration Systems 647
24.1 Cooling Systems 647
24.2 Once-Through Water Cooling 647
24.3 Recirculating Cooling Water Systems 647
24.4 Air Coolers 650
24.5 Refrigeration 656
24.6 Choice of a Single-Component Refrigerant for
Compression Refrigeration 662
24.7 Targeting Refrigeration Power for Pure
Component Compression Refrigeration 665
24.8 Heat Integration of Pure Component Compression
Refrigeration Processes 669
24.9 Mixed Refrigerants for Compression
Refrigeration 673
24.10 Expanders 677
24.11 Absorption Refrigeration 681
24.12 Indirect Refrigeration 682
24.13 Cooling Water and Refrigeration
Systems - Summary 682
24.14 Exercises 683
References 685
25 Environmental Design for Atmospheric
Emissions 687
25.1 Atmospheric Pollution 687
25.2 Sources of Atmospheric Pollution 688
25.3 Control of Solid Particulate Emissions to
Atmosphere 690
25.4 Control of VOC Emissions 690
25.5 Control of Sulfur Emissions 703
25.6 Control of Oxides of Nitrogen Emissions 708
25.7 Control of Combustion Emissions 711
25.8 Atmospheric Dispersion 714
25.9 Environmental Design for Atmospheric
Emissions - Summary 716
25.10 Exercises 717
References 720
26 Water System Design 721
26.1 Aqueous Contamination 724
26.2 Primary Treatment Processes 725
26.3 Biological Treatment Processes 729
26.4 Tertiary Treatment Processes 732
26.5 Water Use 733
26.6 Targeting for Maximum Water Reuse for Single
Contaminants for Operations with Fixed Mass
Loads 735
26.7
26.8
26.9
26.10
26.11
26.12
26.13
26.14
26.15
26.16
26.17
26.18
27
27.1
27.2
27.3
27.4
27.5
27.6
27.7
27.8
27.9
27.10
28
28.1
28.2
28.3
28.4
28.5
28.6
28.7
28.8
28.9
28.10
Design for Maximum Water Reuse for Single
Contaminants for Operations with Fixed Mass
Loads 737
Targeting for Maximum Water Reuse for Single
Contaminants for Operations with Fixed
Flowrates 747
Design for Maximum Water Reuse for Single
Contaminants for Operations with Fixed
Flowrates 751
Targeting and Design for Maximum Water
Reuse Based on Optimization of a
Superstructure 758
Process Changes for Reduced Water
Consumption 760
Targeting for Minimum Wastewater Treatment
Flowrate for Single Contaminants 761
Design for Minimum Wastewater Treatment
Flowrate for Single Contaminants 765
Regeneration of Wastewater 767
Targeting and Design for Effluent Treatment and
Regeneration Based on Optimization of a
Superstructure 772
Data Extraction 773
Water System Design - Summary 775
Exercises 776
References 779
Environmental Sustainability in Chemical
Production 781
Life Cycle Assessment 781
Efficient Use of Raw Materials Within
Processes 786
Efficient Use of Raw Materials Between
Processes 792
Exploitation of Renewable Raw Materials 794
Efficient Use of Energy 795
Integration of Waste Treament and Energy
Sytems 805
Renewable Energy 806
Efficient Use of Water 807
Sustainability in Chemical
Production - Summary 807
Exercises 808
References 809
28.11 Exercises 824
References 825
Appendix A Physical Properties in Process Design 827
A.1 Equations of State 827
A.2 Phase Equilibrium for Single Components 831
A.3 Fugacity and Phase Equilibrium 831
A.4 Vapor-Liquid Equilibrium 831
A.5 Vapor-Liquid Equilibrium Based on Activity
Coefficient Models 833
A.6 Group Contribution Methods for Vapor-Liquid
Equilibrium 835
A.7 Vapor-Liquid Equilibrium Based on
Equations of State 837
A.8 Calculation of Vapor-Liquid Equilibrium 838
A.9 Liquid-Liquid Equilibrium 841
A.10 Liquid-Liquid Equilibrium Activity
Coefficient Models 842
A.11 Calculation of Liquid-Liquid Equilibrium 842
A.12 Choice of Method for Equilibrium
Calculations 844
A.13 Calculation of Enthalpy 846
A.14 Calculation of Entropy 847
A.15 Other Physical Properties 848
A.16 Physical Properties in Process
Design - Summary 850
A.17 Exercises 851
References 852
Appendix B Materials of Construction 853
B.1 Mechanical Properties 853
B.2 Corrosion 854
B.3 Corrosion Allowance 855
B.4 Commonly Used Materials of Construction 855
B.5 Criteria for Selection 859
B.6 Materials of Construction - Summary 860
References 860
Appendix C Annualization of Capital Cost 861
Reference 861
Appendix D The Maximum Thermal Effectiveness for 1-2
Shell-and-Tube Heat Exchangers 863
Process Safety 811
References 863
Fire 811
Explosion 812
Toxic Release 813
Hazard Identification 813
The Hierarchy of Safety Management 815
Inherently Safer Design 815
Layers of Protection 819
Hazard and Operability Studies 822
Layer of Protection Analysis 823
Process Safety - Summary 823
Appendix E Expression for the Minimum Number of 1-2
Shell-and-Tube Heat Exchangers for a Given
Unit 865
References 866
Appendix F Heat Transfer Coefficient and Pressure Drop in
Shell-and-Tube Heat Exchangers 867
F. 1 Heat Transfer and Pressure Drop Correlations for
the Tube Side 867
G.3 Staged Compression 877
References 879
F.2 Heat Transfer and Pressure Drop Correlations for
the Shell Side 869
References 873
Appendix H Algorithm for the Heat Exchanger Network
Area Target 881
Appendix G Gas Compression Theory 875
G.1 Modeling Reciprocating Compressors 875
G.2 Modeling Dynamic Compressors 877
Index 883
ROBIN SMITH
School of Chemical Engineering and Analytical Science, The University of Manchester, UK
NEWTOTHE SECOND EDITION: | : I
Restructured, revised and updated throughout
Extensive new material on equipment design
More extensive treatment of process simulation and batch processing
Updated treatment of process integration topics
Increased emphasis on environmental sustainability and safety
This book provides a practical guide to chemical process design and integration for students of chemical
engineering at all levels, practicing process designers and chemical engineers and applied chemists working
in process development.
The Second Edition has been restructured, revised and updated throughout, to make it more accessible to
undergraduate students, as well as maintaining its usefulness to postgraduate students and to practicing
chemical engineers. At the heart of the book are the conceptual issues that are fundamental to the creation
of chemical processes and their integration to form complete manufacturing systems. This edition includes
much greater consideration of equipment and equipment design, without losing any understanding of the
overall conceptual design. Increasing environmental awareness has also dictated the need for a greater
emphasis on environmental sustainability throughout. The main implications of this for process design are
greater efficiency in the use of raw materials, energy and water, and an increased emphasis on process safety.
Consideration of integration is not restricted to individual processes, but instead there is emphasis on
integration across processes, in order to create environmentally sustainable integrated manufacturing
systems. Thus, the text successfully integrates equipment, process and manufacturing system design.
Praise for the first edition
...deserves a place on the library shelves of all universities, departments and companies,
and of any practicing engineer...
~ Institution of Chemical Engineers
...a need for a textbook that gives an overview of broad strategy...Robin Smith s new book
fulfils these aims admirably...
~ Chemical Engineering Research Design
ISBN 978-1-119-99013-0
|
any_adam_object | 1 |
author | Smith, Robin |
author_GND | (DE-588)1117927091 |
author_facet | Smith, Robin |
author_role | aut |
author_sort | Smith, Robin |
author_variant | r s rs |
building | Verbundindex |
bvnumber | BV043677211 |
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ctrlnum | (OCoLC)944238188 (DE-599)BVBBV043677211 |
dewey-full | 660/.28 |
dewey-hundreds | 600 - Technology (Applied sciences) |
dewey-ones | 660 - Chemical engineering |
dewey-raw | 660/.28 |
dewey-search | 660/.28 |
dewey-sort | 3660 228 |
dewey-tens | 660 - Chemical engineering |
discipline | Chemie / Pharmazie |
edition | Second edition |
format | Book |
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genre | (DE-588)4123623-3 Lehrbuch gnd-content |
genre_facet | Lehrbuch |
id | DE-604.BV043677211 |
illustrated | Illustrated |
indexdate | 2024-07-10T07:32:14Z |
institution | BVB |
isbn | 9781119990147 9781119990130 |
language | English |
lccn | 015032671 |
oai_aleph_id | oai:aleph.bib-bvb.de:BVB01-029090199 |
oclc_num | 944238188 |
open_access_boolean | |
owner | DE-703 DE-92 DE-1050 DE-83 |
owner_facet | DE-703 DE-92 DE-1050 DE-83 |
physical | xxiii, 896 Seiten Illustrationen, Diagramme |
publishDate | 2016 |
publishDateSearch | 2016 |
publishDateSort | 2016 |
publisher | Wiley |
record_format | marc |
spelling | Smith, Robin Verfasser (DE-588)1117927091 aut Chemical process design and integration Robin Smith (School of Chemical Engineering and Analytical Science, The University of Manchester, UK) Second edition Chichester, West Sussex, United Kingdom Wiley 2016 xxiii, 896 Seiten Illustrationen, Diagramme txt rdacontent n rdamedia nc rdacarrier Includes index "Written by a highly regarded author with industrial and academic experience, this new edition of an established bestselling book provides practical guidance for students, researchers, and those in chemical engineering. The book includes a new section on sustainable energy, with sections on carbon capture and sequestration, as a result of increasing environmental awareness; and a companion website that includes problems, worked solutions, and Excel spreadsheets to enable students to carry out complex calculations".. Prozessentwicklung Technik (DE-588)4278925-4 gnd rswk-swf Chemische Verfahrenstechnik (DE-588)4069941-9 gnd rswk-swf (DE-588)4123623-3 Lehrbuch gnd-content Chemische Verfahrenstechnik (DE-588)4069941-9 s Prozessentwicklung Technik (DE-588)4278925-4 s DE-604 http://catalogimages.wiley.com/images/db/jimages/9781119990147.jpg Cover image Digitalisierung UB Bayreuth - ADAM Catalogue Enrichment application/pdf http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=029090199&sequence=000003&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA Inhaltsverzeichnis Digitalisierung UB Bayreuth - ADAM Catalogue Enrichment application/pdf http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=029090199&sequence=000004&line_number=0002&func_code=DB_RECORDS&service_type=MEDIA Klappentext |
spellingShingle | Smith, Robin Chemical process design and integration Prozessentwicklung Technik (DE-588)4278925-4 gnd Chemische Verfahrenstechnik (DE-588)4069941-9 gnd |
subject_GND | (DE-588)4278925-4 (DE-588)4069941-9 (DE-588)4123623-3 |
title | Chemical process design and integration |
title_auth | Chemical process design and integration |
title_exact_search | Chemical process design and integration |
title_full | Chemical process design and integration Robin Smith (School of Chemical Engineering and Analytical Science, The University of Manchester, UK) |
title_fullStr | Chemical process design and integration Robin Smith (School of Chemical Engineering and Analytical Science, The University of Manchester, UK) |
title_full_unstemmed | Chemical process design and integration Robin Smith (School of Chemical Engineering and Analytical Science, The University of Manchester, UK) |
title_short | Chemical process design and integration |
title_sort | chemical process design and integration |
topic | Prozessentwicklung Technik (DE-588)4278925-4 gnd Chemische Verfahrenstechnik (DE-588)4069941-9 gnd |
topic_facet | Prozessentwicklung Technik Chemische Verfahrenstechnik Lehrbuch |
url | http://catalogimages.wiley.com/images/db/jimages/9781119990147.jpg http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=029090199&sequence=000003&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=029090199&sequence=000004&line_number=0002&func_code=DB_RECORDS&service_type=MEDIA |
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