Produktbild: Chemical Process Design and Integration

Chemical Process Design and Integration For the Efficient Use of Resources and Reduced Environmental Impact

Fr. 94.90

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Beschreibung

Produktdetails

Einband

Taschenbuch

Erscheinungsdatum

07.01.2005

Verlag

John Wiley & Sons Inc

Seitenzahl

650

Maße (L/B/H)

28/21.8/2.9 cm

Gewicht

1620 g

Auflage

1. Auflage

Sprache

Englisch

ISBN

978-0-471-48681-7

Beschreibung

Produktdetails

Einband

Taschenbuch

Erscheinungsdatum

07.01.2005

Verlag

John Wiley & Sons Inc

Seitenzahl

650

Maße (L/B/H)

28/21.8/2.9 cm

Gewicht

1620 g

Auflage

1. Auflage

Sprache

Englisch

ISBN

978-0-471-48681-7

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  • Produktbild: Chemical Process Design and Integration
  • Preface.

    Acknowledgements.

    Nomenclature.

    Chapter 1 The Nature of Chemical Process Design and Integration.

    Chapter 2 Process Economics.

    Chapter 3 Optimization.

    Chapter 4 Thermodynamic Properties and Phase Equilibrium.

    Chapter 5 Choice of Reactor I - Reactor Performance.

    Chapter 6 Choice of Reactor II - Reactor Conditions.

    Chapter 7 Choice of Reactor III - Reactor Configuration.

    Chapter 8 Choice of Separator for Heterogeneous Mixtures.

    Chapter 9 Choice of Separator for Homogeneous Fluid Mixtures I - Distillation.

    Chapter 10 Choice of Separator for Homogeneous Fluid Mixtures II - Other Methods.

    Chapter 11 Distillation Sequencing.

    Chapter 12 Distillation Sequencing for Azeotropic Distillation.

    Chapter 13 Reaction, Separation and Recycle Systems for Continuous Processes.

    Chapter 14 Reaction, Separation and Recycle Systems for Batch Processes.

    Chapter 15 Heat Exchanger Networks I - Heat Transfer Equipment.

    Chapter 16 Heat Exchanger Networks II - Energy Targets.

    Chapter 17 Heat Exchanger Networks III - Capital and Total Cost Targets.

    Chapter 18 Heat Exchanger Networks IV - Network Design.

    Chapter 19 Heat Exchanger Networks V - Stream Data.

    Chapter 20 Heat Integration of Reactors.

    Chapter 21 Heat Integration of Distillation Columns.

    Chapter 22 Heat Integration of Evaporators and Dryers.

    Chapter 23 Steam Systems and Cogeneration.

    Chapter 24 Cooling and Refrigeration Systems.

    Chapter 25 Environmental Design for Atmospheric Emissions.

    Chapter 26 Water System Design.

    Chapter 27 Inherent Safety.

    Chapter 28 Clean Process Technology.

    Chapter 29 Overall Strategy for Chemical Process Design and Integration 649

    Appendix A Annualization of Capital Cost.

    Appendix B Gas Compression.

    Appendix C Heat Transfer Coefficients and Pressure Drop in Shell-and-tube Heat Exchangers.

    Appendix D The Maximum Thermal Effectiveness for 1-2 Shell-and-tube Heat Exchangers.

    Appendix E Expression for the Minimum Number of 1-2 Shell-and-tube Heat Exchangers for a Given Unit.

    Appendix F Algorithm for the Heat Exchanger Network Area Target.

    Appendix G Algorithm for the Heat Exchanger Network Number of Shells Target.

    Appendix H Algorithm for Heat Exchanger Network Capital Cost Targets.

    Index.