Chemical Engineering & Technology

Cover image for Vol. 33 Issue 2

February, 2010

Volume 33, Issue 2

Pages 187–346

  1. Cover Picture

    1. Top of page
    2. Cover Picture
    3. Overview
    4. Contents
    5. Forum
    6. Scientific Highlights
    7. Reviews
    8. Research Articles
    1. Cover Chem. Eng. Technol. 2/2010

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.201090000

  2. Overview

    1. Top of page
    2. Cover Picture
    3. Overview
    4. Contents
    5. Forum
    6. Scientific Highlights
    7. Reviews
    8. Research Articles
    1. Overview Contents: Chem. Eng. Technol. 2/2010 (page 187)

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.201090001

  3. Contents

    1. Top of page
    2. Cover Picture
    3. Overview
    4. Contents
    5. Forum
    6. Scientific Highlights
    7. Reviews
    8. Research Articles
    1. Contents: Chem. Eng. Technol. 2/2010 (pages 188–193)

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.201090002

  4. Forum

    1. Top of page
    2. Cover Picture
    3. Overview
    4. Contents
    5. Forum
    6. Scientific Highlights
    7. Reviews
    8. Research Articles
    1. Forum: Chem. Eng. Technol. 2/2010 (pages 194–195)

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.201090003

  5. Scientific Highlights

    1. Top of page
    2. Cover Picture
    3. Overview
    4. Contents
    5. Forum
    6. Scientific Highlights
    7. Reviews
    8. Research Articles
    1. Scientific Highlights: Chem. Eng. Technol. 2/2010 (pages 196–197)

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.201090004

  6. Reviews

    1. Top of page
    2. Cover Picture
    3. Overview
    4. Contents
    5. Forum
    6. Scientific Highlights
    7. Reviews
    8. Research Articles
    1. Product Design and Process Engineering using the Example of Flavors (pages 199–212)

      J. Uhlemann and I. Reiß

      Article first published online: 16 DEC 2009 | DOI: 10.1002/ceat.200900508

      Thumbnail image of graphical abstract

      In the food flavours industry, an exact knowledge of the physico-chemical properties of the flavor and carrier materials is important if process engineering measures are to be used to influence product properties. Recent progress in microencapsulation of flavors is discussed and a detailed discussion of the processes of spray drying, spray granulation, extrusion and multi-material nozzles, is provided.

    2. Solid-state Materials and Methods for Hydrogen Storage: A Critical Review (pages 213–226)

      K. L. Lim, H. Kazemian, Z. Yaakob and W. R. W. Daud

      Article first published online: 12 JAN 2010 | DOI: 10.1002/ceat.200900376

      Thumbnail image of graphical abstract

      Hydrogen is important as a new source of energy for automotive applications. It is clear that efficient hydrogen storage is required to develop this technology. Hydrogen solid-state storage materials and methods including carbon based materials, metal hydrides, metal organic frameworks, hollow glass microspheres and capillary arrays, clathrate hydrates, metal nitrides and imides, doped polymer and zeolites, are critically reviewed.

  7. Research Articles

    1. Top of page
    2. Cover Picture
    3. Overview
    4. Contents
    5. Forum
    6. Scientific Highlights
    7. Reviews
    8. Research Articles
    1. Experimental Investigation of Performances of Microcapsule Phase Change Material for Thermal Energy Storage (pages 227–230)

      G. Fang, H. Li, X. Liu and S. Wu

      Article first published online: 2 DEC 2009 | DOI: 10.1002/ceat.200900224

      Thumbnail image of graphical abstract

      Microcapsule phase change material for thermal energy storage is prepared by a complex coacervation method with gelatin and acacia as wall materials and paraffin as core material in an emulsion system. The microencapsulated paraffin has a larger phase change latent heat, suitable phase change temperature, and better thermal stability, proving its great potential for thermal energy storage systems.

    2. Effect of Ultrasound on SO2 Desorption from Sodium Alkali Desulphurization Regeneration Solution (pages 231–236)

      H. Xu, S.-T. Zhang, X.-B. Lu, Y. Liu and X.-Y. Yu

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900330

      Thumbnail image of graphical abstract

      The application of ultrasound for the desorption of SO2 gas from sodium alkali desulphurization regeneration solution is reported. Ultrasound is seen to accelerate the SO2 release rate and the ultrasound enhancement effect is investigated by analyzing the compositions of desorption solutions at different pH values.

    3. Coalescence of Water Droplets in Crude Oil Emulsions: Analytical Solution (pages 237–243)

      A. E. Bresciani, R. M. B. Alves and C. A. O. Nascimento

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900234

      Thumbnail image of graphical abstract

      The equations of forces acting on the droplets in a water/crude oil emulsion submitted to an electrical field can be solved. Considering a pseudo-steady state, the equations enable the analytical calculation of the time between collisions and the velocities of the droplets. The influence of the operational variables (temperature, water content, and electrical field) on the separation of the phases may be analyzed and the crude-oil desalting process may be optimized.

    4. Chitosan/titanate Nanotube Hybrid Membrane with Low Methanol Crossover for Direct Methanol Fuel Cells (pages 244–250)

      J. Geng, Z. Jiang, J. Wang, Y. Shi, D. Yang and L. Xiao

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900443

      Thumbnail image of graphical abstract

      Titanate nanotubes were prepared by a hydrothermal method and incorporated into a chitosan matrix to fabricate chitosan/titanate nanotube hybrid membranes, which exhibited much lower methanol crossover and higher mechanical strength than the pure chitosan membrane. These hybrid membranes had the potential application of proton exchange membrane for direct methanol fuel cells.

    5. A Case Study in the Pre-Calculation of Henry Coefficients (pages 251–257)

      R. Franke, B. Hannebauer and S. Jung

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900505

      Thumbnail image of graphical abstract

      Gas solubilities represent the property data basis for absorption processes and are important in the design of gas-liquid reactors. We determine Henry coefficients as a measure of gas solubility by means of a series of computational approaches used in industrial practice and compare the results to experimentally determined values. Temperature-varied values for hydrocarbon-alcohol systems constitute the object of the study.

    6. Computational Fluid Dynamics Study of a Styrene Polymerization Reactor (pages 258–266)

      H. Patel, R. Dhib and F. Ein-Mozaffari

      Article first published online: 11 JAN 2010 | DOI: 10.1002/ceat.200900440

      Thumbnail image of graphical abstract

      Computational fluid dynamics (CFD) is utilized to investigate the effect of mixing on styrene polymerization with a benzoyl peroxide initiator in a laboratory-scale continuous stirred-tank reactor equipped with a pitched-blade impeller. The CFD model is used to compute the monomer conversion as a function of the impeller speed and the residence time.

    7. Effects of Operating Parameters on the Cinnamaldehyde Content of Extracted Essential Oil Using Various Methods (pages 267–274)

      H. Baseri, A. Haghighi-Asl and M. N. Lotfollahi

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900263

      Thumbnail image of graphical abstract

      Supercritical fluid extraction (SFE) of essential oils from commercial cinnamon bark was compared with essential oils that were obtained by hydrodistillation. Effects of operating parameters on extraction yield and composition of the extracted volatile oil were studied. In the hydrodistillation process, the effect of the pH of the solvent was also studied.

    8. Sulfur Removal from Low-Sulfur Gasoline and Diesel Fuel by Metal-Organic Frameworks (pages 275–280)

      S. Achmann, G. Hagen, M. Hämmerle, I. M. Malkowsky, C. Kiener and R. Moos

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900426

      Thumbnail image of graphical abstract

      The reduction of the content of sulfur compounds in commercial gasoline and diesel fuels is a major concern of the petroleum, automotive and power generation industries. This is required to meet regulatory requirements and also to enhance the life-time of exhaust gas aftertreatment systems and sensors or fuel cell components. A series of metal-organic frameworks is investigated to determine their desulfurization capacity for commercial gasoline and diesel fuel.

    9. Heat and Mass Transfer between Air and Liquid Desiccant in Cross-flow Contact Systems (pages 281–291)

      D. Babakhani, M. Soleymani and A. Moheb

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900383

      Thumbnail image of graphical abstract

      This paper reveals an analytical solution for the simultaneous heat and mass transfer processes in a packed cross-flow dehumidifier/regenerator. The results show that good agreement exists between the analytical results and the experimental data in the literature.

    10. Influence of a Lipid Phase on the Physical Properties of Spray-Dried Maltodextrin Powders (pages 292–298)

      P. C. Martins and T. G. Kieckbusch

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900461

      Thumbnail image of graphical abstract

      The knowledge of the physical properties of the instantaneous time (wetting) and flowability of samples containing different proportions of lipid fractions with different melting points can provide important information on the influence of the lipid phase in the agglomeration of powdered food, and is investigated in detail.

    11. Synthesis of a Graphite Oxide Polyaniline Nano-Composite by an Electrochemical Method (pages 299–304)

      M. R. Rahimipour and B. Yazdani

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900361

      Thumbnail image of graphical abstract

      In order to produce a polyaniline graphite oxide nano-composite, electro-polymerization of aniline was performed within the graphite oxide layers via electrochemical treatment of aniline-intercalated graphite oxide in the supporting electrolyte. The polyaniline graphite oxide nano-composite was characterized by FTIR, XRD, TGA and SEM.

    12. Continuous-Flow Surface Aeration Systems (pages 305–314)

      B. Kumar and A. R. Rao

      Article first published online: 11 JAN 2010 | DOI: 10.1002/ceat.200900403

      Thumbnail image of graphical abstract

      An aeration process in an activated sludge plant is a continuous-flow system. The efficiency of the surface aeration systems is governed by geometric and dynamic parameters. The objective of this study is the scale-up of laboratory results into field installation. The optimal geometric configuration of a continuous-flow surface aeration system is established.

    13. Modeling of Particle Layer Detachment under Consideration of Transient Kinetic Effects (pages 315–320)

      Q. Zhang and E. Schmidt

      Article first published online: 16 DEC 2009 | DOI: 10.1002/ceat.200900399

      Thumbnail image of graphical abstract

      Particle layer detachment is extremely nonstationary concerning place and time, primarily due to changing conditions for the forces on the one hand and changes in the particle layer morphology on the other hand. A model and a simulation considering such transient kinetic effects on filter cake detachment are described and diverse computing results presented and discussed.

    14. Mixing Agglomeration in a High-Shear Mixer with a Stirred Mixing Vessel (pages 321–326)

      B. Daumann, X. Sun, H. Anlauf, S. Gerl and H. Nirschl

      Article first published online: 8 DEC 2009 | DOI: 10.1002/ceat.200900259

      Thumbnail image of graphical abstract

      The agglomeration process in an Eirich-type high-shear mixer was investigated. Using a ceramic product, various influencing parameters, such as the agitator speed, vessel speed, or mixing tool, were investigated. The results will help the practical user to decide which parameters have to be considered for an optimum mixing agglomeration.

    15. Experimental Study of the Mixing Time in a Jet-Mixed Gas-Liquid System (pages 327–333)

      T. Yousefi Amiri and J. S. Moghaddas

      Article first published online: 11 JAN 2010 | DOI: 10.1002/ceat.200900011

      Thumbnail image of graphical abstract

      Previous studies on jet mixing have been limited to single liquid-phase mixing. Since the agitated gas-liquid vessels are widely used in chemical, biochemical and petroleum industries, the novelty of the present study is that it proposes the use of the jet fluid as a mixer in complex gas-liquid systems and attempts to experimentally investigate the jet mixing behavior in such systems.

    16. High Temperature Cyclic Oxidation Resistance of Iron Chromium Base Alloys (pages 334–340)

      V. F. C. Lins, M. M. R. Castro, R. Z. Domingues and T. Matencio

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900365

      Thumbnail image of graphical abstract

      The cyclic oxidation behavior of an experimental stainless ferritic steel, without molybdenum and with copper-aluminum-titanium-lanthanum additions, developed for solid oxide fuel cell applications, was evaluated and compared with the oxidation behavior of commercial austenitic and ferritic stainless steels. For the cyclic oxidation tests, the steel samples were tested at temperatures ranging from 600 to 800 °C.

    17. Roles of Pumps and Bypass in Chemistry Induced by Hydrodynamic Cavitation (pages 341–346)

      P. Braeutigam, Z.-L. Wu, A. Stark and B. Ondruschka

      Article first published online: 28 JAN 2010 | DOI: 10.1002/ceat.200900434

      Thumbnail image of graphical abstract

      A self-made low pressure device for creating hydrodynamic cavitation was optimized by using the Weissler reaction. First results suggest that upstream pressure is an important parameter for the optimization of hydrodynamic cavitation. Further research is required on the remaining parameters.

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