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  • Articles  (254)
  • Wiley  (254)
  • American Association for the Advancement of Science (AAAS)
  • Institute of Physics
  • 2010-2014  (254)
  • Chemical Engineering and Technology  (113)
  • 4519
  • 1
    Publication Date: 2011-04-27
    Description: Spray drying is widely used to manufacture many powdered products, with the drying process parameters having significant influence over the final powder's surface properties and propensity for unwanted caking. In most cases caking experiments are performed on bulk powders, but especially in multi-component powders, it is often difficult to interpret these results, where interaction effects between particles can be complex. Here the technique of scanning probe microscopy is used to characterize the nanoscale properties of spray dried model milk powders in order to investigate the surface properties of the powders. The topography, hardness and material properties of single particles in a spray dried powder were characterized by using atomic force microscopy techniques. It has been shown that the material properties both at the surface and in the particle wall of a model milk powder system are not uniform.
    Print ISSN: 0930-7516
    Electronic ISSN: 1521-4125
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 2
    Publication Date: 2013-12-06
    Description: The application of computational fluid dynamics (CFD) as a tool to simulate bubble column bioreactors is investigated. A three-dimensional model utilizing the Euler-Euler approach is evaluated. The role of various terms, i.e., lift, drag, bubble-induced turbulence, and volume fraction correction terms for drag, is determined. Good agreement between experimental data and simulation results was obtained by means of a single-bubble size model provided that bubble-induced turbulence and the reduction in drag due to the presence of other bubbles were taken into account. There is increasing interest in using CFD to model aerobic bioreactors. The influence of various terms like lift, drag, and bubble-induced turbulence in the CFD modeling of bubble column reactors was investigated. Reasonable agreement between simulation results and experimental data was obtained by incorporating bubble-induced turbulence and a volume fraction correction term for drag.
    Print ISSN: 0930-7516
    Electronic ISSN: 1521-4125
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 3
    Publication Date: 2013-10-31
    Description: The holdup and bubble size distribution (BSD) in bubble columns using both air/water and an industrially relevant air/fermentation media system are investigated. It was found that the BSD in the air/fermentation media system was quite narrow and did not change with height. In contrast, the BSD in the air/water system varied considerably with height depending on the sparger design used. Holdup measurements were also performed for different superficial velocities. The holdup in the air/fermentation media system was greater than that for the air/water system, a result attributed to the presence of surface-active compounds in the fermentation media. Bubble column reactors are widely used in the biotechnology industry to perform large-scale aerobic fermentations. The bubble size distribution and holdup in bubble columns for air/water and air/fermentation media systems is studied experimentally. Unlike for air-water, the bubble size distribution in fermentation media is narrow and does not change with height.
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    Electronic ISSN: 1521-4125
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 4
    Publication Date: 2011-04-26
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    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 5
    Publication Date: 2013-10-30
    Print ISSN: 0930-7516
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    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 6
    Publication Date: 2013-06-07
    Description: In situ radio-frequency heating (ISRFH) combined with soil vapor extraction was demonstrated at a contaminated field site of a former hydrotreatment plant in Zeitz near Leipzig. The project was carried out in several phases including cold soil vapor extraction for comparison. During the test, a soil volume of about 300 m 3 was heated to an average temperature of 54 °C. As expected, the extraction rate for hydrocarbons (especially the main contaminant benzene) was markedly enhanced by soil heating. Furthermore, microbial degradation of organic compounds was supported. Although a total amount of approximately 1.4 t of hydrocarbons was removed from the soil, the demonstration project was not aimed at complete remediation of the site. Conditions limiting the extent of cleanup are discussed in detail and conclusions for an efficient application of ISRFH in soil remediation are derived whereas experiences from other sites are also implied. Potential and limitations of the combination of in situ radio-frequency heating (ISRFH) and soil vapor extraction are exemplarily discussed for a demonstration project carried out at a former industrial site. Conditions restricting the extent of cleanup are discussed and conclusions for an efficient application of ISRFH in soil remediation are deduced.
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    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 7
    Publication Date: 2011-06-29
    Description: A nonequilibrium model was developed and simulated by adopting a dual-scale pore network approach. The distributions of temperature, moisture, and pressure in drying air, as well as the temperature and moisture content profiles in grain kernels were obtained from the pore scale model and the kernel scale model, respectively. A small test bin was built to conduct in-bin drying experiments and to validate the model. The results from the experiments and the simulations indicate that the dual-scale pore network approach could explain the drying process of the deep-bed grain drying process well. The influences of grain bulk porosity and cereal particle size distribution were also investigated by numerical simulations. A non-equilibrium model was developed and simulated by adopting the dual-scale pore network approach. The distributions of temperature, moisture, and pressure in drying air, as well as the temperature and moisture content profiles in grain kernel were obtained from the pore scale model and the kernel scale model, respectively. A small test bin was built to conduct in-bin drying experiments and to validate the model.
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    Electronic ISSN: 1521-4125
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 8
    Publication Date: 2013-02-08
    Description: Biological techniques for the removal of gaseous pollutants such as hydrogen sulfide (H 2 S) have proved to be effective, environmentally friendly, and economically viable. However, when high concentrations of H 2 S are treated, the process is severely restricted by the oxygen deficit in the liquid phase. The oxygen transfer efficiency provided by a membrane diffuser is evaluated under typical pressure and salinity conditions used for the biological treatment of H 2 S in biogas. The optimal operating parameters for enhanced oxygen transfer were determined. The addition of pure oxygen with a membrane diffuser to increase the oxygen transfer rate and the use of a nonaqueous phase to improve oxygen transfer in a bioscrubber system are also evaluated. The effect of operating variables on the oxygen mass transfer process was tested in a pilot plant using a membrane diffuser as intensive gas-liquid contactor. Tests simulated the conditions of biofiltration of H 2 S at high loads for biogas sweetening. Interesting effects were observed with higher solution ion concentration and additional nonliquid phase.
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    Electronic ISSN: 1521-4125
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 9
    Publication Date: 2011-03-30
    Description: Porous glass monoliths are suitable model systems to study pore size-related effects in gas diffusion. Here, mesoporous glass membranes with different surface properties and pore diameters covering the lower mesopore range were synthesized and used to study gas permeation of adsorbable and non-adsorbable gases. Dynamic single gas permeation measurements were performed using a modified Wicke-Kallenbach cell. Chemical surface modification of the inner surface of the membranes resulted in altered adsorption and diffusion properties. Due to their favorable properties, porous glass monoliths are suitable model systems to study pore size-related effects in gas diffusion. Mesoporous glass membranes were synthesized and characterized by dynamic single-gas permeation measurements. A chemical surface modification was used to alter the adsorption and mass transfer properties of the mesoporous membranes.
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    Electronic ISSN: 1521-4125
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 10
    Publication Date: 2011-01-25
    Description: Deoxygenation is a critical step in making hydrocarbon-rich biofuels from biomass constituents. Although the thermal effects of oxygenate aromatization have been widely reported, the effect of pressure on this critical reaction has not yet been closely investigated, one primary reason being the unavailability of a reactor that can pyrolyze oxygenates, especially those in solid form, under pressurized conditions. Here, the first of a series of studies on how oxygenates behave when catalytically pyrolyzed under elevated pressure and temperature conditions is reported. Methanol, the simplest alcohol, was selected as the candidate to study the chemical phenomena that occur under pressurized catalytic pyrolysis. The reactions were carried out over the shape-selective catalyst ZSM-5 (SiO 2 /Al 2 O 3 = 30) under varying pressure (0 to 2.0684 MPa (300 psi) in 0.3447 MPa (50 psi) increments) and temperature (500 to 800 °C in 50 °C increments) conditions. Benzene, toluene, ethyl benzene, and xylenes (BTEX) were analyzed as the deoxygenated products of the reaction. The results indicate that the reactor pressure significantly affects deoxygenated product composition. Methanol with the potential to be synthesized via renewable feedstocks is a good substitution for petroleum fuel if the process economics were scaled down. One way to address this issue is the development of the process to a level with high hydrocarbon yield. Pressure proved to be an important parameter to achieve higher selectivity toward hydrocarbons.
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    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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