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Column Environmental Model

The environmental model defines the system boundaries and the relations between the system and its surroundings. In the environmental diagram (Fig. 16.1), it is assumed that the feed flow and conditions are determined externally. [Pg.219]

Concerning the system outputs, a distinction can be made between the controlled and the uncontrolled variables. If the purpose of the column is to produce a required product quality, then the top and bottom qualities are the most important controlled variables. At a tray only the temperature can be continuously measured. It gives a good indication of the condition of the column. [Pg.219]

Process Dynamics and Control Modeling for Control and Prediction. Brian Roffel and Ben Betlem. [Pg.219]


Fig. 16.1. Sketch and environmental model of distillation column with floating pressure. L<,oB Fig. 16.1. Sketch and environmental model of distillation column with floating pressure. L<,oB<fenj = condensate flow, D = top product flow, R = reflux fraction Ln ilLcondens), B = top product flow, M = molar mass, x = liquid mol fraction, T = temperature.
Fig. 16.2. Alternative environmental model of a distillation column with controlled pressure. Fig. 16.2. Alternative environmental model of a distillation column with controlled pressure.
Airlift loop reactor (ALR), basically a specially structured bubble column, has been widely used in chemical industry, biotechnology and environmental protection, due to its high efficiency in mixing, mass transfer, heat transfer etc [1]. In these processes, multiple reactions are commonly involved, in addition to their complicated aspects of mixing, mass transfer, and heat transfer. The interaction of all these obviously affects selectivity of the desired products [2]. It is, therefore, essential to develop efficient computational flow models to reveal more about such a complicated process and to facilitate design and scale up tasks of the reactor. However, in the past decades, most involved studies were usually carried out in air-water system and the assumed reactor constructions were oversimplified which kept itself far away from the real industrial conditions [3] [4]. [Pg.525]

In Tables 14.9 and 14.10, the last column reports the environmental impact points (EIPs) for typical applications of organic and conventional pesticides derived from the Pesticide Environmental Assessment System, or PEAS. This model produces relative rankings of risks based on defined use rates and use patterns (the formulation used to apply a pesticide, timing, target of the application, spray equipment used, etc). PEAS scores reflect an equal balancing of acute pesticide risks to farm workers, chronic risks via dietary exposure and exposures to birds, Daphnia and bees. [Pg.279]

Alemi, M. H., D. A. Goldhamer and D. R. Nelson, 1991, Modeling selenium transport in steady-state, unsaturated soil columns. Journal of Environmental Quality, 20,89-95. [Pg.509]

Jurgens et al. [33] carried out a series of laboratory experiments to study the behavior of estrogens in the aquatic environment and set up a model to estimate their likely environmental concentrations in the water column and bed-sediments. According to this study, between 13 and 92% of the estrogens entering a river system would end up in the bed-sediment compartment with the majority of sorption occurring within the first 24 h of contact. [Pg.8]

At the same time, one should notice that the real catalysts are applied in the gas/liquid environments at usually an increased temperature so that dynamic structural evolution of a real catalyst would not be probed in a conventional electron microscope. To bridge the gap, in situ environmental electron microscope is developed by placing a micoreactor inside the column of an electron microscope to follow catalytic reaction processes [58-62], However, the specimen in an in situ TEM may suffer from interaction with ionised gas (plasma), making the interpretation of in situ TEM study of catalytic reaction more complicated. Characterisation of static, post-reaction catalysts is still the most commonly used. Well-designed model catalysts and reasonable interpretation of the results are essential to a successful study. [Pg.475]

Alessio RJ, Li X, Martin DF. Removal of BPA model compounds and related substances by means of column chromatography using Octolig . Journal of Environmental Science and Health 2012 47 000-000. [Pg.146]

Figure 16.7—Ion mobility spectrometer. Ions enter the analyser tube by control of the polarity of the acceleration grid. An example of a recording in the repetitive mode (RIP Reactant Ion Peak) for tolyl isocyanate (TDI), the compound analysed, is shown. A commercial model of an Environmental Vapour Monitor is also shown (reproduced by permission of Grasby Electronics, UK). This instrument uses a GC column to improve compound identification. Figure 16.7—Ion mobility spectrometer. Ions enter the analyser tube by control of the polarity of the acceleration grid. An example of a recording in the repetitive mode (RIP Reactant Ion Peak) for tolyl isocyanate (TDI), the compound analysed, is shown. A commercial model of an Environmental Vapour Monitor is also shown (reproduced by permission of Grasby Electronics, UK). This instrument uses a GC column to improve compound identification.
The remainder of the modified parfait column consisted of an MSC-1 cation-exchange and an A-162 anion-exchange bed. The elution conditions for these beds were modified to minimize contamination of eluates and to selectively desorb organic anions and cations. With the modified protocol, 20 model compounds (Table I), selected by the U.S. Environmental Protection Agency (USEPA) Health Effects Research Laboratory (HERL), were used to evaluate the recovery efficiency of the method. Recoveries were determined in the presence of 2 ppm of a humic acid supplied by HERL. [Pg.491]

Angley, J.T., Brusseau, M.L., Miller, W.L. Delfino, J.J. (1992). Nonequilibrium sorption and aerobic biodegradation of dissolved alkylbenzenes during transport in aquifer material column experiments and evaluation of a coupled-process model. Environmental Science Technology, 26(7), 1404-10. [Pg.240]

Huang W H, Chang C Y, Chiu C Y, Lee S J, Yu Y H, Liou H T, Ku Y, Chen J N (1998) A refined model for ozone mass transfer in a bubble column, Journal Environmental Science Health A 33 441-460. [Pg.107]

Vaughan, R.L., Jr., Reed, B.E. and Smith, E.H. (2007) Modeling As(V) removal in iron oxide impregnated activated carbon columns. Journal of Environmental Engineering, 133(1), 121-24. [Pg.429]


See other pages where Column Environmental Model is mentioned: [Pg.219]    [Pg.219]    [Pg.262]    [Pg.33]    [Pg.569]    [Pg.219]    [Pg.452]    [Pg.246]    [Pg.445]    [Pg.840]    [Pg.47]    [Pg.42]    [Pg.700]    [Pg.281]    [Pg.230]    [Pg.713]    [Pg.700]    [Pg.36]    [Pg.775]    [Pg.458]    [Pg.521]    [Pg.78]    [Pg.494]    [Pg.2327]    [Pg.202]    [Pg.486]    [Pg.138]    [Pg.420]    [Pg.51]    [Pg.416]    [Pg.185]    [Pg.340]    [Pg.457]    [Pg.246]    [Pg.203]   


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