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Mechanical aeration water treatment

Mechanical aerators (4,6) can effectively remove VOCs and are commonly used in wastewater treatment, not water treatment. The aerators use surface or subsurface mechanical stirring mechanisms to create water-air mixing turbulence. Figure 14 illustrates a surface and subsurface aerator installations. [Pg.36]

A recirculating methodology is an attempt to maintain the water quality of the test solution without altering the toxicant concentration. A filter may be used to remove waste products or some form of aeration may be used to maintain dissolved oxygen concentration at a specified level. The advantage of this system is the maintenance of the water quality of the test solution. Disadvantages include an increase in complexity, an uncertainty that the methods of water treatment do not alter the toxicant concentration, and the increased likelihood of mechanical failure. [Pg.45]

In many countries (including the United States), regulations require mine operators to comply with specific limitations relating to effluents. In order to meet these lequiranents, the following treatments are typically anployed (1) addition of alkaline material, such as Ume or sodium hydroxide, (2) natural or mechanical aeration, and (3) settling. When the pH is raised to 7 or 8 and settling has occurred, most drainage waters will meet the standards for iron content and suspended solids. [Pg.742]

The various types of plug flow bioreactors were recently surveyed by Moser (1985a). They utilize surface aeration by means of a variety of rotating brushes, rotors, cone aerators, or gas or fluid jets such as are found in biological waste water treatment plants. Beyond all mechanically driven systems, reactors can also be both aerated and mixed pneumatically, or one pump can serve for both mixing and hydrodynamic stirring. [Pg.67]

The other major separation task in boiler feed water treatment is the removal of dissolved gases, especially oxygen and carbon dioxide, which will cause corrosion in the boiler. These can be removed by mechanical de-aerators, or chemicals may be added that will scavenge these gases. [Pg.234]

The function of aeration in a wastewater treatment system is to maintain an aerobic condition. Water, upon exposure to air, tends to estabUsh an equihbrium concentration of dissolved oxygen (DO). Oxygen absorption is controlled by gas solubiUty and diffusion at the gas—hquid interface. Mechanical or artificial aeration may be utilised to speed up this process. Agitating the water, creating drops or a thin layer, or bubbling air through water speeds up absorption because each increases the surface area at the interface. [Pg.339]

Oxygen corrosion usually takes the form of deep pitting and involves both tuberculation and differential aeration corrosion mechanisms. The BW commonly is brown and murky, and chemical treatment reserves usually are very low or absent. The source of the oxygen is either MU water dissolved oxygen (DO) or air in-leakage. [Pg.178]

This process, according to the manufacturer,54 has been developed in such a way that space requirements are kept to a minimum. A BIOPAQ IC reactor is used as the initial step in the treatment process. The name of this anaerobic reactor is derived from the gas-lift driven internal circulation that is generated within a tall, cylindrical vessel. These reactors have been operational in the paper industry since 1996. The second step in the purification process is a mechanically mixed and aerated tank. The aerating injectors can be cleaned in a simple way without the need to empty the aeration tank. Potential scaling materials are combined into removable fine particles. At the same time, the materials that may cause an odor nuisance are oxidized into odorless components. The process can be completed by a third and a fourth step. The third step focuses on suspended solids recovery and removal. The fourth step is an additional water-softening step with lamella separation and continuous sand filters in order to produce fresh water substitute. The benefits claimed by the manufacturer are as follows54 ... [Pg.894]

Lee, J. C. and Buckley, P. S. In Biological Fluidised Bed Treatment of Water and Wastewater by Cooper, P. F. and Atkinson, B., (eds.), Ellis Horwood, Chichester (1981), 62. Fluid mechanics and aeration characteristics of fluidised beds. [Pg.367]

Gas-to-liquid mass transfer is a transport phenomenon that involves the transfer of a component (or multiple components) between gas and liquid phases. Gas-liquid contactors, such as gas-liquid absorption/ stripping columns, gas-liquid-solid fluidized beds, airlift reactors, gas bubble reactors, and trickle-bed reactors (TBRs) are frequently encountered in chemical industry. Gas-to-liquid mass transfer is also applied in environmental control systems, e.g., aeration in wastewater treatment where oxygen is transferred from air to water, trickle-bed filters, and scrubbers for the removal of volatile organic compounds. In addition, gas-to-liquid mass transfer is an important factor in gas-liquid emulsion polymerization, and the rate of polymerization could, thus, be enhanced significantly by mechanical agitation. [Pg.1163]

Product obtained from vegetable raw material—either by distillation with water or steam or—from the epicarp of Citrus fruits by a mechanical process, or—by dry distillation (ISO/ DIS 9235.2, 1997, p. 2). Steam distillation can be carried out with or without added water in a still. By contrast, dry distillation of plant material is carried out without the addition of any water or steam to the still (ISO 9235, 1997). Note 2 in Section 3.1.1 of ISO/DIS 9235.2 is of importance. It states that Essential oils may undergo physical treatments (e.g., re distillation, aeration) which do not involve signi cant changes in their composition (ISO/DIS 9235.2, 1997, p. 2). [Pg.129]


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See also in sourсe #XX -- [ Pg.205 ]




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