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Effluent treatment others

The depressed prices of most metals in world markets in the 1980s and early 1990s have slowed the development of new metal extraction processes, although the search for improved extractants continues. There is a growing interest in the use of extraction for recovery of metals from effluent streams, for example the wastes from pickling plants and electroplating (qv) plants (276). Recovery of metals from Hquid effluent has been reviewed (277), and an AM-MAR concept for metal waste recovery has recentiy been reported (278). Possible appHcations exist in this area for Hquid membrane extraction (88) as weU as conventional extraction. Other schemes proposed for effluent treatment are a wetted fiber extraction process (279) and the use of two-phase aqueous extraction (280). [Pg.81]

Toxic or malodorous pollutants can be removed from industrial gas streams by reaction with hydrogen peroxide (174,175). Many Hquid-phase methods have been patented for the removal of NO gases (138,142,174,176—178), sulfur dioxide, reduced sulfur compounds, amines (154,171,172), and phenols (169). Other effluent treatments include the reduction of biological oxygen demand (BOD) and COD, color, odor (142,179,180), and chlorine concentration. [Pg.481]

Waste treatment prior to disposal may introduee phase ehanges whieh result in quite different pollution eontrol eonsiderations. For example, the gases generated by ineineration of a solid waste ean be serubbed with liquid in order to meet an aeeeptable diseharge eriterion henee, in addition to ash for disposal, a liquid effluent stream is produeed and requires treatment. Other waste treatment proeesses may result in the liberation of flammable or toxie gaseous emissions as exemplified in Table 16.5. [Pg.498]

Other challenges in engineering chemical processes Effluent treatment Effluent treatment Fiber drawing and coating processes Ceramic processing... [Pg.52]

On the other hand, we need to ensure that stronger sanitisers do not damage the health of workers during discharge of toilet tanks nor upset normal biodegradation processes in effluent treatment plants. [Pg.124]

Effluent treatment regulations might specify a level of BOD5, COD or both. Increasingly, the tendency is toward the specification of toxicity. This measures the toxicity of an effluent to some kind of living species. Other contaminants that might be specified are ... [Pg.584]

The current production of microalgae is mainly focused around a few species, such as Spirulim, Chlorella, Dunaliella or Haematococcus for nutritional purposes (for humans) and animal feed (especially aquaculture). Other sectors, such as cosmetics, effluent treatment and bioenergy, have shown interest, incorporating these or other species of microalgae and cyanobacteria into commercial products. Currently, 95% of the production of microalgae is based on open systems... [Pg.105]

Since cyclodextrins form complexes with various other substances, including many dyes and surfactants, it is clear that they could be useful in effluent treatment. They are potentially suitable for the reduction or removal of polluting substances either by immobilisation or by solubilisation and extraction and thus can accelerate detoxification [30]. [Pg.65]

The effluent waters of a waste water treatment plant (Ruhleben) in Berlin (Fig. 3) show the highest positive Gd anomaly observed to date. Strong positive Gd anomalies are common in effluents of other treatment plants across the world (e.g. Australia, USA, Austria, Germany, and Czech Republic) due to the inability of the treatment processes to remove the highly stable and water soluble Gd complexes. This is also the cause for their presence in river and lake waters and in groundwater which receive these effluent waters either directly (input into rivers) or indirectly (infiltration). [Pg.220]

Mechanical and biological methods are very effective on a large scale, and physical and chemical methods are used to overcome particular difficulties such as final sterilization, odor removal, removal of inorganic and organic chemicals and breaking oil or fat emulsions. Normally, no electrochemical processes are used [10]. On the other hand, there are particular water and effluent treatment problems where electrochemical solutions are advantageous. Indeed, electrochemistry can be a very attractive idea. It is uniquely clean because (1) electrolysis (reduction/oxidation) takes place via an inert electrode and (2) it uses a mass-free reagent so no additional chemicals are added, which would create secondary streams, which would as it is often the case with conventional procedures, need further treatment, cf. Scheme 10. [Pg.185]

Question 5 ("Is combustion with air the only chemistry intended at your facility ") can be answered YES in this case, assuming the "facility" being addressed is limited to the incinerator system. Due to the great number of combustion systems in operation, many other resources are available for ensuring safe design and operation of the combustion part of the incinerator facility. However, it should be noted that many combustors now have effluent treatment systems, such as selective catalytic reduction (SCR) systems, that involve intentional chemistry beyond the combustion reaction. [Pg.132]

Figure Seven (7) depicts a general schematic for membrane processes. In these technologies the implication of increasing the dewatering process is described by the term "recovery", which is defined as the purified water volume divided by the incoming stream volume in other words, percentage of the feed flow which is pumped through the membrane. Typically, for effluent treatment applications, the recovery figure is at least 90%. As recovery is increased (to decrease concentrated solute volume), the concentration of solute and suspended solids in the concentrate stream increases. Figure Seven (7) depicts a general schematic for membrane processes. In these technologies the implication of increasing the dewatering process is described by the term "recovery", which is defined as the purified water volume divided by the incoming stream volume in other words, percentage of the feed flow which is pumped through the membrane. Typically, for effluent treatment applications, the recovery figure is at least 90%. As recovery is increased (to decrease concentrated solute volume), the concentration of solute and suspended solids in the concentrate stream increases.
Water and Effluent Treatment in Nuclear and other chemical plants. Corrosion resistant linings for water treatment vessels and pipelines, pumps, valves, flowmeters, agitators, chemical dosing tanks, effluent tanks etc. Soft natural rubber or ebonite, EPDM, butyl, neoprene or hypalon. [Pg.55]

In conclusion, a greater knowledge of the effect of the key controlling parameters of this powerful separation technique, as well as improvement in membrane life time of the currently available commercial electromembranes and reduction in their costs, would ensure further growth beyond desalination and salt production and foster ED applications in the food sector, as well as in the chemical, pharmaceutical, and municipal effluent treatment areas. This will of course need extensive R D studies and will highly likely result in hybrid processes combining ED to other separation techniques, such as NF, IE, and so on, so as to shorten present downstream and refining procedures. [Pg.351]

Table 8.3 summarizes the actual or estimated prices to build a variety of chemical and refinery process plants. The stated costs do not include associated tankage, utilities, effluent treatment, service roads, general-purpose buildings, spare parts, or all the other components required to complete a major project. These additional offsite facilities are typically considered to add 50% onto the cost of a project. [1, 2]... [Pg.304]

Concerns about groundwater contamination and municipal water supply quality have driven much of the growth of various water treatment schemes involving nanofiltration as a stand-alone process or in combination with RO and/or UF in a broad range of water treatment systems delivering precise purity levels and attractive process economics. Other established applications include corn syrup concentration, recycling of water-soluble polymers, effluent treatment for the food and beverage industry, metal... [Pg.383]

Oxidation of phenols, dyes, and polycyclic aromatic hydrocarbons [48,49], decolorization of Kraft bleaching effluents, binding of phenols and aromatic amines with humus [47] Transformation of phenols, aromatic amines, polyaromatic hydrocarbons, and other aromatic compounds, decolorization of Kraft bleaching effluents, treatment of dioxins, pyrene [86-89,114] Improved sludge dewatering [59]... [Pg.435]

The nitrophenols have been identified in effluents from several industries. 2-Nitrophenol has been detected in effluents from photographic and electronics industries (Bursey and Pellizzari 1982). Nitrophenols (isomer unidentified) at a concentration of 5 mg/L was detected in oil shale retort water (Dobson et al. 1985). Nitrophenols have been identified in effluents from other chemical plants, as well. 4-Nitrophenol has been identified in effluent from a pesticide plant (EPA 1985). Both 2-nitrophenol and 4-nitrophenol were detected in the final effluent from the waste water of a petroleum refining industry (Snider and Manning 1982). Nitrophenols have also been identified in primary and secondary effluents of municipal waste water treatment plants. For example, both nitrophenols were identified in the secondary effluent from a waste water treatment plant in Sauget, Illinois, (Ellis et al. 1982), and 4-nitrophenol was detected in both primary and secondary effluent... [Pg.74]


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